90
Curriculum Vitae Personal data: Name: Morten Hovd Date and place of birth: 12 th of September 1963 in Harstad, Norway Address: Lindeveien 23a, N-7058 Jakobsli, Norway Present position: Professor of process control, Engineering Cybernetics Department, Norwegian University of Science and Technology Education: Institution Duration Course/degree University of Salford, England 1982-1986 Natural Gas Engineering / BSc with Honours Norwegian Institute of Tecnology, Department of Chemical Engineering 1989-1992 Process Control / Doktor Ingeniør (PhD) Work experience: Institution / Company Department Duration Position Institue for Continental Shelf Research Center for Petroleum Related Process Technology 1986-1987 Engineer Norsk Hydro Process Technology Department, Technology and Development Division 1987-1989 Engineer Sintef Technical Chemistry Department 1992 Scientist Fantoft Prosess Process Control Group 1993 Engineer Sintef Technical Chemistry Department (assigned to projects for Norske Skog Research) 1993-1995 Scientist Fantoft Prosess Process Control Group 1996-1997 Engineer Fantoft Prosess Process Control Group 1997-1998 Head of group Norwegian University of Science and Technology Department of Engineering Cybernetics 1998 - Professor Consultancies: (company, date): Fantoft Prosess 1998 – 2000 Sintef Electronics and Cybernetics 1999 – Honeywell HiSpec Solutions 2000 – 2003 Cybernetica 2004 – Other appointments and activities: - IFAC Technical Committee on Mining, Mineral and Metals Processing, member. - Visiting professor, Mechanical and Aerospace Engineering Department, University of California San Diego, July 2002 – June 2003. - Editor, Modeling, Identification and Control (from 2004). - Board member, Norwegian Society for Automation (from 2004) Membership in professional organizations: - Institute of Electrical and Electronics Engineers - American Institute of Chemical Engineers - Norwegian Society of Chartered Engineers (Tekna) - Norwegian Society for Automation (NFA)

Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

  • Upload
    others

  • View
    2

  • Download
    0

Embed Size (px)

Citation preview

Page 1: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Curriculum Vitae

Personal data: Name: Morten Hovd Date and place of birth: 12th of September 1963 in Harstad, Norway Address: Lindeveien 23a, N-7058 Jakobsli, Norway Present position: Professor of process control, Engineering Cybernetics Department, Norwegian University of Science and Technology

Education:

Institution Duration Course/degree University of Salford, England 1982-1986 Natural Gas Engineering / BSc with Honours Norwegian Institute of Tecnology, Department of Chemical Engineering

1989-1992 Process Control / Doktor Ingeniør (PhD)

Work experience: Institution / Company Department Duration Position

Institue for Continental Shelf Research

Center for Petroleum Related Process Technology

1986-1987 Engineer

Norsk Hydro Process Technology Department, Technology and Development Division

1987-1989 Engineer

Sintef Technical Chemistry Department 1992 Scientist Fantoft Prosess Process Control Group 1993 Engineer Sintef Technical Chemistry Department

(assigned to projects for Norske Skog Research)

1993-1995 Scientist

Fantoft Prosess Process Control Group 1996-1997 Engineer Fantoft Prosess Process Control Group 1997-1998 Head of

group Norwegian University of Science and Technology

Department of Engineering Cybernetics

1998 - Professor

Consultancies: (company, date):

Fantoft Prosess 1998 – 2000 Sintef Electronics and Cybernetics 1999 – Honeywell HiSpec Solutions 2000 – 2003 Cybernetica 2004 –

Other appointments and activities:

- IFAC Technical Committee on Mining, Mineral and Metals Processing, member. - Visiting professor, Mechanical and Aerospace Engineering Department, University of

California San Diego, July 2002 – June 2003. - Editor, Modeling, Identification and Control (from 2004). - Board member, Norwegian Society for Automation (from 2004)

Membership in professional organizations:

- Institute of Electrical and Electronics Engineers - American Institute of Chemical Engineers - Norwegian Society of Chartered Engineers (Tekna) - Norwegian Society for Automation (NFA)

Page 2: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Prizes: - International Chemistry Olympiad, Stockholm, 1982: Bronze medallist. - Institution of Gas Engineers, UK, 1986: awarded the Charles Hunt Memorial Medal as the

best student in Gas Engineering (Distribution of natural gas). Supervision of doctoral students: Name of student Research topic Starting date Kristin Hestetun Use of data for anodic current distribution in aluminium

electrolysis Feb. 2000

Arjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG)

Jan. 2004

Courses taught: Modelling of contiuous-time dynamical systems (1998) Structures in process control (1999 – 2000) Robust control (2001 – ) Advanced process control (2001 – )

Bibliography of Morten Hovd Dr. ing. thesis: Studies on Control Sturcture Selection and Design of Robust Decentralized and SVD Controllers. Department of Chemical Engineering, Norwegian Institute of Technology, 1992. Book chapter: Hovd, M. and Skogestad, S. (2000). Techniques in the Control of Interconnected Plants, pp. 139-200 in C. T. Leondes (Ed.) Mechatronic Systems Techniques and Applications. Vol 5: Diagnostic, Reliability and Control System Techniques. Gordon and Breach Science Publishers International journal publications: 1. Skogestad, S., Hovd, M., and Lundström, P. (1991). Simple Frequency Dependent Tools for Analysis of Inherent Control Limitations. Modeling, Identification and Control, Vol. 12, No. 4, pp. 159-177. 2. Hovd, M. and Skogestad, S. (1992). Simple Frequency-dependent Tools for Control System Analysis, Structure Selection and Design. Automatica, Vol. 28, No. 5, pp. 989-996. 3. Hovd, M. and Skogestad, S. (1993). Improved Independent Design of Robust Decentralized Controllers. Journal of Process Control, Vol. 3, No. 1, pp. 43-51. Reprinted in: Modeling, Identification and Control, (1994), Vol. 15, No. 2, pp. 93-107. 4. Hovd, M., Lee, J. H. and Morari, M. (1993). Truncated Step Response Models for Model Predictive Control. Journal of Process Control, Vol. 3, No. 2, pp. 67-73. 5. Hovd, M. and Skogestad, S. (1993). A Procedure for Regulatory Control Structure Selection with Application to the FCC Process. AIChE Journal, Vol. 39, No. 12, pp. 1938-1953. 6. Hovd, M. and Skogestad, S. (1994). Control of Symmetrically Interconnected Plants. Automatica. Vol. 30, No. 6, pp. 957-973. 7. Hovd, M. and Skogestad, S. (1994). Sequential Design of Decentralized Controllers. Automatica, Vol. 30, No. 10, pp. 1601-1607. 8. Hovd, M. and Skogestad, S. (1994). Pairing Criteria for Decentralized Control of Unstable Plants. Industrial & Engineering Chemistry Research, Vol. 33, No. 9, pp. 2134-2139. 9. Hovd, M., Braatz, R. D. and Skogestad, S. (1994). SVD Controllers for H2-, H` - and µ-optimal Control. Automatica, Vol. 33, No. 3, pp. 433-439.

Page 3: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

10. Skogestad, S. and Hovd, M. (1995). Letter to the editor on decentralized vs. multivariable control, Journal of Process Control, Vol. 5, pp. 399-400. 11. Hovd, M., Michaelsen, R., and Montin, T. (1997). Model Predictive Control of a Crude Oil Distillation Column. Computers and Chemical Engineering, Vol. 21, Suppl. pp. S893-S897. 12. Hovd, M. (1997). Review of: “Multivariable Control System Design Techniques. Dominance and Direct Methods” by G. F. Bryant and L. F. Yeung. Journal of Process Control, Vol. 7, No. 6, pp. 467-468. 13. Hovd, M., Braatz, R.D. and Skogestad, S. (1997) ``SVD Controllers for H2-, H∞-, and µ-optimal

control, Automatica, Vol. 33, pp.433-439. 14. Ma, D.L., VanAntwerp, J., Hovd, M. and Braatz, R. (2002) Quantifying the potential benefits of

constrained control for a large scale system. IEE-Proc Control Theory Appl., Vol 149, No. 5, pp. 423 – 432.

15. Hovd, M., Ma, D.L. and Braatz, R.D. (2003). On the computation of disturbance rejection measures. Ind. Eng. Chem. Res., Vol 42, No. 10, pp. 2183 – 2188. (Also in Modeling, Identification and Control, Vol 25, No. 1, pp.45-56).

International conference publications 1. Skogestad, S. and Hovd, M. (1990). Use of Frequency-Dependent RGA for Control Structure

Selection. Proc. American Control Conference, pp. 2133-2139, San. Diego, USA. 2. Hovd, M., Lundström, P. and Skogestad, S. (1990). Controllability Analysis Using Frequency-dependent Measures for Interactions and Disturbances. American Institution of Chemical Engineers (AIChE) Annual Meeting, paper 321j, Chicago, Illinois, USA. 3 P. Lundström, S. Skogestad, M. Hovd and Wang, Z.-Q. (1991). Non-uniqueness of Robust H` decentralized PI-control. Proc. American Control Conference, pp. 1830-1835, Boston, USA. 4. Hovd, M., Lee, J. H. and Morari, M. (1991). Model Requirements for Model Predictive Control. Proc. European Control Conference, Grenoble, Frankrike, pp. 2428-2433. 5. Skogestad, S., Hovd, M. and Lundström, P. (1991). Towards Integrating Design and Control: Use of Frequency-dependent Tools for Controllability Analysis. Proc. Process Systems Engineering 91, pp. III.3.1-III.3.15, Canada 6. Hovd, M. and Skogestad, S. (1991). Impact of Model Uncertainty on Control Structure Selection for the Fluid Catalytic Cracking Process. Preprints IFAC Symposium ADCHEM'91, Toulouse, Frankrike, pp. 107-112. 7. Hovd, M. and Skogestad, S. (1991). Controllability Analysis of the Fluid Catalytic Cracking Process. AIChE Annual Meeting, paper 145g, Los Angeles, California, USA. 8. Wolff, E. A., Skogestad, S. and Hovd, M. (1992). Controllability of Integrated Plants. AIChE Spring National Meeting, Paper 67a, New Orleans, USA. 9. Hovd, M. and Skogestad, S. (1992). Robust Control of Systems Consisting of Symmetrically Interconnected Subsystems. Proc. American Control Conference, Chicago, Illinois, USA, pp. 3021-3025. 10. Hovd, M. and Skogestad, S. (1992). Controllability Analysis for Unstable Processes. Preprints IFAC Workshop on Interactions Between Process Design and Process Control, London, England, pp. 127-132. 11. Wolff, E. A., Skogestad, S., Hovd, M. and Mathiesen, K. W. (1992). A procedure for Controllability Analysis. Preprints IFAC Workshop on Interactions Between Process Design and Process Control, London, England, s. 49-54. 12. Hovd, M. and Skogestad, S. (1992). Design of Robust Decentralized Controllers. AIChE Annual Meeting, paper 127d, Miami Beach, Florida, USA. 13. Hovd, M,, Braatz, R. D. and Skogestad, S. (1993). On the Structure of the Robust Optimal Controller. Proc 12th IFAC World Congress, Sydney, Australia, Vol 4., pp. 27 - 30. 14. Hovd, M. and Skogestad, S. (1993). Improved Independent Design of Robust Decentralized Controllers. Proc. 12th IFAC World Congress, Sydney, Australia,

Page 4: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Vol. 5, pp. 271 - 274. 15. Hovd, M. and Skogestad, S. (1993). Robust Sequential Design of Decentralized Controllers. Proc. European Control Conference, Groningen, Nederland, pp. 1050-1055. 16. Hovd, M. and Skogestad, S. (1993). Robust Control of Symmetric Processes. AIChE Annual Meeting, paper 146k, St. Louis, Missouri, USA. 17. Hovd, M. and Skogestad, S. (1993) Pairing Criteria for Unstable Plants. AIChE Annual Meeting, paper 149i, St. Louis, Missouri, USA. 18. Hovd, M., Braatz, R. D. and Skogestad, S. (1994). SVD Controllers for H2-, H`- and µ-optimal Control, Proc. American Control Conference, pp. 1233-1237, Baltimore, USA. 19. Hovd, M., Michaelsen, R., and Montin, T. (1997). Model Predictive Control of a Crude Oil Distillation Column. PSE’97-ESCAPE-7, Trondheim, Norway. 20. Hovd, M., Eikaas, T. I., and Foss, B. A., (1999). Merging physical experiments into the learning arena. AIChE Annual Meeting, paper 205o/206o, Dallas, Texas, USA. 21. Hovd, M. and Glende, E., (1999). Interactions between design and control in offshore oil production

platforms. AIChE Annual Meeting, paper 208ab, Dallas, Texas, USA. 22. Hovd, M. and Braatz, R. D. (2000). On the computation of disturbance rejection measures.

Preprints of IFAC Symposium ADCHEM’2000, Pisa, Italy, pp.63-68. 23. Foss B. A., Eikaas, T. I., Hovd, M. (2000). Merging Physical Experiments back into the Learning Arena, American Control Conference, Chicago, USA. 24. Hovd, M. and Braatz, R. D. (2001). On the use of soft constraints in MPC controllers for plants

with inverse response. IFAC Symposium DYCOPS- 6, Chejudo Island, Korea. 25. Hovd, M. and Braatz, R. D. (2001). Handling state and output constraints in MPC using time-

dependent weights. American Control Conference, Arlington, Virginia, USA. 26. Jakobsen, S. R., Hestetun, K. Hovd, M. and Solberg, I. (2001). Estimating alumina concentration

distribution in aluminium electrolysis cells. 10th IFAC Symposium on Automation in Mining, Mineral and Metals Processing, Tokyo, Japan.

27. Hovd, M. and Bitmead, R. R. (2004). Directional leakage and parameter drift. Accepted for publication at IFAC Symposium on Dynamics and Control of Process Systems (DYCOPS-7), Boston, July 2004.

28. Hovd, M. and Bitmead, R. R. (2004). Interaction between control and state estimation in nonlinear MPC. Accepted for publication at IFAC Symposium on Dynamics and Control of Process Systems (DYCOPS-7), Boston, July 2004.

Submitted for publication 1. M. Hovd (2004). Adaptive MPC for reference tracking applications. Submitted to the IEEE

Conference on Decision and Control, Bahamas, Dec. 2004.

Publications in national journals (in Norwegian) 1. M. Hovd (2000). Modellbasert prediktiv regulering. Automatisering, no. 1, pp. 12-17.

Trondheim, 02 June 2004

Page 5: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

C U R R I C U L U M V I T A E Name: BJØRN NYGREEN Born: April 7th 1946 Nationality: Norwegian Address: Group for Managerial Economics and Operations Research

Department of Economics and Technology Management Norwegian University of Science and Technology (NTNU). 7491 Trondheim, Norway Phone/fax: +47 73593607 / +47 73593603 E-mail: [email protected] Academic degrees: 1969: M.Sc. in Applied Physics - The Norwegian Institute of Technology. 1973: Dr.ing. in Operations Research - The Norwegian Institute of Technology. Employment after dr.ing: 1974 - 1990: Associate professor, Department of Managerial Economics and Operations Research -

NTH. 1980 - ....: Scientific adviser for SINTEF Industrial Management, Economics and Logistics. 1991 - ....: Professor (Operations Research), Group for Man.Ec. & Op. Res. - NTNU. 1999 - 2002: Professor II (Logistics), Department for Economics, Molde College. Sabbatical years: 1984 - 1985: "Visiting Academic" at Imperial College (mining and petroleum), London combined

with cooperation with Scicon Ltd., London and Milton Keynes, England. 1995 - 1996: "Visiting Professor" at Brunel University (maths), London, England. 2001 - 2002: "Visiting Professor" at University of Edinburgh (maths), Edinburgh, Scotland. Academic society memberships: 1972....: NORS (The Norwegian Operations Research Society, group of PF) 1988....: The Mathematical Programming Society 1993....: Norwegian Council-member in IFORS. 1993....: Norwegian Council-member in EURO. 1994…: Operational Research Society Main interests: Mixed discrete optimization applied to real planning problems in transportation and process production with focus on ship scheduling and petroleum production. Ongoing international collaboration: Professor Ken McKinnon, School of Mathematics, University of Edinburgh, UK (Gas production) Major Norwegian Companies I have collaborated with: Hydro (Metals, Oil and gas, Refinery, Ammonia), Saga (Gas), Statoil (Oil and gas, Gas stations), Elkem (metals), Norske Skog (paper), British Petroleum (Distribution) Norwegian Applied Research Institutions I have collaborated with: SINTEF (Industrial Management, Applied Mathematics, MARINTEK), Norwegian Centre for Transport Research Governmental bodies I have collaborated with: Norwegian Petroleum Directorate

Page 6: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Participation in international evaluations: 1999: Readership evaluation in Edinburgh, Scotland 2002: PhD evaluation in Linköping, Sweden Supervised PhD (Dr.ing.) candidates: Finished candidates: Kjetil K. Haugen: “Possible Coputational Improvments in a STicastic Dynamic Programming Model for Scheduling of Off.Shore Petroleum Fields”, NTH 1991. He is now an associate professor at Molde College. Marielle Christiansen: “Inventory and Time Constrained Ship Routing – A mathematical programming approach”, NTNU 1996. She is now a professor at NTNU. Gerhard L. Doorman (only co-supervised): “Peaking Capacity in Restructured Power Systems”, NTNU 2000. He is now a senior scientist at SINTF Energy Research. Current candidates: Nina L. Ulstein: “Thesis on logistics including ship routing”. She plans to finish in 2004. Geir Brønmo: “Thesis on heuristic methods for ship and vehicle routing”. He plans to finish in 2005. Refereed publications from 1998: 1998: (co-author: M. Christiansen) "A method for solving ship routing problems with inventory

constraints". Annals of Operations Research, Vol. 81, p 357-378. 1998: (co-authors: T. Bjørkvoll, M. Christiansen, K. Haugen and Ø. Kristiansen) "Modeling Norwegian

petroleum production and transportation". Annals of Operations Research, Vol. 82, p 251-267. 1998: (co-authors: P.Baricelli og G. Mitra) "Modeling of augmented makespan problems (AMAPs):

Computational experience of applying integer presolve at the modelling stage". Annals of Operations Research, Vol. 82, p 269-288.

1998: (co-author: M. Christiansen) "Modelling path flows for a combined ship routing and inventory

management problem". Annals of Operations Research, Vol. 82, p 391-412. 2000: (co-authors: K. Kularajan, G. Mitra and F. Ellison) "Constraint Classification, Preprocessing

and a Branch and Relax Approach to Solving Mixed Integer Programming Models". International Journal of Mathematical Algorithms, Vol. 2, p 1-45.

2002: (co-authors: G. Doorman) "An integrated model for market pricing of energy and ancillary

services". Electric Power Systems Research, Vol. 61, p 169-177. 2003: (co-authors: G. Doorman) "Market Price Calculations in Restructured Electricity Markets ".

Annals of Operations Research, Vol. 124, p 49-67

Page 7: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

2005: (co-author: M. Christiansen, K. Fagerholt and D. Ronen) "Maritime Transportation" in a volume

of “Handbooks in Operations Research and Management Science” edited by C. Barnhart and G. Laporte, Elsevier (forthcoming)

2005: (co-authors: M.M. Sigurd, N.L. Ulstein and D.M. Ryan) "Ship Scheduling with Recuring Visits

and Visit Separation Requirements" in “Column generation” edited by G. Desaulniers, J. Desrosiers and M. Solomon, Kluwer (forthcoming)

2005: (co-author: M. Christiansen) "Robust Inventory Ship Routing by Column Generation" in

“Column generation” edited by Guy Desaulniers, Jacques Desrosiers and Marius Solomon, Kluwer (forthcoming)

Participation in International Conferences from 1998: 1998: "Applied Mathematical Programming and Modelling", Limassol, Cyprus. Paper: "Integer

Column generation by use of Subroutine Libraries for Mathematical Programming" co-author: M. Christiansen and co-author to paper given by G. Mitra "Constraint Classification, Preprocessing and Branch and Relax Approach to Solving Mixed Integer Programming Models".

1998: "The 5th Nordic MPS-meeting", Molde, Norway. Paper: "Integer programs and subroutine

libraries for mathematical programming". 1998: "The 40th British OR-conference ", Lancaster, England. Papers: "Governmental use of MP in

planning the Norwegian petroleum production" and "Integer presolve and model formulation of integer programs ".

1999: "The 15th Triennial Conference of The International Federation of Operational Research

Societies", Beijing, China. Paper: " Nonlinear Capacitated Lot Sizing " co-authors: K. Haugen and A. Olstad and co-author to the paper " A Ship Routing Problem with Soft Time Windows " given by M. Christiansen.

2000: "Applied Mathematical Programming and Modelling", London, England. Paper: "An Integrated

Model for Market Pricing of Energy and Ancillary Services" co-author: G. Doorman. 2000: "The 17th International Symposium on Mathematical Programming", Atlanta, GA, USA. Paper:

"Short term planning of natural gas production off-shore" co-author N. Ulstein. 2001: "The 43rd British OR-conference", Bath, England. Paper: "Planning gas production off-shore" 2001: "The 7th Meeting of the Nordic Section of the Mathematical Programming Society",

Copenhagen, Denmark. Paper: "Does it pay to upgrade MP software". 2002: "Applied Mathematical Programming and Modelling", Varenna, Italy. Co-author together with

M. Christiansen, R. Grønhaug and N. Magnussen to the paper: "Strategic capacity planning in the metal-working industry" given by N. Ulstein.

Page 8: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

2002: "The 16th Triennial Conference of The International Federation of Operational Research Societies", Edinburgh, Scotland. Paper: "Optimization of routing in oil and gas gathering networks" co-author: K. McKinnon and co-author to the paper "Developing a system for sea transport between Norway and Europe" given by N. Ulstein.

2002: "The 8th Meeting of the Nordic Section of the Mathematical Programming Society", Bergen,

Norway. Paper: "Routing in oil and gas gathering networks" co-author K. McKinnon. 2002: "Maritime Logistics Workshop", Georgia Institute of Technology, Atlanta, GA, USA. Paper:

"Ship scheduling in vendor managed inventory systems" co-author M. Christiansen and co-author together with N. Ulstein, R. Grønhaug and N. Magnussen to the paper "Supply Chain Design and Production Planning in Elkem ASA" given by M. Christiansen.

2003: "Odysseus 2003 - second international workshop on freight transportation and logistics"

Sicily, Italy. Co-author with K. Fagerholt and G.Brønmo to the paper: "Short-term scheduling of chemical tankers" given by M. Christiansen.

2003: "The 18th International Symposium on Mathematical Programming", Copenhagen, Denmark.

Paper: "Optimal routing of oil and gas from wells to separators" co-author K. McKinnon and co-author together with M. Christiansen, K. Mannsåker Reikvam and M. Storhaug Jensen to the paper: "A stochastic programming model for strategic capacity planning in the metal-working industry" given by N. Ulstein.

2004: "CO 2004 Combinatorial Optimisation Conference", Lancaster, England. Paper: "Robust

inventory routing in the shipping industry” co-author M. Christiansen. Co-author together with M. Christiansen to the paper “Ship Scheduling with Flexible Cargo Sizes” given by Geir Brønmo.

2004: "Applied Mathematical Programming and Modelling", London, England. Paper: "A hybrid

search heuristic for real Ship Scheduling problems" co-authors: Geir Brønmo, Marielle Christiansen and Kjetil Fagerholt and co-author together with M.M. Sigurd and D.M. Ryan to the paper "Ship Scheduling with Recuring Visits and Visit Separation Requirements" given by N.L. Ulstein.

International guest lectures hold at the following institutions Department of Mathematical modelling, Denmark Technical University, Lyngby, Denmark Department of Mathematics, University of Linköping, Linköping, Sweden Department of Mathematics, Royal Institute of Technology, Stockholm, Sweden School of Manufacturing & Mechanical Engineering, University of Birmingham, Birmingham, England Graduate School of Management, University of Lancaster, Lancaster, England Department of Mathematics, University of Kent at Canterbury, England Department of Mathematics and Statistics, Brunel University, London, England Department of Mathematics and Statistics, University of Edinburgh, Edinburgh, Scotland Department of Operational Research, London School of Economics, London, England Department of Engineering and Applied Science, George Washington University, Washington, USA

Page 9: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

1

Curriculum Vitae Asgeir Tomasgard

Born: October 16th 1970 Nationality: Norwegian Marital status: Married, two children Title: Dr. Ing. (PhD) Profession: associate professor /senior researcher Address: Rudolf Nilsens vei 1, N-7024 Trondheim, Norway

Home: + 47 72560446 Work: +47 73591267 / +47 73590806

Mobile phone: + 47 93058771 EMail: [email protected]

Employment record

1998- : SINTEF Industrial Management, Economics and Logistics, Senior researcher (from 2002), part time (50%) from 2001.

Tasks include:

Projects: Tomasgard has been involved in projects within supply chain optimization, investment analysis and risk management (aluminium extrusion, food production , electricity (production, sales and risk management), natural gas (production, transportation, financial trades and sales). Tomasgard has also been responsible for developing a valuation framework for new technology based firms. Client companies include: Statoil, Hydro, Iberdrola, Enel, Norsk Kjøtt (Gilde), NSB, Volvo Aero, Alcatel.

Project manager : Tomasgard has been responsible for managing national and international projects with duration from a few months and up to several years.

Project coordination: Tomasgard is currently acting as a coordinator for all research projects in the SINTEF group towards Norsk Kjøtt (Gilde). Tomasgard has been responsible for negotiating long term agreements with Norsk Kjøtt and NSB.

Tomasgard has been responsible for arranging several international workshops and national seminars within the topics liberalized natural gas markets, venture capital and supply chain optimization.

2002- : NTNU, Department of Industrial Economics and Technology Management, associate professor in business economics.

- Group leader for the managerial economics and operations research group from fall 2002 (13 staff and research fellows).

- Teaching at under-graduate and graduate level, courses with 5-200 students. Responsible for developing 3 new courses : production- and network economics, production economy and markets, planning and economical analysis in supply chains.

- Student supervision at PhD level, masters level (about 5-10 student groups every year) and student projects (about 5-10 groups per year) within subjects: investment analysis, logistics, supply chain optimization, risk management and liberalized energy markets (electricity and gas). Most projects have been towards industry.

- Core team member in SMARTLOG (25 mill research project in logistics). Member of Næringslivets idefond, area transportation and logistics. Contact person at NTNU/SINTEF natural gas technology center in the field Energy economics.

Page 10: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

2

2000-2002 : NTNU, Department of Industrial Economics and Technology Management, adjunct associate professor in business economics (part-time position 20-50%).

1995-1998: Department of Industrial Economics and Technology Management, research fellow (stipendiat).

1995 - 1998: Consultant.: Tomasgard consulted in small projects for SINTEF Industrial Management, Fokus forvaltning ( development of sales reports from Microsoft SQL database)

07.02.94 - 01.12.94: Norwegian Armed Forces: Software design and database development.

01.06.93 - 20.08.93: Statoil, system development: Development of software for accounting and portfolio management.

Education

01.12.94 -30.11.98: Dr.Ing. in operations research, Department of Industrial Economics and Technology Management, Norwegian University of Science and Technology. "Aspects of service provision and distributed processing in a telecommunication network". Scholarship from Telenor Research . (Supervisor Stein.W. Wallace, co-supervisors, Leen Stougie, Shane Dye, Jan Audestad).

1989 - 1993: Siv.Ing (M.Sc.) in Industrial Economics, The Norwegian Institute of Technology (NTH), (Average score 1.5). Thesis written for Statoil: "Deterministic versus dynamic stochastic analysis of development projects: Influence on project evaluation and decisions”.

Research visits

05.08.96 - 20.12.96: Visitor at the Tinbergen Institute Amsterdam

12.06.95 - 04.08.95: Visitor at Edinburgh Parallel Computing Centre (EPCC) under the Training and Research on Advanced Computing Systems (TRACS) program.

Additional information: Publications and presentations

Publications

International journals

1. S. Dye, L. Stougie, A. Tomasgard, The single resource service provision problem , Naval research logistics, 50, 869-887, 2003.

2. S. Dye, L. Stougie, A. Tomasgard, Approximation algorithms and relaxations for a service provision problem on a telecommunication network , Discrete applied mathematics, 129, 63-81, 2003.

3. A. Tomasgard, J.A. Audestad, S. Dye, L. Stougie, M.H. van der Vlerk, S.W. Wallace, Modelling Aspects of Distributed Processing in Telecommunications Networks . Annals of Operations Research, 82:161-184, 1998

4. S. Dye, A. Tomasgard, S.W. Wallace, "Feasibility in Transportation Networks with Supply Eating Arcs" , Networks, 31: 165-176, 1998.

Published popular science papers

5. E. Matson, A. Tomasgard and L.H. Vik, Verdsetting av høyteknologibedrifter , Magma: Tidsskrift for økonomi og ledelse, 4 (4), 2001.

Page 11: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

3

6. S.F. Fleten, A. Tomasgard, S.W. Wallace, Produksjonsplanlegging og risikostyring i et deregulert kraftmarked med finansielle instrumenter. Magma: Tidsskrift for økonomi og ledelse, 4 (5), pp. 22-33, 2001.

7. S. Dye, A.Tomasgard, S.W. Wallace, "New aspects of service provision and technology strategies", Telektronikk, Telenor research, Kjeller, Norway, to appear 1998.

Published in books

8. A. Tomasgard, and E. Høeg, ‘A supply chain optimization model for the Norwegian Meat Co-operative’, in Ziemba, W.T. and Wallace, S.W., eds, ‘Applications of stochastic programming’, MPS-SIAM series on optimization, to appear 2004.

9. A. Tomasgard and E. Høeg, Supply chain optimization and demand forecasting, in Olhager, Persson, Selldin, Wikner (editors),‘Produktionslogistik 2002-Modeller for effektiv produktionslogistik". Linköpings tekniske högskola, 2002.

10. Aspects of service provision and distributed processing in a telecommunication network: using stochastic programming, Dr.Ing thesis, Supervisor: Stein W. Wallace, co-supervisors: Jan A. Audestad, Shane Dye and Leen Stougie. NTNU, 1998.

11. S.W. Wallace, S. Dye, A. Tomasgard, "Feasibility in bipartite uncapacitated networks", in E. Matson, A.Tomasgard, E. Meiestad, S. Dye (eds.), "Essays in honour of Bjørn Nygreen on his 50th birthday", Dept. Of industrial economics and technology management, Norwegian University of Science and Technology, 1996.

Other refereed publications

12. T. Bjørkvoll, S.F. Fleten, M. P. Nowak, A. Tomasgard og S. W. Wallace, Power generation planning and risk management in a liberalised market, IEEE Porto Power Tech Proceedings, pp. 426-431, 2001.

13. A. Tomasgard, E. Høeg, Supply Chain Optimization for the Norwegian Meat co-operative, Conference proceedings: NOFOMA 15, Trondheim, June 2002.

14. N. Olsson, A. Tomasgard, C.C. Røstad, B. Andersen, I.-A.F. Sætermo, Major logistic changes, a project perspective, Conference proceedings :NOFOMA 15, Trondheim, June 2002.

Selected Non-refereed publications

15. J.J.J van der Broek, L. Stougie, and A. Tomasgard, Location of slaughterhouses under eonomics of scale, Working paper NTNU, 2003, (submittd)

16. S. Dye, L. Stougie, A. Tomasgard, Single node service provision with fixed charges ,working paper #4-98, Department of Economics and Technology Management, Norwegian University of technology and Science, 1998. (submitted)

17. Tomasgard, A, Borgen, E., Elevenes, J. and Hynne, H., A spreadsheet model for valuation of venture projects, in Matson, E. (editor), Valuation of new technology projects, Department of Industrial economics and technology management, NTNU, 2003.

18. H.J. Dahl, F. Rømo and A. Tomasgard, An Optimisation Model for Rationing-Efficient Allocation of Capacity in a Natural Gas Transportation Network, Conference proceedings: IAEE Praha, June, 2003.

19. Rømo, F., Tomasgard, A.., Røvang, L.B. and Pedersen, B., Optimal routing of natural gas in pipeline networks, SINTEF working paper, SINTEF Industrial Management, Trondheim, Norway, 2003.

20. Rømo, F. Sæthermo, I.A. and Tomasgard, A., Slaughterhouses and Courts of Justice - A location analysis approach, Conference proceedings Uddevalla Symposium, Sweden, 2001.

Page 12: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

4

21. Tomasgard, "Deterministic versus dynamic stochastic analysis of development projects: Influence on project evaluation and decisions" (in Norwegian), Thesis for the degree Siv.Ing. at Department of Managerial Economics and Operations Research, The Norwegian Institute of Technology, Norway. Thesis supervisor: Stein W. Wallace, 1993.

In addition Tomasgard has coauthored a number of SINTEF reports.

Presentations at conferences/seminars

1. Tactical and operational planning in – the VENOGA perspective, 3rd SINTEF International Workshop on Integrated natural gas market and transportation systems, Trondheim 2003.

2. Issues on modelling financial markets under imperfect competition, 3rd SINTEF International Workshop on Integrated natural gas market and transportation systems, Trondheim 2003.

3. Introduksjon til operasjonsanalyse, Smartlog industri seminar : Optimeringsbasert beslutningssøtte I industrien, Trondheim, 2003.

4. Facility location under economics of scale, ISMP 2003,Copenhagen, August 2003.

5. Weekly Supply Chain Coordination with Stochastic Demand, ISMP 2003, Copenhagen, August 2003.

6. Tactical and operational planning in a deregulated gas market - the VENOGA perspective, 2nd SINTEF International Workshop on integrated natural gas market and transportation systems, Selbu, October, 2002.

7. Supply chain optimization and demand forecasting, Plan forsknings og tilämpningskonferens, Linköping, August 2002.

8. Supply Chain Co-ordination with Stochastic Demand, IFORS 2002, Edinburgh, July, 2002.

9. Supply Chain Optimization for the Norwegian Meat co-operative, NOFOMA, Trondheim June 2002.

10. Value Chain Management in the Liberalized Natural Gas Market, APMOD 2002, Varenna, Italy, June, 2002.

11. The VENOGA project, 1st SINTEF International Workshop on integrated natural gas market and transportation systems, Røros, October, 2001.

12. Optimization models in a liberalized natural gas market, The Seventh Meeting of the Nordic Section of the Mathematical Programming Society, Copenhagen, October, 2001.

13. A Supply Chain Management Model with stochastic demand, 9th international conference on stochastic programming, Berlin, August, 2001.

14. The value of flexibility and the price of risk, International workshop on decision making under uncertainty, Håholmen, May, 2001.

15. Et beslutningsstøtteverktøy for verdivurdering av kunnskapsbedrifter , Fagkonferanse i bedriftsøkonomiske emner (FIBE), NHH, Bergen, January 2001.

16. En modell for verdsetting av ny teknologi og intellektuell kapital, Seminar om venturekapitalselskapenes virksomhet vedrørende bedriftsetablering og industriutvikling basert på ny teknologi, Trondheim, September 2000.

17. A Stochastic Supply Chain Management Model for the Norwegian Meat Cooperative, , 17th International Symposium on Mathematical Programming (ISMP2000), Atlanta, august 2000.

18. A Supply Chain Optimization Model for the Norwegian meat industry, International Working Conference on Information and Communication Technology (ICT) in Logistics and Production Management, IFIP WG 5.7, Tromsø, Norway, June 28-30, 2000.

Page 13: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

5

19. Scenario generation and valuation of new technology based firms, 26th Meeting of Euro working group on financial modelling, Trondheim, Norway, May 4-6, 2000.

20. Stokastisk programmering i lys av opsjonsteori, Institutt for Industriell økonomi og teknologiledelse, Trondheim, Norway, 1. februar, 2000

21. SINTEF’s evaluering av pilotprosjekt med FAST systemene, ITTFs konferanse om ERP og logistikk spesialsystemer, Hamar, Norway, november 16-17, 1999

22. Stochastic Integer Programming, Guest lecture, Department of Industrial Economis and Technology Management, NTNU, Trondheim, Norway , October, 1999.

23. New Aspects of Service Provision and Technology Strategies in Telecommunications, Department seminar, Norwegian school of economics and business administration, Department of finance and management science, Bergen, October 1,1999.

24. Complexity and approximation of a stochastic integer program, The Sixth Meeting of the Nordic Section of the Mathematical Programming Society, Vesterås, September 25, 1999.

25. Optimeringsbasert beslutningsstøtte i verdikjeder, SINTEF Teknologiledelse's fagdager i logistikk, Selbusjøen hotell og gjestegård, September 23, 1999.

26. Approximation of a Stochastic Integer Program with applications in telecommunications, 19th IFIP TC7 Conference on System Modelling and Optimization, Cambridge, England, July 12 - 16, 1999

27. Solution methods for the service provision problem, OR98 International Conference on Operations Research, Zurich, September 1998.

28. Solving a stochastic service provision problem in telecommunications using branch and bound and relaxations, Eindhoven University of Technology, August 1998.

29. Solving a stochastic service provision problem in telecommunications using branch and bound and relaxations, VII International Conference on Stochastic Programming, Vancouver, August 1998.

30. Service provision and distributed processing in a telecommunications network: using stochastic programming, The Fifth Meeting of the Nordic Section of the Mathematical Programming Society, Molde, May 1998.

31. A stochastic service provision problem: decomposition methods, 4th INFORMS telecommunications conference, Boca Raton, Florida, March 1998.

32. Modelling Aspects of Distributed Processing in Telecommunication Networks, Telenor Research, Kjeller, November 1997.

33. Modelling in Distributed Telecommunications Networks, 16th International Symposium on Mathematical Programming (ISMP97), Lausanne, August 1997.

34. Stochastic Programming Models For Distributed Communications Models, EURO/INFORMS-97, Barcelona, July 1997.

35. Service configuration in Intelligent Networks: A mixed-integer formulation, TRACS-seminar, Edinburgh Parallel Computing Centre (EPCC), 1995.

Page 14: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV Name: Olav Bolland Born: 1962 Nationality: Norwegian Present position: Professor Degrees: Siv.Ing. (M.Sc.): Norwegian University of Science and Technology, Mech. Eng., 1986 Dr.Ing.: Norwegian University of Science and Technology, Mech. Eng., 1990 Work experience: • Visiting researcher at Siemens AG/UB KWU in Erlangen,

Germany, 01.01.87 - 01.08.87 • Scientific advisor for SINTEF, 01.01.88 - 01.11.96, 01.03.98 -

present • Associate Professor, Department of Energy and Process Engineering, Norwegian University of

Science and Technology, 01.02.1990 - 01.05.2002 • Professor, Department of Energy and Process Engineering, Norwegian University of Science

and Technology, 01.05.2002 - present • Sabbatical year from august 1996 to august 1997. Working as a scientific guest at the

Eidgenössische Technische Hochshule Zürich - ETHZ, (Swiss Federal Institute of Technology) Membership in academic and professional committees: • Member of the Lead Author Team of the IPCC Special Report on CO2 Capture, Transport and

Storage (2003-2005) • University programme Energy and Environment (500 students), Chairman of the Board • ASME member • Norwegian Research Council, Klimatek evaluation committee • Several times in Ph.D.-committees • Professorship evaluation committee – 3 times, 2003-2004 • Member of Faculty Board, 2 periods Present doctoral students and post.docs supervised: Øyvind Brandvoll 2001-2004 Chemical Looping Combustion Rehan Naqvi 2003-2005 Chemical Looping Combustion Bjørn Thorud 2001-2004 Dynamic performance SOFC Christoph Stiller 2003-2005 Dynamic performance SOFC Ragnhild Ulfsnes 2001-2004 Dynamic performance of oxy-fuel gas turbine cycle Maria Jonsson 2004-2005 Gas turbine cycle modelling and analysis (post-doc) Khasayar Nasrifar 2004-2005 LNG technology (post-doc) Ola Maurstad 2004-2006, Modelling and simulation of power cycle with CO2 capture Supervised doctoral students: Ola Maurstad 1998-2002 Academic and professional publications Peer-reviewed

1. Maurstad O., Bredesen R., Bolland O., Kvamsdal H., and Schell M., "SOFC and gas turbine power systems - evaluation of configurations for CO2 capture", submitted for review to GHGT-7, Vancouver, Sept. 2004

Page 15: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

2. Kvamsdal H., Maurstad O., Jordal K., and Bolland O., "Benchmarking of gas-turbine cycles with CO2 capture", submitted for review to GHGT-7, Vancouver, Sept. 2004

3. Bolland O., Kvamsdal H., Boden J.C., "A comparison of the efficiencies of the oxy-fuel power cycles Water-cycle, Graz-cycle and Matiant-cycle", in press for publication in the book 'The CO2 Capture and Storage Project for Carbon Dioxide in Deep Geological Formations for Climate Change Mitigation', by Elsevier, final result of the CCP-project, 2004

4. Jordal K., Möller B.F., Bolland O., and Torisson T., 'Optimisation with genetic algorithms of a gas turbine cycle with H2-separating membrane reactor for CO2 capture', submitted for review to the International Journal of Green Energy, 2004

5. Ertesvåg I., Kvamsdal H., and Bolland O., "Exergy analysis of a gas-turbine combined-cycle power plant with precombustion CO2 capture", in press for publication in the journal Energy, 2004

6. Jordal K, Bredesen R., Kvamsdal H.M., O. Bolland O., “Integration of H2-separating membrane technology in gas turbine processes for CO2 sequestration”, presented at and in the proceedings of the Sixth International Conference on Greenhouse Gas Control Technologies - GHGT-6, Kyoto, Japan, October 2002, in press for publication in Energy, 2004

7. Jordal K., Bolland O., and Klang Å., "Aspects on cooled gas turbine modelling for the semi-closed O2/CO2 cycle with CO2", presented at the ASME TURBO EXPO conference, 16-19 June, 2003, Atlanta, USA, ASME Paper No. GT-2003-38067, in press for ASME Journal of Engineering for Gas Turbines and Power, July 2004

8. Brandvoll Ø. and Bolland O., "Inherent CO2 capture using chemical looping combustion in a natural gas fired power cycle", presented at the ASME TURBO EXPO conference, 3-6 June, 2002, Amsterdam, The Netherlands, ASME Paper No. GT-2002-30129, in press for publication in the ASME Journal of Engineering for Gas Turbines and Power, 2004

9. Imsland L., Snarheim D., Ulfsnes R., Bolland O., Foss B. "Modeling and control of a O2/CO2 gas turbine cycle for CO2 capture, to be presented at the 7th International Symposium on DYnamics and COntrol of Process Systems (DYCOPS), Cambridge, Massachusetts USA, 5-7 July, 2004

10. Bredesen R., Jordal K. and Bolland O., "High-Temperature Membranes in Power Generation with CO2 capture", invited review paper, in press for publication in the Journal of Chemical Engineering and Processing, Elsevier, 2004

11. Veér T., Ulvestad A. and Bolland O., "Frame, a Tool for Predicting Gas Turbine Condition as well as Reliability, Availability Performance", ASME Paper No. GT2004-53770, to be presented at and in the proceedings of the ASME TURBO EXPO conference, 14-17 June, 2004, Vienna, Austria

12. Veér T., Haglerød K.K. and Bolland O., "Measured Data Correction for Improved Fouling and Degradation Analysis of Offshore Gas Turbines", ASME Paper No. GT2004-53760, to be presented at and in the proceedings of the ASME TURBO EXPO conference, 14-17 June, 2004, Vienna, Austria

13. Naqvi R., Bolland O., Helle K. and Brandvoll Ø. "Chemical Looping Combustion-Analysis of Natural Gas Fired Power Cycles With Inherent CO2 Capture", ASME Paper No. GT2004-53359, to be presented at and in the proceedings of the ASME TURBO EXPO conference, 14-17 June, 2004, Vienna, Austria

14. Stiller C., Thorud B., Seljebø S., Mathisen Ø., Karoliussen H., and Bolland O., "Simulation-Based Comparison of Combined SOFC/GT Cycles with Planar and Tubular Fuel Cell Models - part 1", submitted for review in the Journal of Power Sources, 2004

15. Stiller C., Thorud B., Seljebø S., Mathisen Ø., Karoliussen H., and Bolland O., "Simulation-Based Comparison of Combined SOFC/GT Cycles with Planar and Tubular Fuel Cell Models - part 2", submitted for review in the Journal of Power Sources, 2004

16. Veér T. and Bolland O., "Reliability and Availability – a challenge of Increasing Importance for the Energy Industry", presented at and in the proceedings of the ECOS - 16th International Conference on Efficiency, Costs, Optimization, Simulation and Environmental Impact of Energy Systems, Copenhagen, Denmark, 30 June - 2 July, 2003

Page 16: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

17. Ulfsnes R., Karlsen G., Jordal K., Bolland O. and Kvamsdal H., "Investigation of physical properties for O2/CO2 gas turbine cycle with CO2 capture", presented at and in the proceedings of the ECOS - 16th International Conference on Efficiency, Costs, Optimization, Simulation and Environmental Impact of Energy Systems, Copenhagen, Denmark, 30 June - 2 July, 2003

18. Brandvoll Ø., Kolbeinsen L., Olsen N., Bolland O., Chemical Looping Combustion - reduction of nickel oxide - nickel aluminate by hydrogen", presented at and in the proceedings of ICheaP-6, The Sixth Italian Conference on Chemical and Process Engineering, Pisa, Italy, 08 -11 June 2003

19. Ulfsnes R., Bolland O. and Jordal K., "Modelling and simulation of transient performance of the semi-closed O2/CO2 gas turbine cycle for CO2 capture", presented at the ASME TURBO EXPO conference, 16-19 June, 2003, Atlanta, USA, ASME Paper No. GT-2003-38068, accepted for publication in the ASME Journal of Engineering for Gas Turbines and Power

20. Veér T. and Bolland O, "Using Probabilistics and advanced Software Tools for Reliability and Availability Assessment and Lifing", presented at the ASME TURBO EXPO conference, 16-19 June, 2003, Atlanta, USA, ASME Paper No. GT-2003-38474.

21. Bolland O., Undrum H., A novel methodology for comparing CO2 capture options for natural gas-fired combined cycle plants, Advances in Environmental Research, Volume 7, Issue 4, (2003) 901-911, Elsevier Science Ltd., available online www.elsevier.com/locate/aer, 2003

22. Zvolinschi A., Kjelstrup S., Bolland O. and van der Kooi H.J., "Including exergy analysis in industrial ecology: The case of combined cycle power plants with CO2 capture", presented at and in the proceedings of the ECOS - 15th International Conference on Efficiency, Costs, Optimization, Simulation and Environmental Impact of Energy Systems, Berlin, Germany, 3-5 July, 2002

23. Kvamsdal H.K., Ertesvåg I.S., Bolland, O., and Tolstad T., "Exergy analysis of gas-turbine combined cylce with CO2 capture using pre-combustion decarbonization of natural gas", presented at the ASME TURBO conference, 3-6 June, 2002, Amsterdam, The Netherlands, ASME Paper No. GT-2002-30411, 2002

24. Maurstad, O., Liu L.X., Bolland O., and Litster J.D., "Experimental study of the particle size distribution in fluidized bed granulation", In Proceedings of the 6th World Congress of Chemical Engineering, Melbourne, Australia, 2001

25. Bolland O., Nicolai R., "Describing Mass Transfer in Circulating Fluidized Beds by Ozone Decomposition", Chemical Engineering Communications, Vol. 187, pp. 1-21, 2001

26. Kvamsdal H.M., Andersen T., and Bolland O., "Natural gas fired power plants with CO2-capture - Process integration for high fuel-to-electricity conversion efficiency", presented at ESCAPE 10 conference - European symposium on computer aided process engineering, May 2000, published in Computers and Chemical Engineering, #8, ISBN: 0444505202, pp. 331-336, 2000

27. Andersen T., Kvamsdal H.M., and Bolland O., "Gas turbine combined cycle with CO2 capture using auto-thermal reforming of natural gas", presented at the ASME Gas Turbine and Aeroengine Congress and Exposition in München , May 8-12, 2000

28. Bolland O., Nicolai R., "Describing Mass Transfer in Circulating Fluidized Beds by Ozone Decomposition", presented at the Advanced Technologies for Particle Processing (AiChE annual meeting), November 15-20, 1998, Miami Beach, USA. Published in AIChE Symposium Series No. 321, Volume 95, Advanced Technologies for Fluid-Particle Systems, ISBN 0-8169-0815-X, pp. 52-60, November 1999.

29. Bolland, O. and Mathieu, P., 1998, Comparison of Two CO2 Removal Options in Combined Cycle Power Plants, Energy Conversion and Management, 39 (16-18), p.1653-1663, presented at the FLOWERS'97 conference July 30-August 1, 1997

30. Bolland, O., Førde, M. and Hånde, B. "Air Bottoming Cycle - use of gas turbine waste heat for offshore power generation", presented at the ASME COGEN TURBO conference, August 23-25, 1995, Vienna, Austria, ASME Paper No. 95-CTP-050, published in the ASME Journal of Engineering for Gas Turbines and Power, Volume 118, No. 2, Apr 1996.

Page 17: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

31. Bolland, O. and Stadaas, J.F., "Comparative Evaluation of Combined Cycles and Gas Turbine Systems with Water Injection, Steam Injection and Recuperation", presented at the ASME Gas Turbine and Aeroengine Congress and Exposition May 24-27, 1993, Cincinnati, ASME Paper No. 93-GT-57, 1993, published in the ASME Journal of Engineering for Gas Turbines and Power, Vol. 28, Jan 1995.

32. Bjerve, Y. and Bolland, O., "Assessment of Power Generation Concepts on Oil Platforms in Conjunction with CO2 Removal", presented at the ASME International Gas Turbine and Aeroengine Congress and Exposition, June 13-16, 1994, Hague, the Netherlands, ASME Paper No. 94-GT-378, 1994.

33. Bolland, O. and Sæther, S., "New Concepts for natural Gas Fired Power Plants which Simplify the Recovery of Carbon Dioxide", presented at the First International Conference on Carbon Dioxide Removal, Amsterdam, The Netherlands, March 4-6, 1992, published in Energy Convers. Mgmt Vol. 33, No. 5-8, pp. 467-475, 1992

34. Bolland, O., "A Comparative Evaluation of Advanced Combined Cycle Alternatives", presented at the ASME Gas Turbine and Aeroengine Congress and Exposition June 11-14, 1990, Brussels, ASME Paper No. 90-GT-335, published in the ASME Journal of Engineering for Gas Turbines and Power, Vol. 113, 1991

International conference proceedings (not peer-reviewed)

1. Thorud B., Stiller C., Weydahl T., Bolland O., Karoliussen H., "Part-load and load change simulation of tubular SOFC systems", to be presented at the Fuel Cell Forum, Luzerne, 28 June – 2 July 2004

2. Veér T. and Bolland O., "Derating and Degradation Considerations within FMECA", 6th

International Conference on Heat Engines and Environment, Balatonfured, Hungary, May, 2003

3. Zvolinschi A., Kjelstrup S., Bolland O. and Kooi, H.J. van der, "Exergy Analysis for the Assessment of the Sustainability of Combined Cycle Power Plants with CO2 Capture", poster, 14th World Hydrogen Energy Conference, Montréal, Canada, June 9-13, 2002 Awarded as the best poster in conference

4. Kvamsdal H.K., Ertesvåg I.S., Bolland, O., and Tolstad T, "Combined Cycle with CO2 capture based on the pre-combustion method", Second Nordic Minisymposium on Carbon Dioxide Capture and Storage, Göteborg, October 26, 2001. available at http://www.entek.chalmers.se/~anly/symp/symp2001.html

5. Brandvoll Ø., Bolland O., Vestøl S.., "Chemical looping Combustion - fuel energy conversion with inherent CO2 capture", poster, paper published in the proceedings of the International Conference POWER GENERATION AND SUSTAINABLE DEVELOPMENT, Liège (Belgium), 8-9 October, 2001

6. Bolland O., Ertesvaag I.S., and Speich D., "Exergy analysis of gas-turbine Combined Cycle with CO2 capture using auto-thermal reforming of natural gas", poster, paper published in the proceedings of the International Conference POWER GENERATION AND SUSTAINABLE DEVELOPMENT, Liège (Belgium), 8-9 October, 2001

7. Bolland O., Kvamsdal H.K., and Boden J.C., "A thermodynamic comparison of the oxy-fuel power cycles Water-Cycle, Graz-Cycle and Matiant-Cycle", presentation, paper published in the proceedings of the International Conference POWER GENERATION AND SUSTAINABLE DEVELOPMENT, Liège (Belgium), 8-9 October, 2001

8. Undrum, H., Bolland, O., and Aarebrot, E., “Economical assessment of natural gas fired combined cycle power plant with CO2 capture and sequestration”, presented at the Fifth International Conference on Greenhouse Gas Control Technologies, Cairns, Australia, August 2000.

9. Bolland, O., Undrum, H., and Myhre-Nielsen, M., “Natural gas fired power cycles with integrated CO2 capture”, presented at the Fifth International Conference on Greenhouse Gas Control Technologies, Cairns, Australia, August 2000.

Page 18: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

10. Bolland O., Undrum H., "Removal of CO2 From Natural Gas Fired Combined Cycle Plants", presented at the Power-Gen '99, Frankfurt, Germany, June 1999

11. Bolland O., Undrum H., "Removal of CO2 from Gas Turbine Power Plants: Evaluation of pre- and postcombustion Methods", presented at the Fourth International Conference on Greenhouse Gas Control Technologies, Interlaken, Switzerland, September 1998

12. Bolland, O., "Thermal Power Cycles for the Future", presented at the poster session of the Eurogas '94 conference, March 21-23, Trondheim, Norway, 1994

13. Bolland, O. and Pettersen, J., "Improved Cycles for Natural Gas Power Generation", presented at the IEA International Conference on Natural Gas Technologies: Energy Security, Environment and Economic Development, October 31 - November 3, Kyoto, Japan, published in conference proceedings pp. 121-130, 1993

14. Sæther, S. and Bolland, O., "Thermal Power Production", presented at the poster session of the SPUNG Seminar, Trondheim, Norway, October 5-6, 1993

Invited lectures (selection)

1. Bolland O., "Power generation with CO2 capture and sequestration", invited keynote speaker at the annual program seminar for the Swedish Gas Turbine Center, 19-20 November 2003

2. Bolland O., "STATUS FOR GASSKRAFTVERK MED CO2-HÅNDTERING (Status for gas fired power plants with CO2 capture)", invited speaker at the Norges Energidager conference, organised by The Norwegian Water Resources and Energy Directorate (NVE), 17 October 2003

3. Bolland O., "Gassteknisk Senter NTNU – SINTEF Satsning på gasskraftverk med CO2-innfanging (The Gas Technology Center - efforts for making power plants with capture of CO2)", invited speaker at the Energirike Haugalandet conference, 23 September 2003

4. Bolland O. and Veer T., "CENTENARY OF THE FIRST GAS TURBINE TO GIVE NET POWER OUTPUT: A TRIBUTE TO ÆGIDIUS ELLING", presented (with no paper) at the ASME TURBO EXPO conference, 16-19 June, 2003, Atlanta, USA,

5. Bolland O., "Gassteknisk Senter NTNU – SINTEF (Gas Technology Center NTNU – SINTEF)", invited lecture at the conference Gass- og energiteknologi, Skjærgården Hotell og Badepark, Langesund, 3-4. June 2003

6. Bolland O., "Oppsummering og vurdering av teknologier rundt CO2-fjerning (Summary and conclusion about CO2 capture methods)", invited lecture at the conference Gass- og energiteknologi, Skjærgården Hotell og Badepark, Langesund, 3-4. June 2003

7. Bolland O., Om brenselceller, gassturbiner og CO2-fangst - Eksempel på et forskningsprosjekt (About fuel cells, gas turbines and CO2 capture - example of a research project), invited lecture at opening of the Gas Technology Center NTNU - SINTEF, Trondheim, 22 April 2003

8. Bolland O., CO2 removal before combustion, invited lecture at CONFERENCE ON CYCLES FOR LOW CARBON DIOXIDE PRODUCTION, Cranfield University, School of Engineering, UK, March 24-25, 2003

9. Bolland O., Policy, research and implementation of CO2 sequestration technologies in Norway, invited lecture at Swiss Federal Institute of Technology - ETH Zürich - Switzerland. November 22, 2002

10. Bolland O., Policy, research and implementation of CO2 sequestration technologies in Norway, invited lecture for Studiengruppe Energieperspektiven - Baden, Switzerland. November 21, 2002

11. Bolland O., Options for oxy-fuels & pre-combustion decarbonisation cycles, invited lecture for Alstom Power Cross Segment CO2 Mitigation Group - Baden, Switzerland. October 11, 2002

12. Bolland, O., "Fossila bränslen men ingen CO2 ? (Fossile fuels but no CO2 ?)", presented at NORDVARME-Symposium i Nyköping, Sweden, June 2002

Page 19: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

13. Bolland O., "Gasskraftverk med CO2-håndtering (Gas fired power plant with CO2 sequestration)", invited lecture at 2nd International Symposium on High Strength Steel, Stiklestad/Verdal, 24 April 2002

14. Bolland O. and Brandvoll Ø., "Inherent CO2 capture using chemical looping combustion in a natural gas fired power cycle", invited lecture at the national NTNU seminar on CO2 capture, Trondheim, 22 April 2002

15. Bolland O., "Technology for gas turbine power plants - an environmental view", invited lecture at the IBC Conference New Dynamics of Scandinavian Gas & Power Oslo, 11-12 February 2002

16. Bolland O., "Status for norsk satsning innen miljøvennlig utnyttelse av naturgass (Status for the Norwegian efforts related to utilization of natural gas)", presentation at the Miljøforum, The Norwegian Oil Industry Association, 15 October 2001

17. Bolland, O., "Particle technology research at NTNU in general, and in particular measurement of bubble velocity in fluidized bed reactors", invited lecture at the University of Queensland, Brisbane, August 2001

18. Bolland, O., "Naturgass til kraft - miljøvennlig ? (natural gas for power generation - environmentally friendly ?", invited lecture at the UMOE 100 year anniversary seminar, 11 April 2000

19. Bolland, O., "Removal of CO2 from Natural Gas Combined Cycle Power Plants", lecture at the seminar Flowsheet synthesis and optimisation of CHP power plants, Nordic Council of Ministers, Helsinki, 3-5 March 2000

20. Bolland, O., and Aam, S., "SINTEFs synspunkter i gasskraftdebatten" (SINTEFs points of view in the debate about Gas Power Generation), presented to the Committee of Energy and Environment of the Norwegian Storting, Oslo, December 1999

21. Bolland O., "Experimental examination of bubble rise velocity in a fluidised bed", Presentation at the Norsk Hydro seminar on Fluid Bed Technology, Sluiskil in the Netherlands, October 27-28, 1999

22. Bolland O., "Semi-industriell prosess for granulering og belegging (Semi-industrial sized process for granulation and coating)", Presentation at the NTNU Dewatering Laboratorium Seminar, October 13-14, 1999

23. Bolland, O., "CO2 - fjerning og lagring" (CO2 - removal and storage), Invited lecture at the seminar "Et energieffektivt Norge" (Norway - energy efficient), Trondheim, April 1999

24. Bolland O., "Agglomeration & Drying Granulation in fluidized Bed", Presentation at the opening of the NTNUSINTEF Dewatering Laboratorium, September 1998

25. Bolland O., "Natural Gas Power Generation", 3-hour lecture at the Norsk Hydro Seminar on Hydrokraft, Gas Power and Hydrogen as Energy Carrier, Oslo, June 1998

26. Bolland, O., "Gasskraftverk - teknologisk status og utviklingstrender (Gas Fired Power Plants - Technology state-of-the-art and trends, Lecture for NFTS - the Norwegian Society for Turbomachinery, Trondheim, Norway, October 30, 1997

27. Bolland, O., "CO2 und der Treibhauseffekt - ein Blick aus Norwegen (CO2 and the greenhouse effect - a view from Norway), Colloquium at the Swiss Federal Institute of Technology, Zürich, Switzerland, April 24, 1997

28. Bolland, O., " Teknologisk status for gassturbiner og kombinerte gass/dampturbin-prosesser (State-of-the-art gas turbines and combined cycles)", invited speaker at the Bergen Gas Conference, Bergen, Norway, 1996

29. Bolland, O. and Pettersen, J., "Improved Cycles for Natural Gas Power Generation", presented at the IEA International Conference on Natural Gas Technologies: Energy Security, Environment and Economic Development, October 31 - November 3, Kyoto, Japan, published in conference proceedings pp. 121-130, 1993.

Page 20: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Patent Rønning S.O., Bjerve Y., Falk-Pedersen O., Glittum G., and Bolland O., "A method for removing and preventing emissions into the atmosphere of carbon dioxide (CO2) from exhaust gas of gases from heat engines", WO 95/21683, PCT/NO95/00033, 1995, Registered patent in Norway #940527 "Fremgangsmåte til fjerning av karbondioksid fra forbrenningsgasser", 1994, US-patent 5,832,712 - 1998 Fields of interests and present research activities • Gas turbines and gas turbine power plants – design and operation Design of gas turbine power cycles using tools like the in-house code GTSIM, GTPRO/GTMASTER (Thermoflow, Inc.) and PRO/II (Simsci, Inc.). Research work includes Rankine bottoming cycles with alternative working fluids (other than steam/air) and so-called Air Bottoming Cycle. Operation of gas turbines: Working with a reliability and availability study in cooperation with Statoil and Norsk Hydro. The goal is to develop a prediction tool, which takes into account the connection between the external parameters (environmental conditions, fuel quality and mode of operation) and their influence on degradation of the gas turbine. • Power generation with CO2 capture Research work includes a large range of power cycle modelling and simulations, with pre- and post-combustion methods as well as oxy-fuel combustion cycles. The methodologies are both theoretical and experimental. The theoretical work includes cycle design with a several state-of-the-art software tools, transient modelling and simulation using the tool gPROMS (PSE, Ltd.), methodology related to generalisation of efficiency penalty in CO2 capture, and exergy analysis for pre-combustion methods.. The experimental work is within so-called “Chemical Looping Combustion”, where the kinetics of oxidation and reduction of Ni/NiO is studied in two experimental set-ups. • Solid oxide fuel cells – modelling and simulation Research work includes cycle modelling and simulation as well as 2-D modelling of both planar and tubular SOFCs. The work is on both steady state where an in-house code for the 2-D analysis has been developed and coupled with the flowchart simulator PRO/II, and on transient modelling and simulation using the tool gPROMS (PSE, Ltd.), • Particle technology Research work includes gas-solid mass transfer, agglomeration and oxidation and reduction processes in fluidised systems. I was the project manager in a 5-year experimental program in the department’s laboratory on magnesium chloride granulation, in cooperation with Norsk Hydro.

Page 21: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 1 of 10

Curriculum Vitae for Truls Gundersen

Date of print: 25 May, 2004

1. CIVIL DATA ∗ Born: 4 October 1952, Nes, Akershus, Norway ∗ Home: Olaf Bulls vei 50, N-7024 Trondheim, Norway Phone: + 47-72-560070 (house) or + 47-916-81726 (mobile) ∗ Office: Department of Energy and Process Engineering, NTNU, Kolbjoern Hejes vei 1.A, N-7491 Trondheim, Norway Phone: + 47-73-593721 (office) or + 47-916-817-26 (cellular) Fax: + 47-73-598390 E-mail: [email protected] 2. EDUCATION AND ACADEMIC EXPERIENCE • 1971 - 1977 Norwegian Institute of Technology (NTH), Trondheim, M.Sc in Physics.

Thesis: "Simulation of a Hydrogenation Plant" (in Norwegian).

• 1978 - 1982 Norwegian Institute of Technology (NTH), Trondheim, Ph.D in Chemical Engineering. Thesis: "Decomposition of Large Scale Chemical Engineering Systems".

• 1978 - 1981 Lecturer in Process Control and Teaching Assistant in Process Dynamics and Process Simulation, Chem. Engng. Dept., NTH.

• 1983 - 1986 Lecturer in Process Simulation and Synthesis, Chemical Engineering Department, NTH, Trondheim.

• 1986 - 1996 Professor (II) of Chemical Engineering with lecturing and supervision of M.Sc and Ph.D students, NTH, Trondheim.

• 1987 - 1988 Sabbatical Year at Carnegie Mellon University in Pittsburgh, working on Process Synthesis and Mathematical Programming with Professors I.E. Grossmann, L.T. Biegler and A.W. Westerberg.

• 1989 - 1996 Lecturing a new Senior Year Course in Process Synthesis, Chemical Engineering Department, NTH, Trondheim.

• 1992 - 1993 Guest Lectures (24 hours) on Heat Exchanger Network Design and Optimization, Telemark Institute of Technology, Porsgrunn.

Page 22: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 2 of 10 • 1993 - 1996 Professor in the Department of Process Technology, Telemark Institute

of Technology, Porsgrunn, Norway.

• 1997 - 2002 Professor (II) in the Department of Process Technology, Telemark Institute of Technology, Porsgrunn, Norway.

• 1996 - now Professor in the Department of Energy and Process Engineering, Norwegian University of Science and Technology, Trondheim, Norway.

3. INDUSTRIAL AND OTHER WORK EXPERIENCE • 1977 7 weeks with SINTEF (Society for Industrial and Technological Research),

Department of Technical Chemistry, Computer-Aided Process Design and Simulation, Trondheim, Norway.

• 1977 4 months with the Defense Research Centre (FFI), Department of Weapons and

Materials, Kjeller, Norway, as part of the compulsory national military service. • 1981 - 1993 Norsk Hydro a.s, Research Centre, Chemical Engineering Department,

Porsgrunn, Norway. Research and Applications in the area of Process Simulation and from 1984 in the area of Process Synthesis with special emphasis on the Efficient Use of Energy in new as well as existing plants in a company that is involved in Chemicals, Fertilizers, Light Metals, Petrochemicals, Oil and Gas and Pharmaceuticals.

• 1991 20 weeks with Kaiser Aluminum and Chemical Company, Gramercy,

Louisiana, USA. "On the plant training" for Norsk Hydro a.s in a Bayer process for aluminum oxide operated by Kaiser. Focus on overall Process Design and Energy Consumption.

• 1996 - now Scientific advisor for Sintef Energy Research, Department of Thermal

Engineering, Trondheim, Norway. 4. VARIOUS APPOINTMENTS, AWARDS, Etc. • Awarded a Fulbright Fellowship in Natural Science for a Postgraduate Stay at Carnegie Mellon

University in Pittsburgh, USA, from 1987 to 1988. • Awarded a Research Fellowship from the Royal Norwegian Council for Scientific and Industrial

Research to pursue Advanced Studies in the USA from 1987 to 1988. • Elected Chairman of the Process Integration Research Consortium at University of Manchester

Institute of Science and Technology (UMIST), supporting the research in Professor Bodo Linnhoff's group, for the two year period 1990 - 1992.

• Elected member of the Norwegian Academy of Science and Technology (NTVA) in May 1991,

based on contributions in the area of Process Design in general and Heat Exchanger Network Synthesis in particular.

• Appointed Referee for the following international journals: 1. Computers and Chemical

Engineering (from 1987) 2. Industrial and Engineering Chemistry, Research and Design (from 1989) 3. Modeling, Identification and Control (from 1989) 4. Chemical Engineering Science (from 1991) 5. American Institute of Chemical Engineers Journal (from 1996) 6. Chemical Engineering Research and Design, Part A: Trans. of the Institution of Chemical Engineers

Page 23: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 3 of 10

(from 1997), 7. Canadian Journal of Chemical Engineering (from 2001), 8. Chemical and Engineering Technology (from 2001) and Applied Thermal Engineering (from 2003), 9. Kirk-Othmer Encyclopedia of Chemical Technology (from 2004).

• Appointed Operating Agent for Annex I of the IEA Implementing Agreement on Process

Integration for the period September 1995 to September 1997 and the Extension from September 1997 to October 1998. Then again Operating Agent for the continuation of Annex I as a small Secretariat on an annual basis from October 1998 to March 2002. This should be viewed on the background that Norway does not participate in this Agreement.

• Appointed Nordic Research Professor in the Process Integration Scientific Programme within

the Nordic Energy Research Programme for the period 1 December 2001 to 31 December 2002. • Given the Best Lecturer Award by the students in the Energy and Environment Study Program

at the Norwegian University of Science and Technology, May 2004. 5. JOURNAL PUBLICATIONS (see section 7 for more publications) J1 Gundersen T. "Numerical Aspects of the Implementation of Cubic Equations of State in Flash

Calculation Routines", Comput. and Chem. Engng., vol. 6, no. 3, pp. 245-255, 1982. J2 Gundersen T. and Hertzberg T. "Partitioning and Tearing of Networks - Applied to Process

Flowsheeting", Modeling, Identification and Control, vol. 4, no. 3, pp. 139-165, 1983. J3 Skogestad S., Gundersen T. and Johnsen O. "Compositional Simulation of a Refinery Coker

Furnace - An Industrial Example of Two-Phase Flow with Chemical Reaction", Modeling, Identification and Control, vol. 7, no. 1, pp. 24-44, 1986.

J4 Gundersen T. and Naess L. "The Synthesis of Cost Optimal Heat Exchanger Networks - An

Industrial Review of the State of the Art", Comput. and Chem. Engng., vol. 12, no. 6, pp. 503-530, 1988.

J5 Gundersen T. and Naess L. "The Synthesis of Cost Optimal Heat Exchanger Networks - An

Industrial Review of the State of the Art", Heat Recovery Systems and CHP, vol. 10, no. 4, pp. 301-328, 1990.

J6 Gundersen T. and Grossmann I.E. "Improved Optimization Strategies for Automated Heat

Exchanger Networks through Physical Insights", Comput. and Chem. Engng., vol. 14, no. 9, pp. 925-944, 1990.

J7 Gundersen T. "Process Integration Methods, Software and Applications - Towards a State-of-

the-Art Survey" (in Polish), Fuel and Energy Management (Gospodarka Paliwari i Energia), Special Issue on Process Integration, no. 9, pp. 2-8, 1997.

J8 Glemmestad B., Skogestad B. and Gundersen T. "Optimal Operation of Heat Exchanger

Networks", Comput. and Chem. Engng., vol. 23, pp. 509-522, 1999. 6. INVITED PRESENTATIONS AT INTERNATIONAL MEETINGS I-1 AspenWorld'88, Amsterdam, The Netherlands, 13-16 November 1988: "The Practice and

Benefits of Pinch Technology in Norsk Hydro". I-2 FOCAPD-89 (Foundations of Computer Aided Process Design), Snowmass, Colorado, USA, 9-

14 July 1989: "Retrofit Process Design - Research and Application of Systematic Methods".

Page 24: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 4 of 10 I-3 IMP-90 (25th Anniversary of Instituto Mexicano del Petroleo), Conference on Conservation

and Efficient Use of Energy, Mexico City, 25 May 1990: "Industrial Applications of Heat Recovery Techniques".

I-4 SPE-90 (Society of Petroleum Engineers), Seminar on Enhancing Safety and Environmental

Standards in Offshore Operations, Grindelwald, Switzerland, 9-14 September 1990: "Use of Systematic Methods for Energy Optimization".

I-5 PSE-91 (International Conference on Process Systems Engineering), Montebello, Canada, 5-9 August 1991: "Achievements and Future Challenges in Industrial Design Applications of

Process Systems Engineering". I-6 AspenWorld'91, Cambridge, Massachusetts, USA, 4-6 November 1991: "Achievements and

Future Challenges in Industrial Design Applications of Process Systems Engineering". I-7 IEA-92, Workshop on Process Integration organized by the International Energy Agency,

Gothenburgh, Sweden, 28-29 January 1992: "Implementation Problems and Organizational Aspects".

I-8 IEA-93, Workshop on Process Integration organized by the International Energy Agency,

Berlin, Germany, 4-5 October 1993: "Definition of Process Integration in an IEA Context". I-9 FOCAPD-94 (Foundations of Computer Aided Process Design), Snowmass, Colorado, USA,

10-15 July 1994: "Commentator for the Poster Session on Design and Synthesis". I-10 Nordic PI-95 (Nordic Annual Meeting on Process Integration), Copenhagen, Denmark, 8

November 1995: "Classification and Evaluation of Process Integration Methods". I-11 UNWS-96 (UN Workshop on Process Integration), Manchester, UK, 11 June 1996: "IEA

Implementing Agreement on Process Integration - Survey of Process Integration Methods, Software, Applications and End-User Needs".

I-12 IMP-97 (3rd Forum of Advances in the Refinery Industry), Mexico City, 25-26 September,

1997: "State-of-the-Art in Process Integration Methods, Software and Industrial Applications". I-13 AspenWorld'97, Boston, USA, 12-16 October 1997: "Recent Trends and Hot Topics in

Process Integration Methods, Software and Applications". I-14 Nordic PI-97 (Nordic Annual Meeting on Process Integration), Copenhagen, Denmark, 27

November 1997: "Topology Traps in Evolutionary and Simultaneous Strategies for Heat Exchanger Network Synthesis".

I-15 CHISA' 98, Prague, Czech Republic, 24-28 August 1998 (Keynote): "Recent Trends in

Process Integration Methods, Software and Applications". I-16 PI' 99, Copenhagen, Denmark, 7-10 March 1999: "From Gothenburg'92 to Copenhagen'99 -

Major Trends and Developments in Process Integration". I-17 Mexico-01, Mexico City, 22 October 2001 (International Seminar on Process Integration for

Environmental Protection): “An Introduction to the Methods and Industrial Benefits of Process Integration”.

I-18 Durban-02, Durban, South Africa, 18-20 November 2002 (International Seminar on Advanced

Achievements in Pinch Technology, keynote): “From University Pinch through Industrial Savings to Environmental Improvements”.

Page 25: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 5 of 10 7. OTHER PUBLICATIONS (many with normal international referee procedures) P1 Gundersen T. "Decomposition of Large Scale Chemical Engineering Systems", Dr.Ing Thesis,

Chemical Engineering Department, The Norwegian Institute of Technology, Trondheim, Norway, April 1982.

P2 Gundersen T. and Hertzberg T. "Partitioning and Tearing Chemical Process Flowsheets",

Proceedings from PSE-82 (International Conference on Process Systems Engineering), volume from Technical Sessions, pp 9-21, Kyoto, Japan, August 1982.

P3 Hertzberg T. and Gundersen T. "Process Flowsheeting; Part 1: Algorithms for solving

Flowsheeting Problems, and Part 2: Partitioning and Tearing in Flowsheeting Calculations", in R. von Schalien, Proceedings from the Symposium Use of Modeling and Simulation in Energy Research, Aabo Academy, Dept. of Chem. Engng., Finland, December 1983.

P4 Gundersen T. and Naess L. "The Synthesis of Cost Optimal Heat Exchanger Networks - An

Industrial Review of the State of the Art", Proceedings from CEF-87 (The Use of Computers in Chemical Engineering), pp 675-704, Giardini Naxos, Sicily, Italy, April 1987.

P5 Gundersen T. and Grossmann I.E. "Improved Optimization Strategies for Automated Heat

Exchanger Networks through Physical Insights", AIChE Annual Meeting, Washington D.C., November 1988.

P6 Gundersen T. "Retrofit Process Design - Research and Application of Systematic Methods", in

J.J. Siirola, I.E. Grossmann and G. Stephanopoulos, Proceedings from Foundations of Computer Aided Process Design (FOCAPD-89, Snowmass, Colorado, July 1989), CACHE Elsevier, pp 213-240, 1990.

P7 Sagli B., Gundersen T. and Yee T.F. "Topology Traps in Evolutionary Strategies for Heat

Exchanger Network Synthesis", in H.T. Bussemaker and P.D. Idema, Proceedings from Computer Applications in Chemical Engineering (ComChem'90, The Hague), Elsevier, pp 51-58, 1990.

P8 Gundersen T. "Achievements and Future Challenges in Industrial Applications of Process

Systems Engineering", Proceedings from the International Symposium on Process Systems Engineering (PSE-91, Montebello, Canada), vol. I - Design, pp I.1.1-I.1.32, August 1991.

P9 Gundersen T., Sagli B. and Kiste K. "Problems in Sequential and Simultaneous Strategies for

Heat Exchanger Network Synthesis", in L. Puigjaner and A. Espuna, Proceedings from Computer-Oriented Process Engineering (COPE'91, Barcelona, Spain, October 1991), Elsevier, pp 105-116, 1991.

P10 Mathisen K.W., Skogestad S. and Gundersen T. "Optimal Bypass Placement in Heat Exchanger

Networks", Paper 67e, Session on Plant-wide Control, AIChE Spring Meeting, New Orleans, April 1992.

P11 Gundersen T., Duvold S. and Hashemi-Ahmady A. "An Extended Vertical MILP Model for

Heat Exchanger Network Synthesis", Comput. and Chem. Engng., vol. 20, Suppl. (Proc. from the European Symposium of Computer-Aided Process Engineering, ESCAPE-6, Rhodes, May 1996), pp S97-S102, 1996.

P12 Glemmestad B., Mathisen K.W. and Gundersen T. "Optimal Operation of Heat Exchanger

Networks based on Structural Information", Comput. and Chem. Engng., vol. 20, Suppl. (Proc. from the European Symposium of Computer-Aided Process Engineering, ESCAPE-6, Rhodes, May 1996), pp S823-S828, 1996.

Page 26: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 6 of 10 P13 Gundersen T., Trædal P. and Hashemi-Ahmady A. "Improved Sequential Strategy for the

Synthesis of Near-Optimal Heat Exchanger Networks", Comput. and Chem. Engng., vol. 21, Suppl. (Proc. from the joint PSE-97/ESCAPE-7, Trondheim, May 1997), pp S59-S64, 1997.

P14 Glemmestad B., Skogestad S. and Gundersen T. "On-line Optimization and choice of

Optimization Variables for Control of Heat Exchanger Networks", Comput. and Chem. Engng., vol. 21, Suppl. (Proc. from the joint PSE-97/ESCAPE-7, Trondheim, May 1997), pp S379-S384, 1997.

P15 Glemmestad B. and Gundersen T. "A Systematic Procedure for Optimal Operation of Heat

Exchanger Networks", Proceedings from FOCAPO'98 (Third International Conference on Foundations of Computer-Aided Process Operations, Snowbird, Utah, 5-10 July, 1998), AIChE Symp. Series, vol. 94, no. 320, pp. 451-457, 1998.

P16 Hashemi-Ahmady A., Zamora J.M. and Gundersen T. "A Sequential Framework for Optimal

Synthesis of Industrial Size Heat Exchanger Networks", AIChE Annual Meeting, Session 218 (Poster), Miami Beach, November 1998.

P17 Gundersen T. "From Gothenburg'92 to Copenhagen'99 - Major Trends and Developments in

Process Integration", Proceedings from PI'99 (International Conference on Process Integration, Copenhagen, Denmark, 7-10 March, 1999), vol. 1, pp. 7-24, 1999.

P18 Hashemi-Ahmady A., Zamora J.M. and Gundersen T. "A Sequential Framework for Optimal

Synthesis of Industrial Size Heat Exchanger Networks", Proc. from PRES'99, Budapest, Hungary, 31 May - 2 June, pp. 329-334, 1999.

8. NON - INVITED INTERNATIONAL PRESENTATIONS

NI-1 PSE-82 (International Conference on Process Systems Engineering), Kyoto, Japan, August 1982: "Partitioning and Tearing Chemical Process Flowsheets".

NI-2 PIRC-84 (Annual Meeting of the Process Integration Research Consortium), London, October

1984: "SUPERTARGET - Prototype Software for Heat Exchanger Network Design". NI-3 PIRC-86 (Annual Meeting of the Process Integration Research Consortium), Manchester,

October 1986: "On the Use of ∆Tmin Contributions in Retrofit Projects - Experience from an Energy Study of an Ammonia Plant".

NI-4 CEF-87 (European Conference on the Use of Computers in Chemical Engineering), Giardini

Naxos, Sicily, Italy, April 1987: "Synthesis of Cost Optimal Heat Exchanger Networks - An Industrial Review of the State of the Art".

NI-5 PIRC-88 (Annual Meeting of the Process Integration Research Consortium), Manchester,

October 1988: "Is the Use of a Global ∆Tmin in HENS another Topology Trap ? ". NI-6 AIChE-88 (Annual Meeting of the AIChE), Washington D.C., December 1988: "Improved

Optimization Strategies for Automated Heat Exchanger Network Synthesis through Physical Insights".

NI-7 NTH-90 (Seminar on Mathematical Programming: Modern Optimization Techniques in

Process Design and Control), Norwegian Institute of Technology, Trondheim, Norway, May 1990: "The Advantage of Simultaneous Strategies in the Design of Heat Exchanger Networks".

Page 27: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 7 of 10

NI-8 COPE-91 (European Conference on Computer-Oriented Process Engineering), Barcelona, Spain, October 1991: "Problems in Sequential and Simultaneous Strategies for Heat Exchanger Network Synthesis".

NI-9 NTH-92 (Short Course on Process Design Tools and Techniques), The Norwegian Institute of

Technology, Trondheim, May 1992: "Advanced Techniques in Synthesis of Heat Exchanger Networks".

NI-10 ESCAPE-6 (European Symposium on Computer-Aided Process Engineering), Rhodes, Greece,

May 1996: "The Extended Vertical MILP Model for Heat Exchanger Network Synthesis". NI-11 PSE-97/ESCAPE-7 (Joint Process Systems Engineering and European Symposium on

Computer-Aided Process Engineering), Trondheim, Norway, May 1997: "Improved Sequential Strategy for the Synthesis of Near-Optimal Heat Exchanger Networks".

NI-12 AspenWorld'97, Boston, USA, 16 October 1997: "An IEA Initiative on Process Integration". NI-13 PRES'99, Budapest, Hungary, 1 June 1999: "A Sequential Framework for Optimal Synthesis of

Industrial Size Heat Exchanger Networks". 9. INTERNATIONAL SEMINARS S1 Carnegie Mellon University (CMU), Pittsburgh, USA, October 1987: "The Synthesis of Cost

Optimal Heat Exchanger Networks - An Industrial Review". S2 Carnegie Mellon University (CMU), Pittsburgh, USA, November 1987: "Flexibility of Heat

Exchanger Networks". S3 University of Maryland, College Park, USA, December 1987: "A Systems Approach to Process

Design". S4 Aspen Technology Inc., Boston, USA, March 1988: "A Review of Developments in Heat

Exchanger Network Synthesis". S5 Massachusetts Institute of Technology (MIT), Boston, USA, March 1988: "Automatic

Generation of Heat Exchanger Networks". S6 University of Pennsylvania, Philadelphia, USA, April 1988: "Automatic Synthesis of Heat

Exchanger Networks". S7 Centre for Process Systems Engineering (Autumn Seminar Series), Imperial College of Science,

Technology and Medicine, London, November 1992: "Process Structure - The Key to Low Cost and Good Operation".

S8 Department of Chemical Engineering, Denmark Technical University (DTU), June 1995: "Use

of Mathematical Programming in Heat Exchanger Network Synthesis and the Extended Vertical MILP Model".

10. PH.D (OR DR.ING / DR.TECHN) COMMITTEES • Tulio R. Colmenares "Design of Heat and Power Recovery Systems for Energy Conservation in

Chemical Plants", Ph.D, Chem. Engng. Dept., University of Pennsylvania, Philadelphia, USA, April 1988.

Page 28: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 8 of 10 • Stephen G. Hall "Targeting for Multiple Utilities", Ph.D, Chem. Engng. Dept., University of

Manchester, Institute of Science and Technology (UMIST), Manchester, UK, Dec. 1989. • Terrence F. Yee "Simultaneous Optimization Models for Heat Integration Systems", Ph.D,

Chem. Engng. Dept., Carnegie Mellon University (CMU), Pittsburgh, USA, March 1990. • Per E. Wahl "Synthesis of Heat Integrated Distillation Sequences: Approaches Combining

Knowledge Based and Operations Research Techniques", Dr.Ing, Chem. Engng. Dept., The Norwegian Institute of Technology, Trondheim, Norway, June 1991.

• C.W. ("David") Hui "Process Integration between Areas of Integrity", Ph.D, Chem. Engng.

Dept., University of Manchester, Institute of Science and Technology (UMIST), Manchester, UK, October 1991.

• Ingrid S. Melaaen "Probabilistic Modeling on the Influence of Inaccuracies in Thermo-dynamic

Properties on Process Plant Design", Dr.Ing, Dept. of Refrigeration Engng., The Norwegian Institute of Technology, Trondheim, Norway, November 1993.

• Tore Omtveit "Studies on Conceptual Design of Chemical Reactor Systems", Dr.Ing, Chem.

Engng. Dept., The Norwegian Institute of Technology, Trondheim, Norway, March 1994. • Knut W. Mathisen "Integrated Design and Control of Heat Exchanger Networks", Dr.Ing,

Chem. Engng. Dept., The Norwegian Inst. of Technology, Trondheim, Norway, April 1994. • Torbjørn Pettersen "Design of Membrane based Separation Processes", Dr.Ing, Chem. Engng.

Dept., The Norwegian Inst. of Technology, Trondheim, Norway, November 1994. • Jan Sandvig Nielsen "Energy Optimization of Integrated Process Plants", Ph.D., Chem. Engng.

Dept., The Danish Technical University, Copenhagen, Denmark, June 1995. • Nii D.K. Asante "Automated and Interactive Retrofit Design of Practical Heat Exchanger

Networks", Ph.D., Dept. of Process Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, April 1996.

• Erik Wallin "Process Integration of Industrial Heat Pumps in Grassroot and Retrofit

Situations", Ph.D., Dept. of Heat and Power Technology, Chalmers University of Technology, Gothenburg, Sweden, May 1996.

• Victor M. Briones Vallejo "An Integrated Framework for the Design of Heat Exchanger

Networks", Ph.D., Dept. of Process Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, December 1996.

• Xiurong ("William") Nie "Optimization Strategies for Heat Exchanger Network Design

considering Pressure Drop Aspects", Ph.D., Dept. of Process Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, May 1998.

• Erik Sauar "Energy Efficient Process Design by Equipartition of Forces - With Applications

to Distillation and Chemical Reaction", Dr. Techn., Dept. of Physical Chemistry, Norwegian University of Science and Technology, Trondheim, Norway, November 1998.

• Steinar Hauan "On the Behaviour of Reactive Distillation Systems", Dr. Ing., Department of

Chemical Engineering, Norwegian University of Science and Technology, Trondheim, Norway, January 1999.

• Jens B. Mikkelsen "Thermal Energy Storage Systems in Batch Processing", Ph.D., Dept. of

Energy Engineering, Technical University of Denmark, Copenhagen, Denmark, January 1999.

Page 29: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 9 of 10 • Joao Jorge da Silva Ferreira Alves "Analysis and Design of Refinery Hydrogen Distribution

Systems", Ph.D., Dept. of Process Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, September 1999.

• Bunyaphat Suphanit "Design of Complex Distillation Systems", Ph.D., Dept. of Process

Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, November 1999.

• Dorrie Wan Tze Chow "Design and Optimization of Wastewater Treatment Networks",

M.Phil., Dept. of Process Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, September 2000.

• Lalita Tantimuratha "Automated Design of Flexible and Operable Heat Exchanger Networks",

Ph.D., Dept. of Process Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, January 2001.

• Ivar Halvorsen "Minimum Energy Requirements in Complex Distillation Arrangements", Dr.

Ing., Department of Chemical Engineering, Norwegian University of Science and Technology, Trondheim, Norway, May 2001.

• Pierre Krummenacher “Contribution to the Heat Integration of Batch Processes (with or

without Heat Storage)”, Ph.D., Department of Mechanical Engineering, École Polytechnique Fédérale de Lausanne, Switzerland, November 2001.

• Lieke Wang “Performance Analysis and Optimal Design of Heat Exchangers and Heat

Exchanger Networks”, Ph.D., Department of Heat and Power Engineering, Lund Institute of Technology, Sweden, December 2001.

• Henrik Dalsgård “Simplification of Process Integration in Medium Size Industry”, Ph.D.,

Department of Mechanical Engineering, Denmark Technical University, Copenhagen, Denmark, September 2002.

• Fang Liu “Hydrogen Integration in Oil Refineries”, Ph.D., Dept. of Process Integration,

University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, October 2002.

• Hilde Kathrine Engelien "Process Integration applied to the Design and Operation of

Distillation Columns", Dr. Ing., Department of Chemical Engineering, Norwegian University of Science and Technology, Trondheim, Norway, March 2004.

• Jiaona Wang "Synthesis and Optimization of Low Temperature Gas Separation Processes”,

Ph.D., Dept. of Process Integration, University of Manchester Institute of Science and Technology (UMIST), Manchester, UK, June 2004.

• Jon Agust Thorsteinsson "Modeling of Fishing Vessel Operation for Energy System

Optimization”, Department of Energy Technology, Aalborg University, Aalborg, Denmark, June 2004.

11. SUPERVISION OF PH.D. OR DR. ING. STUDENTS • Bjørn Glemmestad "Optimal Operation of Integrated Process - Studies on Heat Recovery

Systems", Telemark Institute of Technology, Porsgrunn, Norway, 1994-1997. Finished on 12 December, 1997.

Page 30: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV for Truls Gundersen Page 10 of 10 • Abdolreza Hashemi-Ahmady "Use of Modern Optimization Techniques in Process Inte-

gration", Telemark Institute of Technology, Porsgrunn, Norway, 1994-1998. Did not finish. • Tom Ole Øvrum "Process Integration in Energy and Water Management Systems - Mass

Transfer Processes and Wastewater Minimization", Telemark Institute of Technology, Porsgrunn, Norway, 1995-1998. Did not finish.

• Arne Lind "Analysis and Design of Hydrogen Distribution Networks in Oil Refineries",

Department of Energy and Process Engineering, Norwegian University of Science and Technology, Trondheim, Norway, 1999-2003. Finished on 15 March, 2004.

• Syed Own Abbas "Top-Level Analysis for Utility Systems in Natural Gas based Industrial

Plants", Department of Energy and Process Engineering, Norwegian University of Science and Technology, Trondheim, Norway, 2003-2006.

• Rahul Anantharaman "Process Synthesis – Solving Industrial Problems with Mathematical

Programming and Insights", Department of Energy and Process Engineering, Norwegian University of Science and Technology, Trondheim, Norway, 2003-2006.

• Kristin Herder Kaggerud "Process Synthesis with Emphasis on Energy and Chemicals

Integration", Department of Energy and Process Engineering, Norwegian University of Science and Technology, Trondheim, Norway, 2003-2006.

• Jelena Malenovic "Next Generation LNG Heat Exchangers", Department of Energy and

Process Engineering, Norwegian University of Science and Technology, Trondheim, Norway, 2003-2006.

Trondheim, 25 May, 2004 Truls Gundersen

Page 31: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Curriculum vitae Name: Hallvard Fjøsne Svendsen Present pos.: Professor of Chemical Engineering, Norwegian University of Science

and Technology. Born: March 7th, 1948 Status: Married (1971), two children (1973,1975) Address: Frydenbergvn. 20 D, 7035 Trondheim, Norway Education: Sivilingeniør (M.Sc.) Dept. of Chem.Eng., NTH 1971 Dr.Ing. (Ph.D) Dept. of Chem.Eng., NTH 1976 Pedagogisk Utdanning for Sivilingeniører (PUFS), 1976 Employment: 72 - 73: University of Trondheim, Norwegian Institute of Technology(NTH), Research assistant, Department of Inorganic Chemistry. 73 - 76: University of Trondheim, Norwegian Institute of Technology(NTH), Dr.Ing. (PhD) studies, Department of Chemical Engineering. 76 - 78: University of Dar es Salaam, Tanzania. Lecturer in Chemical Engineering, Chemistry Department,(NORAD contract) 78 - 84: SINTEF, Division of Applied Chemistry, Research Scientist. 84 - 94: University of Trondheim, Norwegian Institute of Technology (NTH), Department of Chemical Engineering, Associate Professor 94 - Norwegian University of Science and Technology, Department of Chemical Engineering, Professor On sabbatical leave as academic visitor: 83 - 84 University of Nevada, Reno, Chemical and Metallurgical Engineering Department, Visiting Professor 92 - 93 Institut National Polytechnique de Toulouse, Ecole Nationale Superieure d'Ingenieurs de Genie Chimique, Visiting Professor

Page 32: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Publications: /J1/ Anundskås, A., Grjotheim, K., Schultz, A., Svendsen, H., and Øye, H.A. Benetzungseigenschaften in Systemen von Interesse für die Magnesium- Elektrolyse (Teil III). Metall 29, (1975) 493 /J2/ Svendsen, H.F. and Thorsen, G.

Mine water treatment by solvent extraction with carboxylic acids Proceedings from the Oslo Symposium, Univ. of Oslo, June 1982 /J3/ Thorsen, G., Svendsen, H.F., and Grislingås, A.

The integrated organic leaching-solvent extraction operation in hydro-metallurgy. In Hydrometallurgical Process Fundamentals, Plenum Press 1984, Ed R.G. Bautista

/J4/ Jeffreson C., Svendsen H.F. Selection of Sampling Frequency for Digital Process Control Systems Ind.Eng.Chem.Fund. 25,(1986),771-775 /J5/ Svendsen H.F., Schei G., Osman M. Kinetics of Extraction of Zinc by Di(2-Ethyl-Hexyl)Phosphoric Acid in Cumene Hydrometallurgy 25,(1990),197-212 /J6/ Torvik R., Svendsen H.F., Modelling of Slurry Reactors. A Fundamental Approach. Chem. Eng. Sci. 45(8),(1990),2325 /J7/ Luo H., Svendsen H.F. Turbulent Circulation in Bubble Columns from Eddy Viscosity Distribution of Single Phase Pipe Flow. Can. J. Chem. Eng. 69,(1991),1389-94 /J8/ Svendsen H.F., Jakobsen H.A., Torvik R. Local Flow Structures in Internal Loop and Bubble Column Reactors Chem. Eng. Sci. 47,(1992),3297-3304 /J9/ Jakobsen H.A., Svendsen H.F., and Hjarbo K.W. On the Prediction of Local Flow Structures in Internal Loop and Bubble Column Reactors using a Two-fluid Model. Computers & Chem. Eng. 17S,(1993),S531-36 /J10/ Svendsen H.F., Luo H., Hjarbo K. Non-uniform Distribution Model for Determining Bubble Sizes and Interfacial Area in Bubble Columns Using Dynamic Gas Disengagement. EUROGAS conference ,Trondheim, March 1994

Page 33: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

/J11/ Essadi H., Delmas H., Svendsen H.F. Friction on a Solid Sphere Exposed to Gas-Liquid and Gas-Liquid-Solid Flow in Bubble Column and Fluidized Bed Reactors J. Chem. Tech. Biotechnol. 62, (1995), 301-309 /J12/ Øyaas J., Storrø I., Lysberg M., Svendsen H.F., Levine D. Determination of Effective Diffusion Coefficients and Distribution Constants in Polysaccharide Gels with Non-steady-State Measurements. Biotechnology and Bioengineering, 47, (1995), 501-507 /J13/ Øyaas J., Storrø I., Svendsen H.F., Levine D. The Effective Diffusion Coefficient and Distribution Constant for Small Molecules in Calcium Alginate Gel Beads. Biotechnology and Bioengineering, 47, (1995), 492-500. /J14/ Syaiful S., Wilhelm A.M., Svendsen H.F., Delmas H. Upward Cocurrent Gas-Liquid-(Solid) Contactors: Holdup,Axial dispersion Gas-Liquid Mass Transfer. Trans. IChemE, 73A,(1995),pp643-648 /J15/ Luo, Hean, and Svendsen, H.F.,

Simulation of liquid circulation in bubble columns J. of Chem. Ind. & Engn. (China),vol. 46(4), 1995, 458

/J16/ Sannæs B.H., Dudukovic, M.P., Svendsen H.F.

Experimental and Numerical Investigation of Solids Dynamics in Slurry Bubble Columns. Fluidization & Fluid Particle Systems Prepr., pp 159-163 AIChE Ann. Meet., Florida Nov. 1995

/J17/ Svendsen H.F., Luo H. Modeling of Approach Processes for Equal or Unequal Sized Fluid Particles Can. J. Chem Eng. 74(3),(1996), 321-330 /J18/ Luo H., Svendsen H.F. A Theoretical Model for Drop or Bubble Breakup in Turbulent Dispersions AIChE J, 42,(5),(1996),1225-1233

/J19/ Grevskott S., Sannæs B.H, Dudukovic M., Hjarbo K.H., Svendsen H.F. Liquid circulation, bubble size distribution and solids movement in two- and three-phase bubble columns. Chem. Eng. Sci. 51,(1996),pp 1703 - 1713

/J20/ Luo H. And Svendsen H. F. Modelling and Simulation of Binary Approach by Energy Conservation Analysis. Chem. Eng. Comm., 145, (1996),pp 145-153

Page 34: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

/J21/ Jakobsen H.A., Sannæs B.H., Grevskott S., Svendsen H.F. Modeling of Vertical Bubble-Driven Flows. Ind. Eng. Chem. Res., 39(10),1997,pp 4052-4074 /J22/ Svendsen H.F., Luo H., Hjarbo K.W., Jakobsen H.A. Experimental Determination and Modeling of Bubble Size Distributions in Bubble Columns. Chin. J. of Chem. Eng., 6(1),1998,pp 29-41 /J23/ Tayebi D., Svendsen H.F., Grislingås A., Mejdell T, Johannessen K.

Dynamics of fluidized-bed reactors: Development and application of a new multi-fiber optical probe.

Chem. Eng. Sci. 54(13-14),1999,pp2113-2122 /J24/ Kvamsdal H., Svendsen H.F., Hertzberg T., Olsvik O. Dynamic simulation and optimization of a catalytic steam reformer Chem. Eng. Sci. 54(13-14),1999,pp2697-2706 /J25/ Mejdell T., Pettersen T., Naustdal C., Svendsen H.F. Modelling of Industrial S-PVC Reactor. Chem. Eng. Sci. 54,(13-14),1999,2459-2466 /J26/ Hagesæther L., Jakobsen H.A., Svendsen H.F. Theoretical analysis of fluid particle collisions in turbulent flow.

Chem Eng Sci..54, 1999, 4749-4755 /J27/ P. Kittilsen, R. Tøgersen, E. Rytter, H. Svendsen;

How to avoid gas-liquid mass transfer limitations during olefin polymerization In Metalorganic Catalysts for Synthesis and Polymerization; W. KaminskyEd.; Springer Verlag, Berlin Heidelberg, 1999; pp. 643-651.

/J28/ Hagesaether, L., Jakobsen, H. A., Hjarbo, K. W. and Svendsen, H. F. A coalescence and breakup module for implementation in CFD-code Computer-Aided Chemical Engineering, 8,(2000), 367-372.

/J29/ Jakobsen, H. A., Bourg, I., Hjarbo, K. W. and Svendsen, H. F. Interaction Between Reaction Kinetics and Flow Structure in Bubble Column Reactors. In Parallel Computational Fluid Dynamics – Trends and Applications, Elsevier Science B.V, 2001

/J30/ Tayebi D., Svendsen H.F, Jakobsen H.A., Grislingås A.

Measurement Techniques and Data Interpretation for Validating CFD Multi-phase Reactor Models

Chem. Eng. Com. Vol. 186, (2001), 57 - 159

/J31/ Kittilsen P., McKenna T., Svendsen H.F, Jakobsen H.A., Fredriksen S. The Interaction between Mass Transfer Effects and Morphology in Heterogeneous Olefin Polymerization Chem. Eng. Science, 56, (2001), 4015-4028.

Page 35: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

/J32/ P. Kittilsen, R. Tøgersen, E. Rytter, H. Svendsen; "Determination of Gas-

Liquid Mass Transfer Limitations in Slurry Olefin Polymerization." Industrial & Engineering Chemistry Research, 40, (2001), 1329 -1336

/J33/ P. Kittilsen, R. Tøgersen, E. Rytter, H. Svendsen;

Modeling of Gas-Liquid Mass Transfer Limitations in Slurry Olefin Polymerization. Industrial & Engineering Chemistry Research, 40, (2001), 1090 -1096

/J34/ P. Kittilsen, H. Svendsen, T. McKenna

Modeling of Transfer Phenomena on Heterogeneous Ziegler Catalysts: Part IV. Convection effects in gas phase processes Chemical Engineering Science, 56, (2001), 3997-4005

/J35/ Svendsen H.F., Poplsteinova J., Hoff K.A., Da Silva E.F., " Absorption as a method for CO2 capture", Proceedings from: Second Nordic Minisymposium on Carbon Dioxide Capture and Storage, Gøteborg, Oct. 2001.

/J36/ Hagesæther L., Jakobsen H.A., Svendsen H.F.

Modeling of dispersed phase distributions in bubble columns. Industrial & Engineering Chemistry Research, 41,(2002), 2560-2570 /J37/ Hagesæther L., Jakobsen H.A., Svendsen H.F. A model for turbulent binary breakup of dispersed fluid particles. Chem. Eng. Science, 57,(2002), pp 3219-3235. /J38/ Falk-Pedersen O., Palla N., Svendsen H.F., Meyer H.S. Membrane Gas/Liquid Contactors for Natural Gas Dehydration. IGRC 2001, Amsterdam, Nov. 2001.

/J39/ Karl A. Hoff, Jana Poplsteinova, Hugo A. Jakobsen, Olav Falk-Pedersen, Olav Juliussen, and Hallvard F. Svendsen, Modeling of Membrane Reactor.

IJCRE 1,(2003),A9 /J40/ Kittilsen P., Svendsen H.F., McKenna T.F., "Viscoelastic Model for Particle

Fragmentation in Olefin Polymerizaton", AIChE Journal, 49,(6), 2003, pp 1495-1507

/J41/ Eirik Falch Da Silva and Hallvard F. Svendsen, " Prediction of the pKa Values

of Amines Using ab Initio Methods and Free Energy Perturbations", Ind. Eng. Chem. Res 42 , 2003, pp 4414 - 4421

/J42/ Bertola F., Grundseth J.,Hagesæther L., Dorao C.,Luo H.,Hjarbo K. W.,

Svendsen H. F., Vanni M., Baldi G., Jakobsen H. A., "Numerical Analysis and Experimental Validation of Bubble Size Distributions in Two-Phase Bubble Column Reactors", 3rd European-Japanese Two-Phase Flow Group Meeting, Certosa Di Pontignano, Sept 2003

Page 36: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

/J43/ P. Kittilsen, H. F. Svendsen, “Three-level mass-transfer model for the

heterogeneous polymerization of olefins”, Journal of Applied Polymer Science, 91 (4), 2158-2167 (2004)

/J44/ Karl Anders Hoff,Olav Juliussen,Olav Falk-Pedersen, and Hallvard F.

Svendsen, “Modeling and Experimental Study of Carbon Dioxide Absorption in Aqueous Alkanolamine Solutions Using a Membrane Contactor”, Accepted Ind Eng Chem Res.

/J45/ Eirik Falch Da Silva and Hallvard F. Svendsen, " Ab Initio study of the

reaction of carbamate formation from CO2 and alkanolamines" Accepted Ind. Eng. Chem. Res.

Patents: /P1/ Eide O., Lysberg M., Oterholm B., Storrø I., Svendsen H.F., Winnberg A. Fremgangsmåte for kontinuerlig fremstilling av ulike biotekniske produktgrupper ved anvendelse av kontinuerlig membranreaktor. Utlegningsskrift 174588, Jan. 1992 /P2/ Eide O., Lysberg M., Oterholm B., Storrø I., Svendsen H.F., Winnberg A. Fremgangsmåte for kontinuerlig fremstilling av biokatalysatorpartikler. Utlegningsskrift 174589, Jan 1992. /P3/ Tayebi D., Svendsen H.F., Grislingås A., Mejdell T. "Måling av partiklers og boblers bevegelse i fluidseng" Norsk Patentsøknad nr 980191 Other publications and international Conferences: /O1/ Svendsen, H.F.

Solvent extraction as method for recovery of heavy metals from industrial waste waters

Dr.Ing. thesis, Department of Chem. Engn., NTH, June 1976 /O2/ Anundskås, A., Grjotheim, K., Schultz, A., Svendsen, H., and Øye, H.A.

Surface Properties Related to Magnesium Electrolysis The Metallurgical Society of AIME, annual meeting (1977)

/O3/ Svendsen H.F., Schei G., Osman M. Kinetics of Extraction of Zinc by Di(2-Ethyl-Hexyl)Phosphoric Acid EFChE, Working Party on Distillation, Absorption and Extraction, Cologne, May 1989 /O4/ Torvik R., Svendsen H.F.,

Page 37: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Modelling and Simulation of 2-Phase Bubble Column using a k-ε Turbulence Model. The 6th International Summer School, Varna Bulgaria, !989. /O5/ Svendsen H.F., Lysberg M., Sivakumar S., Torvik R. Reactor modelling , advantages and shortcomings. The SINTEF Methanol process experience. SPUNG seminar, Trondheim, Sept. 1989 /O6/ Lysberg M., Sivakumar S., Svendsen H.F. Model Studies of Three Phase Methanol Synthesis AIChE Annual Meeting, San Fransisco, Nov. 1989. /O7/ Torvik R., Svendsen H.F. Modelling of Three Phase Bubble Columns, Comparison with Experimental Results. CHISA'90, Prague, Aug. 1990 /O8/ Svendsen H.F., Lysberg M., Migiro C.L.C., Storrø I., Winnberg A. Prediction of Ethanol Production Rate in Immobilized Yeast Cultures. Proceedings from Chemical and Process Engineering for Development, Dar es Salaam, Tanzania, Sept. 1990. /O9/ Pervez I., Svendsen H.F., Strøm T., Vassbotn T. Gas Desorption During Turbulent Flows with Short Residence Times AIChE Annual Meeting, Chicago Nov. 1990 /O10/ Pervez I., Svendsen H.F., Strøm T., Vassbotn T. Mass Transfer During Highly Developed Turbulent Flows 4th World Congress of Chemical Engineering, Karlsruhe, June 1991 /O11/ Bart H-J., Kolarik Z., Slater M.J., Svendsen H.F. Progress in assessment of D2EHPA for use as a recommended system for liquid-liquid extraction. EFChE, Working Party on Distillation, Absorption and Extraction, Guildford, UK, May 1992 . /O12/ Luo H., Hjarbo K., Svendsen H.F. Experimental Characterization of Flow Structures in Multiphase Reactors. SPUNG Seminar, Trondheim, Sept 1993. /O13/ Jakobsen H.A., Svendsen H.F., Hjarbo K. On the Prediction of Chemically Reacting Systems in a Bubble Column Reactor. Proceedings from the 1st Industrial Chemical Engineering Technology Topical Conference, St. Louis, Nov 1993. /O14/ Syaiful S., Wilhelm A.M., Svendsen H.F., Delmas H. Upward Cocurrent Gas-liquid-(solid) Contactors: Holdup, Axial Dispersion, Gas-liquid Mass Transfer.

Page 38: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

2nd International Conference on Gas-Liquid-Solid Reactor Engineering, The Institution of Chemical Engineers, Cambridge, March 1995, Page A52-A58. /O15/ Svendsen H.F., Luo H., Hjarbo K.W., Jakobsen H.A. Experimental Determination and Modeling of Bubble Size Distributions i Bubble Columns. ACHEMASIA'95, Beijing, May 1995, Scientific Lectures Proc., page 47-48. /O16/ Sannæs B.H., Dudukovic M., Svendsen H.F. Experimental and Numerical Investigations of Solids Dynamics In Slurry Bubble Columns. AIChE Annual Meeting,Miami,Nov.,1995 /O17/ Grevskott S., Svendsen H.F. The effect of superficial gas velocity and initial turbulence level on radial phase distribution in bubble columns. AIChE Annual Meeting, Miami, Nov. 1995 /O18/ Hagesæther L, Luo H., Svendsen H.F. The Modelling of Coalescence of Oscillating Liquid Drops CHISA’96, Prague August 1996, Paper C1.5 /O19/ Svendsen H.F. Modeling of Bubbly Flows Invited Plenary Lecture, Engineering Foundation Conference on Computational Fluid Dynamics in CRE, San Diego, Oct. 1996 /O20/ Sannæs B.H., Dudukovic M.P. and Svendsen H.F. Solids Motion and Concentration Profiles in Slurry Bubble Columns ECCE 1, Florence, May 1997, pp1775-1778 /O21/ Grevskott S. and Svendsen H.F

The effect of drag formulation and boundary conditions on bubble column flow prediction

ECCE 1, Florence, May, 1997, pp 1779-1782

/O22/ Tayebi D., Svendsen H.F., Grislingås A., Mejdell T, Johannessen K. Dynamics of fluidized-bed reactors: Development and application of a new multi-fiber optical probe.

ISCRE15, Newport Beach,USA, Sept. 1998 /O23/ Kvamsdal H., Svendsen H.F., Hertzberg T., Olsvik O.

Dynamic simulation and optimization of a catalytic steam reformer ISCRE15, Newport Beach,USA, Sept. 1998 /O24/ Mejdell T., Pettersen T., Naustdal C., Svendsen H.F. Modelling of Industrial S-PVC Reactor. ISCRE15, Newport Beach,USA, Sept. 1998

Page 39: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

/O25/ Kittilsen P., Tøgersen R., Rytter, E., Svendsen H. How to avoid gas-liquid mass transfer limitations during polymerization of olefins., Int. Symp.on Metalorganic Catalysts for Synthesis and Polymerization, Hamburg, Germany, Sept. 13-17, 1998.

/O26/ Svendsen H.F., Absorption of CO2 using a membrane contactor. Presented at EFChE, Working part on Absorption, Distillation and Extraction, Trondheim, May 1999.

/O27/ Hagesæther L., Jakobsen H.A., Svendsen H.F. Theoretical analysis of fluid particle collisions in turbulent flow.

Presented at 4th Int. Conf. On Gas-liquid and Gas-Liquid-Solid Reactor Engineering , Delft August 1999.

/O28/ Hagesæther L., Jakobsen H.A., Hjarbo K.W., Svendsen H.F. A Coalescence and Breakup Module for Implementation in CFD Codes.

Presented at Escape 10, Florence, May 7-10, 2000, /O29/ Jakobsen, H. A., Bourg, I., Hjarbo, K. W. and Svendsen, H. F. Interaction Between Reaction Kinetics and Flow Structure in Bubble Column Reactors. Paper at Parallel CFD 2000 Conference, Trondheim, May 22-25, 2000. /O30/ Hugo A. Jakobsen and Hallvard F. Svendsen. Challenges on Predictive Fluid Dynamic Modeling of Bubble Column Reactors. Paper presented at CHISA 2000, Prague, Czech Republic, August 27-31, 2000. /O31/ Kittilsen P., McKenna T., Svendsen H.F.

The interaction between Mass Transfer Effects and Morphology in Heterogeneous Olefin Polymerization. Presented at 1st European Conference on the Reaction Engineering of Polyolefins Processes(ECOREP 2000), Lyons, July 3-6, 2000

/O32/ Dannström H., Stuksrud D.B, Svendsen H.F

Membrane Gas/Liquid Contactors for Natural Gas Sweetening GPA Spring Meeting, Aberdeen, May, 2000.

/O33/ P. Kittilsen, T. McKenna, H. Svendsen and S.B. Fredriksen The Interaction between Mass Transfer Effects and Morphology in Heterogeneous Olefin Polymerization Lecture at ECOREP, Lyon, France, 3-6 July 2000

/O34/ P.Kittilsen, H.Svendsen, H.A. Jakobsen, T. McKenna, S.B. Fredriksen

The Effect of Initial Conditions on Morphology in Heterogeneous Olefin Polymerization. Subitted to "International Symposium on Future Technologies for Polyolefin and Olefin Polymerization Catalysis", Tokyo, March 2001

Page 40: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

/O35/ Svendsen H.F., “Removal of CO2; from global problem to practical application.”, INPT, ENSIACET, Toulouse, June 2001

/O36/ Svendsen H.F. "Capture of CO2 by absorption in chemical solvents" 1st Polish-Norwegian Seminar on Selected Research Topics., Warsaw, Oct.

2001 /O37/ Falk-Pedersen O., Nagaraju Palla, Hallvard Svendsen, Howard S. Meyer,

“Membrane Gas/Liquid Contactors for Natural Gas Dehydration”, International Gas Research Conference, Amsterdam, 2001.

/O38/ Svendsen H.F., "Absorption as a method for CO2 capture", Andra nordiska minisymposiet om koldioksidrening och lagring, Chalmers, Gøteborg Universitet, Gøteborg, 26 October 2001

/O39/ King S.I., Falk-Pedersen O., Stuksrud D.-B., Grønvold M. S., Svendsen H.F.,

Palla R., Meyer H.S., Leppin D., "Membrane Gas/Liquid Contactors for Natural Gas Dehydration", 52nd Annual Laurance Reid Gas Conditioning Conference, Feb. 2002

/O40/ Poplsteinova J., Hoff K. A., Jakobsen H. A., Svendsen H. F.

Modeling of Membrane Absorption Reactors. Presented at ISCRE17, Hong Kong, August 2002

/O41/ Poplsteinova J., Svendsen H.F., and Lee L.L

"Modeling Vapor-Liquid Equilibrium for Systems H2O-MEA-CO2 and H2O-MDEA-CO2 " Presented at CHISA17, Prague August 2002

/O41/ Svendsen H.F, "Mekanismer ved oppbryting og koalesens",

Separasjonsteknologi, olje/gass/vann. Liv og lære NIF-seminar Tønsberg 26-27 september 2002 /O42/ Svendsen H.F., Hoff K. A., "Membrane Reactor Modelling", EMS Summer

School, Trondheim August 2003. /O43/ Svendsen H.F., "Possibilities and challenges in post-combustion CO2 capture", Power Production with CO2 Capture, Klimatek Conference Oct., 2003. Scientific reports: /R1/ Svendsen, H. and Thorsen, G.

Extraction of Zinc from wastewater from the production of Rayonwool STF21 F75028, 1975

/R2/ Svendsen, H. and Thorsen, G.

Copper recovery from Pyrite Cinders purification leach solutions, Part 1 (Norw.) STF21 F79013

/R3/ Svendsen, H. and Thorsen, G.

Page 41: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Purification of Pyrite Cinders, Part 2 (Norw.) STF21 F79068

/R4/ Svendsen, H. and Thorsen, G.

Treatment of hydroxide slurry and mixed oxides from Boliden Metall, Rönnskär, Sweden (Norw.), STF21 F79090.

/R5/ Svendsen, H., Grislingås, A., and Thorsen, G.

Process Development for Copper Residue, Part 1 (Norw.) STF21 F79049

/R6/ Svendsen, H. and Thorsen, G. Process Development for Copper Residue, Part 2 (Norw.)

STF21, F80035 /R7/ Steineke, F., Svendsen, H., and Thorsen, G. Process development for Copper Residue, Part 3 (Norw.)

STF21 F80035 /R8/ Grislingås, A., Svendsen, H., and Thorsen, G.

Upgrading of Lead/Silver residue, Part 1 (Norw.) STF21 F79050

/R9/ Røssel, M., Svendsen, H., and Thorsen, G.

Upgrading of Lead/Silver Residue, Part 2 (Norw.) STF21 F80049

/R10/ Røssel, M., Svendsen, H., and Thorsen, G. Leaching of pyrite (pyrite cinders) from Løkken (Norw.)

STF21 F80081 /R11/ Urstad, J., Svendsen, H., Christensen, H., and Thorsen, G.

Cement Copper Project Solvent Extraction Process for Recovery of Metal Values from Zinc Purification Residues, April 1981

/R12/ Svendsen, H. and Thorsen, G.

Metal recovery from mine water (Norw), STF21 F82011, 1982 /R13/ Svendsen, H. and Thorsen, G.

Metal extraction from chloride and fluoride containing waste waters(Norw) STF21 F83003, January 1983 /R14/ Svendsen H.F., Hennie E. Process Equipment in Motion. Project progress report. STF88 F83023, 1983 /R15/ Svendsen H.F., Hennie E., Berg Hansen T., Reitan M., Langø E. Process Equipment in Motion. Appendix to final report. STF88 F83036, 1983 /R16/ Svendsen H.F., Juliussen O., Hennie E. Sandtorv H. Process Equipment in Motion. Final report. STF88 F84023, 1984 /R17/ Svendsen H.F., Hennie E. Process Equipment in Motion. Project progress report 1.

Page 42: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

STF88 F84024, 1984 /R18/ Svendsen, H.

Assessment of NORAD support to Chemistry Dept. and Dept. of Chemical and Process Engineering, University of Dar es Salaam, Tanzania

STF21 A83037 , STF21 A83040, STF21 A87006, STF21 A88008, STF21 A88094, STF21 A90003, STF21 A91020, STF21 A91096, STF21 A92062 /R19/ Svendsen H.F., Kolderup H., Juliussen O., HeggemP., Hennie E., Stenersen D. Glykolinjeksjon. Hyperbar rigg, -prosjektering STF21 mars 1985 /R20/ Lund A., Svendsen H.F. Hennie E., Juliussen O. Forprosjektering av sirkulasjonssløyfe for måling av hydratkinetikk i kondensat og tofase-strømning, STF21 F86008, 1986 /R21/ Ardø B.A., Celius H.K., Grimnes K., Hennie E., Svendsen H.F. Sentrifugalseparering innen offshore oljeproduksjon IKU rapp. F86051, 1986 /R22/ Svendsen H. Ekstraksjon av metaller fra Silgrainsyre med TBP, STF21 F86077, 1986 /R23/ Lysberg M., Svendsen H.F., Torvik R. Slurryreaktorer, -en oversikt over korrelasjoner og modeller., STF21 A88036, 1988 /R24/ Kolderup H., Juliussen O., Grislingås A., Svendsen H.F., Lindeberg E. Improved well stream tests, IWST, STF21 F88069, 1988 /R25/ Juliussen O., Strøm T, Svendsen H.F. Gasstørking med TEG, STF21 F90028, March 1990 /R26/ Juliussen O., Strøm T, Svendsen H. Gas Dehydration , STF21 F90040, May 1990 /R27/ Grislingås A., Juliussen O., Svendsen H.F., Thorsen T. Utnyttelse av Vanillinavlut. Forprosjekt, STF21 F90058, 1990 /R28/ Hjarbo K., Kolderup H., Svendsen H.F. Faststoffordeling i slurryreaktor. Metodeutvikling, STF21 F91033, 1991 /R29/ Svendsen H.F., Pervez I., Strøm T., Vassbotn T. Desorpsjon av gass ved høye drivende krefter og lave oppholdstider. STF21 A91070, 1991 /R30/ Svendsen H.F., Sivakumar S., Lysberg M. Generalisert dispersjonsmodell for slurryreaktor. Modellunderlag og program- beskrivelse., STF21 A92004, 1992 /R31/ Svendsen H.F. Lutning av kobberholdig sulfidmineralisering fra Sulitjelma., STF21 F92026, 1992 /R32/ Riibe, S., Svendsen H., Holte S., Erga O. CO2 removal with MDEA, the static mixer concept. Verification report Kværner Process Systems, July 1991

Page 43: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

/R33/ Svendsen, H.F. CO2 removal with MDEA, the static mixer concept. Phase 2 , evaluation report STF21 F92032, 1992 /R34/ Lysberg M., Svendsen H.F. CO2 removal with MDEA, the static mixer concept. Phase 2 , Modelling report STF21 F92038, 1992 /R35/ Svendsen H.F., Hjarbo K. Jakobsen H.A. Boblestørrelse og lokal gassfraksjon fra konduktivitetsmålinger. STF21 F93103, 1993 /R36/ Svendsen H.F. Slurryteknologi. Sluttrapport., STF21 A94011, 1994 /R37/ Svendsen H.F. Slurry teknologi. SPUNG Kjemisk konvertering. Faglig sluttrapport STF21 A94005, 1994 /R38/ Svendsen H.F, Hjarbo K.W. STF21 A95017, 1995 /R39/ Svendsen H.F., Erga O., Strøm T. Sleipner Vest CO2 - removal verification study - Final report STF21

F95027, 1995 R/40/ Svendsen H.F, TAN047 short review of the Dept. of Chemical and Process Eng. UDSM 1995, STF21

A96003, 1996 R/41/ Svendsen H.F, Grevskott S., Lysberg M., "Pseudohomogen og heterogen to-dimensjonal

dispersjonsmodell for gassfase fixed bed reaktorer., STF21 F96035, 1996 /R41/ Grislingås A., Hagen R.I, Svendsen H.F., Thorsen G., Thorsen T. Magnesium from sea water. A

preliminary study report 1. - Working draft report., STF66 F96050, 1996 /R42/ Svendsen, H.F, Lysberg, M. Selektiv fjerning av H2S fra CO2 i statisk mixer - en forstudie STF66

F97021, 1997 /R43/ Lundstrøm P., Lysberg M., Skjetne P., Strøm T. and Svendsen H.F. Physical Modeling of a Polyolefin

Flash Pipe., STF66 F98007, 1998 /R44/ Svendsen H.F, Lysberg M., Selektiv fjerning av H2S fra CO2 i statisk mikser – videreføring 1998

STF66 F98068, 1998 R/45/ Svendsen, H.F., Lysberg, M. Selektiv fjerning av H2S fra CO2 i statisk mixer - videreføring i 1998

STF66 F98116, 1998 R/46/ Svendsen H.F., Sleipner Vest, CO2 removal., STF66 F98134, 1998 R/47/ Lundstrøm P., Lysberg M., Morud J., Skjetne P., Strøm T., Svendsen H.F., Physical Modelling of a

Polyolefin Flash Pipe. Updated version, september 1999., STF66 F99109 R/48/ Svendsen H.F., Lysberg M., Sleipner Vest study, Modeling, STF66 F99119, 1999 R/49/ Svendsen H.F., Lysberg M., Sleipner Vest study, Modeling, Version 2.STF66 F00074, 2000

Page 44: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 1 of 14

BIOGRAPHICAL DATA

HEINZ A. PREISIG

Titles and Degrees Contact Information

Professor of Process Systems Engineering Department of Chemical Engineering PhD. Tech. Sci. ETH Norwegian Uni of Sci and Tech (NTNU)

Dipl. Ing ETH, Chemical Engineer ETH N-7491 Trondheim Dipl. Ing. HTL, Chemist HTL Norway

Professional Chemist Telephone +47 - 735.9.28.07 Facsimile +47 - 735.9.40.80 E-mail [email protected]

Education 3/78 − 7/84 Ph.D., Technical Sciences, Swiss Federal Institute of Technology

(ETH, Prof. Dr. DWT Rippin), 1984. 8/74 − 3/78 Diploma (M.Sc.), Chemical Engineering, Swiss Federal Institute of Technology

(ETH), 1978; top 10% 9/74 − 8/75 Transition course HTL--ETH, top 1 % of the country. 8/71 − 8/74 Diploma (B.Sc.), Chemist HTL, Technikum Winterthur, 1974; top 5 % 3/68 − 4/71 Chemical laboratory assistant, apprenticeship, Sulzer 1971; best in 10 years.

Experience 01/03 − pre-

sent Norwegian University of Science and Technology (NTNU), Trondheim, Norway Professor of Process Systems Engineering, Fac. of Science and Technology

10/00 − 12/02 Eindhoven University of Technology, Eindhoven, The Netherlands Professor of Systems and Control, Fac. of Electrical Engineering

8/95 − 10/00 Eindhoven University of Technology, Eindhoven, The Netherlands, Section Head Dual Appointment Professor of Systems and Control, Fclts Chem Tech & Appl. Physics

97 pres National University of Singapore, regular Visiting Professor and advisor to Chemical Precess Engineering Centre (CPEC)

2/9 − 8/95 University of New South Wales, Sydney, Australia Senior Lecturer, School of Chemical Engineering and Industrial Chemistry & Electrical Engineering

8/85 − 12/89 Texas A&M University, College Station, Texas, USA Assistant Professor, Chemical Engineering.

8/84 − 7/85 Texas A&M University, College Station, Texas, USA Visiting Assistant Professor, Chemical Engineering.

3/78 − 7/84 Swiss Federal Institute of Technology (ETH), Zürich, Switzerland Teaching and Research Assistant and MS/PhD Supervisor.

74 − 79 Gewerbeschule Winterthur, Winterthur, Switzerland Substitute teacher at apprentice school for chemical laboratory assistants.

6/73 − 8/73 Cementa Inc., Hällekies, Sweden, laboratory technician. 4/68 − 8/71 Sulzer Inc., Winterthur, Switzerland, laboratory technician

Page 45: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 2 of 14

Professional Associations Former member of Dutch Institute of Systems and Control, DISC Former member of Dutch Process Technology Research School, OSPT Former member of SMBT (Stichting Meet en Besturings Technologie) (former head of Process Control

Section) Former member of the steering board and the executive board of PATO control section, the continuous

education program of the Dutch Engineering Society Former Member of the Stevin Institute, an interdisciplinary research school at Eindhoven Institute of

Technology Member of American Institute of Chemical Engineers, Associate to Computer Aids for Chemical Engineers (CACHE), Former member of Institute of Engineers Australia, Section Control (member of the board).

Profile in Brief I am devoted to interdisciplinary research using the systems approach to provide the supporting platform on which the specific applications rest with a strong emphasis on knowledge integration. On the theoretical side I have been interested in the fields of linear and nonlinear model predictive control, process identification, modelling and control of hybrid systems, with applications to sequential control and fault diagnosis and de-tection, time-scale analysis both in modelling and identification primarily using advanced wavelet technol-ogy and singular perturbation, modelling of macroscopic systems with an emphasis on system representa-tion, the latter inducing model reduction and integrating all scales of dynamics from sudden events to steady state. I hold a worldwide recognised leading position in the field of modelling hybrid systems and computer-aided modelling of macroscopic systems.

Having started my professional career in industry, carrying theoretical knowledge to bear its fruit in indus-trial applications is my objective. Applications include concept design of live support systems and distributed waste water installations, waste water plants, modelling of electrical arc cutting machines for control, tuning of a cyclotron, reduced-order modelling of heat exchangers, post-harvest food processing, membrane proc-esses and many more.

Page 46: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 3 of 14

RESEARCH STUDENTS

ETH Zürich Students Degree Year Urs Koster Process identification Ms Sci 1983 Urs Koster Batch plant control PhD discont. Ling Di Qi Optimal control of discrete systems Ass Prof guest 1981-3

Texas A&M University Collaborate projects with C.D. Holland, head of department and well-recognised specialist in simulation and design of distillation columns and R.E. White a specialist in battery modelling. Students Degree Year Two Process identification BS Sci 1985-7 M. Kimmich Reduced-order modelling of heat transfer processes and

mixing Ms Sci 1988

T.Y. Lee Computer-aided modelling PhD 1991 G. Mijares multi-variable control (with C.D. Holland) PhD 1988 J.D. Cole distillation control (with C.D. Holland) PhD 1989 Several Battery dynamics (with C.D. White) Ms Sci 1987-9

University of New South Wales Students Degree Year Guo, D.-Z. ; (PhD Queensland Univ., Chemical Engineering)

Tree representation of the physical topology of physical-chemical-biological processes.

Post Doc 1991-2

Levitsky, V.; (PhD Odessa, Physics)

Object oriented representation of physical-chemical-biological processes.

Post Doc 1993-4

Li, D.V. Discrete-event system modelling Post Doc 1994 Ma, X.M. Dynamic reduced-order modelling of heat exchangers PhD 1990-3 Mehrabani, A.Z. Computer-aided modelling of physical-chemical-biological

systems PhD 1995

Maridable, P. Modelling of event-discrete chemical processes and controller synthesis

PhD 1992

Renz Jochen Synthesis of supervisory control systems Ms Sci 1992-3 Gasendo, G. (lec-turer LaSalle Uni, Manila Philippi-nes)

Modelling and identification of a catalytic process Ms Sci 1992-3

Castillo, Gil Knowledge representation in computer aided modelling Ms Sci 1993-7 Mun , Sally Process Identification in Batch Processes Ms Sci 1990 Subur , Sophia Comparison of Kalman Filter and Spline-Type Modulating

Functions Ms Sci 1990

Rys Van, Auto Tuning of Process Controllers Ms Sci 1990 Momsen , Steven Sequential of Dynamic Chemical Processes Ms Sci 1990 Couldridge, A.T. Identification of Heat Transfer Process Ms Sci 1991

Page 47: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 4 of 14

McLauglin, Discontinued Ms Sci 1991 Yem, Raymond Supervisory Control of A Chemical Process Ms Sci 1991 Thee, C.G. Dynamic Temperature Measurements Ms Sci 1991 Thangarajah, C. Scheduling of Batch Processes Ms Sci 1991 Panov , V. Laminate Production Process Ms Sci 1992 Tika, P. Simulation and Identification of Fixed-Bed Reactor Ms Sci 1992 Rahmadi, A. Identification of Dynamic Heat Transfer Model Ms Sci 1992 Woodburn, K. Identification of Local Heat Transfer Parameters in Jacketed

Stirred Tank Reactor Ms Sci 1993

Newman, S. Distillation Column Modelling Ms Sci 1993 Bushell, G. Identification of Fixed-Bed Reactor Ms Sci 1993 Chang, C. Identification of Dynamic Heat Transfer in Jacketed Stirred

Tank Reactor Ms Sci 1993

Halsted, J. Simulation and Optimisation of a Multi-Producer-Storage-Multi-Customer Problem

Ms Sci 1993

Bushell, G. Identification of a Kinetic Model in a Fixed-Bed Reactor Ms Sci 1993 Co-supervision of various electrical engineering students working on the School's pilot plant in an effort to replace the existing control system. The new system included new event-discrete system components devel-oped in my group. One project student has been accepted to MIT and several other major US universities. Another student was rewarded an Australian Overseas Student grant for continuation to PhD.

Eindhoven University of Technology Students Degree Year Verwaater van der, S

Recipe Development and Model-Based Recipe Optimisation in the Batch Processing Industry (co-supervisor with O. Rade-maker)

PhD 1995

Eijpe R.A. Modellering van biologische defosfatering in Carrousel 2000 Ms Sci 1995 Dr. M. Weiss, (PhD Mathemat-ics in Groningen, The Netherlands)

Computer-aided modelling: Consistency and completeness of mechanistic models in DAE form and index reduction And Discrete-event dynamic system modelling and fault detection

Post Doc 1995-99

Bossink S. Geen verslag in archief Ms Sci 1996 Sijbers M. Parameteridentificatie uit batchexperimenten voor het IMs

SciWQ Model No. 1 Proj 1996

Ortmans R.H.M.H.

HMs SciRT Protocol and Control Proj 1996

Pijpers M.J.H. Modelling for supervisory control Ms Sci 1996 Umans F.J.Ms Sci.

Toepassingsmogelijkheden van MPC voor regeling van een polymerisatieproces

Proj 1996

Dr. Y. Lammerts (PhD Mechanical Engineering in Eindhoven, The Netherlands),

Teaching laboratory for systems and control education and batch process control

Post Doc 1996-00

Kovanen J.P. Design, modelling and simulation of a two-vessel batch plant Proj Vis. 1997 Lipsch, Roel Discrete-event dynamic control of batch reactor PhD discont. Verdijk G.J.C. Modellering en Regelaarontwerp ten behoeve van een

industrieel droogproces Ms Sci 1997

Oosterum van Ms Sci.

Praktikum Systeem- & Regeltechniek, een eerste opzet Proj 1997

Broek van den Closed-loop Identification Using Finite Data Ms Sci 1997

Page 48: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 5 of 14

J.R.M. Westerweele M.R.

Concepts and Design of Modeller, a Computer-Ms Sciided Modelling Tool

Ms Sci 1997

Eekhof M. Fault Detection as an Observability Problem Proj 1997 Bruinsma U.B.D.M.R.

State-event discrete modelling of non-linear batch plants Ms Sci 1997

Leur van J.L.F. The first tests with a new interface for experiments Proj 1997 Heuvel van den I.T.M.

Evaluations of experiments& first completed experiment for two practical courses

Proj 1997

Waal de, Marc Control structure selection (co-supervisor with J. Kok) PhD 1998 Stouten B. Development of a Heating-Cooling System with two solenoid

valves Proj 1998

Meulenberg R. Heating Cooling System HTS / Ms Sci

1998

Oosterum van Ms Sci.

Using First Principles Models and Neural Networks for hybrid system identification

Ms Sci 1998

Dekkers R.M. SyMoM, a Symbolic computation package for analysis and manipulation of dynamical models

Ms Sci 1998

Gastel van P. "De Limonade Fabriek": De kunst van het vullen van een willekeurige beker

HTS 1998

Wagemakers J.Ms Sci.C.

Het ontwerpen en bouwen van een positioneereenheid HTS 1998

Francisca R. Dynamics flow and temperature control in a one-pipe airco HTS / Ms Sci

1998

Niemans D. Experiment "The Two Vessel Batch Plant" HTS 1998 Giebels M. Experiment "The Two Vessel Batch Plant": Hardware and

Software design HTS 1998

Schuurbiers M. "One-pipe airco": De software-ontwikkeling HTS 1998 O'Neill L. Ms Sci Lemonade Maker Proj Vis 1998 Pauly M. External Communications via RS232 for SIMULINK Real-

Time Workschop HTS 1999

Grimm R.Ms Sci.

Low-Order Modelling of the Dynamic Behaviour of Heat Exchangers: Theory and Experimental Verification

Ms Sci 1999

Huisman L. Experiment with an 'Extended Bath Tub' and a 'Multi Compartment Tank', Design, Realization, Ms Scinalysis and Control

Ms Sci 1999

Vaassen S. On Spline-Tuype Modulating Functions and Wavelets Proj 1999 Krabbendam P. Dynamics of Energy Dissipation in a Batch Reactor driven by

a Heating Cooling System Ms Sci 1999

Grijseels, S.C.M. On the Subject of Single-Phase Simple Systems: Ms Sci Thermodynamic Modelling Concept

Ms Sci 1999

Weijers, Stefan Modelling and control of waste water treatment plants PhD 2000 Mertens, H. Real-Time Control of Laboratory Experiments with

Matlab/Simulink Ms Sci 2000

Brok, W. Neuromorphic Modelling of Binoural Localisation Proj 2000 Brink, R Design and Realisation of a Novel High-Precision Gas Flow

Meter Ms Sci 2001

Philips, P P H H Modelling, Control and Fault Detection of Discretely-Observed Systems

PhD 2001

Verdijck, Ger-wald

Model Predictive Control of Post-Harvest Processes (industrial project)

PhD 2002

Westerweele, M R

Consistent Dynamic Process Models PhD 2003

Vleuten-Balkema van der, A J

Sustainable Wastewater Treatment PhD 2003

Page 49: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 6 of 14

Norwegian University of Science and Technology Students Degree Year Hayer, Fatemeh Theme in computer-aided process modelling: application

oriented PhD Ongoing

Zhu, Zhengjie Theme in computer-aided process modelling: theoretically oriented

PhD Ongoing

Proj Project student Proj Vis Foreign visiting project student HTS Polytechnic diploma student Ms Sci Master of Science PhD Doctoral promotion Post Doc Post doctoral researcher

Page 50: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 7 of 14

REFEREED PUBLICATIONS1

# Authors Title Medium Year

1. Mijares, G. Cole, J D Naugle, N W Preisig, H A Holland, C D

New Criteria for System Stability and Pairing of Control and Manipulated Variables

AIChE Journal pp 1439-1449

1985

2. Mijares, G. Cole, J D Preisig, H A Holland, C D

The Jacobi Eigenvalue Criterion: An Analysis and Dynamic Extension

DYCORD 86, Bournmouth, UK

1986

3. Mijares, G. Cole, J D Preisig, H A Holland, C D

Stability and Performance Relations Between Triangular and Decentralised Control Systems

ACC 87, Minneapolis, USA pp 1701

1987

4. Mijares, G. Cole, J D Preisig, H A Holland, C D

Use of Point and Group Linear Iterative Methods for the Design of Decentralised Control Structures

ACC 87, Minneapolis, USA pp 664

1987

5. Preisig, H A Kimmich, M R Rippin, D W T

A Study of Dynamic System Modelling CEF 87, Taomina, Sicily, Italy

1987

6. Dovi, V G Paladino, O Preisig, H A

The Importance of Correct Boundary Conditions in the Estimation of Diffusion Coefficients form Mass Sorption Experiments

Com. Heat & Mass Transfer , 15 pp 669-679

1988

7. Dovi, V G Preisig, H A

Estimation of Parameters in Models Involving Partial Differential Equations with Unknown Boundary Conditions

Zentralblatt für Mathematik

1988

8. Preisig, H A Optimising Control--A Survey IECON'01, Denver, Colorado, USA, Nov 29 - Dec 02 pp 47

1988

9. Preisig, H A The Use of Differential Information for Batch Reactor Control

ACC 88, Atlanta, USA pp 671

1988

10. Preisig, H A Kimmich, M R Rippin, D W T

A Study of Dynamic System Modelling Computers & Chemical Engineering , 12, 5 pp 455-460

1988

11. Cole, J D Preisig, H A Holland, C D

The Design of Squaring Compensators for the Feedback Control of Non-Square Systems

ACC 89, Pittsburg, Pennsylvania, USA, 21-06 / 23-06 pp 107

1989

12. Dovi, V G Paladino, O Preisig, H A

Minimax Approximations to Theoretical Models Using Experimental Data

Applied Mathematics Letters

1989

13. Dovi, V G Paladino, O Preisig, H A

Inverse Free Boundary Problems Applied Mathematics Letters

1989

14. Preisig, H A The Application of Finite Automata Theory DYCORD 89, 1989 1 The data base may generate similar entries as conference proceedings and subsequent publication in journals may both be present.

Page 51: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 8 of 14

to Sequential Control of Chemical Processes

Maastricht, Netherlands, 21-09 / 23-09 pp 75-82

15. Preisig, H A On-line observation of the composition in non-isothermal batch reactors with non-linear reactions

ACC 89, Pittsburg, Pennsylvania, USA, 21-06 / 23-06, TP 4 pp 1549

1989

16. Preisig, H A Estimation of Mismatch Errors of Dynamic Models for Stirred Tank-Reactor Equipment: Part II Heat Dissipation in the Contents, Impact of Mixing

Chem Eng Sci , 44, 12 pp 2957-2965

1989

17. Preisig, H A Estimation of Mismatch Errors of Dynamic Models for Stirred Tank-Reactor Equipment: Part I Heat Exchange with Jacket, Impact of Model Reduction

Chem Eng Sci , 44, 12 pp 2943-2955

1989

18. Preisig, H A Lee, T Y Makela, M Whittacker, A D Little, F

On the Representation of Life-Support System Models

19th ICES, San Diege, USA, 891479 pp 13

1989

19. Preisig, H A Lee, T Y Little, F

A Prototype Computer-Aided Modelling Tool for Life-Support System Models

20th ICES, Williamsburgh, PA, USA, 901269 pp 10

1990

20. Preisig, H A Rippin, D W T

Application of Observer Using Differential Information to Bench-Scale Reactor

ACC 90, San Diego, USA

1990

21. Preisig, H A White, R E

A Solver for Sets of Nonlinear Ordinary Differential Equations

Computers & Chemical Engineering , 14, 2 pp 179-196

1990

22. Ma, X H Preisig, H A Wood, R M

Model Reduction of Counter-Current Heat Exchangers

CHEMECA 91, Newcastle, Australia pp 808-815

1991

23. Preisig, H A Discrete-Event Controlled Systems in the Chemical Processing Industry

CHEMECA 91, Newcastle, Australia pp 983-945

1991

24. Preisig, H A Guo, D Z Mehrabani, A Z

Computer-Aided Modelling: A New High-Level Interface to Process Engineering Software

CHEMECA 91, Newcastle, Australia pp 954-960

1991

25. Preisig, H A Subur, S

Comparison of Two Schemes for the Observation of Composition in Stirred-Tank Reactors Operating in Batch Mode

CHEMECA 91, Newcastle, Australia pp 889-895

1991

26. Ma, X H Preisig, H A Wood, R M

How Accurate Are Low-Order Models For Heat Exchangers ?

CHEMECA 92, Canberra, Australia pp 541-542

1992

27. Ma, X H Preisig, H A Wood, R M

On the Modelling of Heat Exchangers For Process Control

ACC 92, Chicago, USA pp 1441

1992

28. Preisig, H A An Object-Oriented Approach to Computer-Aided Modelling

CHEMECA 92, Canberra, Australia, 2 pp 394-400

1992

29. Preisig, H A Discrete-Event Controlled Systems in the Chemical Processing Industry

DYCORD 92, College Park, Maryland, USA pp 277

1992

30. Preisig, H A Towards Discrete Event Dynamic Models of Chemical Processes

CHEMECA 92, Canberra, Australia, 2 pp 385-392

1992

Page 52: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 9 of 14

31. Ma, X H Preisig, H A

Improving the accuracy of the low-order models for heat exchangers

CHEMECA 93, Canberra, Australia

1993

32. Ma, X H Preisig, H A Wood, R M

Reduced-Order Models for Heat Exchangers

IFAC World Congress 93, Sydney, Australia, 19-07 / 23-07, I

1993

33. Preisig, H A Safe Supervisory Control of Chemical Processes

CHEMECA 93, Canberra, Australia

1993

34. Preisig, H A More on the Synthesis of a Supervisory Controller From First Principles

IFAC World Congress 93, Sydney, Australia, 19-07 / 23-07, V pp 275

1993

35. Preisig, H A Rippin, D W T

Theory and Application of the Modulating Function Method--Part II Algebraic Representation of Maletinsky's Spline-Type Modulating Functions

Computers & Chemical Engineering , 17, 1 pp 17-28

1993

36. Preisig, H A Rippin, D W T

Theory and Application of the Modulating Function Method--Part I Review and Theory of the Method and Theory of the Spline-Type Modulating Function Method

Computers & Chemical Engineering , 17, 1 pp 1-16

1993

37. Preisig, H A Rippin, D W T

Theory and Application of the Modulating Function Method--Part III Application to Industrial Process, a Well-Stirred Tank Reactor

Computers & Chemical Engineering , 17, 1 pp 29-39

1993

38. Ma, X H Preisig, H A

Model-Based Controller Design for Heat Exchangers

CHEMECA 94, Perth, Australia, 25-09 / 28-09

1994

39. Ma, X H Preisig, H A

Model-Supported Control of Heat Exchangers

CHEMECA 94, Perth, Australia, 25-09 / 28-09

1994

40. Ma, X H Preisig, H A

Dynamic Modelling and Simulation of Heat Exchangers - What is available?

PSE 94, Seoul, Korea pp 327-332

1994

41. Preisig, H A Computer-Aided Modelling: Species Topology

ADCHEM 94, Kyoto, Japan, 25-05 / 27-05 pp 143-148

1994

42. Preisig, H A Modeller - A production tool for process engineering

FOCAPD 94, Snowmass, Colorado, USA

1994

43. Preisig, H A MODELLER -- A Computer-Aided Modelling Tool

AIChE Symposium Series FOCAPD 94, Snowmass, Colorado, USA, 91, 304 pp 328-331

1994

44. Preisig, H A Ma, X H

Modellgestützte Regelung von Wärmeaustauschern

GVC Jahrestagung 94, Aachen, Germany, 28-09 / 30-09

1994

45. Preisig, H A Ma, X H

Modellgestützte Regelung von Wärmeaustauschern

Chemical Engineering Technology , 11 pp 1

1995

46. Weijers, S R Kok, J J Preisig, H A

Control strategies for nitrogen removel plants and MPC applied to a pre-denitrification plant

FAB 95, Gent, Belgium, 27-09 / 29-09 pp 2435-2443

1995

47. Preisig, H A A Mathematical Approach to Discrete- Event Dynamic Modelling of Hybrid Systems

Computers & Chemical Engineering , 20 pp S1301- S1306

1996

48. Preisig, H A Computer Aided Modelling - Two Paradigms on Control

Computers & Chemical Engineering ESCAPE 6 (1996), Rhodes, Greece, 26-05 / 29-05, 20, B pp S981-S982

1996

Page 53: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 10 of 14

49. Preisig, H A Computer Aided Modelling - Two Paradigms on Control

Computers & Chemical Engineering , 20 pp S981-S986

1996

50. Preisig, H A Event-Discrete Modelling of Manufacturing Systems: Reduction of the State Space

I-CIMPRO 96, Eindhoven, Netherlands, 03-06 / 04-06 1996 pp 434-443

1996

51. Preisig, H A A Mathematical Approach to Discrete- Event Dynamic Modelling of Hybrid Systems

Computers & Chemical Engineering , 20, B pp S1301-S1306

1996

52. Preisig, H A Lim, K W

Design and Implementation of a Real-Time, Event-Based Control System

Chem Eng World Congress 96, San Diego, California, USA, 14-07 / 18-07 1996

1996

53. Weijers, S R Kok, J J Preisig, H A Buunen, A H M Wouda, T W M

Parameter identifiability in the IAWQ Model No. 1 for modelling activated sludge plants for enhanced nitrogen removal

Computers & Chemical Engineering , 20, B pp S1455-S1460

1996

54. Weijers, S R Kok, J J Preisig, H A Buunen, A H M Wouda, T W M

Parameter identifiability in the IAWQ Model No. 1 for modelling activated sludge plants for enhanced nitrogen removal

ESCAPE 6 (1996), Rhodes, Greece, 26-05 / 29-05

1996

55. Weijers, S R Preisig, H A

Parameter estimation of the IAWQ activated sludge model No. 1

ECC 96, Brussels, Belgium, 01-07 / 04-07

1996

56. Weijers, S R Preisig, H A

Identifiability and estimation of parameters in the IAWQ Model No. 1 for modelling activated sludge plants for enhances nitrogen removel

ESCAPE 6 (1996), Rhodes, Greece, 26-05 / 29-05

1996

57. Johns, W R Preisig, H A

Introduction to David Rippin Memorial Issue

Computers & Chemical Engineering , 22, 1 pp 1-29

1997

58. Lim, K W Preisig, H A

Design of a Real-Time Hybrid Controller IFAC Symp AIRT 97, Kuala Lumpur, Malaysia, 22-09 / 25-09 pp 137-142

1997

59. Philips, P P H H Bruinsma, U B D M R Weiss, M Preisig, H A

A Mathematical Approach to Discrete-event Dynamic Modelling of Hybrid Systems

IFAC Symp AIRT 97, Kuala Lumpur, Malaysia, 22-09 / 25-09 pp 185-190

1997

60. Preisig, H A Pijpers, M J H Weiss, M

A discrete modelling procedure for continuous processes based on state-discretization

MATHMOD 2, Vienna, Austria, 05-02 / 07-02 pp 189-194

1997

61. Weijers, S R Engelen, G L Preisig, H A Schagen van, K

Evaluation of model predictive control of nitrogen removal with a carrousel type wastewater treatment plant using different control goals

IAWQ Workshop 97, Brighton, UK, 06-07 / 09-07 pp 401-408

1997

62. Weijers, S R Preisig, H A Buunen, A H M Wouda, T W M

Parameter estimation of the activated sludge Model No. 1 from full-scale plant input / output data

ECC 97, Brussels, Belgium, 01-07 / 04-07 pp CD, Session TH-A H2

1997

63. Weiss, M Preisig, H A

Simplifying hypotheses in computer-aided modelling: a singular perturbation approach

Computers & Chemical Engineering , 21 pp S721-S726

1997

Page 54: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 11 of 14

64. Weiss, M Preisig, H A

Simplifying hypotheses in computer-aided modelling: a singular perturbation approach

ESCAPE 7 (1997), Trondheim, Norway, 26-05 / 29-05

1997

65. Dekkers, R Preisig, H A Weiss, M

SyMoM - a symbolic manipulation package for dynamical models of physical systems

ESCAPE 9 (1999), Budapest, Hungary, 31-05 / 02-06

1998

66. Dekkers, R Preisig, H A Weiss, M

SyMoM - a symbolic manipulation package for dynamical models of physical systems

Computers & Chemical Engineering pp S657-S660

1998

67. Lammerts, I M M Preisig, H A

Computer-Aided Experiments for a Course in Dynamic Systems and Control Technology

ESCAPE 9 (1999), Budapest, Hungary, 31-05 / 02-06

1998

68. Philips, P P H H Weiss, M Preisig, H A

A design strategie for discrete control of continuous systems

ACC 99, San Diego, USA, 02-06 / 04-06

1998

69. Ramkumar, K Philips, P P H H Preisig, H A Ho, W K Lim, K W

Structured fault-detection and diagnosis usig finite-state automation

24th IEEE Ind Elec Soc Conf, Aachen, Germany, 31-09 / 04-09

1998

70. Verdijck, G J C Weiss, M Preisig, H A

Modelling of a Pneumatic Dryer for Potato Starch

Journal of Food Engineering , 37 pp 243-258

1998

71. Verdijck, G J C Weiss, M Preisig, H A

Dynamic model development for an industrial potato starch drier

ACFBP 98, Goeteborg, Sweden, 21-09 / 23-09

1998

72. Weijers, S R Preisig, H A

Robustness analysis of MPC controlled activated sludge plants

ECC 99, Karlsruhe, Germany, 31-08 / 03-09

1998

73. Weiss, M Preisig, H A

Nonlinear systems analysis applied to the numerical conditioning of dynamic models for physical processes

ACC 98, San Diego, USA, 02-06 / 04-06 pp 2667-2671

1998

74. Lammerts, I M M Preisig, H A

Computer-Aided Experiments for a Course in Dynamic Systems and Control Technology

Computers & Chemical Engineering pp S633-S636

1999

75. Philips, P P H H Ramkumar, K Lim, K W Preisig, H A Weiss, M

Automation-based fault detection and isolation

ESCAPE 9 (1999), Budapest, Hungary, 31-05 / 02-06

1999

76. Philips, P P H H Ramkumar, K Lim, K W Preisig, H A Weiss, M

Automation-Based Fault Detection and Isolation

Computers & Chemical Engineering , 23 pp S215-S218

1999

77. Philips, P P H H Ramkumar, K Lim, K W Preisig, H A Weiss, M

Automation-Based Fault Detection and Isolation

ESCAPE 9 (1999), Budapest, Hungary, 31-05 / 02-06

1999

78. Philips, P P H H Weiss, M Preisig, H A

Control based on discrete-event models of continuous systems

ECC 99, Karlsruhe, Germany, 31-08 / 03-09

1999

79. Ramkumar, K Philips, P P H H Ho, W K Preisig, H A

A real-time realisation of fault-detection and diagnosis using finite-state automaton

IFAC World Congress 99, Bejing, China, 05-06 / 09-06, P, 7e-08-6 pp 211

1999

Page 55: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 12 of 14

Lim, K W 80. Verdijck, G J C

Hertog, M L A T M Weiss, M Preisig, H A

Modelling of a potato storage facility for Product Quality Control purposes

Computers & Chemical Engineering , 23 pp S911-S914

1999

81. Verdijck, G J C Hertog, M L A T M Weiss, M Preisig, H A

Modelling of a potato storage facility for Product Quality Control purposes

ESCAPE 9 (1999), Budapest, Hungary, 31-05 / 02-06

1999

82. Verdijck, G J C Weiss, M Preisig, H A

Model based product quality control for a potato storage facility

ACC 99, San Diego, USA, 02-06 / 04-06

1999

83. Weiss, M Preisig, H A

A systemic framework for first principles modelling and control of physical processes

IFAC World Congress 99, Bejing, China, 05-06 / 09-06, N, 7a-03-2 pp 55-60

1999

84. Westerweele, M R Preisig, H A Weiss, M

Concept and Design of Modeller, a Computer-Aided Modelling Tool

ESCAPE 9 (1999), Budapest, Hungary, 31-05 / 02-06

1999

85. Westerweele, M R Preisig, H A Weiss, M

Concept and Design of Modeller, a Computer-Aided Modelling Tool

Computers & Chemical Engineering , 23 pp S751-S754

1999

86. Balkema, A J Preisig, H A Otterpohl, R Lambert, A D J

Developing a model-based decision support tool for the identification of sustainable treatment options for domestic wastewater

Watermex 2000, Gent, Belgium, 18 pp 6

2000

87. Weijers, S R Preisig, H A

Nonlinear model reduction of bioprocess models through singular perturbation for control: an analytical scaling approach

MATHMOD 3, Vienna, Austria, 02-02 / 04-02 pp 615

2000

88. Weijers, S R Preisig, H A

Robustness Analysis of MPC Controlled Activated Sludge Plants

ADCHEM 2000, Pisa, Italy, 14-06 / 16-06

2000

89. Weiss, M Preisig, H A

Structural Analysis in the Dynamical Modelling of Chemical Engineering Systems

Mathematical and Computer Modelling of Dynamical Systems , 6, 4pp 325-364

2000

90. Westerweele, M R Akhssay, M Preisig, H A

Modelling of systems with equilibrium reactions

MATHMOD 3, Vienna, Austria, 02-02 / 04-02

2000

91. Balkema, A J Preisig, H A Otterpohl, R Lambert, A D J Weijers, S R

Developing a Model-Based Decision Support Tool for the Identification of Sustainable Treatment Options for Domestic Wastwater

Water Science Technology , 43, 7 pp 265-269

2001

92. Balkema, A J Preisig, H A Otterpohl, R Lambert, A D J Weijers, S R

The use of indicators in the sustanability assessment of wastewater treatment systems

Water Science Technology , 43, 7 pp 265-269

2001

93. Preisig, H A Concentration Control of Fast Reactions in ICSTR

DYCOPS-6, Jejudo (Chejudo), Korea, 4-6 June 2001 pp 696-699

2001

94. Preisig, H A Using Wavelets in Process Identification: A New Link to the State Space

ESCAPE 11 (2001), Kolding, Denmark, 27-05 / 30-05

2001

95. Verdijck, G J C A Control Methodology for Product Quality ESCAPE 11 (2001), 2001

Page 56: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 13 of 14

Lukasse, L J S Preisig, H A

Control in climate controlled operations involving Agro-materials

Kolding, Denmark, 27-05 / 30-05

96. Verdijck, G J C Straten van, G Preisig, H A

A Modelling and Control Structure for Product Quality Control in Climate Controlled Processing of Agro-Material

Journal of Control Engineering Practice , in print

2001

97. Westerweele, M R Preisig, H A

First Principle Modelling of Processes as Relevant to Process Industry

ESCAPE 11 (2001), Kolding, Denmark, 27-05 / 30-05

2001

98. Xi, Y X Lim, K W Ho, W K Preisig, H A

Fault Diagnosis using Dynamic Finite-State Automaton

IECON'01, Denver, Colorado, USA, Nov 29 - Dec 02

2001

99. Balkema, A J Preisig, H A Otterpohl, R Lambert, A D J

Indicators for the sustainablility assessment of wastewater treatment systems

Urban Water , 4, 2 pp 153-161

2002

100. Preisig, H A On Concentration Control of Fast Reactions in Slowly-Mixed Plants with Slow Inputs

ACC 2002, Anchorage, USA, 8-10 May 2002 pp FP 06-6

2002

101. Preisig, H A Lim, K W Xi, Y X

Computation of Min and Max Transition Times in Automata Representing Discrete-Event-Observed Continuous, Monotone Plants

4th ASCC, Singapore, Singapore, 25-27/09/2002

2002

102. Verdijck, G J C Sillekens, Preisig, H A

A Model Structure for Product Quality in Processing Agro-Material for Process Control Purposes

Journal of Food Engineering , 51 pp 151-161

2002

103. Balkema, A J Preisig, H A Otterpohl, R Lambert, A D J

Augmenting design with sustainability PSE 8 (2003), Kunming, China, 5-10/01/2003 pp 714-719

2003

104. Philips, P P H H Heemels, W P M H Preisig, H A Bosch van den, P P J

Control of Quantised Systems Based on Discrete-Event Models

International Journal of Control, 76, 3 pp 277-294

2003

105. Preisig, H A Westerweele, M R

Effect of Time-Scale Assumptions on Process Models and Their Reconciliation

ESCAPE 13 (2003), Lappeenranta, Finland, 1-4/6/2003 pp 875-880

2003

106. Preisig, H A Westerweele, M R

Modeller--An interactive model editor for physical-chemical-biological models

FOCAPO 2003, Coral Springs, Florida, USA, 12-15 Jan 2003, paper 92 pp 531-534

2003

107. Preisig, H A Xi, Y X Lim, K W

Fault Deagnosis Based on Limited Measurements of Process Variables

ADCHEM 7, Hong Kong, Hong Kong, 11-14/01/2004, 141

2003

108. Preisig, H A Xi, Y X Lim, K W

Tailoring Automata for Fault Diagnosability 29th IEEE Ind Elec Soc Conf, Roanoke, Virginia, USA, 2-6 11 2003

2003

109. Verdijck, G J C Straten van, G Preisig, H A

Optimisation of Product Quality and its Variatio in Climate Controlled Operations

Computers and Electronics in Agriculture , in print

2004

110. Verdijck, G J C Straten van, G Preisig, H A

Direct Product Quality Control for Energy Efficient Climate Controlled Transport of Agro-Material

International Journal of Control , in print pp 42

2004

111. Preisig, H A Modelling: Compartmental Networks and Topologies - A Comparison with Bond

ESCAPE 14 (2004), Lisabon, Portugal, 16-

2004

Page 57: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Heinz A. Preisig Biographical Data 14 of 14

Graphs 19/05/2004 pp 1111-1116

112. Preisig, H A Gymnastic Exercises with Topologies Relating to Time-Scale Assumptions

ESCAPE 14 (2004), Lisabon, Portugal, 16-19/05/2004 pp 1105-1110

2004

Page 58: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

����������������

����������� ����������� �"!#�

$&%�'(�*),+- /.0��1324+65��7�98:�<;�=:�?>@>7�?ACBD%7'FEG��HI%�'(J,KML72N<OQP0RTS�U�VDWYX

Z +-5@[]\3)Q^Q8`_�=:%7abK<cd�3178:���?�-'feDghji]k:hjlnmnkCo"8`�qpsr��-a/8ut?K7=dcd��1�8`�3�?�?'v8:��1wK�x�yI��8:z7�-'v{(8|xDL}%7A&~�'(%��3E�r��-8`a<��H0%7'vJs�-178uK��yI�38`z��?'F{�8`xDL�%�A0��t?8`�-�3t���K7�3E�~��-tFr���%�=`%�17L�e�H0~4HQyQo�2�~,r��6{�8u{?)��Fpsr3K7'vK�t�x(�-'(8:�-K�x(8:%7��%�A,'(�6K7t�xv8`%���t?%7�3E�8|xv8`%��3{�A�%�'t�'FK7tF>@8:��1/%�A�r3�-KMz@L�%78:=TA�'FK7t�xv8`%��3{v� e�~,r��-{(8:{0K7E�z@8u{�%�'-)�~��-'�BD���0�?'(x(�?���?'v1no�2

Z +-5�\n[�)��dr*2 ^�2�8`��psr��-af8:t-K�=3cY��178:���?�-'(8:��1�K]x&p&K7=`8`A�%7'v��8uKQ���{Dxv8|xv��x(�I%7AT~��-tFr3��%7=:%71�L�e�p&K�=`x(�6tFro�2�~,r��6{�8u{-)0�v�@x(�3E�8:�-{%7�<�4%����3{�x ps%7�nx('v%7=T%�A�^Q8:{�x(8:=`=uK]xv8`%��}ps%�=`�3a/�{(�<e�~,r3�-{(8:{IK�E�z@8:{(%7'6)�¡�K���A�'v�-Ew¡}%�'vK7'(8jo�2

¢"£ S�¤3O0¥

Z§¦ ll�¨�©�hjªjª«hjlnm�KMJ&K7'vE��6E�A�%�'�x(r3�}ghji]k:hjlnmnk}E��-17'v�?�}ejxvr3K]x/8:{-��xvr��b'v�-{(��=|x�J&K�{�t�%7afa�����8ut?K]xv�-E�x(%�x(r���H0%7'vJs�-178uK��¬�8:��1no��G+-5n[�5�2

Z"­*® ªjª`¯�°�h|mM±@© ­�² ªjª`³�´�¨(±@h µqejx('FKMz7�-=T17'FK��nxFo&KMJ,K�'FE��-EfA�%�'I17'FK7E��3K]xv� {�x(�3E�8`�6{4K]x p&K�=`x(�6tFr*�G+-5�\7¶32

Z¸· ©�¹7º�l3lhjlnm�¨v¨�©�h µ ² l�¹fKMJ,K�'FE��6E}A�'v%7a�y0��8`zT2�%7A&~�'(%��3E�r��-8`a�A�%7'�1�'vK�E��3K]xv�/{�x(�E�8`�6{�K]x�p&K7=|xv�-tFr*���@�?_�x62�+-5�\7¶b»;��-�*24+-5�\n[�2

Z cd=:�-t�x(�6E�af�?a���-'4x(%�¼T± ²�½ ³]°�´ ² m�h�º�l}¾Q¿Fº7¹ ²�À/Á ³D ¼ ² ¿v±�l3h�¿Fº]ª�gT¿?h ² lT¿ ² ¨�e�H0~,Ã�.Qo��*+-5�\7\32

Z ¼ ² ¹�Ä ² © ² °F¨?³]l�Å ² ¨�©�Ä4ºFµ ² °4¾Q´Yº�°(¹,�@L�x(r���p&.Q��~ÆE�8:z@8:{(8`%��b%�A*.I�(psrcÇe�~,r�� .Iaf�?'v8ut?K��f���3{�x(8`x(��x(�0%7A�psr��?af8ut?K�=cd�3178:���?�-'v{Fo��T+-5�\7532

Z�ÈI² ³]°�m ² gTk*¾IÉ ² ª`¯ Á}Ê&® ©�¨�©Ëº�l�¹�hjlnmfÄ4ºvµ ² °�¾Q´Yº]°(¹��@Lbxvr��/ps%���xv'(%�=��@L�{Dxv�?aÌ�@%�t�8:��xDL�%7A��DcscYcÍe�~,r3�����3{Dxv8|xv��x(�9%�Acd=:�-t�x('v8:t-K�=GK��EwcY=`�6t�xv'(%���8:t cd�3178:���?�-'v{Fo��T+-5�57�wejA�%�'�BD%7��'v�3K7=�_K�_��?'I��%2,+? no�2

Z cd=:�-t�x(�6E�af�?a���-'4x(%�Î ² ©�Ïf³]lnm ² ª«h|m ²�½ ³]°F¨(Ð ²�Ñ hj© ² l�¨(Ð�ºvµ ² °F¨�g ² ªC¨(Ð�º7¯?�*+-5�5�+72

Z�Ê kTÒ ® mn³�gT¿F± ® ¿FÐ9Å ² ¨�©�ÄIºvµ ² °Q¾Q´Yº�°(¹Q�nLfxvr���.Iaf�?'v8ut?K��w.I��xv%7abK]xv8:t�ps%7�nxv'(%�=Gps%����3t�8:=��G+-575n�e�A�%7'4t�%���A��?'v�?�3t?�_3K7_�-'4��%32Y7\�o�2

Z $&%@%7>���¡}��=`x(8:zMK7'(8uK��3=`��;��-�-E��K7tF>wps%���xv'(%�=:�we�ÓÔ8:=:�?L7��+-575�Õ�os{��-=`�6t�xv�-E Ö3'F{DxI'v�������-'�×Ë��_ A�%7'4���nx(�-'(�K]x(8:%7�K�=�A��-E��-'�×K]xv8`%���%�A�.0��x(%�abK]x(8ut�ps%7�nx('v%7=�KMJ&K7'vE/A�%�'s���-{�xsxv��Ø���%n%�>f%�AGx(r3�Q=uK7{�x&¶9L7�-K7'v{Qe��D;�.0p"Ó�%7'v=uE ps%7��1�'(�6{({-��$&�-8 BD8:��13�+-5�575no�2

ÙÚWY¤�Û¸ÜGÝ4Þ�Ü*¤3V�Ü�X0RTÜ

Z +-5@[]53)&¡}8:=:8|xFK�'vL}���?'vzn8ut���K]x H0%7'vJs�-178uK��}^Q��A��?�t��f�4�-{(�-K7'vtFr�ps�-��xv�?'/e�;�;���o�2G�d'v%�BD�6t�xv{08`�@z�%7=:z7�-E<�K]x�xv�?'v8`�6{0K7�3EA����-=�t��-=`=u{?2

Z +-5�\7�]»@\7¶3)*�4�-{(�-K7'vtFrb�-��178:���-�?',K]x&H0%7'F{�>f�IL�E�'v%3ß {&�4�-{(�-K7'vtFr ps�-��xv�?'s8`�w��%7'F{�1�'(���3�*�7^Q�?_3K7'�xva/�-�nx&%7A�psr��?af8ut?K�=cd�3178:���?�-'(8:��132��d'v%�BD�-t�xv{�8`�@z�%7=:z7�-E9_�'v%@t?�-{v{�af%�E��-=`=:8`�313�7{(8`a���=uK]x(8:%7�{�K7�3E9x(r��-'(af%�E�L@�3K�af8ut?{-2�.0_�_%�8`�nxv�-Ebà '(%���_=:�-K7E��?'4%�A�x(r����Y'(%�t?�-{v{&¡�%@E��?=:=`8:��1bK��3E}�@8:a9�3=:K�x(8:%7�}à '(%���_ 8:�á+-5�\7¶�2

Z +-5�\7¶]»@\n[�)��dr�2d^923{�x(�E��?�nx0K��Ew�I�-{(�-K�'FtFr .Q{({(8u{DxFK��nxIK]xQp&K�=:8|A�%�'(�38:K/���3{�x(8`x(��xv��%�A�~��6tFr���%�=`%�17L

Z +-5�\n[6»/_�'v�-{(�?�nx�)d�d'v%�A��6{({(%7'&8`��psr��-af8:t-K�=*cd�3178:���?�-'(8:��1fK]x0H0~4�¸e�K]Ajxv�?'�+-5�5n[�)��3K7af��tFr3K���1��-E�x(%�H0~4HQyQo�2

Z +-5�5� �»@5���)3ÃQ8:{(8|xv8`�310�d'v%�A��6{({(%7'GK]x�yI��8:z7�-'v{(8|xDL0%�Ap&K�=:8|A�%�'(�38:K3�-$&�?'v>7�-=`�-L�e�^Q�?_K�'(x(af�?�nxv{*%�Apsr��?af8ut?K7=�cd�3178:���?�-'(8:��1K��E ¡}�6tFr3K��38:t-K�=*cd�3178:���?�-'(8:��1no�2

Z �����+�»@���)*Ã08u{(8|xv8`��1��Y'(%7A��-{v{�%�'&K�x0yI��8:z7�-'v{(8`xDLb%�AYp&K�=:8|A�%�'(��8uK�����K7�nxvKf$,K�'v�3K�'FK�e��/a/%��nx(r3{Fo�2

+

Page 59: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

��P�����V(RTS�U�V�WYX0¥

Z $&%@%7>T)��T27�@>�%71��-{�xvK7E9K��3E9��2���%�{�x(=:��x(r@J,K�8`x(�����v¡}��=`x(8:z]K�'v8:K7��=`�sA��?�6E��3K�tF>�t�%7�nxv'(%�=7×�K7�3K�=:L�{�8u{�K7�3E/E��-{(8`1��*� �QÓÔ8:=:�?L7�psr�8utFr��-{�x(�-'-�3�n[�9_3K�1��-{�eD+6575�Õ�o�2

Z $&%@%7>T)��T2n�@>7%�17�-{�xvK�EG�*�v�d'v%�{(�-{v{Dxv�?>@��8:>n>���e�����HI%�'(J&�?1�8:K7�o��7~�K�_38`'d�Y����=:8:{(r��?'F{-�7~�'v%7�E�r��?8:a<��¶7 �� _3K�1��-{4e���7����o�2�@�6t�%7�E��6E�8|xv8`%��*�3¶�\7��_3K�1��-{�e�7�7��¶�o�2

Z ¡}%�'(�-'sxvr3K��á+6�7�0BD%7��'v�3K�=G_3����=:8:t-K]x(8:%7�{

Z Õ/�%@%�>�tFr3K�_�x(�?'F{

Z cYE�8|xv%7'4%�A�¶f{�_��-t?8:K7=�BD%7��'v�3K7=�z�%7=:��af�-{

Z ¡}%�'(� x(rK���+6����_����3=`8ut?K�x(8:%7�3{IK�x48`�nx(�-'(�K]x(8:%7�K�=*t�%���A��?'v�?�t��-{

���?��{(�?_3K7'vK�x(��_��3��=`8ut?K�x(8:%7�w=`8u{�x A�%�'IE���xFK�8:=:{-2

����Ü�XIS�¤����ÛYÜ�IXIW�U�Ü��DÜ�R�U�PI¤3Ü�¥

Z �(.0�3K�=:L�{�8u{,K��3E�ps%���xv'(%�=T%�A�^08u{Dxv8`=:=uK]x(8:%7��ps%�=`��af�3{v���p&�0����. ß \n[@���Y'vK7r3K����@�-_�x�+-5�\n[�2

Z �(~�%]J,K�'FE�{G8:��xv�?1�'vK�x(8:��10E��6{�8:17�9K7�3E9t?%7�nx('v%7=�)*y0{(�&%�A�A�'v� �n���?�t�Ln×ËE��?_��?�3E��-�nx�xv%n%�=:{�A�%7'�t�%��nx('v%7=:=:K7��8`=:8`xDL K7�3K�=:L�{�8u{(�3��d'v%�t��6{({4�@L�{�x(�?ab{4cY��178:���?�-'(8:��1<e��&��cso ß 5�+�p&K��3K�E�K���.0��1324+65753+72

Z �(^QL@�3K�af8ut?{�K��3E/ps%7�nx('v%7=n%�A3^Q8:{�x(8:=:=:K�x(8:%7�fps%�=`�3a/�{�×G.Ôps'(8`x(8ut?K7=@�@�3'(z��?L���� ¦(­ ¾����˨ Á]À µ�³]¨�h ®�À Î���� Ê�� Î���� ���7�¡�K7'(L@=uK��3EG��.0_�'-24+6575n

Z �(�I%7���3{�xba9��=`x(8:z]K�'v8:K7��=:��t�%7�nxv'(%�=4�3{�8:��1�� �Úa/�?x(r�%�E�{f»§.I�3K7=`L�{(8:{-�&E��-{(8`1��ÆK7�3E"���3E��3{�x('v8uK�=0.0_�_�=:8:t-K]x(8:%7�{(�3����@z@8|xv�-E<{�r3%7'(x,t?%7��'F{���K�x�+6575�¶�cY��'(%�_�6K��}ps%7�nx('v%7=�ps%���A��?'v�?�3t?�/e�J48|xvr}��23��%�{�x(=:��xvr@J&K78|xv�6o�������=:L�+-5�57¶�2

Z �����nxv�?'FK7t�xv8`%��3{&��?xDJs�-�?�w_�'v%@t?�-{v{4E��-{(8:17�<K��3Ewt�%���xv'(%�=:�3�3p&�I����.9ß 5�¶����d'FK�rK���.I��12 ×D�@�-_�x-2:�*+-5�57¶32

Z �����3_���x�×"!Q��xv_���x ps%7�nxv'(%�=`=uK���8:=:8|xDL�.0�3K�=:L�{�8u{(�3���4�?1�=`�-'(a$#%�xv�7��Ã%#K7{�x(�?''&K7{-���@J&�-E��-�*�(! t�x624+-5�5� 32Z �(^QL@�3K�af8ut?{4K7�3E t?%7�nx('v%7=G%7A�E�8u{�x(8:=`=uK]xv8`%��<t?%7=:��af�3{&×Y. x(��x(%7'v8uK�=G8:��xv'(%�E��t�x(8:%7����Tg Á]À µ3³M¨�h ®�À Î9hu¨�©�hjªjª:º]©�h�³]l�º]l�¹¾�¯�¨�³�°?¯�©�h�³]l)�+*-�¡�K�K7{�x('v8:tFrnx-��H0��x(r3�?'v=:K7�3E�{-�3�@�?_�x62I+-5�5n[�2

Z �v���?=`Aj×�%�_�x(8:af8`�-8`��1�t?%7�nx('v%7=�)<x(r��}af8u{({(8:��1�=`8:��>§��?xDJs�-�?�Ô{Dxv�-K�E�Ln×Ë{�xvK�x(�<%7_�xv8`af8:�-K�x(8:%7�ÔK��3EÆt?%7�nx('v%7=u���&�d'v%@t?�-{v{�@L�{�x(�?ab{4cY��178:�����-�?'v8`��1<e��&��cso47�7������¬��?L�{�x(%7�3�7�3ps%7=:%7'FK7E�%���7��=:L 7�7�7�32

Z �(�Y=:K7�nxDJ48:E���t?%7�nx('v%7=T×dxv%]J&K7'vE3{&Kb{(L�{Dxv�?abK]xv8:t�_3'(%�t��6E���'v�-�3��cd��'v%7_��-K7�<�@L@af_�%�{(8`��a %7�}t?%7af_���xv�?'(×ËK78:E��6E�_3'(%7×t��6{({,�-��178:���-�?'v8`��1<e�c&�3p&.0�scIß:+6�o���~,r����0K717������HI�?x(r��-'(=uK��3E3{?��¡�KMLw��7�n�2

Z �(;3�?�6E��3K7tF>§t�%7�nxv'(%�=,x(r��-%7'vL�)�.0�Ô%]z7�-'(z@8:�?J K7�3EÔt�%������-t�x(8:%7�3{/xv%���8:%@tFr3�?af8:t-K�=0{(L�{Dxv�?ab{fxvr��?%�'(L����4[6xvrÔ����xv=�2�@L@af_*2�%7�<$&8`%�tFr��-af8:t-K�=*{(L@{�x(�-ab{&x(r��-%7'vL72�.Iz��?'v%]L7��HI%�'(J,KML7�T+M[M×�7����������7�7��

Z��ps%7�nx('v%7=G{�x('v�3t�xv��'v� E��6{�8:17��)�ÓÔrK]xI{�r3%7��=uE�J&��t�%���xv'(%�=��@af�-K�{��3'(��K��3E�abK���8:_���=uK]xv�-,6����;�8:'v{�xI.4A�'v8:t-K���ps%7�nx('v%7=�ps%7��×A��-'(�-�3t�����p&K�_���~�%]J4���3�@%7��xvr}.4A�'v8:t-K����7¶�×Ë�n�9^Q�-t?�?a���-'0��7��¶�2

. W�/ Ü W�U+0IÜ*¤ÆS�R�U�V21IV�U�VDÜ�¥

Z psr3K78`'�%�A�xvr��4E�'62 8:��132 t�%�afa/8`x�xv�?�sA�%7'�x(r3�&;K7t��3=|xDL�%7ATpsr��?af8u{Dxv'(L�K7�3E/psr3�?af8:t-K�=�~��-tFr���%�=`%�17L�H0~4�Íe�+-57\�5]×F+-5�57¶�o

Z psr3K78`'4%7A�x(r3��yI��8:z7�-'v{(8|xDL t�%7afaf8`x�x(�-��A�%7'IE�'62 8`��124eD+-5�5���×0+-5�575no

Z ;�%����3E�8:��1btFr3K78`'4%7A�x(r3��HI%7'FE�8ut��d'v%@t?�-{v{Ips%7�nx('v%7=GÓ�%7'v>@8`��1/17'v%7�3_�e�+-5757 �×F+-5�57\�o

Z $&%�K7'vE�a/�-a9���?'4%7A�H0%7'vJs�-178uK�� .Qt?K�E��?a�L�%�A�~��6tFr���8ut?K�=���t�8:�?�3t?�-{�e�H0~,Ã�.Qo�eD+6575nM×4+-5�575�o

Z �I�6K7E %�A�H0~4HQy3����DH0~4cY;&ß {I{�x('v%7��1/_%�8`�nx0t?�?�nx(�-'48`�<_�'v%�t��-{v{,{�L�{�x(�-af{,�-��178:���-�?'v8`��1}e��Y�4!���~Io eD+6575� �× o��

Page 60: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Z psr3K78`'4%7A�H0~4�Q{,A����3E�e�+-5�57Õ9×s��7�n7o

Z $&%�K7'vE�a/�-a9���?'4%7A��Y'(%7A��-{v{�%�'�A�%�'(��a¸HQ~4�¸eD+-5�5�+?×v+65757¶no���psr3K�8:'4%�A��d'v%�A��-{v{(%7'(A�%7'v��a¸H0~4H0y eD+-5�5n[M×�7�7��+Mo��

Z $&%�K7'vE�a/�-a9���?'IK�x4x(r���;K7t��3=|xDL�%7A�tFr3�?af8:{�x('vL�K7�3E��38`%�=`%�17L�H0~4HQy eD+6575�Õ]×F+-575�5�o��

Z �I�6K7E %�A�^0�-_3K�'(x(af�-��x4%7Adpsr��-abt�8ut?K�=*cY��178:���-�?'v8`��1fH0~4HQy eD+6575�5]× o�2

Z ¡}�-a9���?'4%�A�x(r3��HI%7'vJ&�?178uK�� '(�6{��6K�'FtFr�t�%����3t?8`=G�?Ø@_��?'(xI���?xDJs%�'(>�e�+-575�\]×D�����7o

Z ¡}�-a9���?'4%�A�x(r3���7��'vLbA�%�'IHI%7'F{(>��IL�E�'v%3ß {4$s8:'v>7�?=uK��E�.IJ,K�'FEG�G+657575�×

��¤�W��vÜ�¥n¥@V�WYXIS � ¢ R�U�V21IV�U�VDÜ�¥

Z�� ¹�hj©Ë³�°&%7A�.0��x(%�afK�x(8ut?K}e�+-575�Õ]×D�����7o�2¡}�-a9���?'IcYE�8|xv%7'v8:K7=*$s%nK�'FEG)�*± ²�À k � l@m���k�º]lT¹�Ä&°v³-¿ ² ¨v¨�hjl@mbejA�'v%7aÌ��7�3+6o�2¡}�-a9���?'I.0E�zn8u{(%7'vL���K����-=�) ��± ²?À k � lnmnkIgG¿�h�ejA�'v%7a ��7�n7o�2¡}�-a9���?'IcYE�8|xv%7'v8:K7=*$s%nK�'FEG)��³ À µ ® ©Ëk���± ²?À k � lnm7lnmnkIe�A�'(%�a �����7o�2

Z ¡}�-a9���?'0%7AY.Iaf�?'v8ut?K��}���{Dxv8|xv��x(�/%�A&psr��-af8:t-K�=�cY��178:���-�?'F{�e�.0�(psr3cso��T~,r3�����3{�x(8`x(��xv��%7AYcd=:�-t�xv'(8ut?K7=�K��E�cd=:�-t�×x('v%7�38:t�cY��178:���-�?'F{�e��DcYcscso��HI%�'(J&�?1�8:K7�}psr3�?af8:t-K�=��@%�t�8:��xDLáe�H0¬��3o��THI%7'vJ&�?178uK����@%�t?8`�?xDL�%�AY�Y'(%7A��-{v{�8:%7�K�=*cd��×178:���-�?'F{ e�HI�D;�o���HI%�'(J&�?1�8:K7� ����xv'(%�=`�-��a �@%�t�8:��xDL�e�H0�s;�o�2

Z psr3K78`'vabK���%7A !Q'v1�K��38`�-8`��1bps%7afaf8|x(x(�-�QA�%�'4H0~,�.���?af8`�K�',%7��psr��?af8ut?K7=TcY��178:���-�?'v8`��1� ���L7�6K�'F{Y8:�wH0%7'vJ&KML��~�'(%��3E�r��-8`a<��.I�31324+-5�\7532

Z psr3K78`'vabK���%7A�8:�nx(�?'v�3K�x(8:%7�3K7=�_3'(%�17'FK�a¸t�%�a/af8`x�xv�?��A�%7'I{(L@af_%n{�8:��a �&��c�×�cs�3p&.Q�Yc0ß 5@[@��~�'v%7�3E�r3�?8:aw��H0%7'vJ&KML��¡�KML�+6575@[@2

Z ¡}�-a9���?'�%�AY8:�nx(�-'(�3K�x(8:%7�3K7=�_3'(%�17'FK�aÌt�%7afaf8`x�x(�-�bK��3E 3]%7' {��6{({(8`%���tFr3K78`'vabK��}A�%�' K =uK�'v17�9�@��a���-'�%�AY8:�nx(�?'v�3K�×x(8:%7�K�=*t�%���A��?'v�?�t��-{-2

Z ¡}�-a9���?'I%7A�cY��'(%�_�6K��<;��6E��?'FK]xv8`%�� %7Adpsr��-af8:t-K�=�cY��178:���?�-'v{,J&%7'v>@8`�31�1�'(%���_ %���ps%7af_���xv�?'(×Ë.08:E��6E�psr��?af8ut?K�=cd�3178:���?�-'(8:��1<eD+-5�57�9×Ôo

Z ¡}�-a9���?'&%�A�cY��'(%�_�6K���;3�-E��-'vK�x(8:%7��%7A�psr��-a/8ut?K7=�cY��178:���-�?'F{YJ&%7'v>@8`��1917'v%7��_b%�� ^Q8:{�x(8:=`=uK]xv8`%�� K7�3E�.0�3{�%�'(��x(8:%7�eD+6575�\�×Ço

Z���²�À ¯ ² °9³� ² i]º]ª ® º]©�h�³]l�¿F³ À�À hj©�© ²F² ¨sµ�°v³D ² ¨v¨?³�°F¨�±�h µ�,~��?=:�?abK�'v>wps%�=`=:�?1��/e�+-575���o������=:� &K/~��6tFr���8ut?K�=*y0��8:z7�?'F{(8|xDL��.I��x(%7abK�x(8ut�t�%7�nxv'(%�=�e�+-5�5n[�o���*���3E<y0��8`z��?'F{�8`xDL7��.0��x(%�abK]x(8ut�t�%��nx('v%7=�eD+657575no�2

Z c�Ø@xv�?'v�3K�=&c�Ø�K�af8:���?'/K]x9xvr��<yI��8:z7�-'v{(8|xDL�%�A ^QK7'��6{/��K7=:K�K�a<��~�K7���-K7��8uK���K]x/x(r�'v�?� %�t?t?K�{�8:%7�{?)b¡�K7'vtFrÔ+657\7\3�.I_3'(8:=d+-5�\75�K��3E<¡�K7'vtFr�+-5753+72

Z �0² i6h ² ´ ² °IÂ�³]° � .I�(psrc �2:��.I��x(%7abK�x(8ut?K���p&K��3K�E�8:K7���2G%�A0psr��?a<2bcd�3132:��psr��?a<2bcd�3132f�4�-{-2b^0�6{?2}e�yQ¬�o��psr��-aw2 cd��12���t�8�2`�&��ps%�af_*2�K��Eápsr��-a<2 cd�317��12`�*���EG2�cd�3132 psr��-aw2 �4�-{-2`�����nx-2��2*%�A0ps%7�nxv'(%�=��*���nx62��32%�A0.QE�K�_�x(8:z7�<ps%��nx('v%7=sK7�3E��@8:17�K�=,�d'v%@t?�-{v{�8:��1�����nx-2á�2�%7A0�4%7���{DxbK��3E�HI%7�3=`8:���-K7'fps%���xv'(%�=����DcscYc�~�'vK7�3{-2%�AI.0��x(%�aw2�ps%7�nxv'(%�=���H0K]xv8`%��3K�=,��t�8:�?�t���;�%����3E�K�x(8:%7�Çe�yQ��o����2*%�AI�Y'(%�t��6{({9ps%��nx('v%7=����@L�{�x(�?ab{�K��3Eqps%7�nxv'(%�=*�?x�xv�?'F{?2

NwÝ&U�Ü*¤XIS �/ÜGÝ4S / V(XIÜ*¤"S�U§OIW4R�U�Wd¤�S �fO0V(¥n¥nÜ*¤�U@S�U�VDWsX0¥

Z ¬���'(x,cY'(8:>�� #K7171���=`%�a<�@�@ps%7�3{(8u{Dxv�?�nx,t?%7�nx('v%7=T{�x('v�3t�xv��'(� af%�E��?=:8`�31/J48`x(r<K�_3_�=`8ut?K�x(8:%7��x(%bE�8u{Dxv8`=:=:K�x(8:%7�<t�%���xv'(%�=:�3�&.I��%�.I>]K�E��?af8��3;�8`��=uK��EG�3^Q�-t�24+657\�\�2Z psr3K7'(=:%�x(x(�&�@x(���/HI8:�?=u{��-�*�7�7¡���=|xv8`z]K7'(8uK���=:�Y8uE��-��xv8|Ö�t?K]xv8`%��9K��E9t�%��nx('v%7=n%�A3K�����Ø�_��?'v8`af�?�nxFK�=@E�8:{�x(8:=:=:K�x(8:%7��t?%7=:��af�J48`x(r<r��-K�x4_���af_3���^Q~4�9�^Q�?��abK�'v>T��¡�KML�+65757�32

Z .I�E��?'F{4¬�K�'v=:{�x(' #%7a<���7¡�%@E��?=:=`8:��1f%�A�_3K7tF>��-E ��6EwE�8:{�x(8:=`=uK]xv8`%��wt?%7=:��af�3{v���p&~4�����@Js�6E��?���3.I_�'v8:=d+-5�5�+72Z ��%7r��<^0�-=`8utFr*���7~,r���'v%7=:� %7A��?Ø�t��-{v{4abK��38`_��3=:K�x(�-Ewz]K�'v8uK���=:�-{&J48`x(r�8:��t�%���xv'(%�=*{�L�{�x(�-a E��?z��?=:%7_�af�-��xF���3y0��8:z�2Y%�A�@L�E����-L7�3.0�3{�x('FK�=:8:K3�����?_�x62I+-5�5� e�J4'v8|x(x(�?�}{�xvK�x(�?af�-��x4%���=`L�o�2

Page 61: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Z �4%��3K�=uE�%�à/2�ps%7'v'v�-K����@ps%7�nx('v%7=*E��6{�8:17�w%�A�r��?x(�?'v%71��?���-%7�3{,K7�?�?%7x('v%7_�8ut E�8:{�x(8:=:=:K�x(8:%7�<_�=uK��nxv{v���3^ ~4���^0�-��abK�'v>��! t�x624+-5�5��2

Z �nxv�?_�r��-�bÓ�K7=:{(r*�������nx(�-17'FK]xv�-E/E��-{(8`1��b%�AGtFr��?af8ut?K7=3J,K7{�x(�4J,K]x(�-'�x('v�-K�x(af�?�nxY{(L�{Dxv�?ab{(�3�7��af_��?'v8:K7=�ps%7=:=`�-17����y0¬f�����=`L�+-575�¶�2

Z à r3K�{({vK�� .�2I¡}��'FK7E*� �v�4%7���{Dx}a9�3=|xv8`z]K�'v8uK���=:��t?%7�nx('v%7= %�A/8`�E��3{�x('v8:K7=�_�'(%�t?�-{v{��6{?)".�E�8:{vt�'v��xv��×�x(8:a/�áa���=|xv8|×%7��BD�-t�xv8`z���K�_�_�'v%�K�tFr3���@yI�38`z��?'F{�8`xDL�%�A *�-8:t?�-{�x(�?'6��y0¬f� ! t�x-2,+6575���2

Z ��%7r3K7�9���?�3{vK�'6���(��K�'FK�af�?x('v8:t�af�?x(r�%�E�{�A�%7'�%�_�x(8:abK�=uK��3E�'v%7�3�3{Dx�t�%��nx('v%7=u��� &.I��%�.0>]K7E��-a/8�y0��8`z��?'F{�8`xDL7��;�8:��=uK��3EG�;��-�*24+-5�57Õ32

Z �Q83p&K7%3�G�Fps%��nx('v%7=�{�x('v�3t�x(��'v�s{(�?=:�-t�x(8:%7��A�%�'�tFr3�?af8:t-K�=@_�'v%�t��-{v{(�-{*�{�8:��1 8`��_3��x�×Ë%7��xv_���x�t�%���xv'(%�=`=uK��38`=:8|xDL�K7�3K�=:L�{�8u{(�3�yI�38`z��?'F{�8`xDL�%�A�c�Ø��-t?��xv�?'6��y0¬f��¡�K7'vtFr�+-5�57Õ�2

Z ��%7���?'(x�*�3E�=uK�1��7�*��ps%7�nx('v%7=:=uK���8:=`8`xDL9K7�3K�=:L�{�8u{�%�AT8`�E��3{�x('v8:K7=�_�'v%@t?�-{v{��6{(�3�7cd8:�3E�r3%]z7�?�fyI�38`z��?'F{�8`xDL�%�A*~��-tFr��3%7=:%717L��HI�?x(r��-'(=uK��E�{?��H0%]z7�-a9���?'�+-5�5n[@2

Z ��K7afK7'vK4^�27psr��?�3�?'vL7�T�(�Y'(%�t��6{({�t�%7�nxv'(%�=`=uK���8:=:8|xDL K��3K7=`L�{(8:{��3{�8:��1I=:8:���-K7'�K7�3E���%���=`8:���6K�'�%�_�x(8:af8:{vK]xv8`%��3���6��af_�-'(8uK�=ps%7=:=:�?17����*%7�E�%7�*���K7�*2,+-575�\

Z ~,r�%�afK�{�cI2*à ��x�xv8`�317�?'6�0�v¡}��=`x(8:_�=:�f{�x(�6K7E�L�{�xvK�x(�6{�8`�áK��-�?%�xv'(%�_�8ut9K��E�'v�-K�t�x(8:z7�/E�8u{Dxv8`=:=:K�x(8:%7�3�3��cY~4�9������'v8:tFr���������f+-5�57\�2

Z ���?�3{wcd'v8`>Ô�QK��3{(�?�*� �(�Y=:K7��xwJ48:E���E�L@�3K7af8:t�{�8:a9�3=:K�x(8:%7� K7�3E t?%7�nx('v%7=Q%�A�tFr��-af8:t-K�= _�'(%�t?�-{v{��6{(�3�0~��6tFr���8ut?K7=yI�38`z��?'F{�8`xDL�%�A�^0�-��abK�'v>T� *L@��17�@L����7���3�b+-575�\�2

Z ¡�K�E�{IcI2�0K��31�{�x('v��_*�Y�F�nx('FK]xv�?1�8`�6{&A�%7'I8:�3E��3{�x('v8uK�=*a���=|xv8`z]K7'(8uK���=:��t�%��nx('v%7=G×YJ48`x(r�K7_�_�=:8:t-K]xv8`%�� xv%�_�%]Js�-'4_�=:K7�nxt�%��nx('v%7=u����.0K7=`��%7'v1/y0��8:z7�?'F{(8|xDL���^0�-��abK�'v>���;3�?�á+-5�57532

Z ~,r�%�afK�{0�T2T$&'(8:�3{(a/�6K7EG�Y� *8:af8|xF{0%7Adt�%7�nxv'(%�=`=:�-Ew_��?'(A�%7'vafK7�3t���),ps=:%�{(8`�31fx(r���1�K�_<z@8uKb%7_�xv'(8:af%�{vK]xv8`%��3���3y0��8:z�2%�A�HI�-J&t-K7{�x(=:�7��.I�{Dxv'vK7=`8uK���^Q�-t724+-575�5 e�J4'(8`x�xv�?�}{�xvK]xv�?af�?�nxI%���=`L�o�2

Z ��K7�3E��?'bà 'v%n�-���?�E�8 BD>T���v�d=uK��nxDJ48:E���t�%���xv'(%�=`=uK��38`=:8|xDLáK��E�{�x('v�3t�xv��'vK7=Y%�_�x(8:af8`�6K]x(8:%7�§%�AI_�=uK��nxF{9J48`x(r§'(�6t�L�t�=:�-�3�yI�38`z��?'F{�8`xDL�%�A�.Iab{�x(�?'FE�K7aw�¡�K�'FtFrw7�7�7�32

Z ~�%7'v��-���IKMz@��.I�3E��?'F{��-�*��� !Q_�-'vK�x(8:��19E��6{�8:17��K7�3Eb%�_�-'vK�x(8:%7�b%�A*_3'(%�t��6{({Y8`�nxv�?17'FK]xv�-EbE�8u{�x(8:=`=uK]xv8`%��3���@~��6tFr���8ut?K7=yI�38`z��?'F{�8`xDL�%�A�^0�-��abK�'v>T� *L@��17�@L���HI%]z7�-a9���?'I������2

Z �@r��-r��-K�K7E�¬�%nK7tFr3K7=`8��Q�v^0�-z7�-=`%�_�af�?�nx9%�AI_3'(%�t��6{({9{�L@�nx(r��6{�8u{9x(%@%7=u{�A�%�'9'v�-K7t�x(8:%7�qK7�3Eq{(�?_3K7'vK�x(8:%7�á����xDJ&%7'v>�{(�3�yI�38`z��?'F{�8`xDL�%�A�ÓÔ8|xF{�z]K�x(�?'F{('vK7�3EG�3�@%���x(r}.4A�'v8ut?K�����������7�7�7¶we�J4'v8`x�x(�-�}{DxFK]x(�-af�?�nxI%7��=:L�o�2

Z $&8`'v178`x�xFK}¬�'(8u{�x(8uK��3{v{�%��*�I�v�d�D^ t?%7�nx('v%7=:=`�-'v{�E��-{(8`1��áK7�3E��?z]K�=:�3K�x(8:%7�3�3��psr3K7=`af�?'F{�y0��8`z��?'F{�8`xDL�%7AI~��6tFr���=:%7=:%717L���@J&�-E��-�*��.I�317�3{�xQ����7¶�2

�������� ���������������� ���������������� �������!" ����#��$&%'$&(*) +6o0^QK71 �BD���31 �n��8u{Dx6� �'!Q��=`8:�����6{Dxv8`abK]xv8`%��}8`����%7��=:8:���-K7'{�xvK�x(�?×Ë{(_3K7t?��af%�E��?=u{ J48|xvr K�_3_�=`8ut?K�x(8:%7�Ôxv%§t-K]xvK7=`Lnxv8:t�t�'FK7tF>@8`�31����I^Q8:z�2 %7A9cd��12¸psL@���?'v����xv8:t-{?��+-575���2 7o����?x(�-'��8`��1n{DxFK7EG�I��¡}%�E��?=:8:��1qK��3EÆa���=`x(8:zMK7'(8uK��3=`��t?%7�nx('v%7=I%7A�r�8`1�rÔ_�'v�-{v{���'v�}K���xv%�t�=uKMz7�}'v�-K7t�x(%�'v{/A�%�'�_%�=`L@af�?'v8:�-K]xv8`%��Æ%�A�?x(r��-���-�3�&^Q8:z�2"%�A�cd��12ÔpsL@���?'v����xv8:t-{?�Q+-5�5��2"¶�o/cd'v=:8`��1á.0K32"��%7rK������6{({(�?�����v�@L@�nx(r3�-{(8:{/%�A�E�8u{({(8`_K]x(8:z7�w%7��x(_���xA��-�-E��K7tF>}t�%���xv'(%�=`=:�?'F{-)&.0_�_�=:8:t-K]x(8:%7��x(%�af�6tFr3K���8ut?K7=�{(L�{Dxv�?ab{(�3��^Q8:z�2Q%�AYcY��132�psLn���?'v���?x(8ut?{-�T.0_�'v8`=&+-5�5n[@24 @oI$&�?�nxv��92Y��K��3�,+4{?���v�@%�=`8uE�{/af%]z7�-a/�-�nxfK7�3E�t?%7�3t?�?�nx('FK]xv8`%��q_�'v%�Ö3=:�-{/8:�"t?%7=:��af�"{(=`�3'('vLá'(�6K7t�xv%7'F{(�3�d^0�-_�x-2"%�A�psr��?af8ut?K�=cY��178:���-'('v8`�313��¡�KML +6575n[�2���od¬��@��x&$,K7>n>��7���(c�Ø�_��?'v8`af�-��xFK�=3K7�3Efxvr��?%�'(�?x(8ut?K�=�{Dxv�3E�Lf%�A*'v�.-��Øft?%7�3E��?�3{vK]xv8`%��3���n^0�-_�x-2%7A,�I��A�'v8`1��?'FK]x(8:%7�áK��E�.08`'fps%7�3E�8`x(8:%7�38`��1��^Q�-t72�+-5�5n[�2�Õ�o !Q=uKMz��@=:��_�_�r3K7��13�Q� !Q��'(%����3{�x9t�%��3{Dxv'vK78`�3�-E���%7��=:8:���-K7't?%7�nx('v%7=�K7�3E�rnL@��'v8uE�t?%7�nx('v%7=�)�$,¡}�Ë×�K7�3Ef¡��&pY×Ë�3K7{(�-E�{DxFK]xv��×�A��?�-E��3K7tF>�{vtFr��?af�6{(�3�7^0�-_�x-2�%7ATcY��132�psLn���?'v���?x(8ut?{-��^Q�-t�2+6575�\�2 [�o�à �-=`�-8`�q¡q2�E���¬�%@�?8 BD�?'6�0�vcd���-'(1�L}�./�t�8:�?�nx�%�_�-'vK�x(8:%7�á%�A4E�8u{Dxv8`=:=:K�x(8:%7��t�%�=`�3a/�{�K��3EáK<'v�-K�t�x(%�'�K�_�_3=`L@8:��18:'v'(�-z7�?'F{(8`��=:�Qx(r��-'(af%�E�L@�3K�af8ut?{v����¡�KML 7�7�n�2

Page 62: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

� Ü*S�R 00V(X����ÆÜ�¥nÞ�WYX0¥@V � V"�(V�U�VDÜ�¥�0x(�6K7tFr�x(r���t?%7��'F{��f~4¬��d +67���d'v%�{(�-{v{Dxv�?>@��8:>@> A�%�'�{Dxv�3E��-��xF{�8:��xvr���]�3E�L7�6K�'�%�AIpsr��?af8ut?K7=dcd��1�8`���-�?'v8`�31wK7�3E

¶7'vE L7�6K�',%�A�_���x('v%7=:�?�3a �?��1�8`�3�?�?'v8:��132y0�3E��-'(1�'vK�E��3K]xv�st?%7��'F{���)��@�D¬�7�����Q�d'v%�t��-{v{�ps%7�nx('v%7=Ge�K7_�_�'v%MØG2���� {�x(�3E��-�nxv{��-K�tFr9L��-K�'�o�2�����7¶�)�ps%7��'F{��s8:{�xFK���1�rnx

�@Lw�d'v%�A��-{v{(%7',�I�?8:�����Y'(�6{�8:132y0�nx(8:=9+-5�5753)�à 'vK�E��3K�x(��t�%���'F{��qe�K]x ^Q8`z@8u{�8:%7�Ô%7A�cd=:�-t�xv'(8ut?K7=Icd��1�8`�3�?�?'v8:��1no�)� �¶�5�+M[�¡}�3=|xv8`z]K�'v8uK���=:��;�'v� �n���-�3t�L

.0�3K�=:L�{�8u{�e�K7_�_�'v%MØG2&+6�f{Dxv�3E��?�nxF{,�-K7tFrwL7�6K�'�o�2�&K�=u{�%/xv�-K7tFr x(r3��_�'(%�t?�-{v{4t�%7�nxv'(%�=�_K�'(x�e�K���%7��x0Õ/=:�-t�x(��'v�-{Fos%�A�x(r���t?%7��'F{����@�D¬�7��+-�f�@�-_3K�'FK7{�BD%7�3{�x(�->@��8`>@>T��K��3E �

1�8`z��QK7�%���x&¶9=`�6t�x(�3'(�6{d%7� E�L@�3K�af8utIaf%�E��?=:=`8:��1fK��3E�{�8:a9��=uK]xv8`%���K7{s_3K�'(xs%7AGx(r�� t�%���'v{(�Q�@�D¬�7�7Õ@[��d'v%�{(�-{v{���x�A�%7'vaf8`�3132�fK�=u{(%qt�%�xv�-K�tFr�xDJ&%�af%@E���=`�6{fA�%7'�x(r����]x(rÔL��-K�'�{(_��-t�8uK�=:8:�-K]xv8`%��*)��@�D¬�7�7.0��.QE�z]K��3t?�-EÆ_�'v%�t��6{({bt?%7�nx('v%7=IK7�3E

���D¬���7.����@_�6t�8uK�=Gxv%7_�8ut?{�e�E�8u{Dxv8`=:=:K�x(8:%7�o�2� ¤�S�O0P0S�U@Ü�O�Ô¤� �nX����� �)0�������¥�U�PQOIÜ�XsU�¥

+724~,r�%�'I¡}�DB�E��-=`=�� � ¨�©�h À º�©Ë³�°F¨dÂ�³]°,µT°(³-¹ ® ¿�©4¿F³ À µ�³]¨�hj©�h�³�l�hjlá¹]hu¨�©�hjªjª:º]©�h�³]l�¿v³�ª ®�À l�¨��3HI%]zT2,+-5�57�32�24cd=:=:8`��1fÓ 23�nK7t?%7�3{(�?���g�© ® ¹�h ² ¨9³�l�¹ Á lTº À h�¿�¨/º�l�¹ ¿v³�l3©�°(³]ª�³DÂ�¹]hu¨�©�hjªjª`º]©�h�³]lq¿F³]ª ®�À l3¨F��^Q�-t72I+-5�5�+�2¶�24¡}%�'�xv�?���I%]z�EG��g© ® ¹]h ² ¨�³]lq¿F³]l©�°v³]ª*¨�©�° ® ¿�© ® ° ² ¨ ² ª ² ¿?©�h�³�l�º]lT¹w¹ ² ¨�h|m7lq³DÂ�°(³7¯ ® ¨�©4¹ ² ¿ ² l3©�°(º�ª«h�� ² ¹<º�l�¹ g Ñ Î ¿F³�l �©�°(³]ªjª ² °F¨��(! t�x624+-5�5��2

324¬��@��x4Ó 23¡�K�x(r�8u{��-�*� ¦ l3© ² m7°(º�© ² ¹�¹ ² ¨�h|m7láº�l�¹�¿F³�l3©�°(³]ª�³�Â0± ² º]© ² É@¿v±3º]lnm ² °�l ² ©�´Y³�°(ÐM¨��3.0_�'(8:=d+6575� 2��24cd'v8:>�.�2�Ó�%7=�����g© ® ¹]h ² ¨�³�l�¿F³]l©�°v³]ª�³�Â�hjl3© ² m7°(º�© ² ¹ µTª`º]l©�¨��3����=:L�+-5�5� 2Õ�24cdz]Kb���7'(�-�3{��-�*��g© ® ¹]h ² ¨9³]l�³Fµ�©�h À º�ª�³Fµ ² °(º]©�h�³]l�º]lT¹�¿F³]l©�°v³]ª�³�Â�¯vº�©Ë¿F±�¹]hu¨�©�hjªjª:º]©�h�³]lq¿F³]ª ®�À l�¨���.I�31324+-5�5� [@24��2����x�xv�?' ����3E�{�x(' #%7a<�Tg© ® ¹]h ² ¨�³]l�°v³7¯ ® ¨F© À�® ª|©�hji]º]°�h�º�¯�ª ² ¿F³�l3©�°(³]ª�³�Â�¹]hu¨�©�hjªjª`º]©�h�³]lq¿F³]ª ®�À l�¨��3.0��132,+6575� 2\�24��%7r���pQ23¡}%�'(�3E*�3Î Á lTº À h�¿�¨9º]lT¹�¿F³]l©�°v³]ª�³�Â�hjl3© ² m�°(º�© ² ¹QµTª`º]l©�¨�´�hj©�±}° ² º�¿�©�³]°F¨���.0_�'-24+6575�Õ�25�2 �Q8:��1���r3K7%3�Tg�© ® ¹�h ² ¨9³]l À ³6¹ ² ª«hjlnm<º�l�¹w¿v³�l3©�°(³]ª�³�Â9¿F³]l©�hjl ® ³ ® ¨�¯�h�³�© ² ¿F±@l3h�¿Fº�ª�µT°(³-¿ ² ¨F¨ ² ¨��3.I�31324+-5�57Õ32+6��24.&x(=:��pQ2Tpsr3'(8u{Dxv8:K7�3{(�?�*�Tg�© ® ¹�h ² ¨9³]lá³vµT©�h À º]ª�¹ ² ¨�h|m�l�º]lT¹ ³Fµ ² °(º]©�h�³]l�³DÂ�hjl3© ² m7°(º�© ² ¹w¹]hu¨�©�hjªjª:º]©�h�³]lqº]°�°(º�lnm ²�Àb² l3©�¨F��nK��*2,+-5�57\32

+�+724¬&BD��xv8`=��0KMz@'(����g© ® ¹]h ² ¨�³�l�¿F³]l©�°(³�ªjª`º7¯?hjª«hj© Á º�l�º]ª Á ¨Fhu¨�º�l�¹w¿F³]l3©�°(³�ªT¨F©�° ® ¿?© ® ° ² ¹ ² ¨Fh|m7l3��;��-�*24+-5�57\�2+M�24$&�?'v�3E�ÓÔ8|x(x(17�-�3{-� � É�µ ² °�h Àb² l©Ëº�ªdi ² °�h �s¿Fº�©�h�³�l"³DÂb¹ Á l�º À h�¿<³vµ ² °vº]©�h�³]l"³�Â�¿F³]l3©�hjl ® ³ ® ¨fº�l�¹ À/® ª«©�hji ² ¨F¨ ² ªY¯Fº]©�¿v±

¹]hu¨�©�hjªjª`º]©�h�³]l��^Q�-t724+-5�575�2+6¶�24~�'(��=u{ �K7'v{v{(%7�*��g© ® ¹]h ² ¨�³]lbµTª`º]l©�´�h�¹ ² ¿v³�l3©�°(³]ª|�3.I��12Y����7��2+- 324cdz]K�×ˬ�K�x('v8`���Q�I8:=`af�?���Gg ² µ�º�°(º]©�h�³]lá³DÂ�º�� ² ³�©�°(³Fµ�h�¿ À h|É�© ® ° ² ¨ �/¼3³6³]ª«¨�Â�³�°9º]lTº]ª Á ¨�hu¨9º]lT¹/¨�© ® ¹�h ² ¨�³]l�¯Fº�©Ë¿F±�¹�h�º]©�hjª �

ª`º�©�h�³�l�³vµ ² °(º]©�h�³]l�^Q�-{-2Y��7����2+M��2,��z]K�'I�2��0K7=`z�%7'F{��-� � hjl3h À/®�À̲ l ² °�m Á ° ²���® hj° ²�Àb² l©�¨�hjl�¿F³ À µTª ² É<¹�hu¨F©�hjªjª`º�©�h�³�l�º�°�°(º]l@m ²?Àb² l©�¨��3¡�KML�7�7�3+72+6Õ�24¡�K7'(8:�3{I�T23à %]z]K]xF{�abK7'(>b���nx(�-17'FK]xv�-E %7_�xv8`af8:�-K]xv8`%��wK7�3Ewt�%7�nxv'(%�=��3�@�-_�x-2Y7�7��¶�2+][@24.I�E����};3K�K����6{0ps%7�nx('v%7=:=:K7��8:=`8`xDL�K��3K7=`L�{(8:{,K7�3E<t�%7�nxv'(%�=T{�x('v�3t�x(��'v�-{-�3�@�?_�x-2Y����7¶32+6\�24�I8:=uE��0¬f27cY��17�-=`8:�?�b�d'v%�t��6{({�8:�nx(�?1�'vK�x(8:%7�fK�_�_3=`8:�-E�x(%�x(r��0E��-{(8`1��fK7�3E/%7_��?'FK]xv8`%��/%7ATE�8:{�x(8:=`=uK]xv8`%���t�%�=`��af�3{-��¡�K�'62

����� 2+65�2I�nxFK]x(r38:{0��>7%7�3'vK�{s�0��x(�-'(%nK��-�?%�xv'(%�_�8ut0�3K�xvtFr<E�8u{Dxv8`=:=:K�x(8:%7�*)d;3�-K�{�8:��8:=`8`xDL�K��E %�_�-'vK�x(8:%7�*��¡�KMLw��7�7 32

� W �]¥nP0Þ�Ü*¤�1IV�¥nWd¤ �FWd¤�!+724$�B"��'v� à =`�-afa/�6{DxFK7EG� Ê µ�©�h À º]ª ³Fµ ² °(º�©�h�³�l ³�Â}hjl3© ² m�°vº]© ² ¹}µ�°v³-¿ ² ¨v¨ ² ¨?k g© ® ¹ Á ³�lÔ± ² º]©f° ² ¿F³]i ² ° Á ¨ Á ¨�© ²�À ¨ �f�~��?=:�?abK�'v>b���3{�x(8`x(��xv��%�A�~��6tFr���%7=:%71�L7��^Q�-t�20+-575@[be��@��_��?'vzn8u{(%7'6)�~�'v��=:{Qà ���3E��-'v{(�?�o

Page 63: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

��¤�Ü�¥�Ü�XYU��Ô¤� �nX��� � �)0��� ��¥7U�PQOIÜ�XsU�¥+72��������������� ����Çe���8`zT2 8`��12spsr��?a<2 cd��12`��HQ~4H0y9�*+-5�575�o��Ä ² ©�°(³�l3h�¿�¨�2��� ��! ���!�� � � ����!���� ����! e�¡�2C��t72`�d;3�-EG2 yI��8:zT2���K�'FK�8:�3K���$s'FK��-8`=�����7�n7o����d³]l©�°(³�ªjª`º7¯?hjª«hj© Á º�l�º�ª Á ¨�hu¨�´�hj©j±ºvµ�µ�ª«h�¿Fº�©�h�³�l�¨9©�³blTº]© ® °(º]ª3mnºM¨�¨ Á ¨�© ²?À ¨

¶�2 � ����� � ��� �����������"�}e��@8:zT2 8:��12`�3HQ~4H0y9�������+Mo�� ½ º�© ® °(º�ª È ºM¨�¨ Á ¨F© ²?À ¨ ² lnm7hjl ²F² °�hjl@mbe�K7=:{(%bK]x0�nxFK]x(%�8`=jo 32������������#������e��@8`zT2 8`�3132�psr��-aw2 cd�3132:��HQ~4H0y9��+-5�\7Õ�o���Î Á l�º À h�¿�¨qº]l�¹ ¿F³]l3©�°(³�ª�³�Âq¹]hu¨�©�hjªjª`º]©�h�³]lǵ�°(³6¿ ² ¨F¨ ² ¨�2e�_3'(�6{��-��xv=`L K]x0�nxvK�x(%�8`=jo

��2�� � � � ���� ��� ���� Ôe��@8:zT2 8:��12`�3HQ~4H0y92�����7¶no��3Ä&ª`º�l3©�´�h�¹ ² ¿F³]l3©�°(³�ª*´�hj©j±�ºvµ�µ�ª«h�¿Fº]©�h�³]lá©�³"! ½bÈ µ�ª`º�l3©�¨Õ�2 % !,� �$# ��� e��@8:zT2 8:��132:�Tcd��1�8`���-�?'v8`�31�psL@���?'v����xv8:t-{?��H0~4HQy���+-5753+6o�� ¦ l© ² m7°(º]© ² ¹�³vµT©�h À h��6º]©�h�³]l�º�l�¹w¿v³�l3©�°(³]ª�´�hj©j±ºvµ�µ�ª«h�¿Fº�©�h�³�l�©�³�¿?° ® ¹ ² ³]hjª�¹]hu¨�©�hjªjª`º]©�h�³]l

[@2�%&� ������&����"� � ����� Çe��@8`zT2 8`�3132:�3H0~4HQy���A�L�{(8`>@>T������+Mo���g©�º7¯?hjª«h��6º]©�h�³]l�³D À/® ª«©�h µ�±3ºM¨ ²(' ³�´�2\�2 � ��) � *&���! �+�����e��@8`zT2 8`�3132:��HQ~4H0y >6BD�?af8`x(�?>@��8:>@>T�Y+-5�575no�� Ê µ ² °(º�©�h�³�l"³�Â�¿v± ²�À h�¿Fº]ª�µ�°(³6¿ ² ¨F¨ ² ¨bhjl ® l3¨�©Ëº�¯�ª ²° ² m7h�³]l�¨�2

5�2���� ��,� �(&�� � � ���� � � �qe�$4�T23�I%���%7'F{-�@y0��8:z�2scYE�8:�@�%�'(%���17r*�������+Mo�� ½ º�©�° ® º�ª È ºM¨�¨ Á ¨�© ²?À ¨ ² lnm7hjl ²F² °�hjl@m+6��2�� �#� � ( ���� ���,e��@8:zT2 8:��12`��HQ~4H0y >6BD�?af8`x(�->n�38`>@>T�*+-5�575no��3Ä ² ©�°(³�l3h�¿�¨�2+�+72���� ����� �.- !0/ �� �� �21Çe�¡q2 ��t7�3��%7=:Lnx(�6t���8:%/E�8�¡}8:=:K7��%3�37�7���o���Ò Á ¹�°(³vm ² l�¨ Á ¨�© ²?À ¨ ² lnm7hjl ²F² °�hjlnm

3 �#� � �

+72I�T2��@>�%717�6{DxFK7E�K��E���2]��%�{�x(=:��x(r@J,K�8`x(����v¡}��=`x(8:zMK7'(8uK��3=`�YA��?�-E��3K7tF>�t�%��nx('v%7=�×GK��K�=:L@{(8u{�K��E�E��-{(8:17�*� �0ÓÔ8:=:�?L7��psr38:tFr�×�-{�x(�-'-�3�n[�9_3K�1��-{�eD+6575�Õ�o�2 e�{��-��rnx�x(_�) 3 3MJ4J4J�2 tFr��?a���8`%2 �nxv�n��2 ��%�3M�3{(�?'F{ 3]{(>7%71�� 3]�%@%7>T2 r7xvaf=�A�%7',af%7'v��8`��A�%�'(abK�×x(8:%7��o

�2I�T2��>7%71��-{�xvK�EG���(�Y'(%n{��6{({�x(�->n�38`>@>T2�¡�K7{v{��?×d%71f�?�3�?'v178:�3K�=uK��3{(�?'6� ��~�K�_�8:'6�3~�'v%7�E�r��?8:a<�3¶� n�/_3K�1��-{�e�7�7����o�2�e�{��-�rnx�xv_*) 3 3MJ4J4J�2 tFr��?a���8:%32 ��xv�@�*2 �3%'3M�{��-'v{ 3]{(>7%�17� 3]�%�>T2 rnx(af=@A�%�'4a/%�'(��8:��A�%7'vabK]xv8`%��o

4 � 365 �87¸!�� ���:9 �

�nXsU@Ü�¤3XIS�U�VDWYX0S �<;&WYPI¤XIS ��¥+72I�T2@�@>7%�17�-{�xvK�EG�G�(cdØ�_�-'(8:�?�3t?�,8`��H0%7'F{�>9�0L�E�'(%�J48`x(r ps�3��8:t0c��n�3K]xv8`%��3{�%�A��nxFK]xv�-��� ­ ª ® h�¹ ÄY±�ºM¨ ² ����® hjª«h�¯?°�h�º]�>=@?*�+M[�5]×F+-\�\�eD+657\7¶no�2

�24~�2G�0K7��1�×ËÓ�K7'(���?'v1 K7�3E��G2G��>7%71��-{�xvK�EG�,�(�d'v�-E�8:t�x(8:%7��%7AYà �c $&�?rKMzn8:%7'Q8`�qps%7�t��?�nxv'vK�x(�-E�cd=:�-t�xv'(%�=`Lnxv�/�@%�=`��×x(8:%7�{(�3� ­ ª ® h�¹�Äd±3ºM¨ ² � ��® hjª|h�¯�°�h�º��A=@?*�¶� 3+?×˶n����e�+-5�\7¶�o�2

¶�24¡�2n¡}%7'FK�'v8�K��3Eb�T2@�@>7%�17�6{DxFK7EG�*�vc �T�-t�xd%�A*¡}%�E��?=yI�3t?�?'(xvK�8:�nxDL9%��f^QL@�3K�af8utI�4�6{�8:=`8:�?�t��-�3� ¦ k �*± ²�À k � k�g Á]À µ3³ �¨�h ®�À g ² °�h ² ¨���$&!�� B>C*�� �5�¶]×D���� /eD+657\���o�2&e�;�'v%7a �s��c�\n��)�~,r3�0y0{(�4%�A�ps%7af_���xv�?'F{�8`� psr3�?af8:t-K�=3cY��178:���-�?'v8`��1�p&K�a���'v8:E�1��7��y0¬f�.I_�'v8`=�+657\n�7o�2

32I�T2��@>�%717�6{DxFK7EG�@~�2�à ���3E��-'v{(�?�wK��3E !�2@��%7r3�3{��-�*���Fps%�a/_�%�{(8`x(8:%7�3K7=��@8:a9��=uK]xv8`%���%7A�K��I��Ö3���-'(L�ps%�>7�?',;��3'(�3K�t���).I�Ô���E��3{�x('v8:K7=Qc�Ø�K7a/_3=`�}%7A�~,J&%�×Ë_�r3K�{��};�=:%]J J48`x(r psr��-af8:t-K�=Q�I�-K7t�x(8:%7�3�3� � ³6¹ ² ª«hjl@m�� ¦ ¹ ² l3©�h �s¿Fº]©�h�³]lͺ]l�¹�d³]l©�°(³�ª«�ED*�7�]×� � e�+-57\�Õ�o�2

��24^�2 c02n�48:z7�-'vK3�n¡q2n¡}%�'vK7'(8K��3E��G2���>7%71��-{�xvK�EG���(����xv�?'v�3K�=�¡}%�E��?=*ps%7�nxv'(%�=3 32��Y�D^Íps%���xv'(%�=`=:�?'s^0�6{�8:17�3�3� ¦ l�¹�k F� l@m�k���± ²?À k4Ä&°v³-¿ ² ¨v¨0Î ² ¨?k,Î ² i]k:�ECEGG�3��7M×D�Õn��e�+-57\�Õ�o�2

Õ�2I�T2��@>�%717�6{DxFK7EbK7�3E�¡�2�¡}%�'vK7'(8����(^Q�-{(8`1���%�A��I�-{(8`=:8`�-�nx,�Y'(%�t��6{({(8:��1��d=uK��nxv{d»b�IH92�c �T�-t�x&%7A�¡}%�E��?=Gy0�3t��-'�xFK�8:��xDL%7�<^QLn�K�af8:t��I�-{(8`=:8`�-�3t��6��� ��± ²?À k � lnmnkIgG¿�h�kKJ�CG�[��G+M[]Õn�M×F+M[�\7��e�+-57\@[�o�2

[@2I�T2@�@>7%�17�-{�xvK�EfK��3Ef¡�2@¡}%7'FK�'v8�� *�?x�x(�-'dxv%�x(r��QcYE�8`x(%�'d%7�b_3K78`'v8:��1�{��-=`�6t�xv8`%��fA�%7'YE��6t��-��xv'vK7=`8:�?�6Ebt�%���xv'(%�=��@¾ ¦ ��± �L�³ ® °�lTº]ª«�M?E?*�T[@�[]�3+�×�[]�nbeD+657\n[7o�2

Õ

Page 64: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

\�2I�T2��@>7%�17�6{DxFK7E�K��Eq¡�2�¡}%7'FK�'v8�� �(~,r3� c �T�-t�x�%7A0^08u{Dxv��'v�3K��3t?� ^Q8`'v�-t�x(8:%7�3{�%7�Æps=`%n{��6E *%@%7_����-'�A�%�'(abK7�3t��6���¦ lT¹7k F � lnmnk��*± ²�À k �0² ¨ ² º�°(¿F±@�EC � ��+-����7���5�×�7�7¶n�beD+657\n[7oI2

5�2I�T2���>7%71��-{�xvK�E�K7�3Ef¡�2�¡}%�'vK7'(8��G�Fps%��nx('v%7=ps%7��Ö317��'FK]xv8`%��f���?=:�-t�xv8`%��/A�%7'Y^Q8:{�x(8:=:=:K�x(8:%7��ps%7=:��af�3{v���@¾ ¦ ��± � L�³ ® ° �l�º�ª«� ?E?*�G+6���G+6Õ����×v+6Õ7¶n�feD+-5�\n[7o�2

+6��2I�T2d�@>�%717�6{DxFK7EqK7�3E�¡q2d¡}%7'FK�'v8����v~,r��<^0%�a/8:�3K7��xb~,8:a/��ps%7�{DxFK��nx�A�%�'b^08u{Dxv8`=:=uK]x(8:%7�Ôps%7=:��af�3{v��� �d³ À µGk F��± ²?À k � l@m�k:�A= =���Õ���Õ��n[M×ËÕ3+M[be�+-5�\n[�o�2

+�+72I�T23�@>�%71��-{�xvK7E�K��3Ew¡�2�¡}%�'vK7'(8�������af_�=:8:t-K]x(8:%7�{s%7A �K�'v17�Q�4à�.I×ËcY=`�-a/�-�nxv{,%7��ps%7�nxv'(%�=����-'�A�%�'(abK��t��-�3� ¦ l�¹�k F� l@m�k���± ²?À k �Q² ¨ ² º]°(¿F±@�>C � �G+7+��3�¶�7¶]×D�¶�¶7��e�+-57\@[�o�2&e�.I=u{�%�{(�?��¿F³]°�° ² ¿?©�h�³�lfx(%�c �2,+6¶�8:��C D*�����\�57\weD+657\7\no�o�2

+M�2I�T2d�@>�%717�6{DxFK7EáK��E�¡�2�¡}%�'vK7'(8����(. ��L@{�x(�-abK]x(8ut�.0_�_�'v%�K�tFr�x(%�^08u{Dxv8`=:=uK]x(8:%7�Ôps%7=:��af�"ps%7�nxv'(%�=:�3� ¦ k ��± ²?À k � kg Á]À µ3³M¨�h ®�À g ² °�h ² ¨���$&!�� =��MJ��*. [�+�×�.0\7Õ�eD+657\n[7o9e�;�'v%7a�^Q8u{Dxv8`=:=:K�x(8:%7�áK��3E�.I�3{(%7'v_�xv8`%���\n[��*$&'(8:17rnx(%��*�*y0¬f��@�-_�x-24+657\n[7o�2

+6¶�2I�T2��@>�%71��-{�xvK7E�K��3E�¡�2*¡}%�'vK7'(8��,� �ÃI×�ps%7�nx('v%7=�%�A,K �08`1�r�×Ë�Y��'v8|xDL�^Q8:{�x(8:=:=:K�x(8:%7�qps%7=:��af�3��� ��± ²?À k � l@m�k gG¿�h�k:�J>?*�G+���¶7¶]×Ë �\weD+657\�\�o�2

+- 32I�T2T�@>7%�17�-{�xvK�EG��¡�2�¡}%7'FK�'v8*K��3E}�2«pQ23^0%]L@=:�7�s�(�4%����3{�x ps%7�nx('v%7=G%7A���=:=�ps%7�3E�8`x(8:%7�3�-E}�d=uK��nxF{?)Y�08`1�r�×��d��'v8|xDL ^08u{D×x(8:=:=:K�x(8:%7�3�3� ¦ ��� � ¼�°(º�l�¨?k ¾ ® ©�³ À k ��³�l3©�°(³]ª|�>?E?*��+6���+-��5�]×v+�+-����eD+657\7\no�2�e�.0=:{(%�{(�?� ¿F³�°�° ² ¿�©�h�³]lbxv%��T×Ë%7_�xv8`abK�=t�%��nx('v%7=:=`�-'&8:��?MJ��3Õ���Õ@[� eD+657\75no�o�2

+M��2I�T2G�@>7%�17�6{DxFK7E<K��3E}¡q2�¡}%�'vK7'(8��Y�F�@%7af��H0�?J��d'v%7_��?'(x(8:�-{I%�A�x(r3�/�nxv'(�3t�x(��'v�-E��@8`�317��=uK�'IÃdK7=`�3�-��� ¦ ��� � ¼�°(º�l�¨?k¾ ® ©�³ À k �d³]l©�°v³]ª«� ?E?��G+6��G+�+6��+�×F+7+6�� �eD+657\7\no�2

+6Õ�2I�T2��@>�%717�6{DxFK7E�K7�3E�¡q2�¡}%7'FK�'v8����(y0�3E��-'v{�xvK7�3E�8:��1�xvr���^0L@�3K7a/8ut�$&�?r3KMz@8:%7'Y%7A�^Q8:{�x(8:=`=uK]xv8`%��}ps%�=`�3a/�{(�3� ¦ l�¹�k F� l@m�k���± ²?À k �Q² ¨ ² º]°(¿F±@�>C D*�G+-�3�G+-\� n\]×F+-\�Õ�be�+-57\�\�o�2

+][@2I�T2��>7%71��-{�xvK�E K7�3E<¡�23¡}%�'vK7'(8����(�4%����3{�x0���?'(A�%7'vabK��3t?�Q%7A�^Q�-t?�?�nx('FK�=:8`�-�-E}ps%7�nx('v%7=���L@{�x(�-ab{4�@L����3E��-_�-�3E��-��x^Q�-{(8`1��3{(�3�¾ ® ©Ë³ À º�©�h�¿Fº�� C G*�G+7�*+�+-5�×v+M7�be�+-57\�5�o�2

+6\�2I�T27�@>�%71��-{�xvK7E*�M��2 ����3E�{�x(' #%7a�K7�3E/cI2]Ó 2��nK7t�%��3{(�?�*�G�F�@�?=:�-t�x(8:��10xvr��,��6{DxYE�8:{�x(8:=`=uK]xv8`%���t?%7�nx('v%7=�t�%���Ö31���'vK�x(8:%7�3�3�¾ ¦ ��± � L�³ ® °�lTº]ª«�E? � �3����[7��¶�×D[�Õ� �e�+-575���o�2

+65�2I�T2T�@>7%�17�-{�xvK�EG�3��2 *���3E3{Dxv'-#%�a K��E}cI23Ó 2���K�t�%��3{��-�*�d�v�4�?_�=:L x(%�t?%7afaf�?�nxv{4�@L<�32��48:171�{v���T¾ ¦ ��± � L�³ ® °�lTº]ª«�? � �[��G+7+6��M×F+7+M�Õ�e�+-575���o�2

7��2I�T24�@>7%�17�6{DxFK7E"K��3EÇ��2 *���E�{Dxv'-#%�a<�b�(¡}��×Ë%7_�x(8:afK7= �ÃI×�t�%���xv'(%�=I%�A�E�8u{�x(8:=`=uK]xv8`%�� t�%�=`��af�3{v��� �d³ À µ ® © ² °F¨�º]l�¹��± ²?À k � l@m�l@m�k:�A=�J��� '37���@ ��3+�×Ë 3+6¶�eD+6575���o�2

�+72I�T2��@>�%717�6{DxFK7EG�McI2MÓ 2]�nK7t�%��3{(�?��K��E9¡�2]¡}%�'vK7'(8���(���3K7E�� �n�3K7t?LQ%7A{�x(�-K�E�Ln×Ë{�xvK�x(�&K��3K7=`L�{(8:{*A�%7'�A��?�-E��3K7tF>�t�%��nx('v%7=�)^Q8:{�x(8:=`=uK]xv��×Ë�%7x�xv%7a t?%7�nx('v%7=T%7A�E�8u{�x(8:=`=uK]xv8`%��wt?%7=:��af�3{?2d�3� ¦ lT¹7k � lnmnk���± ²?À k �0² ¨?k:�EC B*�G+M��3�¶�¶75�×�7¶� �Õbe�+-5�57��o�2

��24cI2nÓ 2@��K�t�%7�{��-��K��3E��G2@�@>�%71��-{�xvK7E*���(¡���=|xv8`_3=`���nx(�6K7E�L��nxFK]x(�6{Y8:���DE��6K�=T~,Js%��d'v%@E��3t�x,^08u{Dxv8`=:=uK]x(8:%7�����¾ ¦ ��± �L�³ ® °�lTº]ª«�M?>DG�3 3�� �5�5]×D��+�+9eD+6575�+Mo�2

7¶�2I�T2��@>�%71��-{�xvK7E*���Fps%��3{�8u{�x(�?�t�L}%�A,�nx(�6K7E�Ln×D�nxvK�x(�b¡}%�E��?=u{�y0{(8`�31 ���3{(8:17rnx�K���%7��x�c�Ø@x(�-�3{(8`z���ÃdK7'(8uK���=:�-{v��� ¦ l�¹�k� l@m�k���± ²?À k �Q² ¨?k:� ?��*�� ��Õ��� �×�Õ7Õ�+/eD+6575�+Mo�2

� 32I�T2��@>�%71��-{�xvK7E}K7�3E�cI2TÓ�%�= ���I�v~�.QH0¬����Y� �×I. �d'v%�t��6{({�ps%7�nx('v%7=�à�K�af�6��� ��¾��*Ò � ½9² ´�¨����d���3=`8u{�r3�-E��@Lp&.0p&�0cÇps%�'(_�%7'FK]xv8`%��*��.I�3{�x(8:�*�3~���Ø�K7{-2�HI%2 ¶n��G+�×Ë 3���@_3'(8:��1<+-5�5�+72

���2I�T2-��>7%71��-{�xvK�EG�-c02 Ó 2?�nK7t?%7�3{(�?��K��E�¡�2?¡}%�'vK7'(8��Mps%�a/af�-��xF{G%7�<�v~����38`��1Qps%��nx('v%7=:=`�-'v{�%7��^Q8:{�x(8:=:=:K�x(8:%7��ps%7=:��af�3{J48`x(rÔxvr���^Q8:{�x(8:=:=:K�x(��×�$&%�x(x(%7ab{w�nx('v�3t�xv��'v�-�Ôe�ps%�'('v�-{(_�%7�3E��-�3t��Mo�� ¦ l�¹7k � lnmnk ��± ²?À k �0² ¨?k:� ?����0��3+-5�×�7����eD+65753+6o�2

7Õ�24~�2d¡}��B�E��?=:=IK��3EÆ�T2Y�@>�%71��-{�xvK7E*���(cY{�x(8:abK]xv8`%���%�A�^08u{�x(8:=`=uK]xv8`%��Ôps%�a/_�%�{(8`x(8:%7�3{�A�'v%7a ¡}��=`x(8:_�=:��~��-af_�-'vK�x(��'v�¡}�6K7{(��'(�-af�?�nxv{��3{(8`��1���K�'(x(8uK�=`× ��-K�{Dx(×����n�3K7'(�6{��4�?1�'(�6{({(8:%7�3�3� ¦ l�¹�k � l@m�k ��± ²?À k �0² ¨?k:�K?����I+M��Y7�� �¶�×���7�7�eD+65753+6o�2

n[@24~�2,¡}�DB�E��-=`=�K7�3E �T24�@>7%�17�6{DxFK7EG�b��ps%7af_%n{�8`x(8:%7�Çcs{Dxv8`abK�x(%7' 8`� K��d8:=:%�x �Y=:K7��x<^08u{�x(8:=`=uK]xv8`%�� ps%7=:��af�Ç�3{(8`�31¡}��=`x(8:_�=:��~��-af_�-'vK�x(��'v�-{v��� ¦ l�¹7k � l@m�k���± ²?À k �Q² ¨?k:�M?��*��+6�����7�7�]×����Õ7 �eD+6575�+Mo�2

[

Page 65: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

7\�24��2�*���E�{Dxv'-#%�a<���T27�@>�%717�6{DxFK7E�K7�3E ��× ��2MÓáK���1�*�(���-'�A�%�'(abK��t��dJ&�?8:17rnx�{��-=`�6t�x(8:%7�9A�%7'��4×Ë8:��Ö3��8`xDL9K��E �T×�t�%���xv'(%�=af��xvr�%�E�{(�3�s¼�°vº]l�¨?k ¦ l3¨�©Ëk ³D ��² ºM¨ ® ° ²?Àf² l3©4º]lT¹$�d³]l©�°v³]ª«� =@?��3���� 3+�×D7��beD+65753+6o�2

75�24cd=:=:8`��1áÓ 2&��K�t�%7�{��-�*� �8`%����?= �K�'v%�tFr��7�&¡�K���A�'(�6E"¡�%7'FK�'v8��,�@8`1���'FEÆ��>7%71��-{�xvK�E�K��E"�0�?��'v8:>�Ó 2s.0�3E��-'v{(�?�*��(�I%7���3{�x ps%7�nxv'(%�=*%�A��I%�a/%�17�-���?%��3{4.I�-�?%�xv'(%�_�8ut�^08u{Dxv8`=:=uK]x(8:%7��ps%�=`�3a/�{(�3�T¾ ¦ ��± � L�³ ® °�l�º]ª|�E?>DG��+6���+-\�+6�]×D] eD+65753+6o�2

¶���2I�T2��>7%71��-{�xvK�EG��¡�23�I%]z�EwK��3E<��2 ����3E�{�x(' #%7a<���v��8`af_�=:��A�'(�-�n���?�3t?Ln×ËE��-_�-�3E��-��x4xv%@%7=u{&A�%7'IK��K�=:L@{(8u{,%�A�8:��r��-'(�-�nxt�%��nx('v%7=T=`8:af8|xFK]xv8`%��3{(�3� � ³-¹ ² ª«hjl@m�� ¦ ¹ ² l©�h �&¿vº�©�h�³�l�º�l�¹ ��³�l3©�°(³]ª|� =@C*�� 3�G+M��5�×v+][7[be�+-5�5�+6o�2

¶3+724¬f2*Ó 2�¡�K]xvr�8:{(�?�����T2��@>7%�17�6{DxFK7E�K7�3E�cI2�Ó�%�= ���Q�v$&Ln_K7{v{��@�?=:�-t�x(8:%7�áA�%7'fps%7�nx('v%7=�%7A,�0�-K]x/c�Ø�tFr3K��317�?'�H0��x�×J&%7'v>@{v������³ À µ ® © ² °F¨/º�l�¹ �*± ²�À k � l@m�l@m�k:� = � �T�@��_�_�=�2:�G�3�Õ7¶�×��3�[� eD+6575n7o�2�e��@��_�_3=`�-a/�-�nx0A�'v%7aÌ{�L@af_%n{�8:��acs�p&.0�Ycd×v+���cd=u{�8:��%7'v�7��^Q�?��abK7'(>T��¡�KML�+6575n7o�2

¶n�24¡�2M�I%]z�E�K��E��T2M��>7%71��-{�xvK�EG�3�F�@8`af_�=:�s;3'(�-�n���?�3t?Ln×Ë^Q�?_��?�3E��?�nx�~�%@%7=u{TA�%7'dps%7�nx('v%7=n�@L�{Dxv�?a .I�3K7=`L�{(8:{-�]�nx('v�3t�xv��'v��@�-=`�6t�x(8:%7�<K��Ew^Q�-{(8:17�3�3�¾ ® ©Ë³ À º�©�h�¿Fº]� C � �����5�\75]×�575�Õ�eD+6575n7o�2

¶�¶�2I�T2G�@>7%�17�6{DxFK7E}K��E�¡�2T¡}%7'FK�'v8��s��ÃdK7'(8uK���=:���@�-=`�6t�xv8`%��}A�%7'�^0�6t��-��xv'vK7=`8:�?�6E�ps%7�nx('v%7=u��� � ³-¹ ² ª«hjl@m�� ¦ ¹ ² l3©�h �s¿Fº]©�h�³]lº]lT¹ �d³�l3©�°(³]ª«�<= ?��0���+�+-¶]×F+6���e�+-5�5�7o<e�'(�-_�'v8`�nx�%7A���K7_�-'�+67\7t _�'v�-{(�?�nx(�6EÔK]x .0�(psr3c .0���@�3K�= ¡}�?�?x(8:��13�ÓáK7{(r�8`�31�x(%��w^�pQ�3H0%]z�2,+657\7\���{��-� _K�_��?'�+7+�8:�wx(r���=:8:{�xI%�A�t�%���A��?'v�?�3t?��_�����=:8:t-K]xv8`%��3{vo�2

¶7 324cI2T����'v�?�{��-� ��?z��?'F{����EG���T2�¡�K7t-tFr�8:��x�xv%3�Tà/2T�nxv�3K�'(xQK7�3E��T2G�@>7%�17�-{�xvK�EG�d� !Q_�x(8:abK�=�t?%7�nx('v%7=�K��3E<%���×�=:8:����%7_�×�?'FK]xv8`%���%7AY'(�6K7t�x(8:z7�/�3K]xFtFr�E�8u{�x(8:=`=uK]xv8`%��3��� �d³ À µ ® © ² °F¨bº�l�¹ ��± ²?À k � l@m�l@m�k:� = � ���@��_�_3=�2:����¶�5�+�×D��¶�5��}e�+-5757 no�2e�����_�_�=:�?af�?�nx,A�'v%7a¸{�L@af_�%�{(8`��a¸c&�3p&.0�sc�×�¶���à 'vK7�7�@.I�3{�x('v8:K3���7��=:L��M×�[@��+-5�57¶�o�2�cdØ@x(�?�E��-Ebz��?'F{�8:%7�b8:�*) �d³ À �µ ® © ² °F¨�º�l�¹ �*± ²�À k � lnm7lnmnk:�EC��*��+? �53+�×F+? n57\beD+6575�Õ�o�2

¶n��24¬f2 Ó 2Y¡�K]xvr�8u{��-�*�4¡�2Y¡}%�'vK7'(84K��EÆ�G2s�@>7%�17�6{DxFK7EG���(^QLn�K�af8:t<af%�E��-=:{fA�%�'br��-K�x���Ø�tFr3K7��17�-'v{fK��E§r3�-K]x��?Ø@×tFr3K7��17�-'0���?xDJs%�'(>�{v�����d³ À µ ® © ² °F¨/º]lT¹)��± ²?À k � lnm7lnmnk:� = � �*�@��_�_3=�2:���@ n�75]×D�@ �Õ�¶<eD+-5�5� @o�2�e��@��_�_3=`�-a/�-�nxQA�'v%7a{(Lnaf_�%�{(8`�3a cs�3p&.Q�Ycd×˶3��à 'FK�����.I�3{�x('v8uK�������=`L<�M×�[@�T+-5�57¶no�2

¶�Õ�24�27¡}%7'v�3E/K��3Eb�T2@�@>7%�17�6{DxFK7EG�G�vc �T�-t�xF{�%�AT'v�-t�L�t?=`�,%7�bE�L@�3K7af8:t-{dK��3Eft?%7�nx('v%7=@%�A*tFr��-af8:t-K�=�_�'v%�t��-{v{(8`��1�_�=uK��nxF{(�3��d³ À µ ® © ² °F¨4º]lT¹ ��± ²?À k � lnm7lnmnk:�= � ���@��_3_�=�2:�������5�×����7¶� �eD+65757 no�2&e��@�3_�_�=:�?af�?�nx�A�'(%�aÍ{(L@af_%n{�8:��a cs�3p&.Q�Ycd׶��3à 'FK�����.I�3{�x('v8uK�������=`Lw�M×�[@�G+-5�57¶no�2

¶@[@24cI2 Ó 23�nK7t?%7�3{(�?�<K��3E<�T2T�@>7%�17�-{�xvK�EG���(^QL@�3K�af8ut?{IK7�3E t?%7�nx('v%7=G%7A��3�3{DxFK���=:��E�8u{Dxv8`=:=uK]x(8:%7�}t?%7=:��af�3{(�3� � ³-¹ ² ª|hjlnm �¦ ¹ ² l©�h �&¿Fº]©�h�³]l�º�l�¹ ��³�l3©�°(³]ª|� = J��3��3��5]×�[��eD+65757¶no�2

¶�\�2 �×"��2�ÓáK���1�K7�3E��T2���>7%71��-{�xvK�EG�d�(�I%7���3{�x0t�%��nx('v%7=*%7A�xv8`af��×�E��-=:KML<{�L�{�x(�-af{I�3{�8:��1fxvr��/�@af8`x(r}_�'v�-E�8:t�x(%7'F��� ¦ l3©�kL�k �d³]l3©�°(³�ª«�EGEDG��Õ3�G+? ��n�M×F+? @���e�+-575�¶�o�2

¶�5�24¡�2G�I%]z�E�K��3E��T2��@>7%�17�6{DxFK7EG�&����af_�'v%]z7�6E}8`�E��?_��?�3E��?�nx�E��-{(8`1���%7AY'(%����3{�x�E��-t��-�nx('FK�=:8`�-�-E�t?%7�nx('v%7=:=`�-'v{v��� L�ks³�ÂÄ&°(³6¿ ² ¨F¨��³�l3©�°(³]ª|� ?*�] n¶]×D��+Ie�+-575�¶�o�2se��I�?_�'v8`�nxv�-E�8:� � ³6¹ ² ª«hjlnm � ¦ ¹ ² l3©�h �s¿Fº]©�h�³]l º�l�¹ �d³�l3©�°(³]ª«�M=@G*�]57¶]×F+-�@[@�n+-5�5� 32Co

n��24~�2�¡}�DB�E��?=:=IK��3E"�T2Y�@>7%�17�6{DxFK7EG��� !Q��x(_���xfcs{Dxv8`abK]xv8`%��§yQ{�8:��1á¡}��=`x(8:_�=`���@�6t�%��3E�K�'vL�¡}�-K�{��3'(�-a/�-�nxv{-)��I8:17r�×�d�3'(8`xDL�^Q8:{�x(8:=`=uK]xv8`%��3���¾ ¦ ��± � L�k:�M? B��*+-�3�T+-Õ� +�×F+-Õn��¶�e�+-575�¶�o�2

+724¡�2G�I%]z�E�K��3E��T2*�@>7%�17�-{�xvK�EG�&�(�d'v%�t��6E���'v��A�%7'�'v�?17�3=:K�x(%7'vL<t�%7�nxv'(%�=�{�x('v�3t�xv��'v��{(�?=:�-t�xv8`%���J48`x(ráK�_�_3=`8ut?K�x(8:%7�}xv%x(r3��;�p4pÆ_3'(%�t��6{({v���3¾ ¦ ��± � L@k:�E? B��G+6��G+-57¶�\]×F+-5n��¶beD+6575�¶�o�2

@�24cI2YÓ 2s�nK7t�%��3{(�?�ÆK��3EÔ�T2,�@>7%�17�-{�xvK�EG�9�(���3t�%��3{(8:{�x(�-�3t�8:�-{f8:�Ç^0L@�3K7af8:t�¡�%@E��?=u{fA�%7'���=:=`×Dps%��3E�8`x(8:%7���6E"�Y=:K7�nxv{-).I_3_�=`8ut?K�x(8:%7�bxv% *%]J,×Ë%7'FE��-'d¡}%�E��?=u{Y%7A*^08u{Dxv8`=:=uK]x(8:%7�<ps%7=:��af�3{(�3� ¦ l�¹�k � lnmnk ��± ²?À k �Q² ¨?k:� ?E?*�@¶��@Õ7¶3+�×�Õ� n��e�+-5757 no�2

n¶�2 ��2 × ��2�ÓáK���1�Y��2 *���3E3{Dxv'-#%�a K��3E"�T2d�@>7%�17�-{�xvK�EG���(�I�?_�'v�-{(�?�nxvK�x(8:%7�q%7A0���3t?�?'(xvK78`��x(8:a/�<E��-=:KML�{/8`��x(r��$� �A�'FK�af�?J&%7'v>���� ¦ l3©�k L@k �d³�l3©�°(³]ª«�>GMB���¶���Õn�[6×�Õ7¶�\�e�+-5757 no�2

� 324¡�2d�0%]z@E"K��E"�T2&�@>7%�17�-{�xvK�EG����ps%7�nx('v%7=,%�A��@L@afa/�?x('v8:t-K�=:=`L�����xv�?'Ft�%������-t�x(�6E§�Y=:K7��xF{(�3�&¾ ® ©�³ À º]©�h�¿vº���?����sÕ��5��n[6×�5n[�¶�eD+6575� @o�2

@��24cI2 ÓÚ�nK7t?%7�3{(�?��K��3Ef�T27�@>�%717�6{DxFK7EG�T�(���3{DxFK���8:=:8|xDL�%7A�E�8u{Dxv8`=:=uK]x(8:%7�ft�%�=`�3a/�{(�3��¾ ¦ ��± � L�³ ® °�l�º�ª«� J �*��5���+? nÕ7Õ�×v+- @[]\eD+65757 no�2

nÕ�24¡�2��I%]z�E�K7�3E��T2��@>�%71��-{�xvK7E*���v��� �n���?�nxv8:K7=�E��6{�8:17��%�A�E��6t��?�nxv'vK7=`8:�?�6E�t�%���xv'(%�=`=:�?'F{v���@¾ ® ©�³ À º]©�h�¿Fº]�?��*��+-�3�+6Õ7��+?×+-Õ��n[�eD+6575� @o�2

\

Page 66: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

�[@24¡�2?�0%]z�E K7�3E��T2-��>7%71��-{�xvK�EG�3�v��K�8:'(8:��1,t�'v8|xv�?'v8:KsA�%7'�E��-t?�?�nx('FK�=:8`�-�-E t�%���xv'(%�=]%�A����3{�xvK7��=:��_�=:K7�nxv{v��� ¦ l�¹�k � lnmnk ��± ²?À k �Q² ¨?k:�?E?*��53�3�+-¶7 �×D�+6¶75�e�+-5757 no�2

n\�24cI2����7'(�-�3{(�?� K7�3E �G23�@>7%�17�-{�xvK�EG���Fps%7�nxv'(%�=T�nxv'vK�x(�-178:�-{YA�%7'I�4�6K7t�xv8`z��Q$,K]xFtFr ^Q8:{�x(8:=:=:K�x(8:%7�3�3� L@kGÄ&°v³-¿6k���³�l3©�k:�J�� 3�37���]×��+M[be�+-5�5� no�2

n5�24cI2 .�2@Ó�%7=���K��3Ew�T2��@>7%�17�6{DxFK7EG��� !Q_�-'vK�x(8:%7�b%�A�8`�nxv�?17'FK]xv�-Efxvr�'v�?��×Ë_�'v%�E��3t�x�e����?x(=:Ln�3>�o&E�8u{�x(8:=`=uK]xv8`%�� t�%�=`�3a/�{(�3�¦ lT¹7k � l@m�k ��± ²�À k �0² ¨?k:�>? J���Õ3����5� 7×��+-�7¶be�+-5�5��7o�2

�7��2I�T2d�@>�%717�6{DxFK7E�K7�3Eq¡�2��I%]z�EG��� *�?x�x(�-'9xv%�xvr��w�-E�8`x(%�'�%���E��-t?�?�nx('FK�=:8:�?�-Eqz7�?'F{(�3{�a���=|xv8`z]K7'(8uK���=:� t?%7�nx('v%7=u����L�kÄ&°(³6¿ ² ¨F¨ �d³]l©�°(³�ª«�EG*�3¶75�5]×Ë �����eD+6575���o�2

��+724��2 *���3E3{Dxv'-#%�aw�]�2 �92 ��?���M¡q2M¡�%7'FK�'v87K��3E��T2M��>7%71��-{�xvK�EG�� *8:af8|xFK]x(8:%7�{�%7A3^0L@�3K7a/8utY¡�K]x('v8`Ø�ps%���xv'(%�=:�3� �d³ À µ*kF �*± ²�À k � l@m�l@m�k:� =@B��� ��75�×� @�+��+6575���2

���24��2 *�3�3E�{�x(' #%7a K��E"�T2&�@>7%�17�-{�xvK�EG��� !Q_3_%�'�xv����8`x(8:�-{bK��E§E�8 /�t���=`x(8:�-{fJ48`x(rÇ���q��E�8u{Dxv8`=:=uK]x(8:%7�Æt�%��nx('v%7=u��� L�kÄ&°(³6¿ ² ¨F¨ �d³]l©�°(³�ª«�EG*�] n5]×D�Õ3+7�3+6575n��2

�7¶�24cI2 Ó 23�nK7t?%7�3{(�?�<K��3E<�T2T�@>7%�17�-{�xvK�EG���(¡}�3=|xv8`_�=:�9{�x(�6K7E�Ln×�{DxFK]x(�6{,K��3Ew8:�3{DxFK���8:=:8|xDL 8`��E�8u{�x(8:=`=uK]xv8`%���»�8:af_�=`8ut?K�x(8:%7�3{A�%7'4%�_�-'vK�x(8:%7�wK��3E<t�%��nx('v%7=u��� ¦ lT¹7k � l@m�k ��± ²?À k �0² ¨�k:��? J��� n¶75��]×� � ��n���3+6575n��2

�� 32I�T2*�@>�%717�6{DxFK7EG�&�(. _�'v%@t?�-E��3'(�9A�%7'��@��� ! t?%7�nx('v%7=:=:K7��8:=`8`xDLwK7�3K�=:L�{�8u{I»wJ48`x(r�K7_�_�=:8:t-K]xv8`%��}x(%<E��-{(8:17��%7AY_3� ���?��×x('FK�=:8:�-K]xv8`%���_�'v%�t��6{({(�-{v��� �d³ À µGk ��± ²?À k � lnm7lnmnk:� C ����¶n[�¶]×�¶7\7Õ3�+6575�Õ�2

����24cI2 .�2?Ó�%�= �fK��3E��T2M�@>7%�17�-{�xvK�EG���v~��-a/_��?'FK]xv��'v�dt?K7{vt?K�E���t�%���xv'(%�=]%�A�E�8u{Dxv8`=:=:K�x(8:%7��t?%7=:��af�3{(�3� ¦ l�¹7k � lnmnk �*± ²�À k �0² ¨?k:�?>GG�� �[��M×Ë �\7 3��+-5�57Õ�2

�7Õ�24�2n¡}%�'(�EbK��3E��G2@�@>�%71��-{�xvK7E*���(^QL@�3K�af8ut4���?r3KMz@8:%7��'s%�A*8:��xv�?1�'vK�x(�-E/_�=uK��nxF{(�3�EL�kÄ,°(³-¿ ² ¨F¨��d³]l©�°(³�ª«� � ��+? @�M×F+? nÕ��+-5�57Õ32

�n[@2I�T2��@>�%717�6{DxFK7E�K7�3E�¬f2]�0KMz@'v�7�T�(~,r3�s�3{(�&%�A�xvr��4�,à�."K��E9t�%��3E�8`x(8:%7���n�3a9���?'�K7{�'(%����3{�x(���6{({�af�-K�{���'v�-{v���(�d³ À �µ ® © ² °F¨�º�l�¹ �*± ²�À k � l@m�l@m�k:��C ����@��_3_�=�2:��T+6�7�n�M×F+-��+6��eD+6575�Õ�o�2Ie��@��_�_3=`�-a/�-�nxIA�'(%�a {(Lnaf_�%�{(8`�3a cs�p&.0�Ycd×ËÕ3��4r�%�E��6{?�3à 'v�?�6t�����¡�KML �Õ�×�75��G+6575�Õ�o�2

�7\�24$ 2MÓÔ8|x(x(17�-�3{-����2�*8`x�xv%3�7c027����'v�?�{��-�9K��3Ef�T27�@>�%71��-{�xvK7E*���v~�%7xvK7=�'v�.-3��Ø9%7_��?'FK]xv8`%���%�A�a9��=`x(8:z7�6{({(�?=@�3K�xvtFr�E�8:{�x(8:=|×=uK]x(8:%7���� �d³ À µ ® © ² °F¨�º]lT¹$��± ²?À k � l@m�l@m�k:�>C �����@��_�_�=�2:��T+-�7 3+?×v+6�� �Õbe�+-5�57Õ�o�2&e��@��_�_3=`�-a/�-�nx4A�'(%�a {�L@af_%n{�8:��acs�p&.0�Ycd×ËÕ3���4r�%�E��-{-�3à 'v�?�-t?�7��¡�KMLw�Õ]×D�5��*+-5�57Õno�2

�75�24cI2����7'(�-�3{��-��K��E��T2d�@>7%�17�6{DxFK7EG��� !Q_�x(8:afK7=&{�xvK7'�xv��_�_3'(%�t��6E���'v�-{�A�%7'/�3K]xFtFr§E�8u{Dxv8`=:=uK]x(8:%7���� �d³ À µ ® © ² °F¨<º]l�¹��± ²?À k � l@m�l@m�k:�KC��*���@��_3_�=�2:�Y�T+M7��[M×v+M�Õn�eD+6575�Õ�o�2�e��@��_�_�=:�?af�-��x/A�'v%7a�{�L@af_%n{�8:��a�cs�3p&.Q�Ycd×ËÕ3���4r�%�E��6{?�à 'v�?�-t?�7��¡�KMLw�Õ]×D�5��*+-5�57Õno�2

Õ���2I�T2��@>7%�17�-{�xvK�E�K7�3E�cI2 .�2�Ó�%�= �����Fps%���xv'(%�=`=uK��38`=:8|xDL}af�6K7{(��'(�6{�A�%7'�E�8:{�x(�3'(�3K7�3t��b'v�DBD�6t�xv8`%��3��� � ³-¹ ² ª«hjl@m�� ¦ ¹ ² l �©�h �s¿Fº]©�h�³]lÔº]lT¹ �d³]l©�°v³]ª«��=DG�&+-Õ@[6×F+-\n�e�+-575�Õ�o�2�e��4�?_�'v8:��x/%�A4_3K7_�-'�A�'(%�a��D;�.0p Ó�%7'v>�{�r�%�_á%7�����nx(�-'vK�t�x(8:%7�{����xDJ&�?�?�<_�'v%�t��6{({4E��6{�8:17�<K��Ewt?%7�nx('v%7=�� *%��3E�%��*��@�-_�x-2Q+-575n ��{(�?��_3K7_�-'Q�] f8:� xvr���=:8:{�xI%�AYps%7��A��?'v�?�3t?��_�����=:8|×t?K�x(8:%7�3{Fo�2

Õ3+724cI2*���7'(�-�3{(�?��K7�3E��G2G��>7%71��-{�xvK�EG�,�Fps%7af_3K7'(8u{(%7�}%�A&'(�-17��=uK�' K��3E�8:�nz��?'(x(�6E}�3K]xFtFr�E�8u{�x(8:=`=uK]xv8`%��3��� ��± ²?À k � lnmnkgT¿?h�k:�EG =�3 �5� n5]×Ë �5�Õ���3+-575�Õ�2

Õn�24��2 ^92*$&'FK7K�x(�7�G¡�2G¡}%�'vK7'(8�K��E��T2��@>�%71��-{�xvK7E*�&� *%@%7_{�r3K7_�8:��1bA�%7'�'v%7���{Dx�_�-'�A�%�'(abK7�3t��6��� ¦ l3©�k L�ks³� � ³7¯ ® ¨�©º]lT¹ ½ ³]l3ª|hjl ² º]° �d³]l©�°v³]ª«� � ��\����M×�\�7¶���+-5�57Õ�2

Õ�¶�24¡�2��I%]z�EG�s��2 ^�2�$&'vK�K]x(�wK��3E§�T2Y�@>7%�17�6{DxFK7EG���v��ÃQ^#ps%7�nx('v%7=:=:�?'F{�A�%7' ����×F��� � ×F�YK��3E �T×�%�_�x(8:abK�=4t�%���xv'(%�=:�3�¾ ® ©�³ À º]©�h�¿vº��M? ?��� n¶7¶]×Ë �¶�5��+-575@[@2

Õ7 32I�T2��@>7%�17�6{DxFK7EG��$ 2�ÓÔ8`x�xv17�?�{?�Y��2 �8|x(x(%�K7�3Eqc02����7'(�-�3{��-�*�#�v¡}��=`x(8:z7�-{v{(�?=Y�K]xvtFr§E�8:{�x(8:=:=:K�x(8:%7�3�3� ¾ ¦ �*± � L@k:�5n[�+�×�5n[�\��3+6575@[@2

Õn��2 ��2 ��r3K�%fK��Ew�T2��@>7%�17�-{�xvK�EG���Fps%�a/_K�'v8:{(%7��%7A�z]K7'(8:%7�3{,t?%7�nx('v%7=Gt�%���Ö31���'vK�x(8:%7�3{YA�%7'It?%7�nx(8:�@��%7�{,��8`%�'(�6K7t�x(%7'F{v���¦ lT¹7k � l@m�k ��± ²�À k �0² ¨?k:�>? � ��Õ�5n[M×D[�������+-5�5n[�2

5

Page 67: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Õ�Õ�2I�T2��>7%71��-{�xvK�EG�§�v^0L@�3K7af8:t-{IK��3E�ps%���xv'(%�=G%�A�^08u{�x(8:=`=uK]xv8`%���ps%7=:��af�3{,×s. ps'v8|xv8:t-K�=�����'(z��?L���� � ³-¹ ² ª|hjlnm � ¦ ¹ ² l �©�h �s¿Fº]©�h�³]lÔº]lT¹��d³]l©�°(³�ª«��= � �&+M[7[M×��+M[��d+-5�5n[@2�e��4�-_�'(8:�nx9%�A4_3K7_�-'�A�'v%7a ¦(­ ¾�� �˨ Á]À µ3³M¨�h ®�À Î���� Ê�� Î���� ���7�¡�K7'(L@=uK��3EG��.0_�'-2Yn[6×D�53��+6575n7o

Õ@[@24.�2«pQ2psr�'v8:{�x(8uK��{��-�*���T2��@>7%�17�-{�xvK�E�K��E�¬f2 ¡�2�*8:�?�*�§�Fps%7af_�=:��Ø�^Q8:{�x(8:=:=:K�x(8:%7�<.I'v'vK7��17�-a/�-�nxv{-)�cdØnxv�?�3E�8`��1�x(r3�����xv=`L@��>�8uE��6K7{v��� �d³ À µ ® © ² °F¨�º]lT¹ ��± ²?À k � lnm7lnmnk:��C =�&�@��_�_�=�2:�,��7¶n[M×���� n�e�+-5�5n[�o�2 e��@��_�_�=:�?af�-��xfA�'v%7a{(Lnaf_�%�{(8`�3a �s��cd×Ë5@[ 3�cs�3p&.Q�Yc�×�[@��~�'v%7�3E�r��?8:a<�3HI%�'(J,KML7��7�]×�759¡�KML�+-575@[�o�2

Õ�\�2,��2 �324�0K7=`z�%7'F{��-�ÇK��3E �T2I�@>7%�17�6{DxFK7EG� � !Q_�x(8:af8`�-8`��1"t�%���xv'(%�=Q%7A�����xv=`L@��>ÔE�8u{�x(8:=`=uK]xv8`%��*)�yI�E��?'F{DxFK��3E�8`��1§x(r3�{�x(�-K�E�Ln×Ë{�xvK�x(����-r3KMz@8`%�'v�3� �d³ À µ ® © ² °F¨�º]lT¹ ��± ²?À k � lnm7lnmnk:�8C =���@�3_�_�=�2`����] n5]×D��7�� �eD+-5�5n[7o�2�e��@��_�_�=:�?af�-��xA�'v%7a {(L@a/_�%�{(8:��a �&��c�×�5n[ 3]cs�p&.0�Ycd×D[��7~�'(%��3E�r��-8`a<��HI%�'(J,KML7����M×D�59¡�KML�+-5�5n[�o�2

Õ�5�24$ 2-à =:�?afaf�-{�xvK7E*�]�G26�@>�%717�6{DxFK7E K��3E�~�26à ���3E��-'v{(�?�*�f� !Q��×�=:8:����%7_�xv8`af8:�-K�x(8:%7��K��E tFr3%78ut���%�A�%�_�x(8:af8`�6K]x(8:%7��z]K�'v8`×K��3=`�6{,A�%7'0t?%7�nx('v%7=G%7A�r3�-K]xQ��Ø�tFr3K��317�?',���?xDJs%�'(>�{v��� �d³ À µ ® © ² °F¨�º�l�¹ ��± ²?À k � lnm7lnmnk:�>C =���@��_�_�=�2:�T��¶@[]5�×���¶�\� eD+6575@[�o�2,e�����_�_�=:�?af�?�nxIA�'v%7a {�L@af_%n{�8:��a �s��cd×Ë5@[ 3]c&�3p&.0�sc�×�[@�7~�'v%7�3E�r3�?8:aw��H0%7'vJ&KML���7�M×D�5�¡�KML�+6575n[7o�2

[���2I�T2]�@>7%�17�6{DxFK7EG�/�(^QL@�3K�af8ut?{�K7�3E�t?%7�nx('v%7=�%7A�E�8:{�x(8:=:=:K�x(8:%7�9t?%7=:��af�3{G×T.�x(��x(%7'v8uK�=78:�nx('v%�E��3t�xv8`%��3��� ¼�°(º�l�¨ ¦ �*± ²�À � �DEGG�I��K7'�x�.9�,�@�-_�x-2 +-575@[@�I��¶�5]×D��Õn�e�_�=`�-�3K�'vL"_3K�_��?'�A�'(%�a {(L@a/_�%�{(8:��a Î�hu¨�©�hjªjª`º]©�h�³]l�º]lT¹�¾�¯�¨?³]°?¯?©�h�³�l � *?�¡�K�K7{�x('v8:tFrnx-��H0��x(r3�?'v=:K7�3E�{-��\]×F+-�f�@�?_�x62I+-5�5n[�2 o

[�+724�2CpQ2,¡}%7'v�3EÇK7�3E �G24��>7%71��-{�xvK�EG� �(.I�K�=:L@{(8u{�%7A�8`�3{�xvK7��8:=`8`xDLÔ8`� 8`�E��3{�x('v8:K7= K7a/af%���8:K�'(�6K7t�x(%7'F{v��� ¾ ¦ ��± �L�³ ® °�lTº]ª«�JEJ��\7\7\�×Ë\�5��be�+-5�57\�o�2

[7�24¬f2]�0KMz@'v�YK��3E/�T2��@>7%�17�6{DxFK7EG���vc �T�-t�x�%7A�I�0���?�-'(%n{�K7�3E�_�%7=:�-{�%7��x(r��4{(�?�3{(8|xv8`z@8`xDL A����3t�xv8`%��3{�8`�/a9�3=|xv8`z]K�'v8uK���=:�{(L@{�x(�-ab{(�3� L�k�³DÂQÄ,°(³-¿ ² ¨F¨ �d³�l3©�°(³]ª«� � �G+M�7�M×F+-Õ7 e�+-575�\�o�2

[�¶�24��2 *�3�3E�{�x('v%7a<�,�G2s�@>7%�17�6{DxFK7E�K7�3EÆ�32«pQ2Y^Q%]L@=`���Ú�v~,Js%áE��?1�'(�-�<%�A A�'(�-�-E�%�a t�%���xv'(%�=`=:�?'bE��6{�8:17�§A�%7' K��"8`=:=|×t�%��3E�8`x(8:%7���6E�E�8u{�x(8:=`=uK]xv8`%���_�'v%�t��6{({Q�3{(8`��1<a���×Ë{(L@�nx(r��6{�8u{(�3� ¦ � � � ¼�°(º]l3¨�k)�d³�l3©�°?k g Á ¨�©Ëk�¼ ² ¿v±3k:� D§eD+Mo��d+MM×D�+eD+6575�5�o�2

[] 324~�2 ��2n¡�K7=`8:>T�@�G2���>7%71��-{�xvK�E��F�@��afabK�'vL�%7A�E�8u{(t?�3{({(8:%7��{(�-{v{�8:%7�b%���� 8:�3E��{Dxv'(Ln×�K7t?K�E��?af8ut48:��xv�?'FK7t�x(8:%7�3{sK��3Eb%�_�-�{�xvK��E�K�'FE�{v��ß:� �d³ À µ ® © ² °F¨9º�l�¹$��± ²�À k � lnm7lnmnk:�>C ?*�� @��+?×� @�7�be�+-575�5�o�2

[7��24$ 2�à =:�?afaf�-{�xvK�EG�Y�T2��@>7%�17�-{�xvK�EáK��3E�~�2�à ���3E��-'v{(�?��� � !Q_�x(8:abK�=s%7_��?'FK]x(8:%7�á%7AIr��-K�x9��Ø�tFr3K7��17�-'�����xDJ&%7'v>�{(�3��d³ À µ ® © ² °F¨9º�l�¹$��± ²�À k � lnm7lnmnk:�EC ?*�3�7�75�×���7�e�+-5�575�o�2

[�Õ�2,��2 �32��0K�=:z7%�'v{(�?�}K7�3E��T2G�@>7%�17�6{DxFK7EG� � !Q_�xv8`abK�=�%7_��?'FK]xv8`%��}%�AY����xv=`L@��><E�8u{Dxv8`=:=uK]x(8:%7��),{�x(�6K7E�Ln×�{DxFK]xv����-r3KMz@8`%�'v�3�L�k*Ä&°(³6¿-k��d³]l©�°v³]ª«� B��� ��@[6×Ë n� eD+6575�5�o�2

[�[@24cI2 ¬f27�08`=:af�?�*�@Ã92 H�2@¬�8:zMK9K��3E��T2@�@>7%�17�6{DxFK7EG���v.I�3K7=`L�{(8:{Y%�A*t�=:%�{(�-E/a���=|xv8`z��-{v{��-=3�3K�xvtFr�E�8u{�x(8:=`=uK]xv8`%��b%�ATx(�-'(�3K7'(Laf8|Ø@xv��'(�6{��3{(8`�31��?=:�?af�?�nxFK�'vL9à �c�t��-=`=u{(�3� �d³ À µ ® © ² °F¨ º]lT¹���± ²?À k � lnm7lnmnk:�@C ?}e�����_�_�=�2 o�����¶� �[6×D��¶��7��e�+-575�5�o�2

[�\�24$ 2�ÓÔ8`x�x(1��?�3{0K��3E}�T2��>7%71��-{�xvK�EG�§�vcdz]K�=:�3K�x(8:%7�w%�A�E�L@�3K�af8utQaf%�E��-=:{4%7A�E�8:{�x(8:=`=uK]xv8`%��}t�%7=:��af�3{4J48`x(r}�-af_�r3K7{(8u{%7� x(r3��8`��8`x(8uK�=�'(�6{�_�%7�3{(�-� � ³6¹ ² ª«hjl@m�� ¦ ¹ ² l3©�h �s¿Fº�©�h�³�l�º]lT¹$�d³]l©�°v³]ª«�EC =��3\7¶�×v+6�7¶�e�����7��o�2

[�5�2,��2 �32��0K�=:z7%�'v{(�?����¡�2��@�-'('FK}K��3E§�T2���>7%71��-{�xvK�EG�Ì�(cdz]K7=`�3K�x(8:%7�á%�A0{(�?=`Aj×Ë%7_�xv8`af8u{�8:��1�t?%7�nx('v%7=Y{�x('v�3t�x(��'v�-{�A�%7'�K7�8:��xv�?1�'vK�x(�-E ����xv=`L@��>�E�8:{�x(8:=`=uK]xv8`%��}t�%7=:��af�3�3�<Ò ® lnmnk L�k�³D ¦ l�¹�k �*± ²�À k:� C � �G+7+?×v+M��e�7�7����o�2

\���24$ 2YÓÔ8`x�xv17�?�{ K7�3E �T24�@>7%�17�6{DxFK7EG� �Fps=:%�{(�-E"%7_��?'FK]xv8`%��Ô%�A�a9�3=|xv8`z��-{v{��-=0�3K�xvtFrÇE�8u{Dxv8`=:=uK]x(8:%7��)ácdØ�_�-'(8:af�?�nxvK7=z7�-'(8`Öt-K]x(8:%7����w¾ ¦ ��± � L@k:� J � �G+67�75]×F+6�+M[/e���7����o�2

\3+72I�T2I�@>�%717�6{DxFK7E �v�d=uK��nxDJ48:E���t�%���xv'(%�=�)áxvr���{(�-K7'vtFrÆA�%�'�xvr��á{��-=|Aj×Ë%7_�xv8`af8:�?8:��1Æt�%7�nxv'(%�=Q{�x('v�3t�xv��'(�6��� L�kQÄ&°v³-¿6k�d³]l©�°(³�ª«� =��*�� n\n[M×��7�n[be�����7��o�2

\n�2I�T2*�@>�%717�6{DxFK7EG� �F�@�?=`Aj×Ë%7_�xv8`af8:�?8:��1wt?%7�nx('v%7=�),x(r3�/af8u{({(8:��1�=:8`�3>}��?xDJs�-�?��{�x(�6K7E�Ln×�{DxFK]xv�9%7_�x(8:a/8:�-K�x(8:%7��K��3E�t�%7��×x('v%7=u��� �d³ À µGk ��± ²?À k � lnm7lnmnk:� CMJ����Õ�5]×D��[���e�����7�no�2

\�¶�24.�26;3K�K����6{GK��3E��T2M�@>7%�17�-{�xvK�EG�9�v.�{�L�{�x(�-afK�x(8ut�K�_�_3'(%nK7tFrIxv%4x(r3�dE��-{(8`1���%�A������T�?'GxFK���>�{v���%�d³ À µGk ��± ²?À k � lnm7lnmnk:�CMJ��G+6¶75��]×v+- ��3+�e�����7�no�2

\7 324~�2 �K�'F{({(%7�<K��E��T2��@>�%71��-{�xvK7E*�Ô�(�d=uK��nxDJ48uE���t�%���xv'(%�=�)s.�'v�?z@8`�-J K7�3E<Kb���-JÍE��-{(8`1��w_3'(%�t��6E���'v�-� � ³-¹ ² ª|hjlnm �¦ ¹ ² l©�h �&¿Fº]©�h�³]l�º�l�¹ ��³�l3©�°(³]ª|�>C =�37�75]×D] n��e�7�7����o�2

+-�

Page 68: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

\n��24¬f2��QKMz@'(��K7�3E��T2��@>7%�17�-{�xvK�EG�Ì�(.QtFr�8`�-z]K���=:��_��?'(A�%7'vafK7�3t���%�A4a9��=`x(8:z]K�'v8:K7��=:��{�L�{�x(�-af{9J48|xvrq���3{�xvK7��=:���?�-'(%n{K��E�_�%7=:�-{v��� ¦ l©Ëk L�k ��³�l3©�°(³]ª|�EDJ��G+7+6¶�+?×v+�+-¶75be������+6o�2

\�Õ�24~�2 �K�'F{({(%7�*��¬f2��I�6{Dxv��x(�3�*��c02��I%]z@=uK��3E*��K��3E��T2��@>7%�17�6{DxFK7EG�¸�F�@�?=`Aj× !Q_�x(8:a/8:�?8:��1�ps%���xv'(%�=�%�A4K �K�'v17�?×���t?K�=:��d=uK��nx6)�~,r3��~��-�����-{v{(�?��cYK�{DxvafK7� �Y'(%�t��6{({v��� ¦ l�¹�k � lnmnk��*± ²�À k �0² ¨?k:�MJ��áe�7�o��� n\7\75�×� n57�3+�e������+Mo�2

\@[@24cI2 ¬f2T�I8:=`af�?���*Ã92 H�2G¬�8:zMKwK��E��T2*�@>�%717�6{DxFK7EG� �v~�%�_%�=`%�17Lw%�Adxv�?'v�3K�'vL<à �c E�8uK�1�'vK7af{-)Icd=:�?af�-��xFK�'vL}t��?=:=u{(�3�¾ ¦ ��± � L�³ ® °�lTº]ª«� J � e�77o���[���M×�[��75�e�7�7���o�2

\�\�2I�T2��>7%71��-{�xvK�EG�q�v��8`af_�=:��'(�3=`�6{&A�%7'4af%�E��?=*'v�-E��3t�xv8`%��wK7�3E �Y�D^�t�%��nx('v%7=:=`�-'Yxv����8:��1��3��L�k*Ä&°(³6¿ ² ¨F¨ �d³]l©�°(³�ª«� =@?*��53+�×�¶7��5�e�7�7�7¶no�2

\�5�2,��2 �32��0K7=`z�%7'F{��-�qK��3E"�T2d�@>7%�17�-{�xvK�EG���v¡}8:��8`a���a cd�3�?'v17Lqps%7�3{(��af_�x(8:%7�§8`�"¡}��=`x(8ut�%�a/_�%7�3�?�nxf^Q8u{Dxv8`=:=:K�x(8:%7�*2��K�'(x�+72�Ã0af8:�}^08uK�1�'vK7a A�%7'IKf~,Js%7×Ë�Y'(%�E��t�x0ps%7=:��af�3��� ¦ lT¹7k � lnmnk���± ²?À k �0² ¨?k:�MJ�C�e�¶�o����57 �×�Õ7�7 �e�7�7�7¶no�2

5���2,��2 �32��0K7=`z�%7'F{��-�qK��3E"�T2d�@>7%�17�-{�xvK�EG���v¡}8:��8`a���a cd�3�?'v17Lqps%7�3{(��af_�x(8:%7�§8`�"¡}��=`x(8ut�%�a/_�%7�3�?�nxf^Q8u{Dxv8`=:=:K�x(8:%7�*2��K�'(xI�2d~,r�'v�?�?×Ë�Y'(%�E��3t�x,���?x(=:L@��>�.I'v'vK7��17�-af�?�nxv{v��� ¦ l�¹�k � lnmnk ��± ²�À k �0² ¨?k:�J>Cáe�¶�o���Õ�+-��×ËÕ3+6��e�����7¶no�2

53+72,��2 �32��0K7=`z�%7'F{��-�qK��3E"�T2d�@>7%�17�-{�xvK�EG���v¡}8:��8`a���a cd�3�?'v17Lqps%7�3{(��af_�x(8:%7�§8`�"¡}��=`x(8ut�%�a/_�%7�3�?�nxf^Q8u{Dxv8`=:=:K�x(8:%7�*2��K�'(xs¶32�¡�%7'v�Q~,r3K7� ~,r�'v�?� �d'v%@E��3t�xF{sK7�3E à �-���?'FK�=:8`�-�-E����?x(=:L@��>b.I'v'vK7��17�-a/�-�nxv{v��� ¦ l�¹�k � lnmnk ��± ²�À k �0² ¨�k:�J�C�e�¶�o��3Õ�+6Õ]×�Õ�75�e�7�7�7¶no�2

5n�24¬f2 d2�Ó����&pQ2CpQ2 �d���dÓ 2 Y2 *��L@���?�"K��3E"�T2Y�@>7%�17�6{DxFK7EG���(�4�6K7t�xv%7' 3]{(�?_3K7'vK�x(%�'�_�'(%�t?�-{v{��6{�J48`x(r"'(�6t�L�t�=:�-{�×��2^Q�-{(8`1���A�%�'It�%7af_�%�{(8|xv8`%��wt?%7�nx('v%7=u��� �d³ À µGk%��± ²?À k � l@m�l@m�k:��C D�e�¶�o��� ���+?×� @�+/e�����7¶no�2

5�¶�24~�2 �K�'F{({(%7�*�*¡q2 �T2�à %]z]K]xv{(abK�'v>T���T2��@>�%717�6{DxFK7EG��K��3EqpQ2«pQ2 �d�*� ��ps%7�nx('v%7=�{�x('v�3t�xv��'v��{��-=`�6t�x(8:%7��A�%7'9'(�6K7t�xv%7'6�{(�?_3K7'vK�x(%7',K��E 'v�-t?L�t�=:�Q_�'v%�t��6{({(�-{v��� ¦ l�¹�k � lnmnk ��± ²�À k �0² ¨?k:�J>Cáe�Õ�o��G+67��M×F+67¶� �e���7��¶�o�2

57 32,Ã92 H�24¬�8:z]K��0c02 ¬f2&�I8:=`af�?� K��3E �T2,��>7%71��-{�xvK�EG� �v.I�-�?%�xv'(%�_�8ut}_�r3K�{���� �n��8:=`8:��'v8`��a E�8uK�1�'vK7ab{?)á.�{(��'vz7�-L@�3���± ²?À k � lnmnk`gT¿?h�k:��G � eD+6��o��G+-57��¶]×F+-5n��¶be�7�7��¶�o�2

5n��24�Ƭf2�cd��1��?=:8`�-�*��~�2 �K7'v{v{(%7��K7�3E��G2��@>7%�17�6{DxFK7EG� ����af_�=:�?af�?�nxvK�x(8:%7�/%�A�%7_�xv8`abK�=�%�_�-'vK�x(8:%7�9A�%7'�r��-K�x�8`�nx(�-17'FK]xv�-EE�8u{Dxv8`=:=uK]x(8:%7�<t�%�=`�3a/�{(�3�Ô¼�°(º]l3¨?k ¦ ��± ²?À � � � =�e���K�'(x,. o��n[7[M×�7\�+�e�����7¶�o�2

5�Õ�24.�2G;K7K��3�-{0K7�3E��T2*�@>�%71��-{�xvK7E*� �v$&�����-' ~�K��3><^Q�-{(8:17�}A�%�' .Qt?t��-_�xvK7��=:�fps%7�nxv'(%�=����?'(A�%7'vabK��3t?�-�3� ¦ l�¹7k � lnmnk��± ²?À k �Q² ¨?k:�MJ�C�eD+6��o����+-5�\]×D77�7\be�7�7��¶�o�2

5@[@2,��2 �32��0K�=:z7%�'v{(�?����T2���>7%71��-{�xvK�EG�3�2CpQ2�¡}%7'v�3E<K��3E<Ã�2�.0=:{�xvK�EG� � !Q_�x(8:abK�=�{(�?=:�-t�x(8:%7�}%7A�t?%7�nx('v%7=:=:�-Ewz]K�'v8:K7��=`�6{(�3�¦ lT¹7k � l@m�k ��± ²?À k �Q² ¨?k:�MJ�C�eD+- no���¶n�[�¶]×�¶��\7 �e�7�7��¶�o�2

5�\�24¬f2�QKMz@'(��K7�3E��T2G�@>7%�17�-{�xvK�EG�Ç�F�@�?=:�-t�x(8:%7�}%�Adz]K7'(8uK���=:�-{4A�%7'Q{�xvK7��8:=`8:�?8:��1�t?%7�nx('v%7=*�{�8:��1�_�%7=:��z7�6t�xv%7'F{(�3� ¦ � ���¼�°(º]l3¨�k,¾ ® ©�³ À k �d³]l©�°v³]ª«�MJ � e�\no��*+6¶75�¶]×F+-¶75�\�e�7�7��¶�o�2

5�5�24.�2s;3K7K7���-{fK7�3EÔ�T2s�@>�%717�6{DxFK7EG� �v�nxFK]x(�}{(_3K7t?�<'(�6K�=:8`�6K]x(8:%7�§%�A a/%�E��-=I_�'v�-E�8ut�xv8`z��}t�%7�nxv'(%�=`=:�?'F{(�3� � ³-¹ ² ª|hjlnm �¦ ¹ ² l©�h �&¿Fº]©�h�³]l�º�l�¹ ��³�l3©�°(³]ª|�>CMJ�e� no���¶3+�×D] � �e�7�7�7¶no�2

+6�7��24�T2��@>7%���'FK7{YK7�3E��T2��@>�%717�6{DxFK7EG���v���?_3K7'vK�x(8:%7�b%�AGxv�?'v�3K�'vL/r���xv�?'v%�K��-�?%7x('v%7_�8ut,af8|Ø@x(�3'(�6{Y8:��K9t?=`%n{��6Eba9�3=|xv8`z��-{v{��-=�3K�xvtFr<E�8:{�x(8:=:=:K�x(8:%7��×�E��-t-K��nx(�-',rnL@��'v8uE���� ��± ²?À h�¿Fº]ª � lnm7hjl ²F² °�hjlnm<º]lT¹�Ä&°v³-¿ ² ¨v¨�hjl@m��EJE?áe�¶�o��375�+?×˶��� e������ no�2

+6��+724�T2Y�@>�%71��-{�xvK7E*� �Fps%7�nxv'(%�=,{�x('v�3t�x(��'v�wE��-{(8`1���A�%�'�t�%7af_�=:��xv�}tFr��?af8ut?K�=,_�=uK��nxF{(�3� �d³ À µ ® © ² °F¨�º]lT¹ ��± ²?À h�¿Fº]ª� l@m�hjl ²v² °�hjlnm7�EC � eD+?×��o��3�+-5]×D�¶7 �e�7�7�7 no�2

+6���2,��2 ¬f23cY��17�-=`8:�?�}K��E<�G2�@>7%�17�6{DxFK7EG�"�v�@�-=`�6t�xv8`��1�K7_�_�'v%7_�'v8uK]x(��t�%��nx('v%7=Gz]K�'v8:K7��=:�-{&A�%7'IKfr3�-K]x(×�8:�nx(�-17'FK]x(�6E E�8:{�x(8:=|×=uK]x(8:%7�<{(L@{�x(�-a J48`x(r}_�'v��A�'FK7t�x(8:%7�3K�x(%7'F�����d³ À µ ® © ² °F¨9º]l�¹ ��± ²?À h�¿Fº�ª � l@m�hjl ²v² °�hjlnm7�>C � e���o��3Õ�\7¶�×ËÕ�5�+9e���7�7 no�2

+6�7¶�24�T2��@>7%���'FK7{�K7�3Eq�T2��@>7%�17�-{�xvK�EG���(~,8:af��e�cY���?'v17L�o��I� �n��8:'(�-a/�-�nxv{�8:�"ps=:%�{(�-E�$,K]xFtFrq^08u{�x(8:=`=uK]xv8`%���.I'v'vK7��17�?×af�?�nxv{v��� �d³ À µ ® © ² °F¨9º�l�¹$��± ²�À h�¿Fº]ª � lnm7hjl ²F² °�hjlnm7�EC � e��7o��3\�75]×�\7¶n[�e�7�7�� @o�2

+6�� 32,.�2;3K7K7���-{4K7�3E}�T2�@>�%71��-{�xvK7E*����_�4×Ë���?��xv'vK7=`8:�-K�x(8:%7�*)�8:�nx(�?1�'vK�x(�6E�_�'v%�t��6{({,K��Ewt?%7�nx('v%7=*E��-{(8`1��3��� ��³ À µ ® © ² °F¨º]lT¹$��± ²?À h�¿vº�ª � lnm7hjl ²F² °�hjl@m��>C � e�\�o���+? @[7�M×F+? n\n[fe���7�7 no�2

+6����24�T2��@>�%7��'FK7{&K��3Ew�T2��@>7%�17�6{DxFK7EG���v~,8`af� '(�-���38`'v�?af�?�nxF{dA�%�'sr��?x(�-'(%nK��?�-%�xv'(%�_�8:t0E�8:{�x(8:=:=:K�x(8:%7��8:�w�3K]xFtFr t�%�=`�3a/�{(�3��d³ À µ ® © ² °F¨9º�l�¹$��± ²�À h�¿Fº]ª � lnm7hjl ²F² °�hjlnm7�EC � e�5�o��G+-Õ�\75]×F+M[��7��e������ no�2

+7+

Page 69: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

�áW,WdÛ � 0IS�Þ0U@Ü�¤3¥+72I�T2��@>7%�17�6{DxFK7EG���(¡}%�E��-=`=:8`�319K��3Ewps%7�nx('v%7=%�A�^Q8:{�x(8:=`=uK]xv8`%��wps%7=:��af�3{&K7{&K9� �q���@L�{Dxv�?ab����Î � �GÒ � � ¾ � ³]l�³��m7°(ºvµ3±n¨��=E= � �]��26cstF>7�-'(abK��3�fe�cYEG2Co��] n�7¶�×� +7+4eD+657\75no�e�;3'(%�a���]xvr9cd�3'(%�_*2��@L@af_*2�%7��ps%7af_���x(�?'�.I_3_�=`8ut?K�x(8:%7�3{8:� xvr���psr��-a/8ut?K7=G���3E��3{�x('vL�eËp&.0p&�I�4\75no���cd'v=uK���1��?�*��à �?'vabK��@L7��.0_�'(8:=d+657\75no�2

�2I�T2��>7%71��-{�xvK�EG2��(�4%����3{�xQps%7�nx('v%7=u���Ä&°vº7¿?©�h�¿Fº]ªTÎ�hu¨�©�hjªjª`º]©�h�³]l �d³]l©�°v³]ª«�Ó 2 Y2 *��L@���?�qe�cYE�8`x(%�'Fo���ÃdK��}HI%n{Dxv'vK7�3E�4�-8`��r3%7=uEG�*+-5�5���@75�+�×�¶7��5�2

¶�2,��2]��%�{�x(=:��xvrnJ,K�8`x(�&K��3E/�T2��@>7%�17�6{DxFK7EG� �(�4%����3{�x�a9�3=|xv8`z]K�'v8uK���=:�&t?%7�nx('v%7=n�3{(8`�31� � af��xvr�%�E�{�»�.I�3K7=`L�{(8:{-�]E��-{(8`1��K��E����3E��{Dxv'(8uK�=�.I_3_�=`8ut?K�x(8:%7�3{v��� � ¨F¨?º Á ¨0³]l ��³�l3©�°(³]ª �YÄ ² °F¨�µ ² ¿�©�hji ² ¨Ihjl�©�± ² ¼T± ² ³]° Á º�l�¹�hj©�¨Y¾sµ7µTª«h�¿Fº]©�h�³]l3¨F�@��2 d2~�'(�-��xv=`�-abK���K��E��32«pQ2�ÓÔ8`=:=`�-ab{/e�cYE�{-2Co��G$&8`'v>@r3K��3{(�?'6��+6575�¶}e *�6t�xv��'(����%�xv�-{0A�%7' 8`�@z@8`x(�-E�{�r�%�'�x�t�%���'v{(�9K�x0x(r3�+-5�57¶/cd��'v%7_��-K7�<ps%���xv'(%�=�ps%7��A��-'(�-�3t��Mo��3�Õ�5]×�¶7¶@[@2

324cI2 Ó 2*�nK7t�%��3{(�?��K7�3Eá�T2��@>�%717�6{DxFK7EG�����DE��?�nx(8`Öt?K�x(8:%7��%7As��=:=|×�ps%7�E�8|xv8`%����-E��d=uK��nxF{ ×0.¸$s�-�3tFr�abK�'v>��d'v%7�3=`�-af�3�¼T± ² � ³-¹ ² ª«hjl@m�³� · lT¿ ² °�©�º]hjl3© Á hjl �d³]l3©�°(³�ª�g Á ¨�© ²�À ¨��&Ä&°(³6¿ ²F² ¹]hjl@m]¨�³�Âf©j± ²�� � ����gTº]l©Ëº Å0º�°?¯vº�°(º��}³]°(Ð]¨(±�³Fµ����2�G2�@af8|xvr}K��3Ew¡�23^ K�r�=:�?r�e�cYE�{-2 o���@_�'v8:��17�-'�×ËÃ��?'v=:K713��*%��3E�%7���G+-5757 3��¶7Õ@[6×�¶n[�Õ�2

��2I�T2*�@>�%717�6{DxFK7EG�s�(;3'(�-���3�?�3t?L�×�E�%�afK78`�}af�?x(r�%�E�{QA�%7'�K��K�=:L@{(8u{0K��E�E��-{(8:17�*2 ��2G�4×Ë8`��Ö��8|xDL}af�?x(r�%�E�{ K��3E�'(%����3{�xt�%��nx('v%7=u��2 ��² ©�±�³6¹M¨ ³� � ³-¹ ² ªdÅQºM¨ ² ¹wÄ&°v³-¿ ² ¨v¨$�d³]l©�°v³]ª��QÄ&°v³-¿6k�³D ½ ¾�¼ Ê ��¾ g ¦ hjl�¾Ql3©�º]ª Á º��b¼ ® °(Ð ²?Á �4¾ ® mnk� � ���3���23$&�-'(���?'�e�cYEG2Co��3¬�=:�@Js�-'4.0t?K�E��?af8ut��d���3=`8u{�r3�?'F{?��HI�?x(r��-'(=uK��E�{?��+-575n����+7+6¶]×F+6�7�2

Õ�2I�T2@�@>7%�17�-{�xvK�EG���v;�'v� �n���-�3t�Ln×�E�%7abK�8:�/a/�?x(r�%�E�{YA�%7'sK��3K7=`L�{(8:{dK7�3EbE��6{�8:17�*2��(��2@ps%7�nxv'(%�=`=uK���8:=:8|xDL/K��3K7=`L�{(8:{�%7A��@��� !�@L�{�x(�?ab{v��� ��² ©j±3³-¹]¨�³� � ³-¹ ² ª�ÅQºM¨ ² ¹�Ä&°v³-¿ ² ¨v¨��d³]l©�°(³�ª �0Ä&°(³6¿-k}³� ½ ¾�¼ Ê ��¾ g ¦ hjlá¾Ql3©�º]ª Á º��/¼ ® °(Ð ²�Á �&¾ ® mnk� � ���3���23$&�-'(���?'�e�cYEG2Co��3¬�=:�@Js�-'4.0t?K�E��?af8ut��d���3=`8u{�r3�?'F{?��HI�?x(r��-'(=uK��E�{?��+-575n����+6�7¶]×F+-5�+�2

[@24¡�23�0%]z�EwK7�3E<�T2��@>�%71��-{�xvK7E*���(~��-tFr3��8 �n���6{,8`�wxvr��/ps%7�nxv'(%�=G%�A�����xv�?'Ft�%������-t�x(�6E �Y=:K7��xF{(�3� ��² ¿F±�º]©�°(³�l3h�¿9g Á ¨ �© ²�À ¨�¼ ² ¿v±�l3h �?®3² ¨9º�l�¹�¾&µ7µTª«h�¿Fº]©�h�³]l�¨?k Ñ ³]ª ®�Àb² �&Î9h�º?m7l�³]¨�©�h�¿ � �0² ª«h�º�¯�hjª«hj© Á º�l�¹ ��³�l3©�°(³]ª*g Á ¨�© ²?À ¼ ² ¿v±�l3h �?®3² ¨��pQ2 ~�2 *�-%7�3E��6{�e�cYE*2 o��à %7'FE�%7�<K��E $&'v�-K7tFr}��t?8`�-�3t����d�3��=`8u{(r��?'F{?�37�7�����T+-¶�5]×D��7�32

\�2,��2 �32T�0K7=`z�%7'F{��-�<K7�3E��T2G�@>�%717�6{DxFK7EG� �(~,r��-%7'vL %7AY^08u{�x(8:=`=uK]xv8`%��3���á���*) � l�¿ Á ¿�ª`³Fµ ² ¹�h�º�³DÂ�g ² µ�º�°(º]©�h�³]lágG¿�h ² l�¿ ² k�DK��<^�2�ÓÔ8`=u{(%7��e�csE�8|xv%7'(×�8:��×�tFr�8:��Avo���.0t?K�E��?af8ut��d'v�-{v{?��7�7�7�3�@_�_*24+7+�+M[M×v+�+-¶� 2

5�2I�T2��@>7%�17�6{DxFK7EG���(����xv�?1�'vK�x(8:%7�á%�AI%�_�x(8:abK�=&%7_��?'FK]x(8:%7�qK7�3E�t�%��nx('v%7=u��� ���*) ¼�± ² hjl3© ² m�°(º�©�h�³�ldzD ¹ ² ¨�h|m7lǺ]l�¹¿F³]l©�°(³�ª`k ��23�@��A��-'(�-=`8u{IK7�3E ¡q2CpQ2à �-%7'v178uK7E�8u{�e�csE�8|xv%7'F{vo���cd=u{��-z@8`�-'-������� �n_3_*2� �\n�M×D���7�32

N}OQV�U�Wd¤�W�� ��W,WdÛ S�XQO���WsPI¤3X0S �%1sW���P�/ Ü�¥+72f�(�Y'(%�t?�?�-E�8`��1n{ %�A4{�L@af_%n{�8:��a��s��c0ß 5@[ 3�cs�3p&.Q�Yc�×�[@�T~�'(%��3E�r��-8`a<��¡�KML�+6575n[������@�3_�_�=:�?af�?�nx�xv% ��³ À µ ® © ² °F¨

F �*± ²�À h�¿Fº]ª � lnm7hjl ²F² °�hjlnm7��+��G+-5�5n[@2�cYE�8|xv%7'0�T2��>7%71��-{�xvK�EG2�2f�v���?=:�-t�xv�-E<K��E �?Ø@x(�?�E��-E<_3K7_�-'v{4A�'(%�a x(r3�9{�L@af_�%�{(8`��a %7�}�s��cIß 5n[ 3�cs�3p&.Q�Yc0ßC[�������³ À µ ® © ² °F¨ F ��± ²?À h�¿Fº]ª� l@m�hjl ²v² °�hjlnm7�>C ?��3HI%n{?2d 7×����G+-5�575�2Yà �3�-{�x0cYE�8`x(%�'Q�T2�@>�%71��-{�xvK7E*2Y�@�?��)��(csE�8|xv%7'v8:K7=:�3� ��³ À µ ® © ² °F¨�º]lT¹ ��± ²�À k� l@m�l@m�k:�EC ?��� 7 �5<e�+-575�5�o�2

¶�2f�v���?=:�-t�xv�-Eb_K�_��?'F{dA�'v%7a {(L@a/_�%�{(8:��a¸�s��cd×Ëc&�3p&.0�scIß 5n[@��~�'v%7�3E�r��?8:a<�@¡�KMLw+6575@[]���EL�³ ® °�l�º�ª*³DÂ4Ä&°(³6¿ ² ¨F¨%�d³�l �©�°(³]ª«�EB*��H0%�{-2Y���G+-5�57532�à ���6{Dx0csE�8`x(%7'I�T2��@>7%�17�-{�xvK�EG2

�nXsU@Ü�¤3XIS�U�VDWYX0S � � WsX �FÜ*¤�Ü�XQRTÜ �<S�Þ�Ü�¤3¥+724¡�2M¡}%7'FK�'v8��6�T2]�@>7%�17�6{DxFK7E�K��3E�^�2 cI2M�48`z��?'FK������af_�=:8:t-K]x(8:%7�{*%�A����nx(�-'(�K�=�¡�%@E��?=�ps%7�nx('v%7=]A�%�'��Y�D^"ps%7�nxv'(%�=`=:�?'F{(�3�Ä&°(³6¿6k,¾ Àb² °�h�¿vº�l �d³]l©�°v³]ª��d³]l6 ² ° ² lT¿ ²� ¾�� ���M����K��<^08:�?1�%3�p&K7=`8`A�%7'v��8uK����������f+-5�\� 32

�2I�T2��@>7%�17�6{DxFK7E�K��Eq¡�2�¡}%7'FK�'v8����v¡}%�E��?=&yI�3t?�?'(xvK�8:�nxDL7�d�Y'(%�t��6{({9^0�6{�8:17��K7�3Eq�Y'(%�t��6{({fps%7�nx('v%7=u������K�_��?' +-K3�.I�(psrc".0���@�3K�=�¡}�?�?x(8:��13��psr38:t-K�17%��HI%]zT2,+-57\n��2

¶�2I�T2��@>�%717�6{DxFK7EbK7�3E�¡�2�¡}%�'vK7'(8�����ps%7�nx('v%7=%�A���=:=`×Dps%��3E�8`x(8:%7���6E��d=uK��nxv{-)��I8:17r �Y��'v8|xDLb^Q8:{�x(8:=`=uK]xv8`%��3���@_3K7_�-'4[] �K3�.I�(psrc".0���@�3K�=�¡}�?�?x(8:��13�3¡�8:K7a/8*$&�6K7tFr*��H0%]z�2,+657\7Õ32

32I�T2���>7%71��-{�xvK�E�K7�3Eá¡�2�¡}%�'vK7'(8��I����af_�=:8ut?K]xv8`%���%7A �K�'v17�b�4à�.4×�cd=:�?af�?�nxF{�%7��ps%7�nx('v%7=d���-'�A�%�'(abK7�3t��6���T_3K�_��?'Õ7E*��.I�(psr3cÔ.0���@�3K�=*¡}�-��xv8`��1�3¡}8uK�af8�$&�-K�tFr*��HI%]zT2,+-5�\7Õ�2

+6

Page 70: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

��2I�T2��>7%71��-{�xvK�E K7�3E<¡�23¡}%�'vK7'(8����(�4%����3{�x0���?'(A�%7'vabK��3t?�Q%7A�^Q�-t?�?�nx('FK�=:8`�-�-E}ps%7�nx('v%7=���L@{�x(�-ab{4�@L����3E��-_�-�3E��-��x^Q�-{(8`1��3{(�3�Ä&°(³6¿-k4¾ Àb² °�h�¿Fº�l �d³]l©�°(³�ª��d³]l6 ² ° ² l�¿ ²� ¾�� ���]�*+][]\��]×v+][]5�����¡�8`���3�-K�_�%7=:8u{?���������b+657\n[�2

Õ�2I�T2G�@>7%�17�6{DxFK7E<K��3E�¡�2�¡�%7'FK�'v8��s�Fps%7�nxv'(%�=*%�AY�08`1�r�×Ë�Y��'v8|xDLw^08u{Dxv8`=:=uK]x(8:%7�áps%7=:��af�3{IA�'v%7aÌK��I%7���3{�x(�3�-{v{IÃ08:�?J,×_�%78:��xF���Ä&°v³-¿6k4¾ Àf² °�h�¿Fº]l �d³�l3©�°(³]ª��d³�l- ² ° ² lT¿ ²� ¾�� ���]�*+-¶n7�M×F+-¶�¶7�3��¡}8:�����6K�_�%7=:8:{-���7�3���f+-57\@[@2

[@2I�T23�@>�%71��-{�xvK7E K��3Ew¡�2�¡}%�'vK7'(8����(�4%����3{�xQps%7�nx('v%7=T%�A�^08u{�x(8:=`=uK]xv8`%��}ps%�=`��af�3{v���Ä,° ² µT°�hjl3©�¨ ��� ©�± ¦v­ ¾�� ��³�l- ² ° �² l�¿ ² �3Ã�%7=�2����\3+�×D�\�Õ���¡ #���3tFr��-�*�3����=`L�+-57\@[@2

\�2I�T2��@>�%717�6{DxFK7E�K7�3E�¡q2@¡�%7'FK�'v8���� �ÃI×�t�%���xv'(%�=3%7A�K9�08`1�r�×��d��'v8|xDLb^Q8:{�x(8:=:=:K�x(8:%7��ps%7=:��af�3���3Ä&° ² µ�°�hjl©�¨ ��� ©j± ¦(­ ¾���d³]l6 ² ° ² l�¿ ² �3Ã�%�=�2�\��3 3+-Õ�×� @7����¡ #���tFr��?�*��7��=:L�+657\n[�2

5�2I�T2��@>�%717�6{DxFK7EG���(.0�3K�=:L�{�8u{YK7�3Ewps%���xv'(%�=3%7A�^08u{Dxv8`=:=uK]x(8:%7�}ps%7=:��af�3{v���n���nz@8`x(�6E�=:�-t�xv��'v��p&�I����. ß \n[��n�Y'vK7r3K����@�?_�x+-5�\n[�2

+6��2I�T2��@>7%�17�6{DxFK7EG���(^Q8:{�x(��'v�3K7�3t��0�I�DBD�-t�x(8:%7��8:� ^Q8u{Dxv8`=:=:K�x(8:%7�wps%�=`�3a/�{(�3��Ä&°v³-¿ ²F² ¹]hjlnm�¨��*Ò � � Î0¾�¼n¾�������¶7Õn�M×�¶n[�+7�+-5�x(r<cd��'v%7_��-K7�<ps%���AD2 !Q�}~,r���y0{(��%�A�ps%�af_���x(�-'v{,8:��psr��?a<2dcY��132:�3à #%�xv�?��%7'v13�3�@J&�-E��-�*���������b+-5�\7\32

+�+72I�T2,�@>7%�17�-{�xvK�E�K7�3EÔ¡�2Y¡}%�'vK7'(8�� ��ÃdK7'(8uK���=:���@�?=:�-t�x(8:%7�"A�%7' ^0�6t��?�nxv'vK7=`8:�?�6EÔps%��nx('v%7=u���s��K7_�-'}+67\7t��,.I�(psrc.I�3�n�K�=¡��?��xv8`�313�7ÓáK7{(r�8:��1�xv%7�b^�pQ�nH0%]z�2&+-5�\7\fe��I�?_�'v8`�nxv�-Ef8:�}+-575nQ8`� ��¦ ���n{��-�I_3K�_��?'s¶7¶�8:�b=`8u{Dxs%�A@BD%7��'v�3K7=_����3=`8ut?K�x(8:%7�3{Fo�2

+M�2I�T2s��>7%71��-{�xvK�E�K��E"��2 *���3E3{Dxv'-#%�aw�/�(¡���×�%�_�x(8:abK�=0�Y�D^#{(��x�xv8`�31�{/A�%7' ^08u{Dxv8`=:=uK]x(8:%7� ps%�=`��af�3{v���,��K�_��?'}+M�Õ�AD�.I�(psrc".0���@�3K�=�¡}�?�?x(8:��13��ÓáK7{(r�8:��1�xv%7�<^�pQ�HI%]zT2,+-57\�\�2

+6¶�24~�2*¡}��B�E��?=:=dK��3E��T2��@>�%717�6{DxFK7EG�,�vcY{�x(8:afK�x(�/%�A&_�'(%�t?�-{v{0%���x(_���xv{ A�'v%7a�a9�3=|xv8`_�=:��{(�-t�%��3E�K7'(L<af�-K�{���'v�?af�-��xF{(�3�Ä&°(³6¿6k,¾ Àb² °�h�¿vº�l �d³]l©�°v³]ª��d³]l6 ² ° ² lT¿ ²� ¾�� ���M���+7+MM×D�+M�+7���d8`x�xv{(����'v17r����7���3�b+-57\�5�2

+- 32I�T2���>7%71��-{�xvK�EG��cI2�Ó 2��nK7t�%��3{(�?��K7�3Eá��2 *�3�3E�{�x(' #%7a<�0�F�@�?=:�-t�x(8:��1<x(r��b���-{�x�E�8u{�x(8:=`=uK]xv8`%��át?%7�nx('v%7=d{�x('v�3t�x(��'v�-�3�Ä&° ² µ�°�hjl©�¨ ¦v­ ¾���g Á]À µ3³M¨�h ®�À Î���� Ê�� Î�� � �7��5n�M×�¶7����n¡�K7K7{�x('v8utFr�x6��H d2:�3.0��1324+657\7532

+M��2I�T2M�@>7%�17�-{�xvK�EG���v~,r��sà 8:���3{�×Ë^Q��r��-a c ���K]x(8:%7� %�A��Y'(%�t��6{({G^Q�-{(8:17��K��3E9ps%��nx('v%7=u���?��K7_�-'d+? @]�7�6.I�(psr3c}.0���@�3K�=¡}�-��x(8:��1�3��K��};�'FK��t�8u{(t?%3��HI%]zT2,+-5�\75�2

+6Õ�2I�T2s��>7%71��-{�xvK�EG�sc02�Ó 2Y��K�t�%��3{��-�"K7�3E"¡�2Y¡}%�'vK7'(8��9�v^Q$s×�t�%7�nxv'(%�=&%7A�E�8:{�x(8:=`=uK]xv8`%��Ôt�%7=:��af�3{v���&��K�_��?'}+-Õ@[]$sØG�.I�(psrc".0���@�3K�=�¡}�?�?x(8:��13���K��<;�'FK��3t?8:{vt�%�@H0%]zT24+-57\�5�2

+][@2I�T2s��>7%71��-{�xvK�EG�s��2�����3E�{�x(' #%7a K��3EÆ¡�2s�I%]z�EG�/�Fps%7�nxv'(%�=4%�A�8:E��-�nx(8ut?K�=0_3K�'FK�=:=`�-=4_�'v%@t?�-{v{��6{(�3�Y��K�_��?'}+6Õn[�$&K3�.I�(psrc".0���@�3K�=�¡}�?�?x(8:��13���K��<;�'FK��3t?8:{vt�%�@H0%]zT24+-57\�5�2

+6\�2I�T2���>7%71��-{�xvK�EG�*���D{v{(���-{�8:��E�L@�3K�af8ut,a/%�E��-=`=:8:��1��3{(8`��1�E�8u{�x(8:=`=uK]xv8`%��fK�{dK��f�?Ø�K7af_�=`�6���7�Y'(�6{��-�nx(�-E/K]xYÏ ® °F¨?¹7º-m ² l ²� � � � �H0~4HQy���~�'v%7�3E�r��?8:a<����K7�*2,+-575���2��d���3=`8u{�r3�-Ew�@L�HI�D;&�(! {(=`%2

+65�2I�T2���>7%71��-{�xvK�E�K7�3Ef¡�2��0%]z@E*�*�(yQ{��4%7AT;3'(�-���3�?�3t?L�×�^Q�?_��?�3E��-�nxs�4à�."A�%7'&ps%���xv'(%�=3�nx('v�3t�x(��'v�0�@�?=:�-t�x(8:%7�3�3�@Ä&°v³-¿6k¾ Àb² °�h�¿Fº]l �d³]l3©�°(³�ª��d³]l- ² ° ² l�¿ ²� ¾�� ���]��+-¶7¶�×��+-¶�5�����K7�}^08:�?1�%3��¡�KML�+6575���2

7��24cI2 Ó 2*�nK7t�%��3{(�?��K7�3Eá�T2��@>7%�17�6{DxFK7EG� �(^QL@�3K�af8ut?{�K��3E�ps%7�nxv'(%�=�%7A&y0�3{DxFK���=:�b^08u{�x(8:=`=uK]xv8`%���ps%�=`��af�3{v���Ô�Y'(�?×{(�?�nx(�6E K�x � � ©�± �dº�l�º7¹�h�º]l ��± ²?À h�¿Fº�ª � l@m�hjl ²F² °�hjl@m �d³]l6 ² ° ² lT¿ ² ��QK�=:8|A�K�ØG���7��=:L�+M�M×D�+��+65757�32

�+72I�T27�@>�%71��-{�xvK7E*�Mc02MÓ 27��K�t�%��3{��-�9K��E9��2 *�3�3E�{�x(' #%7a<�G�(¡}%�E��-=`=:8:��1Q'v� �n��8:'v�?af�?�nxv{�A�%�'�'v%7�3�3{Dx�t�%��nx('v%7=@%�AE�8:{�x(8:=`=uK]×x(8:%7�ft�%�=`�3a/�{(�3��Ä&°(³6¿ ²F² ¹]hjl@m]¨ � � ©�± ¦(­ ¾�� �d³]l6 ² ° ² lT¿ ² �7~�K�=:=`8:�*�7cs{Dxv%7��8uK���.0��132&+-5�57�32��d���3=`8u{�r3�-E��@L����-'(1nK�af%7��d'v�-{v{-�+!0Ø@A�%�'vEG��yQ¬f��Ã�%7=�2 Õ3�G+-53+�×F+-5n[�2

��24~�2�¡}��B�E��?=:=�K��Ew�T2��@>7%�17�-{�xvK�EG���Fps%7af_�%�{(8|xv8`%��}ps%��nx('v%7=T%�A�^08u{Dxv8`=:=uK]x(8:%7��ps%�=`��af�3{4yQ{�8:��1b¡}��=`x(8:_�=:��~��-af_�-'vK�×x(�3'(��¡}�6K7{(��'(�-af�?�nxv{v������K�_��?'07¶�1��¾ ¦ ��± � ¾Ql3l ® º�ª ��²v² ©�hjlnm7��psr�8ut?K�1�%3��H0%]z�2,+65757�32

7¶�24cI2 Ó 2T��K�t�%7�{��-��K��3E��G2T�@>�%71��-{�xvK7E*�Y�(¡���=|xv8`_3=`�f�nx(�6K7E�Ln×D�nxvK�x(�-{Q8:���DE��-K7=�~,J&%��Y'(%�E��3t�x ^Q8:{�x(8:=:=:K�x(8:%7�3�3����K7_�-'+-¶�¶7K3��¾ ¦ ��± � ¾Ql3l ® º�ª ��²v² ©�hjlnm7��psr�8ut?K�1�%3��H0%]z�2,+65757�32

� 324cI2 Ó 23�nK7t?%7�3{(�?�*� Y2 �K7'(%�tFr�����¡�23¡}%�'vK7'(8�����2 Ó 2.0�3E��-'v{(�?�<K��3E}�T2T�@>7%�17�6{DxFK7EG���(�I%7���3{�x ps%7�nxv'(%�=G%�A��I%7af%7×17�-���?%��3{,.I�-�?%�xv'(%�_�8ut ^Q8u{Dxv8`=:=:K�x(8:%7�3�3����K�_��?'0�+7+-E*��¾ ¦ ��± � ¾Ql3l ® º]ª ��²v² ©�hjlnm7�Tpsr�8ut?K717%3��H0%]z�2,+65757�32

���24¡�2��I%]z�EG�@��2�*���E�{Dxv'-#%�a¸K��3Ew�T2��@>7%�17�-{�xvK�EG����ps%7�nx('v%7=:=uK���8:=`8`xDLf.I�3K7=`L�{(8:{&y0{(8`�31�;�'v� �n���-�3t�Ln×�E��?_��?�E��?�nx4¡}�-K�×{(��'(�6{&A�%7'4���nx(�-'vK�t�xv8`%��3{,K��3Ew^08u{�x(��'v�3K��t��-{v������K7_�-'4¶�+6�B��¾ ¦ �*± � ¾Qll ® º]ª ��²F² ©�hjlnm7�Tpsr38:t-K�17%��HI%]zT2,+-575���2

+-¶

Page 71: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

7Õ�24��2�*���3E3{Dxv'-#%�aw���T2��@>�%71��-{�xvK7EbK7�3E ��× ��2nÓ�K7��13���(Ó��-8`1�r�x4�@�?=:�-t�x(8:%7��A�%7',� 8:��Ö3��8`xDL�K��E�a9��×Ët?%7�nx('v%7=a/�?x(r�%�E�{» ���3{(8:17rnxv{QK��3E<�?Ø�K7af_�=`�6{4A�'v%7aÌ_�'v%�t��-{v{It?%7�nx('v%7=u���Gg Á]À µ3³M¨�h ®�À ³�l�� � ³�¯ ® ¨�©�d³]l3©�°(³�ª�g Á ¨F© ²?À Î ² ¨Fh|m7l · ¨�hjlnmÒ ��hjl��dlhj© Á º�l�¹ �Q² ª`º�© ² ¹ ��² ©�±�³6¹M¨�� �dp&K7a9��'v8uE�17���y0¬f�T¡�K7'vtFrq+65753+720�Y����=:8:{(r��-E�8`�*)I��2 ��2T�0K7afa/%��3E�e�cYEG2Co�����3{�x(8`x(��xv��%�A�¡}�-K�{��3'(�-a/�-�nx4K7�3E}ps%7�nx('v%7=���*%7�E�%7�*�G+65753+7�T+-¶�5]×F+6��[�2

n[@24cI2�Ó 2��nK7t?%7�3{(�?�*����2 ����3E�{�x(' #%7a�K��3Eq�G2��@>�%71��-{�xvK7E*�0�(¡�%@E��?=:=`8:��1�K7�3Eá�DE��?�nxv8|Öt-K]xv8`%���A�%�'��4%����3{�xfps%7�nxv'(%�=%�As��=`=`×Ët?%7�3E�8|xv8`%����-E��d=uK��nxv{0»<Kw^Q8:{�x(8:=`=uK]xv8`%���p&K�{��b�nxv�3E�L�����Ä&°v³-¿6k�¾ Àf² °�h�¿Fº]l �d³]l©�°v³]ª �d³]l6 ² ° ² l�¿ ² ��] @M×D] n\��$&%�{�x(%��*���7�3���f+-5753+72

7\�24cI26Ó 2]��K�t�%��3{��-��K��3E/�T2��@>7%�17�6{DxFK7EG���Fps%���xv'(%�=7%7AyI�3{�xvK7��=:�&^Q8:{�x(8:=:=:K�x(8:%7�fps%�=`�3a/�{(�3��Ä,°(³-¿6ks¾ Àb² °�h�¿vº�l$�d³]l3©�°(³�ª�d³]l6 ² ° ² l�¿ ² �T[�[]¶]×�[7[�\��n$s%n{Dxv%7�*���������f+6575�+�2

75�24��2 ����3E�{�x(' #%7a<���G2��@>�%717�6{DxFK7EG��¡q2�I%]z�E<K��E&��× ��2�ÓáK��313�d�vHI%7��×����38 �n���-���-{v{4%�A��4%����3{�x�� � E��-t��-�nx('FK�=:8`�-�-E�d�Ë×�t�%��nx('v%7=u����Ä&°(³6¿-k4¾ Àb² °�h�¿Fº]l �d³]l3©�°(³�ª��d³]l- ² ° ² l�¿ ² ��+-\�¶7��×v+6\7¶����7$&%�{�x(%��*���7�3���f+-5753+72

¶���24��2 ����3E�{�x(' #%7a<�@�32 ��2 ��?���n¡�2n¡}%7'FK�'v8�K��Ef�G2n�@>�%717�6{DxFK7EG��� *8:af8|xFK]xv8`%��3{�%�A*^QL@�3K�af8utI¡�K]xv'(8`Øbps%��nx('v%7=u���nÄ&°v³-¿6k�&® °(³Fµ ² º�l �d³]l©�°(³�ª��d³]l6 ² ° ² l�¿ ² ��+6\7¶75�×v+6\� � 3��à 'v�?��%���=:�7������=`L�+-5�5�+72

¶3+72I�T2*�@>�%717�6{DxFK7EG�G¡�2G�0%]z@E�K��3E���2 ����3E�{�x(' #%7a<�4�v~�%]J,K�'FE�{48:�nx(�?1�'vK�x(8:��1 E��-{(8`1���K��E�t�%��nx('v%7=�)Iy0{(��%7AYA�'v� �n���?��×t�Ln×�E��?_��?�E��?�nx,x(%@%7=u{&A�%7'It?%7�nx('v%7=:=uK���8:=`8`xDL�K��K�=:L@{(8u{(�3��Ä&°v³-¿6k4Ä&°(³6¿ ² ¨F¨�g Á ¨�© ²?À ¨ � l@m�hjl ²F² °�hjl@m Äsg � ��� � ����(��2 ¶32`+?×���(��2 ¶32`+M���p&K7�3K7E�K3��.I��124+-5753+72

¶n�24¡�2G�I%]z�E�K7�3E��G2G��>7%71��-{�xvK�EG�s�(��af_3K7t�xQ%�Asa/%�E��-=����3t��-'�xFK�8:�nxDLw%���t�%��nx('v%7=�{Dxv'(�3t�x(��'v��{(�?=:�-t�x(8:%7�}A�%�'0xvr�� -3��8uEt?K�xvK7=`Lnx(8ut�t�'FK7tF>��?'&_�'(%�t?�-{v{(�3��Ä&° ² µT°�hjl3©�¨ ¦v­ ¾��§g Á]À µ�³]¨Fh ®�À ¾IÎ �*Ò � � � � � ��+6�n[M×v+�+6��@~�%7��=:%7�3{(�7��;3'vK7�3t���� ! t�x-25�+�2

¶�¶�24~�2]¡}�DB�E��?=:=�K��3E/�T2��@>7%�17�-{�xvK�EG�T�(cs{Dxv8`abK]xv%7'F{GA�%�'�8:=`=`×�t�%7�E�8|xv8`%����-E9_�=uK��nxv{-)��I8:17r�×�_��3'(8`xDL�E�8u{Dxv8`=:=:K�x(8:%7�3�3��Ä&° ² µ�°�hjl©�¨¦(­ ¾���g Á]À µ3³M¨�h ®�À ¾IÎ �GÒ � � � � � � n�7¶]×Ë ���\��n~�%���=`%��3{(�7��;�'FK��t��7� ! t�x-2d53+72

¶7 324cI26Ó�%7=����7¬f2 Ó 2M¡�K]xvr�8:{(�?�/K��3E/�T2]�@>7%�17�-{�xvK�EG�T�(^QL@�3K�af8ut?{�K��3E�t?%7�nx('v%7=:=uK���8:=`8`xDL %�A3r��6K]x���Ø�tFr3K��317�?'�����xDJ&%7'v>�{(�3��d­ �*± � g Á]À µ3³M¨�h ®�À � Ê Ä � � � � �n$,K7'vt?�?=:%7�3K3�7�@_3K�8:�*�+! t�x62�53+72��Y����=:8:{(r��6E�8:�*)��d��8:16B�K����-'dK��3Efcs{�_��3�3Kbe�csE�{?2Co���d³ À µ ® © ² ° � Ê °�h ² l3© ² ¹�Ä&°(³6¿ ² ¨F¨ � l@m�hjl ²v² °�hjlnm7�3cY=:{(�?z@8:�?'6��+65753+7�T+7+][6×F+67�2

¶n��24cI2 Ó 2��nK7t�%��3{(�?��K7�3Ew�G23�@>7%�17�-{�xvK�EG���(^Q�-{(8`1���af%�E�8|Ö�t?K]xv8`%��3{&A�%7',8:af_�'(%]z��-E t�%7�nxv'(%�=%7A�E�8u{Dxv8`=:=uK]x(8:%7�<t�%�=`�3a/�{(�3��d­ �*± � g Á]À µ3³M¨�h ®�À � Ê Ä � � � � �n$,K7'vt?�?=:%7�3K3�7�@_3K�8:�*�+! t�x62�53+72��Y����=:8:{(r��6E�8:�*)��d��8:16B�K����-'dK��3Efcs{�_��3�3Kbe�csE�{?2Co���d³ À µ ® © ² ° Ê °�h ² l3© ² ¹�Ä&°(³6¿ ² ¨F¨ � l@m�hjl ²v² °�hjlnm7�3cY=:{(�?z@8:�?'6��+65753+7�T+67¶]×F+6�\32

¶�Õ�24cI2 Ó 2���K�t�%7�{��-�áK7�3E��T2��@>�%717�6{DxFK7EG�Q�(c ���6t�x�%7A0¡}��=`x(8:_�=:8:t?8|xDLá%7�q^Q8u{Dxv8`=:=:K�x(8:%7�"ps%�=`�3a/� !Q_�-'vK�x(8:%7�3�3����K7_�-'Õ7�7�7�¾ ¦ ��± � ¾Qll ® º�ª ��²F² ©�hjl@m�� *%�{4.0��17�-=`�6{?��H0%]zT2&+65753+72

¶@[@24cI2 Ó 2?�nK7t?%7�3{(�?��K��3E��T2M�@>7%�17�6{DxFK7EG��(^Q�-{(8`1��Qaf%�E�8`Öt?K�x(8:%7�3{TA�%�'*8:a/_3'(%]z��-EQ%7_��?'FK���8:=`8`xDL0%7A@E�8:{�x(8:=`=uK]xv8`%���t�%7=:��af�3{v�����K�_��?'�+6¶�]1�3¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjlnm7� �%�{,.I��1��?=:�-{-�3HI%]zT2,+-5�5�+�2

¶�\�24cI2����7'(�-�3{(�?� K7�3E<�T2�@>�%717�6{DxFK7EG���Fps%��nx('v%7=:=:K7��8`=:8`xDLf.0�3K�=:L�{�8u{&%�A�Kbps%�a9��8:���6E $,K]xFtFr �4�6K7t�x(%7'�39$,K]xvtFr<^Q8:{�x(8:=|×=uK]x(8:%7��ps%7=:��af�3�3����K�_��?'�+? n������¾ ¦ ��± � ¾Ql3l ® º�ª ��²v² ©�hjlnm7� *%n{4.I��1��?=:�-{-��HI%]zT24+-5�5�+72

¶�5�24¡�2��0%]z@EwK��Ew�T2��@>7%�17�-{�xvK�EG���Fps%7�nxv'(%�=`=uK���8:=:8|xDL�.0�3K�=:L�{�8u{&%�A�x(r���;�=`�38:E�p&K]xFK�=:Lnx(8ut�ps'FK7tF>@8:��1��Y'(%�t?�-{v{(�3�n��K7_�-'+? @�]1��¾ ¦ ��± � ¾Ql3l ® º�ª ��²v² ©�hjlnm7� *%n{4.I��1��?=:�-{-��HI%]zT24+-5�5�+72

n��24~�2d¡}��B�E��?=:=IK��3EÆ�T2Y�@>�%71��-{�xvK7E*���(cY{�x(8:abK]xv8`%���%�A�^08u{�x(8:=`=uK]xv8`%��Ôps%�a/_�%�{(8`x(8:%7�3{�A�'v%7a ¡}��=`x(8:_�=:��~��-af_�-'vK�x(��'v�¡}�6K7{(��'(�-af�?�nxv{&�3{(8`�31����� �4�-17'v�-{v{�8:%7�3�3�n��K7_�-'�+? �\�EG�¾ ¦ ��± � ¾Qll ® º]ª ��²F² ©�hjl@m�� �%�{4.0��17�-=`�6{?��H0%]z�24+65753+72

+724¬f2 Ó 2�¡�K�x(r�8u{��-�*�d�T2���>7%71��-{�xvK�EG��K7�3E�cI2 .�2�Ó�%�= �����Fps%���xv'(%�=`=uK��38`=:8|xDL�%�A4r��-K�x9��Ø�tFr3K7��17�-'����?xDJs%�'(>�{v������K7_�-'+6��]�*�3¾ ¦ ��± � ¾Ql3l ® º�ª ��²v² ©�hjlnm7� *%n{4.I��1��?=:�-{-��HI%]zT2,+-5753+72

@�24��2 ����3E�{�x(' #%7a K��3E��T2n�@>7%�17�-{�xvK�EG�*�v�4%7���{DxYK7�3Ef¡}%�E��?=��d'v�-E�8ut�xv8`z��Ips%��nx('v%7=�%7AG� �9��^08u{Dxv8`=:=uK]x(8:%7� ps%�=`�3a/�{(�3���K�_��?'�+M�] �AD�¾ ¦ ��± � ¾Ql3l ® º�ª ��²v² ©�hjlnm7� *%n{4.I��1��?=:�-{-��HI%]zT24+-5�5�+72

n¶�24cI2 Ó 27�nK7t?%7�3{(�?�/K��3Eb�T2���>7%71��-{�xvK�EG�G�($&8`A���'vt-K]xv8`%��3{�8`�f�DE��6K�=3~,J&%��d'v%�E��3t�xd^Q8:{�x(8:=:=:K�x(8:%7�3�3����K�_��?',+M��\]AD�@¾ ¦ ��± �¾Ql3l ® º]ª ��²F² ©�hjlnm7� �%�{4.I�317�?=:�-{-��HI%]zT2,+-5�5�+�2

� 324��2 *���3E3{Dxv'-#%�aw�d�T2��@>�%717�6{DxFK7E�K7�3E ��2 ��2�ÓáK���1���(y0�3t��-'�xFK�8:��xDL�Ó��-8`1�rnxf�@�-=`�6t�x(8:%7�qA�%7'f�4×Ë8`��Ö��8|xDL�K7�3Eq¡}��×ps%7�nxv'(%�=3¡}��xvr�%�E�{v���@�d'v%@t72��DcscYc�ps%7��AD2�%���^0�6t�8u{�8:%7��K7�3E�ps%7�nxv'(%�=�e�p&^�p,o��T+6�7¶n[M×v+M�] n��]$s'v8:17rnx(%��*�7y0¬f�@^Q�-t�2+-5�5�+�2

+?

Page 72: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

@��2 ��2 ��2?ÓáK���1QK��3E��T2M�@>7%�17�6{DxFK7EG��� �T×�.I�3K7=`L�{(8:{�K��3E��@L@�nx(r3�-{(8:{�%�A�~,8`af�&^0�-=:KML��@L�{Dxv�?ab{*�{�8:��1Q�@af8`x(r9�Y'(�6E�8ut�x(%�'v�3��d'v%�t�2��DcYcscÆps%���AD2�%7�<^Q�-t�8u{(8`%��wK7�3E�ps%7�nx('v%7=�e�p&^�p,o���¶7��¶7¶]×�¶7��¶� �7$&'(8:17rnx(%��*��y0¬f��^Q�-t724+-5�5�+72

nÕ�24cI2 Ó 2��nK7t�%��3{(�?��K7�3Ef�T2��@>�%717�6{DxFK7EG�G�v^0L@�3K7af8:t-{�K��3Ebps%7�nx('v%7=@%7A�yI�{DxFK���=:�I^08u{�x(8:=`=uK]xv8`%���ps%�=`�3a/�{(�3���d'v�?_�'v8`�nxF{¦(­ ¾����˨ Á]À µ�³]¨�h ®�À Î�� � Ê � Î ��� ������¶� @�M×�¶����3��¡�K7'(L@=uK��3E*��.I_�'62Y�[M×�75���+-575n�2

�[@2I�T23�@>�%71��-{�xvK7E*�q�(^QL@�3K�af8ut?{,K��3E}ps%7�nxv'(%�=�%7A�^Q8:{�x(8:=:=:K�x(8:%7��ps%7=:��af�3{&×d. ps'(8`x(8ut?K7=*�@��'vz7�?L��3��e����@z@8|xv�-Ew_�=:�?�3K7'(L=:�-t�xv��'v�6o�2&�d'v�?_�'v8:��xF{ ¦(­ ¾����˨ Á]À µ�³]¨�h ®�À Î�� � Ê � Î ��� ������+?×������¡�K7'(L@=uK��3EG��.0_�'62,n[6×D�5��T+6575�we��4�?_�'v8:��xv�-E<8:�+-5�5n[�8`� ��¦ � �{(�?��_3K7_�-'IÕ7Õ/8:� xvr���=:8:{�xI%�ABD%7��'v�3K�=G_3����=:8:t-K]x(8:%7�{vo�2

n\�24cI2d.92�Ó�%�= ���4�T2Y�@>7%�17�6{DxFK7E�K7�3E"¡�2d�I%]z�EG���Fps%���xv'(%�=`=uK��38`=:8|xDL�%�A 8`�nxv�?17'FK]xv�-E�_�=:K7�nxv{v��� � � � �á¾ ¦ ��± � g�µT°�hjlnm½ º�©�h�³�l�º�ª ��²F² ©�hjlnm7�3HI�-J !Q'v=:�-K��{?��¡�K7'-2 3].0_�'-2&+-5�5���@��K7_�-'4Õn[]K32

n5�24¬f2 Ó 2�¡�K]xvr�8u{��-�*���G2��@>7%�17�6{DxFK7E�K��3Eá~�2�à ���E��?'F{��-�*��� !Q_�xv8`abK�=��@L@_3K�{({�_�=uK7t?�?af�?�nx�8:��r��-K�x���Ø�tFr3K7��17�-' �3��x�×J&%7'v>@{v��� � � ����¾ ¦ ��± � g7µ�°�hjlnm ½ º]©�h�³]l�º�ª ��²F² ©�hjlnm7�3HI�-J !Q'v=:�-K��{?��¡�K7'-2 3].0_�'-2,+6575������K�_��?'4Õn[]�72

�7��2I�T23�@>�%71��-{�xvK7E*���v.I�<cY{v{(KMLf%���xvr���a/%�E��-=`8:��1f%�A����3t?�?'(xvK�8:�nxDLb8`�<t�%��nx('v%7=G{�L�{�x(�-af{v��� ½ g ­�� ¾ ­,Ê g � �}³]°(Ð]¨�±3³vµ³]lÔ¼T± ² � ³6¹ ² ª«hjl@m}³D · lT¿ ² °�©�º]hjl© Á hjl ��³�l3©�°(³]ª*g Á ¨�© ²?À ¨F��y�p ��K��nxvKf$,K�'v�3K�'FK���+-\�×�7���������f+6575��2

��+724¡�2Y�0%]z�E§K7�3E"�G2s�@>7%�17�6{DxFK7EG���v�4%7�3�3{Dx�t?%7�nx('v%7=,%�A�{(L@{�x(�-ab{bt�%7�{�8u{Dxv8`�31�%7A�{(L@a/af�?x('v8:t-K�=:=`Lq8:�nx(�-'vt?%7�����6t�xv�-E{(���3{(L@{�x(�-ab{(�3�Ä&°(³6¿-k4¾ Àb² °�h�¿Fº]l �d³]l3©�°(³�ª��d³]l- ² ° ² l�¿ ² ��psr�8ut?K�1�%3���������f+-5�5���@¶����+�×�¶7�����2

���2 ��2 × ��2&ÓáK���1ÆK��3E �T20�@>�%717�6{DxFK7EG���(�4%����3{�xwt�%��nx('v%7=:=`�-'wE��6{�8:17� A�%7'w���3t?�?'(xvK�8:�Çxv8`af��E��-=:KMLÔ{(L@{�x(�-ab{(�3� ��� ©j±¦ l© ² °�l�º�©�h�³�l�º�ª ��³�l- ² ° ² l�¿ ² ³�l ¾Ql�º�ª Á ¨�hu¨�º�l�¹ Ê µT©�h À h��6º]©�h�³]l�³�ÂQg Á ¨�© ²?À ¨ ��g�©Ëº�© ² º�l�¹ ­ ° ²��?®3² lT¿ Á Î/³ À º]hjlw¾&µ(�µ�°v³-º�¿v± ² ¨YÂ�³�° ¦ l��dl3hj© ² Î9h Àb² l3¨Fh�³�l�º�ªGg Á ¨�© ²�À ¨���@%7_3r�8:K�×Ë.0�nx(8:_%�=`8u{?���������f+6575����Õ�+-��×ËÕn�¶32

�7¶�24cI2,����'v�?�{��-�ÆK7�3E �T2,�@>7%�17�6{DxFK7EG�f�Fps%��nx('v%7=0{�x('FK]xv�?178:�-{bA�%7' K�t�%7a���8:���-EÆ�3K�xvtFrÔ'v�-K�t�x(%�' 3]�3K]xFtFr"E�8:{�x(8:=`=uK]xv8`%��_�'v%�t��-{v{v��� ½ ¾�¼ Ê �<³�°(ÐM¨(±3³vµ�³]l�¯Fº�©Ë¿F±�µT°(³-¿ ² ¨F¨ ² ¨��~���'v>7�?L����7���3�b+-575n�2

�� 32I�T2��@>�%71��-{�xvK7E�K��3E�cI2 .�2TÓ�%7=����¸��ps%7�nx('v%7=:=:K7��8:=`8`xDL af�6K7{(��'(�6{QA�%7'�E�8u{Dxv��'(�K��3t?��'v�DBD�6t�x(8:%7����ÇÄ&° ² µ�°�hjl3©�¨ ¦(­ ¾��´Y³]°(Ð]¨(±�³FµÔ³]l ¦ l3© ² °(º�¿�©�h�³]l3¨f¯ ² ©�´ ²F² l�µT°(³6¿ ² ¨F¨f¹ ² ¨�h|m7l§º]lT¹9µ�°(³6¿ ² ¨F¨f¿F³�l3©�°(³]ª �K!�³]lT¹7³]l �,g ² µ�©�k � � ������cYE�8|xv�-E��@L�2 ^�2���-'(>@8:�3{?�����?'v1�K7a/%��w�Y'(�6{({-�*+6575����¶�×�75<e��4�-_�'(8:�nx(�6E}8`��+6575�Õf8`� ��¦ ���G{(�?��_3K7_�-'QÕ��f8`��=:8u{Dx0%7AGBD%7��'v�3K7=_����3=`8ut?K�x(8:%7�3{Fo�2

����24cI2 .�2�Ó�%�= �����T2��@>7%�17�-{�xvK�EG�*¡�2��0%]z�E�K7�3E�¬f2 Ó 2�¡�K]x(r38:{(�?�*� �(. _�'v%�t��-E���'(��A�%7'�t�%7�nxv'(%�=`=uK���8:=:8|xDL�K7�3K�=:L�{�8u{(�3�Ä&° ² µ�°�hjl©�¨ ¦v­ ¾�� ´Y³]°(Ð]¨�±3³vµ ³�l ¦ l© ² °(º�¿�©�h�³]l3¨�¯ ² ©�´ ²F² l}µT°(³-¿ ² ¨F¨ ¹ ² ¨Fh|m7lÔº]l�¹bµ�°v³-¿ ² ¨v¨ ¿F³�l3©�°(³]ª � !�³�l�¹�³]l � g ² µ�©�k� � �����cYE�8|xv�-Ew�@L��32 ^�23���?'v>@8`�3{-�����?'v1�K7a/%����d'v�-{v{-�G+-575n���+6n[6×F+-¶��2

�7Õ�24¡�2��0%]z@E K��3E<�T23�@>�%71��-{�xvK7E*����ps%7�nx('v%7=:=:K7��8:=`8`xDL/K7�3K�=:L�{�8u{&%�A��3�3{DxFK���=:��_�'v%@t?�-{v{��6{(�3��Ä,° ² µT°�hjl3©�¨ ¦v­ ¾��"´Y³]°(Ð]¨�±3³vµ³]l ¦ l3© ² °vº7¿?©�h�³�l�¨&¯ ² ©�´ ²F² l µ�°(³6¿ ² ¨F¨,¹ ² ¨�h|m7l º]lT¹Yµ�°(³6¿ ² ¨F¨4¿v³�l3©�°(³]ª �E!�³�l�¹7³�l �Gg ² µT©Ëk � � � �7�7csE�8|xv�-E��@L��2 ^�2]���?'v>n8:�3{-����?'v1�K7af%7���Y'(�6{({-�T+-575n��@ �5�×��� 32

�n[@24��2 ^92d$&'FK7K�x(�7�s¡�2d¡}%7'FK�'v8sK7�3EÆ�T2Y�@>7%�17�6{DxFK7EG���v.0E�z]K��t��-{/8:�§'v%7�3�3{Dxf=:%n%�_3{(r3K�_�8:��1n���d��K�_��?'w+6n[]K3�s¾ ¦ ��± �¾Ql3l ® º]ª ��²F² ©�hjlnm7�3¡}8uK�af8�$&�6K7tFr*��HI%]zT2,+-5�5��2

�7\�24��2 *�3�3E�{�x(' #%7a K7�3E/�G27�@>7%�17�-{�xvK�EG�G�(�I%7���3{�x�af%@E��?=�_�'v�-E�8ut�xv8`z��4t�%7�nxv'(%�=n%7A�E�8u{�x(8:=`=uK]xv8`%��/t?%7=:��af�3{(�3�7��K�_��?'&+6� 7���¾ ¦ ��± � ¾Qll ® º]ª ��²F² ©�hjl@m���¡}8:K7af8*$s�6K7tFr*��H0%]zT2&+6575n�2

�75�24cI26Ó 2��nK7t�%��3{(�?��K��E��T2��@>�%717�6{DxFK7EG�������t�%7�{�8u{Dxv�?�3t?8`�6{�8:��E�Ln�K�af8:tYaf%@E��?=u{�A�%�'�8`=:=|×�t�%��3E�8`x(8:%7���6E�_�=uK��nxv{v���]��K7_�-'+6��]����¾ ¦ ��± � ¾Ql3l ® º]ª ��²v² ©�hjlnm7�¡}8uK�af8*$&�-K�tFr*��HI%]zT2,+-5�5��2

Õ���24¡�2T�I%]z�E�K7�3E��T2G�@>7%�17�6{DxFK7EG�s�(^Q�-{(8`1��}%�Ad'v%7���3{�x E��-t��-�nx('FK�=:8`�-�-E}t�%��nx('v%7=:=`�-'v{v���3��K7_�-'9+M�[]E*�T¾ ¦ ��± � ¾Ql3l ® º]ª��²F² ©�hjlnm7�3¡}8uK�af8�$&�-K�tFr*��HI%]zT24+-5�5��2

Õ3+72 ��2 × ��2�Ó�K7��13���T2��@>7%�17�-{�xvK�E�K7�3E ��2 ��r3K7%3� �(. t?%7af_3K�'v8u{�%���%7A,z]K7'(8:%7�3{9t�%7�nxv'(%�=d{Dxv'(�3t�x(��'v�-{�A�%7'9t?%7�nx(8:�@��%7�{��8:%7'v�-K�t�x(%�'v{v���@��K�_��?'�+M�5�1�3¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjlnm7�3¡}8uK�af8�$&�-K�tFr*��HI%]zT2,+-5�5��2

Õn�24¬f2 Ó 2M¡�K]x(r38:{(�?�fK��3E/�T27�@>�%717�6{DxFK7EG�T�v^0�6{�8:17�*�]%�_�-'vK�x(8:%7�9K7�3E9t?%7�nx('v%7=n%�A�'(�6{�8:=:8`�-��x�r��-K�x���Ø�tFr3K��317�?'�����xDJ&%7'v>�{(�3���K�_��?'�+- 3+?1�3¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjlnm7�¡}8uK�af8*$&�-K�tFr*��HI%]zT2,+-5�5��2

Õ�¶�24¡�23�0%]z�EwK7�3E<�T2��@>�%71��-{�xvK7E*���v�4%7�3�3{Dx0{(� �n���-�nx(8uK�=*E��6{�8:17�<%�A�E��6t��?�nxv'vK7=`8:�?�6E t?%7�nx('v%7=:=`�-'v{v���@�d'v%�t�2 � � ��� �&® °v³ �µ ² º�l �d³]l©�°v³]ª��d³]l6 ² ° ² lT¿ ² ��à 'v%7�38`��1��?�*��H d�3�������b+65757¶3�T+-���7�]×F+-�n�7��2

+6�

Page 73: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Õ7 324cI2 Ó 2,��K�t�%7�{��-�ÆK7�3EÇ�T24�@>7%�17�6{DxFK7EG�f���DE��?�nx(8`Öt?K�x(8:%7�Ô%7A9E�L@�3K�af8ut}af%@E��?=u{�A�%�'�8:=`=`×Ët?%7�3E�8|xv8`%����-EÆ_�=uK��nxF{b×b.���?�3tFr�abK7'(>�_3'(%���=`�-ab�����d'v%�t�2 � � ��� �&® °(³Fµ ² º]l �d³]l3©�°(³�ª��d³]l- ² ° ² l�¿ ² �à '(%���8:��17�-�*��H Y�3�7�3���b+-5�57¶���] @M×D] �[@2

Õn��24��2 *���3E3{Dxv'-#%�aw� �T2I�@>7%�17�-{�xvK�EÆK��3E �32«pQ2&^Q%]L@=`�����(~,J&%�E��-17'v�?��%7A�A�'v�?�-E�%7a t�%���xv'(%�=`=:�?' E��-{(8`1��ÔA�%7'<K�� 8`=:=|×t�%��3E�8`x(8:%7���6E�_�=uK��nx��3{(8`��1 �T×Ë{(L@�nx(r��6{�8u{?�G�Y'(%�t�2 � � ��� �&® °(³Fµ ² º]l �d³�l3©�°(³]ª �d³]l6 ² ° ² lT¿ ² ��à 'v%7��8:��1��?�*�GH Y�G�7���3�+-5�57¶3�@5�Õ75�×Ë5@[M 32

Õ�Õ�24cI2 .�2�Ó�%7=���K7�3E}�T23�@>7%�17�6{DxFK7EG���Fps%��nx('v%7=Gt�%���Ö317�3'vK�x(8:%7� {(�?=:�-t�x(8:%7� A�%7'IE�8u{�x(8:=`=uK]xv8`%��wt?%7=:��af�3{,���3E��-'4x(�-af_�-'vK�×x(�3'(��t�%��nx('v%7=u�����d'v%�t�2 � � ��� �&® °(³vµ ² º]l ��³�l3©�°(³]ª �d³]l- ² ° ² l�¿ ² �à '(%���8:��17�-�*��H Y�3�7�3���f+-575�¶���Õ7¶@[6×�Õ� @�2

Õ@[@24¡�2T�I%]z�E}K��E��T2T��>7%71��-{�xvK�EG�d����af_�'v%]z7�6Ew8`�3E��?_��?�3E��-�nx E��6{�8:17�}%7A�'v%7�3�3{Dx E��-t?�?�nx('FK�=:8`�-�-E}t?%7�nx('v%7=:=`�-'v{v�����Y'(%�t72� ��©j± ¦(­ ¾�� �}³]°�ª`¹ �d³]l@m�° ² ¨F¨���@L�E����-L7�3.0�3{Dxv'vK7=`8uK�������=:L�+-\�×�7¶���+-5�57¶�� � !E� � GG�n[@+?×�n[M 32

Õ�\�24¡�2��I%]z�EG�@��2 ^92�$&'FK7K�x(�0K7�3E��T2��@>�%717�6{DxFK7EG��� !Q��x(r���{Dxv'(�t�x(�3'(�Q%�AGx(r3�Q'v%7���{Dx&%7_�xv8`abK�=Gt?%7�nx('v%7=:=`�-'dA�%�'&K�t�=uK7{v{%�A�_�'v%7��=:�?ab{v�����d'v%�t�2 � ��©j± ¦(­ ¾�� �}³]°�ª`¹ �d³]lnm7° ² ¨F¨F�T�@L�E����-L7��.I�{Dxv'vK7=`8uK�������=:L�+-\�×�7¶��T+-5�57¶�� � !E� � J��n[6×�¶7�32

Õ�5�24��2 ����3E�{�x(' #%7a<� ��2 × ��2-Ó�K7��10K7�3E��T2]�@>7%�17�-{�xvK�EG���(¡}%�E��-=`=:8`�31I%�A�1�K78`��K7�3E�E��-=:KML ���3t?�?'(xvK�8:�nxDLQ8:��x(r3�s{�x('v�3t�xv��'(�6E{(8`��1���=uK�'�z]K7=`���dA�'vK7a/�-Js%�'(>��3�6�Y'(%�t�2 � �7©�± ¦(­ ¾�� �}³]°�ª`¹ �d³�lnm7° ² ¨F¨��7�@L�E����-L7�].I�{Dxv'vK7=`8uK��]����=`Lf+6\]×D�¶���+-5�57¶��2� ! � �=��� 7 3+?×� � 7 2

[���2I�T2��@>�%71��-{�xvK7E*�&�(���nx(�?'FK7t�x(8:%7�3{Q����xDJ&�?�?��_�'v%@t?�-{v{�E��-{(8`1���K7�3E�t?%7�nx('v%7=u���T���@z@8|xv�-E�_�=`�-�3K�'vL}=:�-t�xv��'v�7��p&�I����.�ß 57¶���d'FK�rK���.I��12 ×D�@�-_�x-2:�*+-5�57¶32

[�+72 ��2 × ��2YÓ�K7��13�I�T2,�@>7%�17�-{�xvK�E§K7�3E ��2 ��r3K�%�f�(c�Ø�K�t�xb=`8:���6K�'v8`�6K]x(8:%7�Æt�%��nx('v%7=I%7A�t?%7�nx(8:�@��%7�3{���8`%�'(�6K7t�x(%7'F{-)�.t�%�af_3K�'v8:{(%7��%7A�E�8 �T�?'v�?�nx�t?%7�nx('v%7=�{Dxv'(�3t�x(��'v�-{v���M�d'v%�t�2���l�¹ ¦ � � � �d³]l-Â�kQ³]l$�d³]l©�°v³]ª�¾sµ7µTª«h�¿Fº]©�h�³]l3¨F�7ÃdK��3t?%7��z��?'6�p&K��K7E�K3�����?_�x62I+-¶�×v+6Õ���+-575�¶��T+-�@[6×F+7+M�2

[7�24�2�¡}%7'v�3EáK��Eá�G2��@>�%717�6{DxFK7EG�0�(~,r���E�L@�3K7af8:t-{�%�A4tFr��-a/8ut?K7=d'v�-K7t�x(%�'v{ J48`x(r�r��6K]x98:�nx(�?1�'vK�x(8:%7�3�3����K�_��?'97Õ����¾ ¦ ��± � ¾Qll ® º]ª ��²F² ©�hjl@m��T�nx-2 �%7��8u{?��H0%]zT2&+6575�¶�2

[�¶�24¡�2Y�0%]z�E§K7�3EÔ�T2s�@>�%717�6{DxFK7EG���(�4%����3{�x�t�%���xv'(%�=,%�A�{�L@afaf��x('v8ut<_�'(%�t?�-{v{��6{(�3�Y��K�_��?'}+- �Õ�>T�4¾ ¦ ��± � ¾Ql3l ® º]ª��²F² ©�hjlnm7��nx62 *%7�38:{-�3HI%]zT2,+-5�57¶32

[] 324¡�2@�I%]z�E�K7�3E��T2��@>7%�17�6{DxFK7EG���(��K�8:'v8`��1�t?'(8`x(�-'(8uK�A�%7'&���3{�xvK7��=:�0_�=uK��nxv{v���@��K�_��?'0+? �578���¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjl@m���nx62 *%7�38:{-��HI%]zT24+-5�57¶32

[7��24cI2 .�23Ó�%�= ����T2��>7%71��-{�xvK�E K7�3E ¬f2�0KMz@'(�����(^QL@�3K�af8ut?{4K��Ewt?%7�nx('v%7=T%7A�8:�nx(�?1�'vK�x(�6E�xvr�'(�-��×Ë_�'v%@E��3t�x�e����?x(=:L@��>�oE�8u{Dxv8`=:=uK]x(8:%7�<t�%�=`�3a/�{(�3����K�_��?'�+-5n��K3��¾ ¦ ��± � ¾Ql3l ® º�ª ��²v² ©�hjlnm7��nx-2 �%7��8u{-��HI%]zT24+-5�57¶�2

[�Õ�24��2 *�3�3E�{�x(' #%7a<�s��2d;�=uK]x(�@L�K7�3EÔ�T2Y�@>�%717�6{DxFK7EG�9�(c �T�-t�xb%�A -%]J E�L@�3K7a/8ut?{-�&�?���-'(1�L��3K�=uK��3t?�wK7�3E§_�'(�6{({(��'v�E�L@�3K7a/8ut?{�%7�áxvr��w%]z7�?'FK�=:=d'v�-{(_%��3{(��%�A0E�8u{�x(8:=`=uK]xv8`%��§t�%�=`�3a/�{(�3����K7_�-'�+657Õ7t7��¾ ¦ ��± � ¾Qll ® º]ª ��²v² ©�hjlnm7�Y�nx-2*%���8u{?��H0%]z�2,+65757¶32

[�[@24cI2 .�23Ó�%�= ����T2��>7%71��-{�xvK�E K7�3E ¬f2�0KMz@'(�����(^QL@�3K�af8ut?{4K��Ewt?%7�nx('v%7=T%7A�8:�nx(�?1�'vK�x(�6E�xvr�'(�-��×Ë_�'v%@E��3t�x�e����?x(=:L@��>�oE�8u{Dxv8`=:=uK]x(8:%7��t�%�=`��af�3{-��g Á]À µ3³M¨�h ®�À � g��*¾QÄ � � �3��^Q����=:8`�*��¡�K�'FtFrq+-5�5� ���Y����=:8:{(r��-E�8`� ¦ ��± ²�À � g Á]À µGk�g ² °?k½ ³�k ��� *-��+�+7+�×F+7+6\�2

[�\�24cI2 .�2]Ó�%7=����n�2 ^�2����?'v>@8`�{?�7�T2n�@>7%�17�-{�xvK�EG�G�(.Æ_3'(%�t��6E���'v�YA�%�'�%7_��?'FK���8:=:8|xDL9K7�3K�=:L�{�8u{v���@g Á]À µ3³M¨�h ®�À � g ��¾0Ä � � ���^Q����=:8`�*��¡�K�'FtFr�+65757 3���d���3=`8u{�r3�-E 8`� ¦ ��± ²�À � g Á]À µ*kIg ² °?k ½ ³7k ��� *-�5n�M×F+-���2

[�5�24��27;�=uK]x(�@L�����2 ����3E�{�x(' #%7a K��3Eb�T2@�@>7%�17�-{�xvK�EG�*�v�48`1�%7'v%7�3{�E�L@�3K7af8:t4{(8`a���=uK]x(8:%7�f%7ATE�8u{�x(8:=`=uK]xv8`%��ft?%7=:��af�3{d�K7{(�-E%7�<yIÃ0×�-�K7{(r3���Ä&° ² µT°�hjl3©�¨ ¦v­ ¾��"g Á]À µ�³]¨�h ®�À ¾0Î��*Ò � � � � ����¬�L7%�xv%3���nK�_3K7�*��¡�KML�+6575� �@n[]Õ�×�7\��2

\���2 ��2��Tr3K�%"K��3E �T20�@>7%�17�6{DxFK7EG���v.�t?%7af_3K7'(8u{�%��Ç%�A�zMK7'(8:%7�{wt?%7�nx('v%7=�{vtFr��?af�-{�A�%7'}t?%7�nx(8:�@��%7�3{w��8:%7'v�-K�t�xv%7'F���Ä&° ² µ�°�hjl©�¨ ¦v­ ¾���g Á]À µ3³M¨�h ®�À ¾IÎ �*Ò � � � ���3��¬�L�%�xv%3����K7_3K�����¡�KML}+-5�5� 3��¶n7�M×�¶7¶���2

\3+72I�T2���>7%71��-{�xvK�EG�4�Fps%���xv'(%�=`=uK��38`=:8|xDL�K7�3K�=:L�{�8u{ %�A4�@��� ! {�L�{�x(�?ab{v����Ä,° ² µT°�hjl3©�¨ ¦(­ ¾�� g Á]À µ�³]¨�h ®�À ¾IÎ �*Ò � � � � ���¬�L7%7x(%�@�nK�_K��*��¡�KML}+65757 3�@ @[�+�×Ë @[]Õ32

\n�24��2 ����3E�{�x(' #%7a K��E��T2@��>7%71��-{�xvK�EG�*� !Q_3_%�'�xv����8`x(8:�-{YK7�3EbE�8 /�t���=`x(8:�-{sJ48|xvr �MØ3��E�8u{�x(8:=`=uK]xv8`%���t�%���xv'(%�=���Ä&° ² µ�°�hjl©�¨¦(­ ¾���g Á]À µ3³M¨�h ®�À ¾IÎ �GÒ � � � ���3��¬�L�%�x(%����K7_3K��*��¡�KML�+-5757 3��¶n[�\]×�¶7\7 32

\�¶�24cI2�����'v�?�{��-�áK7�3Eq�T2��@>7%�17�6{DxFK7EG�Q� !Q_�xv8`abK�=s%7_��?'FK]xv8`��1}_�%7=:8ut�8:�-{�%7A4�3K]xFtFrqE�8:{�x(8:=:=:K�x(8:%7�3�3�dÄ,°(³-¿6kqg Á]À µ�³]¨Fh ®�ÀÄsg � � ���3�¬�L7%���16BD�*��¬�%7'v�-K3���7���3�/+65757 3�@ 7 n5]×Ë n��Õ32

+-Õ

Page 74: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

\7 324¬f2 Ó 23¡�K]xvr�8u{��-�*��¡�23¡}%�'vK7'(8GK7�3Ew�G2�@>7%�17�6{DxFK7EG��� !Q_�x(8:afK7=G%7_��?'FK]xv8`%�� %7A�r��6K]xI��Ø�tFr3K7��17�-',����xDJ&%7'v>�{(�3��Ä&°v³-¿6kg Á]À µ3³M¨�h ®�À Ä&g � � � ���¬�L�%7��16BD�*��¬�%�'(�6K����������f+-5�5� 3��¶3+6�M×�¶���2

\n��24cI2 .�23Ó�%�= �áK��3E}�T2��>7%71��-{�xvK�EG��� !Q_��?'FK���8:=:8|xDL�%7A�8:�nx(�-17'FK]x(�6E�_3=:K7��xF{(�3��Ä&°(³6¿6k g Á]À µ�³]¨�h ®�À Ä&g � � � ���T¬�L7%7�31-BD���¬�%7'v�-K3���7���3�/+65757 3��Õ7¶�×D[���2

\�Õ�24�2CpQ2T¡}%7'v�3E�K7�3E��T2G�@>�%717�6{DxFK7EG�s�(~,r��/E�L@�3K�af8ut����?r3KMz@8:%7'Q%�Ad8:��xv�?1�'vK�x(�-E<_3=:K7��xF{?��g Á]À µ3³M¨�h ®�À Äsg � � ���3��¬�Ln×%7�31-BD���3¬�%7'v�-K3�n�������b+6575� ��5�+-¶�×Ë53+-\32

\@[@2I�T2Q��>7%71��-{�xvK�EG� �v.�_�'v%@t?�-E��3'(��A�%7'������ ! t?%7�nx('v%7=:=uK���8:=`8`xDL K7�3K�=:L�{�8u{ ×�J48|xvr K�_�_�=:8ut?K]xv8`%�� x(%ÔE��-{(8:17�Í%�Af_3�4×_�'v%�t��-{v{(�-{v����Ä,° ² µT°�hjl3©�¨ ¦v­ ¾�� �}³]°(Ð]¨(±�³Fµ¸³]l ¦ l3© ² °vº7¿?©�h�³�l�¨á¯ ² ©�´ ²F² l"µ�°(³6¿ ² ¨F¨q¹ ² ¨�h|m�l º�l�¹�µT°(³6¿ ² ¨F¨�¿F³�l3©�°(³]ª«�$,K�=`x(8:af%7'v�7���7�3���b+-5�5� 3��7¶]×D�\�2

\�\�24¡�2&�I%]z�EG�4��2 ^92&$s'FK7K�x(�}K��EÇ�T2&�@>�%71��-{�xvK7E*���F�@ÃQ^�ps%7�nx('v%7=:=`�-'v{�A�%�' � � ×F� � ��×F�IK��E �T×Ë%7_�x(8:afK7=0t�%��nx('v%7=��Ä&°(³6¿ ²F² ¹�hjlnm�¨ � � � ��¾ Àf² °�h�¿Fº]l �d³�l3©�°(³]ª��d³�l- ² ° ² lT¿ ² ��$&K7=|xv8`af%�'(���@�������?×Ë����=:L�+-5�5� ��+M�¶�¶]×F+6�¶@[@2

\�5�24��2 ^92�$&'FK7K]xv�7�@¡�2�¡}%7'FK�'v8K7�3E �G2���>7%71��-{�xvK�EG���v�4%7�3�3{Dx,�4�?=:8uK���=:� ^Q�-t?�?�nx('FK�=:8:�?�-Ewps%7�nx('v%7=u����Ä&°(³6¿ ²F² ¹]hjl@m]¨ � � ���¾ Àb² °�h�¿Fº]l �d³]l3©�°(³�ª��d³]l- ² ° ² l�¿ ² �$,K�=`x(8:af%7'v�7���7�3����×��7�3=`L�+65757 3��¶7¶�\� �×�¶7¶�\7\32

5���2I�T2]�@>7%�17�6{DxFK7EG�������_���x�×"!Q��x(_���xdps%���xv'(%�=`=uK��38`=:8|xDL .I�3K7=`L�{(8:{v���6���@z@8|xv�-E ��-t�xv��'v�7�]�4�?1�=`�-'(a$#%7x(�7�6Ã�#K�{Dxv�?''&K7{-�M��Js�6E��?�*�7�]×�7Õ�2�! t�x62&+65757 3�

53+724�23¡}%7'v�3EG��323K7�3E}�T2���>7%71��-{�xvK�EG���(.I=:=:%]J&K7��=`��%�_�-'vK�x(8:��1f'(�-178:%7�3{,%7A�8:�nx(�?1�'vK�x(�6EwE�8:{�x(8:=`=uK]xv8`%��}K�'v'vK7��17�-a/�-�nxv{v�����K�_��?'�+6¶�+-E*��¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjlnm7���K7�<;3'vK7�3t�8u{vt�%3��H0%]z�2,+6¶]×F+-\��T+6575� 2

5n�2I�T2��>7%71��-{�xvK�EG���(^Q�-{(8`1�� af%�E�8`Öt?K�x(8:%7�3{,A�%�'48`af_�'v%]z7�6E t?%7�nx('v%7=:=uK���8:=`8`xDLf×dJ48`x(r�K�_3_�=`8ut?K�x(8:%7� x(%�E��6{�8:17�w%�A������T�?'xvK7��>�{(�3����K�_��?'I7�]����¾ ¦ ��± � ¾Ql3l ® º]ª ��²v² ©�hjlnm7����K7�w;3'vK7�3t�8u{(t?%3��HI%]zT24+6¶]×F+-\���+-5�5� 2

5�¶�2 ��2#��r3K7%9K��3E��G2n�@>�%717�6{DxFK7EG���(¡}%�E��-=`8:��19K7�3Ebt�%���xv'(%�=�%�A*K��38`%�tFr��-a/8ut?K7=�=:%n%�_b'(�6K7t�x(%7'�J48`x(r t��?=:=:afK�{({d'(�6t�L�t�=:�-�3���K�_��?'4¶�57EG�¾ ¦ ��± � ¾Ql3l ® º�ª ��²F² ©�hjl@m��T��K��<;�'FK��t�8u{(t?%3��HI%]zT24+-¶�×v+6\���+-5�5� 32

57 32 ��2 ��r3K�%�K7�3E/�G2��@>7%�17�6{DxFK7EG�G�v¡}%�E��?=:8`�31�K7�3Eft�%���xv'(%�=@%�AGK t?%7�nx(8:�@��%7�{���8`%�'(�6K7t�x(%7'�J48`x(r�t�'v%�{v{�×�-3%]JáÖ=|xv'vK�x(8:%7�3�3��d'v%�t�2��]©j± ¦ l©�ª��d³]l-Âw³]l��d³ À µ"¾sµ7µTª,hjl�ÅIh�³]© ² ¿v±�l�³]ª:³(m Á �,à�K7'(af8u{�r�×Ë��K7'�xv�?��>@8:'vtFr��-�*��à �-'(abK��@L���¡�KML§+6575�����d�3��=�2��@L�^ c&p&�QcY¡�.9�3.�2¡}���3K�tF>�K��3Ew¬f23��tFr@��1��?'v=de�cYE3{?2Co���¶7 7 �×�¶� n\�2

5n��24cI2����7'(�-�3{��-��K��3E �T2@��>7%71��-{�xvK�EG����ps%7af_3K�'v8u{�%��/%7A*8`�@z��?'(x(�-EbK7�3Eb'v�?1���=:K7'd�3K�xvtFr�E�8u{�x(8:=`=uK]xv8`%��3���@�d'v�?_�'v8:��x ¦(­ ¾��g Á]À µ3³M¨�h ®�À Î�� � Ê � Î �4� �d �xvr§�D;�.0p �@L@af_%n{�8:��a %��"^QL@�3K�af8ut?{bK7�3EÆps%��nx('v%7=&%�A9psr��?af8ut?K�=4�4�6K7t�x(%7'F{-�^Q8:{�x(8:=`=uK]xv8`%���ps%7=:��af�3{4K��3E<$,K]xFtFrw�Y'(%�t?�-{v{��6{?�@�I�-=:{(8`�31 ��'6��^0�-��abK�'v>T��[6×�5��������b+6575n����+? 3+?×v+- �Õ32

5�Õ�24$ 2ÓÔ8`x�xv17�-�3{QK7�3E��T2*�@>�%71��-{�xvK7E*�Y�(cYz]K�=:�3K]xv8`%��}%�AYE�L@�3K7a/8ut�af%�E��-=:{Q%�AYE�8u{�x(8:=`=uK]xv8`%���t�%�=`��af�3{QJ48`x(r��-af_�r3K7{(8u{%7��x(r3�&8:��8`x(8uK�=�'v�-{(_�%7�3{(�-�3���d'v�?_�'v8`�nx ¦(­ ¾���g Á]À µ3³M¨�h ®�À Î���� Ê�� Î�� � �] 7x(r/�D;�.0p��@L@af_�%�{(8`��a %7�f^0L@�3K7a/8ut?{K��E�ps%7�nx('v%7=d%7A psr��?af8ut?K7=s�4�6K7t�xv%7'F{?��^Q8:{�x(8:=`=uK]xv8`%��§ps%7=:��af�3{9K7�3Eq$,K]xFtFr��d'v%@t?�-{v{��6{?���I�-=:{(8`�31 ��'6��^0�-��abK�'v>��[6×�5/�7���3�b+-575n�����Õ3+�×D�Õn[�2

5@[@24�2CpQ2�¡}%�'(�3E K��3E<�T23�@>�%71��-{�xvK7E*���v~,r�� E�Ln�K�af8:t-{&%�A�tFr3�?af8:t-K�=T'v�-K7t�x(%�'v{YJ48|xvr r��6K]x48:��xv�?1�'vK�x(8:%7�3�3�n�Y'(%�t�2 � � � �&® °(³Fµ ² º�l �d³]l©�°(³�ª��d³]l6 ² ° ² l�¿ ² ��4%�af�7���ËxvK7=`L���@�-_�x-24+6575������¶7¶�¶]×D�¶�¶7\�2

5�\�2I�T2��@>7%�17�6{DxFK7EG��$ 2�ÓÔ8`x�xv17�?�{?�dc02����7'(�-�3{��-�*��cI2�K��3Eq��2 �2 �8|x(x(%� �v¡}��=`x(8:z7�6{({(�?=s�3K]xFtFr�E�8u{Dxv8`=:=:K�x(8:%7�3�3�Y¾ ¦ ��± �¾Ql3l ® º]ª ��²F² ©�hjlnm7�3¡}8uK�af8�$&�6K7tFr*��HI%]zT2,+-5�5����@��K7_�-'�+-\� �8�2

5�5�24.�2«pQ2dpsr�'(8u{�x(8uK��3{(�?�*�dc02 Ó 2��nK7t�%��3{(�?�*���32 ^�2����-'(>@8:�3{�K7�3E��T2d�@>�%717�6{DxFK7EG� � !Q�áxvr��<E�L@�3K�af8ut?{�%7A0�3K�xvtFrqE�8u{D×x(8:=:=:K�x(8:%7�*)4. {�x(�E�L<%�Ad_3K7'vK7a/�?x('v8:t�{(�?�{�8`x(8:z@8|xDL<8:��8:E��-K�=���8:�3K�'vLwt?%7=:��af�3{v���*¾ ¦ ��± � ¾Qll ® º]ª ��²v² ©�hjlnm7�T¡�8:K7a/8$&�-K�tFr*��HI%]zT2,+-5�5�������K7_�-' +6\� nEG2

+6�7��2,�2CpQ2�¡}%�'(�3E K��3Ew�T2��@>7%�17�6{DxFK7EG�á�(~,r3� E�L@�3K7af8:tQ��-r3KMz@8`%�'s%7A�t?K�{(t-K7E��Q_�'v%@t?�-{v{��6{YJ48`x(rwK�_�_3=`8ut?K�x(8:%7��xv%/E�8:{�x(8:=|×=uK]x(8:%7�<t�%�=`�3a/�{(�3�¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjlnm7�¡}8uK�af8*$&�-K�tFr*��HI%]zT2,+-5�5����@��K7_�-'�+-\757�*2

+6��+72,.�2«pQ2,psr3'(8u{Dxv8:K7�3{(�?�*�4�2CpQ2&¡}%7'v�3EÆK��3EÇ�G2&�@>�%717�6{DxFK7EG�/�(.�t?%7af_3K7'vK�x(8:z7�}K��3K7=`L�{(8:{�%�A�af��x(r3%@E3{bA�%7' {�%�=`z@8:��1{(L@{�x(�-ab{d%�A*�3%7��=:8`�3�-K�'&K�=:17�-��'vK78:t,�-�n�3K]xv8`%��3{?� ��Ä&°v³-¿6kQ³�Â0©�± ² ����©�±�g ¦ � g<g�h À�® ª`º�©�h�³�l��d³]l- ² ° ² l�¿ ² �@~�'v%7�3E�r3�?8:aw��������f+-5�57Õ����+M[6×D�¶���2

+6���2,¬f23�QKMzn'v��K��3E}�T2��@>7%�17�-{�xvK�EG�������3_���x 3]%7��xv_���xQ{(�?=:�-t�x(8:%7�}K��E _K�'(x(8uK�=*t�%��nx('v%7=�� � ¦(­ ¾�� �}³]°�ª:¹ �d³]l@m�° ² ¨F¨�����K7�;�'FK��t�8u{(t?%3���7�3=`L�+6575�Õ��@Ã�%7=:��af��¡��*+6\�+�×F+-\�Õ�2

+M[

Page 75: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

+6�7¶�2,¬f2��QKMzn'v�7���32�¡}%7'v�3EáK��3E��T2��@>7%�17�-{�xvK�EG�0�F�@�?=:�-t�x(8:%7��%�A,A��?�6E��3K�tF>�z]K�'v8:K7��=:�-{ A�%7'�8:af_�=:�?af�?�nx(8:��1�%�_�x(8:af8`�-8`�31t�%��nx('v%7=G{(tFr3�?af�-{-� � · Ï�¾�� � �d³]l- ² ° ² l�¿ ² �d³]l3©�°(³�ª"� � �]�c�Ø��?x(�?'6��y0¬f���@�?_�x624+-5�57Õ��@ n5�+�×Ë �5�Õ�2

+6�� 32,¬f2@�0KMz@'(�QK��3E��G2@�@>�%71��-{�xvK7E*���(c ���6t�x&%�A��I�Q�q�-�?'v%�{YK7�3Eb_�%7=:�-{s%7��_��?'(A�%7'vabK��3t?�I8:��a9��=`x(8:z]K�'v8:K7��=:�Q{(L@{�x(�-ab{?� �· Ï�¾�� ���d³]l- ² ° ² l�¿ ² ��³�l3©�°(³]ª � � �M�Tc�Ø��?x(�?'6��y0¬f����?_�x624+-575�Õ���57¶��]×�57¶n��2

+6����2,¬f2]�0KMz@'v�sK��E��T27�@>�%71��-{�xvK7E*�����@�-=`�6t�x(8:%7��%�A3z]K7'(8uK���=:�-{�A�%7'�'v�?1���=:K�x(%�'(L�t�%���xv'(%�=��{�8:��1 _%�=`�4E�8:'(�6t�xv8`%��3{?� ��¾ ¦ ��± �¾Ql3l ® º]ª ��²F² ©�hjlnm7��psr�8ut?K717%�@H0%]zT2&+6575�Õ�����K�_��?', n�]AD2

+6�7Õ�24�T2��>7%71��-{�xvK�EG���Fps%7�nxv'(%�=T{�x('v�3t�x(��'v��E��-{(8`1��3�b¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjlnm7��psr�8ut?K717%�@H0%]zT2&+6575�Õ�����K�_��?'�+? n57K32+6�n[@2,¬f2M�0KMz@'(�&K��3E��T2��@>7%�17�-{�xvK�E¸� �8`af8`xvK�x(8:%7�3{�8`af_�%�{(�-E��@L��I�Q���-�?'v%�{ 3M_�%7=:�-{*8:�9a���=`x(8:zMK7'(8uK��3=`�&{�L�{�x(�?ab{v���0�Y'(%�t72

� � �+* �&® °(³Fµ ² º�l �d³]l©�°v³]ª��d³�l- ² ° ² lT¿ ² �T$&'(�3{v{(�?=u{?�3$&�-=`1�8`��a<�3����=:L�+6575n[�����K�_��?'0~���×�. ��+�e�Õ]×Ë_3K�1���_3K�_��?'I_3=`�3{+�×Ë_3K717��K��3{�x('FK7t�xFo�2

+6�7\�2,$ 2sÓÔ8`x�xv17�-�3{ K7�3E �T24�@>�%717�6{DxFK7E �(¡���=|xv8`z��-{v{��-=0�3K�xvtFrÇE�8u{�x(8:=`=uK]xv8`%��Ô×/�?Ø�_�-'(8:af�?�nxvK7=0z7�-'(8`Öt-K]x(8:%7������Y'(%�t72{(Lnaf_�%�{(8`�3a�Î�hu¨�©�hjªjª`º]©�h�³]lÔº]lT¹�¾�¯�¨�³�°?¯�©�h�³]l �+*�e���2�^ K�'(x(%7����cYEG2Co����¶�5]×D] �\3��¡�K7K7{�x('v8utFr�x6�*HI�?x(r��-'(=uK��3E3{?��\]×F+-��@�-_�x-24+6575n[�2��Y����=:8:{(r��6E �@L��(psr3�?abcI��yQ¬f2

+6�75�2,.�2«pQ2�psr�'v8u{Dxv8:K7�3{��-�*���G2��@>7%�17�6{DxFK7E�K7�3Eá¬f2 ¡q2 *8:�?�*� �(��K�'(x(8`x(8:%7�3�-E����?x(=:L@��>�K�'v'FK���1��?af�?�nxv{0A�%7'����K]x(�-'(�K�'vL{(�?_3K7'vK�x(8:%7�3{v���9�Y'(%�t72�{(Lnaf_�%�{(8`�3a¸Î9hu¨�©�hjªjª:º]©�h�³]l�º]lT¹�¾�¯�¨?³]°?¯?©�h�³]l$�+*�e���2@^ K�'(x(%7����cYE*2 o���[] n�]×D[7��Õ��]¡�K�K7{�x('v8:tFrnx6�HI�?x(r��-'(=uK��E�{?��\�×v+6�/���?_�x624+-575@[@2��d���3=`8u{�r3�-Ew�@L��(psr��?abc0�3y0¬f2

+�+-��2,.�2«pQ2@psr3'(8u{Dxv8:K7�3{(�?�bK��3Eb�T2@�@>7%�17�6{DxFK7E ���(cY���?'v17L�{(KMz@8:��1�{�8:�b8`�nx(�-17'FK]xv�-Ef����xv=`L@��>/E�8:{�x(8:=:=:K�x(8:%7�bK�'v'vK7��17�-af�?�nxv{-)��af_%�'�xFK��3t?�I%�AG�3{(8:��1�x(r3�0_�'v��A��-'('v�-Eb{(�?_3K7'vK�x(8:%7�3� ¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjl@m��T+-Õ�×��+4HI%]zT2s+6575@[@� �%�{d.0��17�-=`�6{?���K�_��?'�+65757E*2

+�+7+72&��z]K�'b�2d�0K�=:z7%�'v{(�?�§K��3EÆ�@8:17��'FE"��>7%71��-{�xvK�EG� �����3E�8`'v�-t�xf%���×Ë=`8:���w%7_�xv8`af8:�-K]xv8`%���xvr�'v%7��1�r"{�x(�-_%�8`�nx�t�%���xv'(%�=:�3�¾ ¦ ��± � ¾Qll ® º]ª ��²F² ©�hjl@m���+-Õ]×D�+ HI%]zT2,+-5�5n[@���%�{4.I�317�?=:�-{-����K�_��?'�+65� 7r�2

+�+6�2,cI2 ¬f2��I8:=:a/�-�*�n�G2��@>7%�17�6{DxFK7EG��¡�2 ;&27^Q%7r��-'�xDL9K7�3Ef¡�2 ;s2�¡�K�=:%7�����}�����nx(�-17'FK]xv�-E9E��-{(8`1��*��%7_��?'FK]xv8`%��/K7�3E/t�%7�nxv'(%�=%�A��3K�xvtFr��?Ø@x('FK7t�xv8`z���E�8u{Dxv8`=:=:K�x(8:%7�}J48`x(r�Kbaf8:E�E�=`��z7�-{v{(�?=u����¾ ¦ ��± � ¾Ql3l ® º]ª ��²F² ©�hjl@m���+-Õ�×��+�HI%]zT2�+-5�5n[�� *%n{.I�317�?=:�-{-����K�_��?'I7��+?r�2

+�+-¶�2,$ 2GÓÔ8|x(x(1��?�3{�K7�3Eá�T2��@>7%�17�6{DxFK7EG� �(��%7x(�-��xv8:K7=��-���?'v17L�{vKMz@8`�31�{ %�A&a9��=`x(8:z7�6{({(�?=��3K�xvtFráE�8u{Dxv8`=:=:K�x(8:%7�3�3� ¾ ¦ ��± �¾Ql3l ® º]ª ��²F² ©�hjlnm7� �%�{4.I�317�?=:�-{-�G+-Õ�×��+QH0%]z�24+6575@[@�@��K�_��?'I¶� nEG2

+�+? 32&��2 �32d�QK�=:z7%7'F{(�?��K7�3E"�G2s�@>7%�17�6{DxFK7EG� �vy0{(� %7A0A��-�-E��3K�tF>�A�%7'b8:�3E�8:'v�-t�xb%�_�x(8:af8`�-8`��1�t?%7�nx('v%7=�)w.0_�_�=:8:t-K]xv8`%���xv%_���x(=:L@��> E�8:{�x(8:=`=uK]xv8`%��3��� ¦(­ ¾���¨ Á]À µ�³]¨Fh ®�À Î�� � Ê Ä&g � �ps%�'�A����3à '(�-�-t������7\�×v+6�9�������b+-5�57\3�@¶�575�×� n�� 32

+�+6��2,¬f2�QKMz@'(��K7�3E��T2G�@>7%�17�6{DxFK7EG�Ç�F�@�?=:�-t�x(8:%7�}%7AdzMK7'(8uK��3=`�6{,A�%7'Q'(�-17��=uK]xv%7'vL�t�%���xv'(%�=*�3{(8`�31�_�%7=:��z7�6t�x(%�'v{v��� ¦(­ ¾��¨ Á]À µ3³M¨�h ®�À Î���� Ê Äsg(� �ps%7'(A��*�à 'v�?�6t������7\]×F+-���7�3���f+-575�\���Õ�+- �×�Õ�+65�2

+�+-Õ�2,$ 2dÓÔ8`x�x(1��?�3{�K��3EÔ�T2s��>7%71��-{�xvK�EG� �v¡}��=`x(8:z7�-{v{(�?=I�3K�xvtFrÆE�8u{Dxv8`=:=:K�x(8:%7�"×���%7x(�?�nxv8:K7=&�-���?'v17L§{(KMz@8:��1�{v��� ¦(­ ¾��¨ Á]À µ3³M¨�h ®�À Î���� Ê Äsg(� �ps%7'(A��*�à 'v�?�6t������7\]×F+-���7�3���f+-575�\�����+M�M×D�77��2

+�+M[@2,¬f2*�0KMz@'v�/K7�3Eá�T2��@>�%717�6{DxFK7EG� �(���-'�A�%�'(abK7�3t���=`8:af8|xFK]x(8:%7�{ A�%7'����3{�xvK7��=:�b����� ! _�=uK��nxF{(�3�ÇÄ,°(³-¿ ²F² ¹]hjl@m]¨ � � ���¾ Àb² °�h�¿Fº]l �d³]l3©�°(³�ª��d³]l- ² ° ² l�¿ ² ��dr38`=uK7E��-=`_3r�8:K3��yQ��.9�] 7×�7Õ9�������b+65757\3��¶��¶7 �×�¶�7¶7\

+�+-\�24�T2��@>�%71��-{�xvK7E�K��3E���2 �2*�0K7=`z�%7'F{��-�*� �F�@�?=`Aj×�%�_�x(8:af8`�-8`�31wt?%7�nx('v%7=�)Q$,K7{(8ut98u{({(���6{ K7�3E�~�KML@=`%�' {(�?'v8:�-{�K��3K7=`L�{(8:{ �����K�_��?',_�'v�-{(�?�nxv�-EwK]x p !���� Ó�%7'v>@{(r�%�_*��¡�K�>��-E�%���8uK����7\�×Ë��5%! t�x624+-5�57\

+�+-5�2,~�'(��=u{ �K�'F{({(%7�áK��3E��@8:17�3'vE��@>�%717�6{DxFK7EG� � �8`af8`xvK]xv8`%��3{�8:af_%n{��6E��@L�=`%]J&�?'�=uKML7�-'�t�%7�nxv'(%�=Yt�%���Ö317�3'vK�x(8:%7�3{����.I�(psrc".0���@�3K�=�¡}�?�?x(8:��13�3¡�8:K7a/8*$&�6K7tFr*�G+6Õ]×D��9H0%]zT2&+6575�\

+M���24�@8:17��'FE ��>7%71��-{�xvK�EG����z]K7'&�2��0K�=:z7%�'v{(�?� K��3E �7%�r��<pQ2�¡}%�'(�3EÚ�v���?=`Aj×�%�_�x(8:af8`�-8`��1ft�%��nx('v%7=�)�~,r�� �3K�{�8ut08uE��6K�K7�3E~�KMLn=:%7'4{(�?'v8`�6{,K��3K7=`L�{(8:{v���w.I�(psr3cÆ.I�3�n�K�=�¡}�-��xv8`��1��¡}8uK�af8�$&�-K�tFr*�G+-Õ�×�7�9HI%]zT2,+-5�57\3�@��K7_�-'I7�5�t

+M�+72&��2 �32n�0K�=:z7%�'v{(�?�fK��Ef�G2n�@>�%717�6{DxFK7EG���Yy0{(�4%�A��@r�%�'�xFt���x&¡}��xvr�%�E�{�xv%9.I�3K7=`L�{(��!Q_�x(8:abK�=!Q_�-'vK�x(8:%7�f%�A*����xv=`L@��>^Q8:{�x(8:=`=uK]xv8`%���ps%7=:��af�3{(�3�<Ä&°v³-¿6k0g Á]À µ�³]¨Fh ®�À Ä � � g � � ���3¶��/¡�KML�×D��7���3�b+-575�5��@$&�3E�K�_��-{�x-��I����1nK�'vL72

+M7�2&��2 �32��QK�=:z7%7'F{(�?�*��¡�2���?'v'vK/K��3E}�T23��>7%71��-{�xvK�EG���4cdz]K7=`�3K�x(8:%7�w%�A��@�?=`Aj× !Q_�x(8:a/8:�?8:��1 ps%���xv'(%�=*�nx('v�3t�xv��'v�-{&A�%7'IK7����nx(�-17'FK]x(�6E9���?x(=:Ln�3>9^08u{�x(8:=`=uK]xv8`%���ps%�=`�3a/�����Ä&°(³6¿6k4g Á]À µ3³M¨�h ®�À Ä � � g � � ���@¶7��¡�KMLn×D0��������+6575753��$&�3E�K�_��-{�x-��I�3��1�K7'(L�2

+-\

Page 76: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

+M�¶�2,¬f2]�0KMz@'v�&K7�3E��T27��>7%71��-{�xvK�EG� �v.0tFr�8:�?z]K7��=`� � � ×�_��?'(A�%7'vabK��3t?�Y%7Aa9�3=|xv8`z]K�'v8uK���=:�&{(L�{Dxv�?ab{�J48|xvrf���3{�xvK��3=`�&�?�-'(%n{K��E�_�%7=:�-{v���<�d'v�?_�'v8:��xF{ +? �xvr �D;�.0pÇÓ�%7'v=:E}ps%7��1�'(�6{({-��$&�?8 BD8`��1���7�3=`L�+-575�5��nÃ�%32d^��3¶753+�×�¶75�Õ�2

+M] 324�T2��@>�%71��-{�xvK7E*�G��2 �2*�0K7=`z�%7'F{��-�*�G~�2 �K7'v{v{�%���K��E�¡�2C�T2�à %]z]K�xv{(afK7'(>T� �(�d=uK��nxDJ48uE��ft�%7�nxv'(%�=�)�~,r��b{��6K�'FtFr�A�%�'x(r3�9{��-=|Aj×Ë%7_�x(8:a/8:�?8:��1�t?%7�nx('v%7=*{�x('v�3t�xv��'v�-�����Y'(�-_�'v8`�nxv{�+? �xvr<�D;�.0pÔÓ�%7'v=:E�ps%���17'v�-{v{-��$s�-8 BD8:��1�����=`L�+-5�575���Ã�%�=�2H��¶�7�]×˶�¶7�32

+M7��2,.�2,;3K�K����6{�K7�3EÇ�T24�@>7%�17�-{�xvK�EG� ��ps%7�nx('v%7=0{�x('v�3t�x(��'v��{(�?=:�-t�xv8`%��ÔA�%7'w{��-'(8uK�=0_�'(%�t?�-{v{��6{bJ48|xvr K�_3_�=`8ut?K�x(8:%7�Æxv%_3�I×����-��x('FK�=:8:�-K]xv8`%��3���w�d'v%�t�2�cd��'v%7_��-K7�<ps%���xv'(%�=�ps%7��A��-'(�-�3t�����¬�K�'v=:{('(�3r��7���@�-_�x-24+657575

+M�Õ�2,~�2 �K�'F{({(%7�áK��Eq�T2���>7%71��-{�xvK�EG� ��ps%7�nx('v%7=�%7A48`�3E��3{Dxv'(8uK�=sr��-K�x98:��xv�?1�'vK�x(�-EáE�8u{�x(8:=`=uK]xv8`%��qt�%7=:��af�3{v��� .I�(psrc.I�3�n�K�=*¡}�-��x(8:��1�3^QK7=`=uK7{-�G+�×D��HI%]zT24+-5�575�2

+M�[@2,~�2 �K7'v{v{(%7�*�s�G2s�@>7%�17�6{DxFK7EqK7�3EÆpY×�pQ2 �d�*� �Fps%��nx('v%7=&%�AQ'v�-K�t�xv%7'bK��3E"{(�?_3K7'vK�x(%7'/J48`x(rÆ'(�6t�L�t�=:�-�3� .I�(psrc.I�3�n�K�=*¡}�-��x(8:��1�3^QK7=`=uK7{-�G+�×D��HI%]zT24+-5�575�2

+M�\�2&��2 �32��0K7=`z�%7'F{��-�áK7�3Eq�T2d�@>�%717�6{DxFK7EG�Ì�(��a/_3'(%]z��-EáK��3K7=`L�{(8:{�K��3Eq���3E��-'v{�xvK7�3E�8:��1�%�A4xvr�� ���?x(=:L@��>�E�8:{�x(8:=`=uK]xv8`%��t�%�=`�3a/����<.I�(psr3cÆ.I�3�n�K�=�¡}�-��xv8`��1��^QK7=`=uK7{-�G+�×D�/HI%]zT2,+-5�575�2

+M�5�2&��2 �32@�0K7=`z�%7'F{��-�fK7�3E��T2��@>7%�17�6{DxFK7EG���(.0�3K�=:Lnx(8ut4��Ø�_�'v�-{v{�8:%7�{�%�A*af8:��8`a���a¸�?�3�?'v17L�t?%7�3{(��af_�xv8`%���8`��a9��=`x(8ut�%�a�×_�%7���-��x4E�8u{Dxv8`=:=uK]x(8:%7��)�. 'v�?z@8:{(8`x&%7A*x(r���yI�E��?'vJs%@%�Eb�-���K]x(8:%7�{(�3��.I�(psr3c".I���@�3K7=G¡}�?�?x(8:��13��^ K�=:=:K�{?�T+�×D��H0%]zT2+-5�57532

+6¶7��2,.�2�;3K7K7���-{�K7�3E/�G27�@>7%�17�-{�xvK�EG�<��_3�I×��3�?��xv'vK7=`8:�-K�x(8:%7�*)G���nx(�-17'FK]xv�-E�_�'(%�t?�-{v{�K7�3E/t�%7�nxv'(%�=@E��-{(8`1��3�����d'v%�t�2��D;�.0pY×{(Lnaf_�%�{(8`�3a .0E�tFr3�?a<ß 7�7�������d8u{(K3���ËxvK7=`L��G+? �×F+-Õ/������������7���@_�_�2s[��M×�\7�32

+6¶�+724�T2I�@>�%717�6{DxFK7EG� �F�@�?=`Aj×�%�_�x(8:af8`�-8`�31§t�%��nx('v%7=�)á.�E�8u{Dxv8`=:=uK]x(8:%7� t?K7{(��{�x(�E�L���� �d'v%�t�2 �D;�.0pY×Ë{(L@af_%n{�8:��a .0E@×tFr��-awßC����7�3�n�Y8:{vK����ËxFK�=:L7�*+- �×F+-Õ9��������7�7�7�3�@_�_*24+-�3+-¶�×v+6��+-\32

+6¶��2,~�2 �K�'F{({(%7���,�T24�@>�%717�6{DxFK7EG�,¬f2s�0�-{�x(�?x(���*� �v���?=`Aj×�%�_�x(8:af8`�-8`��1§t�%7�nxv'(%�=I%�A�K�=uK�'v17�?×Ë{vt?K7=`�w_�=uK��nx-)á~,r���~��?��×���6{({(�?��cYK�{DxvabK��w_�'(%�t?�-{v{(�3�w�@L@af_%n{�8:��a�psr��?af8ut?K�=��d'v%@t?�-{v{Ips%7�nx('v%7=GÕ��~��3t-{�%��*��.I'v8:�?%7�K��[6×F+6��nK��*2Y7�7��+���d'v�?_3'(8:�nxv{&_�_*2� n\�+�×Ë �\�Õ�2

+6¶7¶�2,~�2��8:EG�I�T2&�nx('FK��3E*�4�G2s�@>7%�17�6{DxFK7EG� � !Q��×Ë=:8`���}%�_�x(8:af8`�6K]xv8`%��§%7A�K�t?'(�3E��}����8`x�r��-K�x���Ø�tFr3K7��17�-'/�3��xDJ&%7'v>@�3��@L@af_%n{�8:��a�psr��?af8ut?K�=*�Y'(%�t?�-{v{4ps%��nx('v%7=GÕ���~��3t?{(%7���3.I'v8`�-%7�3K3�3[6×F+6���K7�*2d��7�3+7���d'v�?_3'(8:�nxv{&_�_*2d �[]Õ�×� n\7��2

+6¶� 32,¡�2C�T2à %]z]K]xF{�abK7'(>T�3�T2��>7%71��-{�xvK�EG�§��ps%7�nx('v%7=*{�x('v�3t�x(��'v��{��-=`�6t�x(8:%7�wA�%�'0K��<�?z]K7_%�'vK�x(8:%7��_3'(%�t��6{({v���<cd�3'(%�_�6K���@L@af_%n{�8:��a %7�<ps%7af_���xv�?'s.08:E��-E��Y'(%�t?�-{v{dcd��1�8`�3�?�?'v8:��1b+7+��n¬�%�=:E�8:��1��^Q�?��abK�'v>T�@n[6×�¶7��¡�KMLb�����+��7cd=u{��-z@8`�-'����$,H �� � 7 @���n[��757 3��_�_�2dÕ���[M×ËÕ�Õ��2

+6¶���2,~�2 *8uEG�Q�T2I�@>�%717�6{DxFK7EG� ����af_�=:�?af�-��xFK]xv8`%��Ô8:{v{��3�-{�A�%7'�'v�-K7=|×�x(8:af��%7_�x(8:a/8:�-K�x(8:%7�Ç%7A9t�'v�3E���r��-K�x ��Ø�tFr3K7��17�-'���?xDJs%�'(>���� cd��'v%7_��-K7�"�@L@af_�%�{(8`��aÚ%7� ps%7af_���x(�?'�.08:E��-EÆ�d'v%�t��-{v{fcd��1�8`�3�?�?'v8:��1Æ+7+7�&¬�%7=uE�8:��13�&^0�-��abK�'v>���[M×˶��9¡�KMLw��7�3+7��cd=u{(�?z@8`�-',����$,H �� 7 � n�7�n[]��5� ��_�_*24+6�� 3+?×v+6�� nÕ�2

+6¶7Õ�2,��2�cd��1��?=:8`�-�*��~�2 �K�'F{({(%7�����T2��@>�%717�6{DxFK7EG�¸�F�@8:a9��=uK]xv8`%���K7�3E�%7_�xv8`af8:�-K]xv8`%��á%�Asr3�-K]x�8:�nx(�-17'FK]x(�6E�E�8:{�x(8:=`=uK]xv8`%��t�%�=`�3a/�{(� ���D¡��������+��@��%�'v{(17'v������2

+6¶n[@2,¡�2C�T2�à %]zMK�xv{(abK�'v>��@�T2��@>7%�17�-{�xvK�EG���v.Çaf��xvr�%�EfA�%7'&{��-=`�6t�xv8`%���%�A�t?%7�nx('v%7=:=`�6E/zMK7'(8uK��3=`�6{YK��Ef'(%����3{�x&{(��x(_�%78:�nxv{v��@�D¡��3��7�3+7����%7'F{(17'v�����*2

+6¶7\�2&��2 �32n�0K�=:z7%�'v{(�?�����T2n��>7%71��-{�xvK�EG�������nxv�?17'FK]xv�-E�ps%7=:��af��^Q�-{(8`1��3{�A�%�'Y¡}8:��8`a���a¸cd���-'(1�L9K��Ebcd�nx('v%7_@L��I� �n��8:'(�?×af�?�nxv{�8:��¡}��=`x(8ut�%�a/_�%7�3�?�nx/^Q8:{�x(8:=:=:K�x(8:%7�3� .I�(psr3c�.0���@�3K�=&af�?�?x(8:��13�d~�%7_�8ut?K7=st?%7��A��-'(�-�3t���%��§�@�-_3K�'FK]xv8`%��3{~��-tFr���%�=`%�17L��@��K7_�-'I�¶7K3���4�?��%�3HI�-z]K7E�K3��HI%]z7�-a9���?'I�M×�5��37�7�3+72

+6¶75�2,cI2C�nxv%7'v>MK�K7{-���T2��@>�%717�6{DxFK7E�K��3E�Ã92*.0=:{�xvK�EG� �F�nxvK7��8`=:8:�?8:��1<%�A&E��-{(8`'v�-E -3%]J 'v�?1�8`af�6{�8`��_�8:_�-=`8:���-{9� .I�(psrc.I�3�n�K�=Gaf�?�?x(8:��13�3��K7_�-'I�\n[�EG���4�-��%3��H0�?z]K7E�K3��HI%]z��?a9���?'0�]×Ë53����7�3+72

+- ���24�T2��@>7%�17�6{DxFK7EG�Ì�(�Y'(%��3K��3=`L}xvr������-{�x/{(8:a/_3=`�w�d�D^¸xv����8:��1�'v��=:�-{98`��xvr���J&%7'v=uE�� .I�(psr3c .I���@�3K7=saf�?�?x(8:��13���K�_��?'In[]Õ�r������-{v{�8:%7�w%7�}.0E�zMK7�3t��6{,8`�<_�'v%�t��6{({,t�%��nx('v%7=����4�?��%��HI�-zMK�E�K���H0%]z7�-a9���?'0�M×�5���7�7��+�2

+- 3+724�@8:17��'FE��@>�%71��-{�xvK7E*���v�d=uK��nxDJ48:E��0t�%���xv'(%�=�)�~�%]J,K�'FE�{dK�{�L�{�x(�-afK�x(8utI_�'v%�t��6E���'v�-� e�_�=:�?�3K7'(L/=`�6t�xv��'(�Mo���cd�3'(%�_�6K���@L@af_%n{�8:��a %��Ôps%�af_���x(�-'�.I8uE��-EÆ�Y'(%�t��6{({/cd�3178:���?�-'(8:��1"+6��sE��?�Ô�0K�K�1�YHI�?x(r��-'(=uK��3E3{?�4�Õ�×�75�¡�KML§7�7����cd=u{(�?z@8`�-',����$,H �� 7 � n��+7+-��5�+���_�_*2Y�n[6×�Õ75�2

+-5

Page 77: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

+- n�2,¡�K7'(8:�3{��T2,à %]z]K]xv{(abK�'v>T�,�@8:17�3'vEÔ�@>�%717�6{DxFK7EG� � !Q_�x(8:abK�=I�@��a���-'�%7A�{�xvK717�-{�8`�ÇE�8u{�x(8:=`=uK]xv8`%��ÔJ48|xvrÔ'(�6{�_��-t�xx(%"t�%���xv'(%�=`=uK��38`=:8|xDL�� cY��'(%�_�6K�� �@L@af_�%�{(8`��a %�� ps%7af_���xv�?'<.I8uE��-E �d'v%@t?�-{v{�cY��178:���?�-'(8:��1Ô+M��0E��-� �0K�K�1�HI�?x(r��-'(=uK��E�{?�37Õ]×D�5/¡�KML��������@cY=:{(�?z@8:�?',����$,H �� � 7 @��+7+6�753+7��_�_�2� �575�×��7�� 2

+- �¶�24�@8:17��'FEq�@>�%717�6{DxFK7EG��¬&BD��xv8`=&�0KMz@'(����~�'v��=:{ �K7'v{v{�%��*� �Fps%7�nxv'(%�=d=`8:af8|xFK]xv8`%��3{�A�%�'9���3{�xvK7��=:��_�=uK��nxv{v� �d'v%@t72<%�A�D;�.0pÆÓ�%7'v=uE}ps%���17'v�-{v{-�n$,K�'Ft��-=`%��3K����+�×D�Õ9����=:Lw7�7�������K�_��?'4~&×Ë;3'�×�¡<×F+6�]×v+�2

+- 7 32,¡�K7'(8:�3{b�T2sà %]z]K]xF{�abK7'(>T�Y�@8:17��'FEÆ�@>7%�17�-{�xvK�EG� �F�@�?=:�-t�x(8:%7��%7A t?%7�nx('v%7=:=`�6Eqz]K�'v8uK���=:�-{fK��E�'v%7���{Dx�{(��x(_�%78:�nxv{v��d'v%�t�2�%�A��D;�.0pÔÓ�%7'v=uE<ps%���17'v�-{v{?��$,K�'Ft��-=`%��3K����+?×�7Õ�����=:L �������@��K7_�-'4~&×Ë¡}%7×Ë¡}×v+�+�×Ë 32

+- n��2&��z]K�'/�32��0K�=:z7%�'v{(�?��K7�3E��@8:17��'FEq�@>�%717�6{DxFK7E �7¡�8`��8:a9�3a��-���?'v17LáK��Eá�?�nx('v%7_@L�'(�-���38`'v�?af�?�nxF{�8`��a9��=`x(8ut�%�a�×_�%7���-��x E�8:{�x(8:=:=:K�x(8:%7�3�3���Y'(%�t�2,%7A ¦ l3© ² °�lTº]©�h�³]lTº]ª�¿v³�l- ² ° ² l�¿ ² ³D Î�hu¨�©�hjªjª`º]©�h�³]l�º�l�¹b¾�¯�¨?³�°�µ�©�h�³]l3�T$,K7E��-��×�$&K�E��?���à �?'vabK��@L7��¶��/���?_*2�×s�n%! t�x-2Y7�7�������K�_��?'4Õ]×D�[�2��Y����=:8:{(r��-Ew�@L�à^0���à �-'(abK7�nL�e�����$,H ¶]×�57¶3+-¶�\� �×�¶n[M×˶no�2

+- �Õ�2,�I8:=uE��}¬f2dcd��1��?=:8`�-�*�Y~�'(��=u{ �K7'v{v{�%���K��E"�@8:17�3'vE"�@>7%�17�-{�xvK�E �(��af_�=`�-af�?�nxvK�x(8:%7��%7AQ%�_�x(8:abK�=4%7_��?'FK]xv8`%��qA�%�'r��6K]x�×Ë8:��xv�?1�'vK�x(�-E/E�8u{Dxv8`=:=uK]x(8:%7�bt?%7=:��af�3{(�3���Y'(%�t�2�%�A ¦ l© ² °�l�º�©�h�³�l�º]ªT¿F³]l- ² ° ² l�¿ ² ³DÂ&Î�hu¨�©�hjªjª`º]©�h�³]l�º�l�¹�¾�¯�¨?³]°�µT©�h�³�l3�$,K7E��-��×�$&K�E��?����à �?'vabK��@L7��¶7���@�-_*2w×Q�� ! t�x-2}����������K�_��?'9¶32 ¶�×˶32��d���3=`8u{�r3�-Eá�@L�à^0����à �?'vabK��@L�e�����$&H¶]×�57¶3+-¶�\� �×�¶n[M×˶no�2

+- @[@24�T23�@>�%7��'FK7{&K��Ew�T23��>7%71��-{�xvK�EÚ�F�@�?_K�'FK]x(8:%7��%�A�xv�?'v�3K�'vLfr���xv�?'v%�K7�?�?%7x('v%7_�8utIaf8`Ø@x(��'v�-{,8:�wK/t�=:%�{(�-E a9�3=|xv8`z��-{v{��-=�3K�xvtFr}E�8u{Dxv8`=:=:K�x(8:%7��×�E��6t?K��nxv�?'4r@L@��'(8uE��3���d'v%@t72d%�A ¦ l3© ² °�lTº]©�h�³]l�º�ª�¿F³]l6 ² ° ² lT¿ ² ³�Â0Î�hu¨�©�hjªjª`º]©�h�³]lqº�l�¹f¾�¯�¨?³]°�µT©�h�³�l3�$,K7E��-��×�$&K�E��?���sà �?'vabK��@L7�Y¶������?_*2§×��� ! t�x-2Ô�������d��K�_��?'b�M×Ë 32§�Y����=:8:{(r��6Eq�@LqÃQ^Q���sà �-'(abK��@LÔe�����$&H¶]×�57¶3+-¶�\� �×�¶n[M×˶no�2

+- �\�2&Ã92�.0=:{�xvK�E9K7�3E/�G2]��>7%71��-{�xvK�EG���v�4%7���{Dx�!Q_�-'vK�x(8:%7���@L9t?%7�nx('v%7=:=:8`��1Ix(r��,'v8`1�r�x�z]K�'v8:K7��=:�st�%�a9��8:�3K�x(8:%7�3�Æ.I�(psrc.I�3�n�K�=Gaf�?�?x(8:��13�3��K7_�-'I] @[]13�@���3E�8uK��K�_�%7=:8:{-��¶]×�\�H0%]zT2Y��7�n�2

+- �5�2,¡�2C�T2�à %]z]K�xv{(afK7'(>T��G2��@>�%717�6{DxFK7EwK��3E��G2¡�K3ß a����*�Ç�v. _�=uK��nxDJ48:E���t�%7�nxv'(%�=*_�'v%@t?�-E��3'(��J48`x(r�K7_�_�=:8:t-K]x(8:%7�wxv%t�%��nx('v%7=T{Dxv'(�3t�x(��'v�QE��-{(8`1���A�%7',K�1�K7{s_�%]Js�-'s_�=uK��nxF� .0�(psr3c".I���@�3K7=�af�-��x(8:��1�@��K7_�-',���5�AD�����3E�8:K7�3K�_�%7=:8:{-��¶]×�\HI%]zT2d������2

+M����2,cI23�@x(%7'v>]K7K�{4K��3E<�T2�@>�%71��-{�xvK7E*���v�@xvK��38`=:8`�6K]xv8`%�� %7A�{(�?z��?'v� {(=`�317178:��1f�3K�{��6E�%��wKf=:%]J,×ËE�8`af�?�{�8:%7�3K7=T��%7��=:8:���-K7'af%�E��?=u� .0�(psr3cÆ.I���@�3K7=*af�?��xv8`�313�3��K7_�-'4���57�7�@���3E�8uK��3K7_%�=`8u{-��¶]×�\�H0%]z�2Y7�7�n�2

+M��+724�T27�@>�%7��'FK7{�K��E��T27�@>�%71��-{�xvK7E*���v���?_3K7'vK�x(8:%7��%7A�~��?'v�3K�'vL��I��xv�?'v%�K7�?�?%7x('v%7_�8utd¡}8`Ø@x(��'v�-{�8:�/K ¡}��=`x(8:z7�6{({(�?=�$,K�xvtFr^Q8:{�x(8:=`=uK]xv8`%���×�^0�6t?K��nxv�?'I�IL@��'v8uE�� .I�(psrcÔ.I���@�3K7=Ga/�-��xv8`��1�3��K�_��?'�+6���E*�����3E�8uK��3K7_%�=`8u{?��¶�×Ë\/HI%]zT2d������2

+M�7�2&Ã926.I=u{DxFK7E�K��E��G26�@>�%717�6{DxFK7EG���Fps%�a9��8:�3K]xv8`%��Q%7A@¡��-K7{(��'v�?af�?�nxF{GK7{�ps%���xv'(%�=`=:�-EQÃdK�'v8uK���=:�-{TA�%�'��@�?=`Aj×"!Q_�x(8:af8`�-8`��1ps%7�nxv'(%�=:�3���d'v%�t�2�cd��'v%7_��-K7���@L@af_%n{�8:��a %7�wps%�af_���x(�-'&.08:E��-E��Y'(%�t?�-{v{dcd��1�8`�3�?�?'v8:��1�e�c&�3p&.0�sc�×F+-¶�o����3+�×��� ������������7¶����K�_�_��?�-��'vK7�nxvK���;�8:��=:K7�3EG2Y�Y����=:8:{(r��6E��@L�cY=:{(�?z@8:�?'6������$,H ��×� � 7 7×���+-¶7Õ�\]× H9��_3_*2d¶��7¶]×�¶���\32

+M��¶�2,��2 ¬f2scY��17�-=`8:�?�ÇK7�3EÇ�T24�@>7%�17�6{DxFK7EG� �v�@�-=`�6t�x(8:��1q.0_�_�'v%7_�'v8:K�x(��ps%��nx('v%7=IÃdK7'(8uK���=:�-{�A�%7'wKq�I�6K]x����nx(�-17'FK]xv�-E^Q8:{�x(8:=`=uK]xv8`%����@L�{�x(�?aÌJ48`x(r��Y'(�?A�'vK�t�xv8`%��3K]xv%7'F�����Y'(%�t�2IcY��'v%7_��-K����@L@af_�%�{(8`��aÌ%���ps%7af_���xv�?' .I8uE��-E��d'v%@t?�-{v{cd�3178:���?�-'(8:��1�e�cs�3p&.Q�Yc�×F+-¶no�����+?×Ë�7 ��������}��7��¶�� �K7_�_��?�?�3'vK7��xFK���;�8`�3=:K7�3EG2q�d�3��=`8u{(r��-E��nL�cY=:{(�?z@8:�?'6������$,H�]×Ë 7 � �×D��+6¶7Õ7\�× H��]_�_*2d n�n[M×� +6�2

+M�] 32,¡�2C�T2Yà %]z]K]xF{�abK�'v>T�Y�T2Y�@>�%717�6{DxFK7EG�Yà/2Y��%7��%@t-K��*�&K��3E§��2dà =:KMz@8ut�� �v.I_�_�=:8ut?K]xv8`%���%7AQKá�d=uK��nxDJ48:E��<ps%7�nxv'(%�=^Q�-{(8`1��<�Y'(%�t?�-E���'v�Qx(%�Kb^Q8:{�x(8:=`=uK]xv8`%���ps%7=:��af�<J48|xvr��I�-K�x0�d��af_3�3�}�d'v%@t72dcd��'v%7_��-K7�<��Lnaf_�%�{(8`�3a %���ps%�a/×_���xv�?'d.08:E��6E��Y'(%�t?�-{v{�cY��178:���?�-'(8:��1/e�cs�p&.0�Ycd×v+6¶�o�����+�×��� Q�7���3�47�7��¶����K7_�_�-�?��'FK��nxFK���;�8`�3=:K7�3EG2��@��_�_�=:�?af�-��xz7%�=`�3a/����_�_*2Y�+�×D�\�2

+M�7��24�T2��@>7%���'FK7{�K7�3E��T2��@>7%�17�6{DxFK7EG�Ì�v���?_3K7'vK�x(8:%7��%�AI.0�?�?%7x('v%7_�8ut�¡}8`Ø@x(��'v�-{�8:�"ps=`%n{��6E�$,K]xvtFrq^Q8u{Dxv8`=:=:K�x(8:%7��.0'�×'FK���1��?af�?�nxv{v���Æ�d'v%�t�2fcd��'v%7_��-K7���@L@af_%n{�8:��a�%7�qps%7af_���xv�?'�.I8uE��6E��Y'(%�t?�-{v{QcY��178:���?�-'(8:��1áe�c&�3p&.0�sc�×F+-¶�o����+?×Ë�7 ��������97�7�7¶3���K�_3_�-�?��'FK��nxvK3��;�8:��=uK��3E*2d�d����=:8u{�r��6E��@Lwcd=u{��-zn8:�?'6�@����$,H �]×Ë 7 � �×D��+-¶�Õ7\�× H��]_�_*2Y5�¶��M×�5� n��2

+M��Õ�2,¡}��=`x(8:_�r3K�{��6�7¶�c02n�nxv%7'v>MK�K7{dK7�3E��T2@�@>7%�17�-{�xvK�EG���v.Ô=:%]J,×ËE�8:af�?�3{(8:%7�3K7=�E�L@�3K�af8ut4af%@E��?=�%�A*{��-z7�-'(�I{(=`�317178:��1�A�%�'t�%��nx('v%7=@E��-{(8`1��9K��E9K��K�=:L@{(8u{(�3�0�d'v%�t�2Y+�+�xvr����nx(�?'v�3K�x(8:%7�3K7=�ps%���A��?'v�?�3t?�s%��9¡}��=`x(8:_�r3K�{�� -3%]JÇe�¡}��=`x(8:_�r3K�{���ß ��¶�o����K7�w�4�-af%3���ËxFK�=:L7�G+7+?×v+6¶���������7�7�7¶3���d����=:8u{�r��6E��@Lw$&�Q� à 'v%7�3_*������$,H +�×�\�����57\�×Ë�7 �\�×D[��]_�_*2I+�+M[6×F+-¶�¶�2

+M��[@2,.�2�;K7K��3�-{/K��3E"�T2d�@>7%�17�-{�xvK�EG���(;��-�-E@A�%�'(J,K�'FE�t�%��nx('v%7=Y�3�3E��?'/xvr�� _3'(�6{��-�3t��w%�AI���t��?'(xvK78`�nxDL���� cd�3'(%�_�6K��ps%7�nxv'(%�=dps%���A��?'v�?�t��<e�c&p4pQß �7¶no���p&K7a9��'v8uE�17���*��+�×��� <�@�?_�x(�?a���-'9����7¶�2/�d���3=`8u{�r3�-E�%7�qp&^¸�@L��DcYc0�TyQ¬�e�Õ_3K717�-{Fo�2

��

Page 78: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

+M��\�2,.�2&;3K�K����6{�K��EÇ�T2&�@>�%71��-{�xvK7E*� � !��G{��?x�×�A�'(�-��~�'FK7tF>@8:��1�ÓÔ8|xvr ¡��,p y0�3E��-' yI�t��?'(xvK78`�nxDLT)�cdØ�_�-'(8:af�?�nxvK7=Ã��?'v8`Öt?K�x(8:%7�3�we�_�%�{�x(�-'Fo��<.0�(psr3cÆ.I���@�3K7=�¡}�-��x(8:��1�3��K��};�'FK��t�8u{(t?%3��HI%]zT2d����7¶�����%n{Dxv�?', �¶�5��*2

+M��5�2&Ã92*¬�K7'(8:J,K�=uK��*�T2��@>�%717�6{DxFK7EG�G�2 ;&2*;3%7'v��6{?��c02 �G2T¡��-K7E�%]JI{?� �v�@L�{�x(�-a�{DxFK���8:=:8`�6K]x(8:%7���3{(8`��1<af8:��8`a���a#8:��_���x�?�3�?'v17L�� e�_%n{Dxv�?'�o��<.I�(psr3cÔ.0���@�3K�=*¡��?��xv8`�313���K7�w;3'vK7�3t�8u{vt�%3��H0%]zT2�7�7��¶�����%�{�x(�-'s n¶75���2

+6Õ7��24�T2��@>�%717�6{DxFK7EG���Fps%7�nxv'(%�=�{�x('v�3t�xv��'(�,E��6{�8:17�*)�ÓÔr3K]x�{�r3%7��=uE�J&�st?%7�nx('v%7=��Ma/�6K7{(��'v�sK��E�abK���8:_���=uK]xv�-,6��2����@zn8`x(�6E_�=:�?�3K7'(Lb=:�-t�x(��'v��K]xI;�8`'F{�x4.IA�'(8ut?K7��ps%7�nx('v%7=�ps%7��A��?'v�?�3t?�7�3p&K�_���~�%]J4�*�3��%7��xvr<.IA�'(8ut?K3���7¶�×Ë�n��^Q�-t��-a9���?'07�7�7¶32

+6Õ�+724�T2T�@>7%�17�-{�xvK�EG�Ç�F�@�?=`Aj×�%�_�x(8:af8`�-8`�31�t�%���xv'(%�=�)&;�'v%7a >7�?Lw_��?'(A�%7'vafK7�3t���8:�3E�8ut?K�x(%�'v{,xv%�t�%��nx('v%7=*%7A��38`%�=`%�178ut?K�=�{�L�{�×x(�-ab{(�3��24\]xvr}����xv�?'v�3K]xv8`%��3K�=�{�L@af_%n{�8:��a %7�}�d'v%�t��6{({0��L@{�x(�-ab{Icd��1�8`�3�?�?'v8:��1�e��&��c�×D����7¶�o������]×v+6���nK��*2I7�7�� �¬�����af8:��13�psr38`�3K}e���Ø@x(�-�3E��6E z��?'F{�8:%7��x(%f����_�����=:8:{(r��6E 8:�}{�_��-t?8:K7=*8u{({(����%�Adp4p&cso�2

+6Õ��2&Ã92T.I=u{�xvK7E}K7�3E��T2T�@>7%�17�-{�xvK�EG�Ç��ps%7a9�38`�3K�x(8:%7�3{I%�A�af�-K7{(��'v�?af�?�nxF{IK7{Qt�%7�nxv'(%�=`=:�-Ewz]K�'v8:K7��=:�-{-)s.I_3_�=`8ut?K�x(8:%7�<xv%K9���?x(=:L@��>bE�8:{�x(8:=:=:K�x(8:%7� t?%7=:��af�3��2����nx(�-'(�K]x(8:%7�K�=G�@L@a/_�%�{(8:��a¸%�A�.QE�z]K��3t?�-E<ps%7�nx('v%7=%�A�psr��-af8:t-K�=T�d'v%@t?�-{v{��6{e�.QE�tFr��-a�×D����7¶no����I%���1b¬�%7��1�G+7+�×F+? /��K7�*2d����� 32

+6Õ7¶�24�T2���>7%71��-{�xvK�EG� � �%]Js�-'�=`8:af8|x�%���t?%7�nx('v%7=:=`�-'�1�K�8:��A�%7'�K7t-t��-_�xvK7��=`�bE�8u{�x(��'v�3K��t��f'(��BD�-t�x(8:%7�3��2b���nx(�?'v�3K�x(8:%7�3K7=�@L@af_%n{�8:��a %�A*.QE�z]K��3t?�-E ps%���xv'(%�=�%�A�psr��-af8:t-K�=�Y'(%�t?�-{v{��6{Ie�.QE�tFr��?a/×D����7¶�o��7�I%���19¬�%���13�+7+�×F+? ��nK���2�7�7�� 2

+6Õ� 32,cI2��nxv%7'v>]K7K7{&K��E �T23�@>�%71��-{�xvK7E*���Fp&K7{vt?K�E���ps%��nx('v%7=�%�A��3�3{DxFK���=:��{�L�{�x(�?ab{&J48`x(r<K�_�_�=:8ut?K]xv8`%���xv%f{�xvK7��8:=`8:�-K�x(8:%7�%�Ad{(=`�31 -3%]JI�<2,����xv�?'v�3K]xv8`%��3K�=��@L@a/_�%�{(8:��a %7Ad.0E�z]K��t��-E�ps%��nx('v%7=*%7AYpsr3�?af8:t-K�=��d'v%@t?�-{v{��6{�e�.0E3tFr��?a/×D��7��¶�o���I%���1b¬�%7��1�T+7+�×F+? f�nK��*2d����� 2

� U+0IÜ�¤ ��Ü�R�U�PI¤�Ü�¥ � £ V�U+0IWYPIUqÞ0¤3V(XsU@Ü�O ÞQS�Þ�Ü�¤ �Z �T2��@>7%�17�6{DxFK7EG�*�v�4%7�3�3{Dx&t�%7�nxv'(%�=3%�A*E�8u{�x(8:=`=uK]xv8`%���t�%�=`��af�3{v����psr��?af8ut?K7=cd�3178:���?�-'(8:��1�^Q�?_3K7'�xv�?af�?�nxvK7=��@�-af8`�3K7'-�yI�38`z��?'F{�8`xDL�%�A�¡�K�'vL@=:K7�3EG�37¶��������b+657\n[�2

Z �T24�@>7%�17�6{DxFK7EG�f�(�I%7���3{�xwt?%7�nx('v%7=0%�A9E�8u{Dxv8`=:=uK]x(8:%7� t�%7=:��af�3{v���0�@�-af8`�3K7' K�xw^Q�3��%7�nx cdØ@_��?'v8:a/�-�nxvK�=��nxvK�x(8:%7�*�ÓÔ8:=`af8:��1�xv%7�*�3^Q�?=uKMJ,K�'v��� /�������b+657\n[�2

Z �T2d�@>�%717�6{DxFK7EG���v�4%7�3�3{Dxft�%���xv'(%�=s%7AQE�8u{Dxv8`=:=uK]x(8:%7�"t�%�=`��af�3{v���&�@�?af8:�3K�'fK]x��@r��-=`=4'v�-{(�-K7'vtFr§ps�-��xv�?'6�d�I%��3{Dxv%7�*�~���Ø�K7{-�37���7�3���b+-5�\n[@2

Z �T2��@>�%71��-{�xvK7E*�4�(�4%����3{�x�t?%7�nx('v%7=�%7A,E�8u{�x(8:=`=uK]xv8`%���t?%7=:��af�3{(�3���@�-a/8:�3K7'�K]x�yI��8:z7�-'v{(8`xDL}%�A4�d8u{(K3�G�ËxvK�=:L7��7 �7�3=`L+-5�\n[�2

Z �T2��@>7%�17�6{DxFK7EG�}�v�d'v%�{(�-{v{���x(A�%7'vaf8`��1n�����d'v�-{(�?�nxFK]x(8:%7� K�xáÏ ® °F¨?¹7º?m ² l ² � ����� � Ïf³]l3i ² °�© ² °�hjlnmͺ]iÆlTº]© ® °�m�º]¨F¨F�H0~4HQy��3~�'v%7�3E�r3�?8:aw��7Õ/��K7�*24+-5�\7\��TeD+�+�_3K�1��-{�� [9_3K717�6{4.I_�_��?�3E�8|Ø �3KMz]K�8:=uK���=:� A�'(%�a HI�D;&�(! {(=`%@o�2

Z �T2��@>7%�17�6{DxFK7EG���(~,r�� �T×�af��xvr�%�E���K7�3E��Fps%��nx('v%7=�%7A�E�8:{�x(8:=:=:K�x(8:%7��t?%7=:��af�3{(�3�����@z@8`x(�-E�=`�6t�x(�3'(�6{sK�x *�3�3E�yI�38`z��?'(×{(8|xDL��3�@Js�6E��?���3�7Õ�×Ë�@[�.I_3'�+-5�\7\

Z �T2��@>�%71��-{�xvK7E*�s�v�4%7���{Dx�t�%���xv'(%�=�%7A&E�8u{�x(8:=`=uK]xv8`%���t�%�=`�3a/�{(�3���@�?af8:�3K�'�K]x &.I��%}yI��8:z7�-'v{(8`xDL7�G;�8`��=uK��EG���7\w^Q�-t�2+-5�\7\32

Z �T2��>7%71��-{�xvK�EG����ÓÔr@L�K��E�r�%]J x(%b_��3��=`8u{(r3����cY��17�-=:{(>n×�>@��'F{?��HQ~4H0y��T[@2d�������f+-5�\75

Z �T23�@>�%71��-{�xvK7E*���v^Q$s�t�%���xv'(%�=:��K��3E��(yQ{���%�A�{��6t�%��3E�K�'vLbaf�-K�{���'v�?af�-��xF{&8`�<E�8u{Dxv8`=:=:K�x(8:%7�3�3��^0�-_3K�'(x(af�-��xFK�=G{(�?af8|�3K7'-� ��?r�8:17r<yI��8:z7�-'v{(8`xDL7�G+-5f�������f+-5�\75

Z �T24�@>7%�17�6{DxFK7EG�f�(^Q�-{�x(8:=:=:K�{�BD%��Æ×/cd�Ô8:�nx(�-'(�6{({vK��nx K7�nz��?�3E��?=u{���KMz§a9��=`x(8:z]K�'v8:K7��=`��'(�-17��=:�?'v8`�31����4;3%7'v�-E�'FK�1áz7�6Eg ² °�i]³ À�� © ² © � ��� ����H0~4HQy���7Õ�2�! t�xv%7���?'�+-5�\75

Z �T2���>7%71��-{�xvK�EG�G�(cs{Dxv8`abK]xv8`%��9%7A�_�'v%�t��6{({�%7��x(_���xF{�A�'v%7a�a���=|xv8`_3=`�I{(�-t?%7�3E�K7'(L�af�6K7{(��'(�-af�?�nxv{v���]Ó�%7'v>�{�r�%�_��d³�l �©�°(³]ª7Â�³�°&µ�°(³"�d©��3yI�38`z��?'F{�8`xDLb%�A�HI�-J&t-K7{�x(=:�7��¶7�32�HI%]z7�-a9���?'�+-5�\75

Z �T2Q��>7%71��-{�xvK�EG���v;�'v� �n���?�t�Ln×ËE��?_��?�3E��-�nx}�4à�. K7�3K�=:L�{�8u{(�3� àsBD�6{Dxv��A�%7'v�?=:�-{(��8:��1Æz7�6E csc ^Q�?_*2:��p&K�=`x(�6tFr*�f+6�2¡�K7'vtFr�+-575��

Z �T2��@>�%717�6{DxFK7EG���v�nxFK]xv8:{(>7�I%�1�E�L@�3K7af8:{(>7�Iaf%�E��-=`=:�?'sx(8:=T_�'(%n{��6{({(%]z7�-'(z &K7>n�38`��12*¡}L@>f>7%7�nxv'vK�r3K7'vE�a/%�E��-=`=:�?'v8:��1��3�;�%�'(�6E�'FK�19z��-E ½ Ï9gƼ ²?À º�¹7º?m � � hjª � � � Ð�� ²�À h�³ Àb² ©�°�hj�T��%7'F{�1�'(�3���*���¶�2�¡�K7'vtFr�+-5�57�

�+

Page 79: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Z �T2G�@>7%�17�6{DxFK7EG�d�v¡}��=`x(8:_�=:��{�x(�-K�E�Ln×Ë{�xvK�x(�6{48`��E�8:{�x(8:=:=:K�x(8:%7��t?%7=:��af�3{(�3��àsBD�6{Dxv��A�%7'v�?=:�-{(��8:��1�z��-E}^ ~4���T^0�-��abK�'v>��+-�32�¡�KML�+-5�57�

Z �T2��@>7%�17�-{�xvK�EG�0�vHI�-J ���{�8:17rnxv{9%7�q¡}%�E��-=|×�$,K7{(�-E�cY{�x(8:abK]x(8:%7�qK7�3E�ps%7�nxv'(%�=:�3��;�%�'(�6E�'FK�1<z7�6E�.I8:'��d'v%�E��3t�xv{-�.I=:=:�?�nx(%]J4�*��\fH0%]z�2d5���2

Z �T2Y�@>�%71��-{�xvK7E*���(^QLn�K�af8:t-{?�Ya9��=`x(8:_�=:�<{�x(�6K7E�Lq{�xvK�x(�6{bK��3E§t�%7�nxv'(%�=s%7A E�8u{Dxv8`=:=uK]x(8:%7�"t�%�=`��af�3{v���4psr��?a<2"cd��12^Q�?_3K7'�xva/�-�nxvK�=����?af8`�K�'6��yI��8:zT2�%�A�¡�K�'vL@=:K7�3EG��5bHI%]zT2�57�32

Z �T2���>7%71��-{�xvK�EG�I�v��K]xv{(z@8:{(�/_�'(%n{��6{({(�?'62 !Q_�x(8:abK�=:8:{(�?'v8:��13�*'v�?1���=:�?'v8`��1w%71<_�'v%�E���>�{�BD%7�3{(_�=uK���=:�?1�178:��1�×Qa/�?x(%�E��-'v�3�;�%�'(�6E�'FK�19z��-E<¬���'F{(E3K�17�-���Q53+7��HQ~4H0y�����K7�*2,+-5�5�+

Z �T2Y�@>�%71��-{�xvK7E*���(^QLn�K�af8:t-{?�Ya9��=`x(8:_�=:�<{�x(�6K7E�Lq{�xvK�x(�6{bK��3E§t�%7�nxv'(%�=s%7A E�8u{Dxv8`=:=uK]x(8:%7�"t�%�=`��af�3{v���4psr��?a<2"cd��12^Q�?_3K7'�xva/�-�nxvK�=����?af8`�K�'6��yI��8:zT2�%�A�ÓÔ8:{vt�%��3{�8:�*�G+M��2�;��-�*2Y5�+�2

Z �T2��@>�%717�6{DxFK7EG���(�I%7���3{�x0ps%7�nx('v%7=u����àsBD�-{�x(�?A�%7'v�?=:�-{(��8`�319z7�6E �@8:z@8`=:8:��17�-��8 �7',��xvE�K7�����-=:{(�?� 8T~��?=:�?abK7'(>�e��@8:~Io��37�2.I_3'-2d53+

Z �v��L@{�x(�-af�?'�af�-E�>7%�a/_3=`�->@{�E�Ln�K�af8`>@>}×0E��-{�x(8:=`=uK7{�BD%7�á{�%�a#��x��-��>7�-=|x��->@{(�?af_��?=u����;3%7'v�-E�'FK�1<H0~,Ã�.���~�'v%7�3E�×r��-8`a<�� 32�.I_�'62 5�+72

Z �T2Y�@>�%71��-{�xvK7E*���(^QLn�K�af8:t-{?�Ya9��=`x(8:_�=:�<{�x(�6K7E�Lq{�xvK�x(�6{bK��3E§t�%7�nxv'(%�=s%7A E�8u{Dxv8`=:=uK]x(8:%7�"t�%�=`��af�3{v���4psr��?a<2"cd��12^Q�?_3K7'�xva/�-�nxvK�=����?af8`�K�'6��.I�����3'(�}yI�38`z��?'F{�8`xDL7�3� 32��7�3���724+6575�+�2

Z �T2Y�@>�%71��-{�xvK7E*���(^QLn�K�af8:t-{?�Ya9��=`x(8:_�=:�<{�x(�6K7E�Lq{�xvK�x(�6{bK��3E§t�%7�nxv'(%�=s%7A E�8u{Dxv8`=:=uK]x(8:%7�"t�%�=`��af�3{v���4psr��?a<2"cd��12^Q�?_3K7'�xva/�-�nxvK�=����?af8`�K�'6�3à �?%7'v178uK/~��6tFr*�37��2���������24+-5�5�+72

Z �T2Y�@>�%71��-{�xvK7E*���(^QL@�3K�af8ut?{-�Ya9�3=|xv8`_�=:�}{Dxv�-K�E�L�{�xvK]xv�-{fK��E§t?%7�nx('v%7=,%�A�E�8u{Dxv8`=:=:K�x(8:%7�Æt�%�=`��af�3{v��K��3E �Fps%���xv'(%�=%�AI�0�-K]x/c�Ø�tFr3K��317�?'�H0��xDJ&%7'v>@{v�����@�?af8:�3K�'F{�1�8`z��?��K]xfps�-�nx('v�bA�%7'9�Y'(%�t?�-{v{��@L�{Dxv�?ab{9cY��178:���?�-'(8:��1����af_�-'(8uK�=ps%7=:=:�?17����*%7�E�%7�*��+6�M×F+-Õ32�����=:L724+-5�5�+�2

Z �T2Y�@>�%71��-{�xvK7E*2 �F�@r�%7'(x�ps%7��'F{��w%7�Æ^Q8:{�x(8:=`=uK]xv8`%��Ô^0L@�3K7a/8ut?{bK7�3EÔps%7�nx('v%7=u��K7�3E ��ps%7�nx('v%7=:=uK���8:=`8`xDLq.I�K�=:L@{(8u{�3{(8`�31�;�'v� �n���?�t�Ln×Ë^Q�?_��?�E��?�nx0¡}�6K7{(��'(�6{&A�%7'I^Q8:{�x(�3'(�3K7�3t��6{IK��E ���nxv�?'FK7t�xv8`%��3{v����*�6t�x(�3'(�6{IK]x ½ ³]°(¹�hu¨�Ð/Î ² ¨�©�hjª �ª`º�©�h�³�l�¨�° ² m ® ª ² °�hjl@m ­ ³]°F¨(Ð�l3hjlnm �}³]°(Ð]¨(±�³vµT�~�'(%��3E�r��-8`a<��.0��1324+6575�+�2

Z �T2T�@>7%�17�-{�xvK�EG�Ç�v¡}%�E��?=:=`8:��1�K7�3E}^QLn�K�af8:t/�@8:a9��=uK]xv8`%��<A�%7'Q�Y'(%�t?�-{v{0ps%7�nx('v%7=u���*� *�6t�xv��'(��K��3E<=:�-t�x(��'v����%7x(�-{A�%7'I{(�?af8:�3K�'4%�� � ³6¹ ² ªjª«hjlnm}º�l�¹ Ê µT©�h À h��6º]©�h�³]l�³D ��± ²?À h�¿vº�ªGÄ,°(³-¿ ² ¨F¨ ² ¨D���3HQ~4H0y9�3~�'v%7�E�r��?8:a<�3.I�31324+-5�5�+�2

Z �T2Y�@>�%71��-{�xvK7E*�������3t?%7�3{(8u{Dxv�?�3t?L�8:�Æ=`%]J,×Ë%7'FE��-'9af%�E��?=u{f%�A 8`=:=|×�t�%��3E�8`x(8:%7���6Eq_�=uK��nxF���&���?af8`�K�'f178:z7�-�§K]x�^ ~4���^Q�?��abK�'v>T�G+-Õ32�¡�K�'FtFr�+6575��2

Z �T2��>7%71��-{�xvK�EG���(¬���'F{&8�E��-{�x(8:=:=:K�{�BD%��3{�'v�?1���=:�?'v8`��1n���@�nxvK�x(%78:=�¡}%���1�{�xvK�EG�T+-532�¡�K�'FtFr�+6575��2

Z �T23�@>�%71��-{�xvK7E*���v.I�3K7=`L�{(� KMzb'v�?1���=:�?'v�3K�'vr���xF����*�6t�x(�3'(��K]xIH0%7'F{�>�;3%7'v�?��8:��1/A�%7'4.I��x(%7abK�x(8u{��-'(8:��1}e�HQ;�.Qo4�@�-a�×8:�3K�'48*�7����xv�?1�'(�-'�x4�d'v%�{(�-{v{(E��-{(8`1��3���+! {�=:%3��Õ�×D[�2�.0_�'v8`=d+6575n�2

Z �T2���>7%71��-{�xvK�EG�*�Fps%��nx('v%7=:=:K7��8`=:8`xDL�%�AT8`�nx(�-17'FK]xv�-E�_�'(%�t?�-{v{�{�L�{�x(�?ab{�×*xvr��I'v�?=uK]xv8`%�������xDJ&�?�-�fE��-{(8`1��fK7�3Eft�%���xv'(%�=:�3�*�6t�xv��'(��K�x�g�±�³�°�©&¿F³ ® °F¨ ² ³]l}Ä&°(³6¿ ² ¨F¨9¹ ² ¨Fh|m7l�©Ë³6³]ªC¨9º�l�¹b© ² ¿v±�l3h �?®3² ¨��3~�'v%7�3E�r3�?8:aw�37�]×D�+ ¡�KML�+-5�5��2

Z �T2*�@>�%717�6{DxFK7EG�,�v.I�3K7=`L�{(8:{Q%�A&a9��=`x(8:z]K�'v8:K7��=`�/t�%���xv'(%�=�{(L�{Dxv�?ab{v��×4 w=`�6t�x(�3'(�6{Qr3�?=uE�K]x�H0%7'F{�>}�IL�E�'v%<�4�-{(�-K7'vtFrps�?�nxv'(���G+-¶]×D�+ �7�3=`L�+-575n�2

Z �T2@�@>7%�17�-{�xvK�EG�*��ps%7�nx('v%7=:=:K7��8:=`8`xDL9af�-K�{��3'(�6{�A�%7'sE�8:{�x(��'v�3K7�3t��I'v�DBD�6t�xv8`%��3��� *�-t�x(��'v�IK]x ��©�± ½ ³]°(¹�h�¿0Ä&°(³6¿ ² ¨F¨ �d³�l �©�°(³]ª �}³]°(Ð]¨(±�³Fµ���à ��x(�-�%�'(1�3�\/.I��124+-575n�2

Z �T2��@>�%71��-{�xvK7E*�4�Fps%7�nxv'(%�=�%7Asr��6K]x���Ø�tFr3K7��17�-'Q�3��xDJ&%7'v>@{v��� ��-t�x(��'v�bK]x�cYE�8:�@����'v17r�yI��8:z7�-'v{(8|xDL���5<�@�?_�x62}+-5�5�K��E K�x0y0¡}����~��¡�K��3tFr3�-{�x(�?'6�T+-�b�@�-_�x-2I+6575n�2

Z �T2���>7%71��-{�xvK�EG�G�Fps%���xv'(%�=`=uK��38`=:8|xDL�af�-K�{��3'(�6{�A�%7'dE�8u{Dxv��'v�3K��3t?�,'(��BD�-t�xv8`%��3��� *�-t�x(��'v�,r��?=uEfK]x *�-8:t?�-{�x(�-'dyI��8:z7�-'v{(8|xDL%7��+7+��@�-_�x-24+6575n�2

Z �T2��@>7%�17�6{DxFK7EG���Fps%��nx('v%7=:=:K7��8`=:8`xDL�K��K�=:L@{(8u{�A�%7'/���3{�xvK7��=:��_�=uK��nxv{v���d�@�-af8`�3K7'/K�x/^ ~4��� *L@��1��@L7�d^Q�?��abK�'v>T��5! t�x624+-5�5��2

7

Page 80: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Z �T2*�@>�%717�6{DxFK7EG�,��ps%7�nx('v%7=:=:K7��8:=`8`xDLwK�{({(�-{v{(a/�-�nx K7{�K�x(%@%7=�A�%�'�t?%7�nx('v%7=�{�x('v�3t�xv��'(�/{��-=`�6t�xv8`%��3��� ¦ l3i6hj© ² ¹wª ² ¿?© ® ° ² K�x¦ � ¾ �<³�°(ÐM¨(±�³Fµq³�l �d³]l©�°v³]ªG¨ Á ¨�© ²?À ¹ ² ¨�h|m7l�Â�³�°�º7¹�iMº�l�¿ ² ¹ ² lnm7hjl ²F² °�hjlnm�¨ Á ¨�© ²�À ¨ ����³ À µTª ² É7hj© Á � ® lT¿ ² °�©�º]hjl3© Á �hjl-Â�³�° À º�©�h�³�lƺ�l�¹�³]°�mnº]lh��6º]©�h�³]l3�����3{�x(8`x(��x(��A�%�'9¡�K�x(r��-afK�x(8ut?{�K7�3E��Ëxv{�.0_�_�=:8:t-K]xv8`%��3{?��¡}8:�����6K�_�%7=:8:{-�s+6¶ ! t�x-2+-5�5��2

Z �T2G�@>7%�17�6{DxFK7EG�&�(�4�-17��=:�?'v�3K7'(r��?x0KMz<_�'(%n{��6{({(�?'F���;�%7'v�-E�'vK71bz7�-E�Ï ® °F¨?¹�º?m ² l ²�½ ¼ ½<· � ���7�*¬���'v{-)f���Q>�%7��%�a/8u{(>17�-z@8`�3{�x4z7�6E K7��x(%�afK�x(8u{��-'(8:��1/%71bE�'v8|Ajx0KMz�_�'(%n{��6{({(�?'F���@~�'(%��3E�r��-8`a<�[6×�\�2��nK��*2,+65757¶32

Z �T2G�@>7%�17�6{DxFK7EG�s�Fps%7�nxv'(%�=`=uK���8:=:8|xDLw.I�3K7=`L�{(8:{v��� *�6t�x(�3'(�9K�x �&® °v³vµ ² º�l ­ ³�° ®�À Â�³]° �*¾QÄ � �0² ¨ ² º�°(¿F± �}³]°(Ð]¨(±�³Fµ��~�'(%��3E�r��-8`a<��5]×F+-�32��nK���24+-575�¶�2

Z �T2��@>7%�17�-{�xvK�EG�0�vc �T�-t�x�%�A4'(�6t�L�t�=:��K��Eá%�x(r3�?'9{(%7��'Ft��6{�%�A4_�%�{(8|xv8`z��fA��?�-E��3K7tF>�%7��x(r3��E�L@�3K�af8ut?{9%�AItFr��?af8ut?K7=_�'v%�t��-{v{(�-{v���d�@�?af8:�3K�'fK]x�ps�?�nxv'(��A�%7'f�d'v%@t?�-{v{��@L�{�x(�-af{fcY��178:���?�-'(8:��1����af_��?'v8:K7=4ps%�=`=:�?1��7� �%7�3E�%��*�4+-5��7�3=`L+-5�57¶32

Z �T2I�@>�%717�6{DxFK7EG� �(^QL@�3K�af8ut?{-�0a9�3=|xv8`_�=:��{Dxv�-K�E�LÇ{DxFK]xv�-{wK��3E t�%���xv'(%�=Q%7A�E�8u{Dxv8`=:=uK]x(8:%7� t�%�=`��af�3{v�����@�?af8:�3K�'}K�x~��-tFr���8u{(>7��yI��8:z7�-'v{(8`xvK]x4$&�?'v=`8:�*�n[�.0��1324+6575�¶�2

Z �T2T�@>7%�17�-{�xvK�EG�d�vc �T�-t�xv8`z��9t�%��nx('v%7=*%7A�E�8:{�x(8:=`=uK]xv8`%���t�%�=`��af�3{0�3{(8`��1�x(�?af_��?'FK]xv��'(�9a/�6K7{(��'v�?af�?�nxv{v��� *�-t�x(��'v�9K�x�@r��-=`=��4�-{(�-K7'vtFr}ps�?�nx(�-'�e�¬����.Qo��.Iab{Dxv�?'FE�K�a<�3¶f{(�?_�x624+-5�57¶�2

Z �T2]�@>7%�17�6{DxFK7EG��(�4�-17��=:�?'v�3K�'vr��?xv{vK��3K7=`L�{(��KMz _�'v%�{(�-{v{��-'T×��?x�af8uE�E��?=�A�%7'���6E�'v�Y_�'v%�{(�-{v{(E��-{(8`1��3���-���?'vz7%�×Ëa �]xv��x-ß 57¶3�HI%�'v{(>�;�%�'(�-��8:��1/A�%7'I.I��x(%7abK�x(8u{��-'(8:��13�

Z �T2��>7%71��-{�xvK�EG���Fps%7�nxv'(%�=`=uK���8:=:8|xDLbK��K�=:L@{(8u{(�3�@H0%7'FE�8ut �Y'(%�t?�-{v{4ps%��nx('v%7=TÓ�%�'(>�{(r�%7_�� *L@��17�@L�����K7�*2�5� 32

Z �T2��>7%71��-{�xvK�EG���(�d=uK��nxDJ48uE���t�%7�nxv'(%�=:�3�@H0%7'FE�8ut �Y'(%�t?�-{v{,ps%���xv'(%�=GÓ�%�'(>�{(r�%7_����L@��17�@L7���nK���2�57 32

Z �T2@�@>7%�17�-{�xvK�EG�G�(.Ô{(L�{Dxv�?ab{dK7_�_�'v%�K7tFr�x(%�E�8:{�x(8:=`=uK]xv8`%��b_�'v%@t?�-{v{��6{�×�~,r��4'v�?��8:'(x(rf%�A*K�'v�-{(�-K�'FtFr�K7'(�6K7�3��psr��?af8ut?K�=cd�3178:���?�-'(8:��1f^0�-_3K�'(x(af�?�nxFK�=*{(�?af8`�K�'F{?��y0��8`z��?'F{�8`xDLb%�AYp&K�=:8`A�%7'v��8:K/K]x0$&�-'(>��?=:�?L��nK��*2d�¶w+6575����yI�38`z��?'F{�8`xDL�%�Adp&K�=:8|A�%�'(�38:K/K]x0^ KMz@8:{4;3�?�*24+6¶ +6575n����K��3EyI�38`z��?'F{�8`xDL�%�Adp&K�=:8|A�%�'(�38:K/K]xQ��K7�nxvKf$,K�'v�3K�'FK9¡�KML 5 +6575n��2

Z �T2��@>7%�17�6{DxFK7EG�*�v. {(L�{Dxv�?ab{YK7_�_�'v%�K7tFr/xv%9E�8u{Dxv8`=:=:K�x(8:%7��_3'(%�t��6{({(�-{�×�~,r��0'(�-��8`'(x(r�%�A*K�'v�-{(�-K7'vtFrfK�'v�-K������@�-af8`�3K7'-�yI�38`z��?'F{�8`xDL�%�A�¡�K7{v{vK7tFr@�3{(��x�xF{,K]xI.Iafr��-'v{�x-�3¶3+�¡�K�'FtFr�+6575���2

Z �T2��@>7%�17�6{DxFK7EG�*��ps%7�nx('v%7=:=uK���8:=`8`xDL�K7�3K�=:L�{�8u{�%7A��@��� ! {(L@{�x(�-ab{(�3�n�@�-a/8:�3K7'-�@^0�-_3K�'(x(af�-��x&%�A*cd=:�-t�x('v8:t-K�=�cd��1�8`���-�?'(×8:��13��y0��8`z��?'F{�8`xDL�%7A�p&K�=:8`A�%7'v��8:KfK�x4$&�-'(>��?=:�?L7��.0_�'v8`=����*+-5�5���2

Z �T2��@>�%717�6{DxFK7EG���(. {(L@{�x(�-ab{sK7_�_�'v%�K7tFrfxv%/E�8:{�x(8:=`=uK]xv8`%���_�'v%�t��6{({(�-{d×�~,r3�Q'v�?��8:'(x(r�%7A�K�'v�-{(�-K7'vtFr�K7'(�6K�e�8`�3t?=`�E�8`�31%7�3'4Ö3'F{Dx0'v�-{(��=`xv{0%7�}a9�3=|xv8`z��-{v{��-=��3K�xvtFr�E�8u{Dxv8`=:=uK]x(8:%7��oD���GÄ&ª ² l�º�° Á ª ² ¿?© ® ° ² ��D;�.0p ��Lnaf_�%�{(8`�3aÌ^ ��p ! �I^ � 5�����I�-=:{(8:��17%�'-��^Q�?��abK�'v>T���7�3����\��G+6575���2

Z �T24�@>7%�17�6{DxFK7EG�b��ps%7�nx('v%7=:=:K7��8:=`8`xDL§K7�3K�=:L�{�8u{b%�A������ !�{�L�{�x(�-af{v��� �@�?af8:�3K�'6�I^0���%7�nxwcdØ@_��?'v8:a/�-�nxvK�=��nxvK�x(8:%7�*�ÓÔ8:=`af8:��1�xv%7�*�3^Q�?=uKMJ,K�'v�7��yQ��.9�3����=`Lw�\��G+6575n��2

Z �T2@�@>7%�17�-{�xvK�EG���v¡}��=`x(8:z7�6{({(�?=��K]xvtFr�E�8:{�x(8:=`=uK]xv8`%��3���@HI%�'vE�8:tI�Y'(%�t?�-{v{Yps%7�nx('v%7=�Ó�%7'v>�{�r3%7_*� &.I=uK��3EG�@.I�317�3{�xQ+6575���2Z �T2I�@>�%717�6{DxFK7EÔK7�3E ¬f2,�0KMz@'v�7����ps%7�nx('v%7= {Dxv'vK�x(�?1�L"{(�?=:�-t�x(8:%7� K��3EÔ_K�'(x(8uK�=�t�%7�nxv'(%�=:�3� *�6t�x(�3'(��K��3EÔ_�%�{�x(�-'-�cd�3'(%�_�6K��Ç� p&¡ af�?��xv8`�31§%�� tFr��?af8ut?K7=Q_�'v%�t��6{({ t�%7�nxv'(%�=��I��af_��?'v8:K7=�ps%�=`=:�?1��7� �%7�3E�%7�*��+- �×F+6�q���?_�xv�?a9���?'+-5�5���2

Z �T2��@>7%�17�6{DxFK7EbK��Eb�32@¡}%7'v�3EG���(.0�3K�=:L�{��QKMz/�{DxFK���8:=`8`x(�?xs8TK�afaf%7��8uK�>@>n×Ë'(�6K�>nx(%�'(�-'v�3�]���?'vz7%7a ��x(��xQ+-575n���n~�'v%7�3E�×r��-8`a<�3H0%]z�2,+6575���2

Z �T2��>7%71��-{�xvK�EG���Fps%7�nxv'(%�=T{�x('v�3t�x(��'v��E��-{(8`1��3��� &.0�%�.0>MK�E��?af8��3;�8`�3=:K7�3EG�*+M��;3�?�*24+6575�Õ�2Z �T2��>7%71��-{�xvK�EG����ps%7�nx('v%7=G{�x('v�3t�xv��'v��E��-{(8`1��3����Ó�%7'v>�{�r�%�_�%��wt?%7�nx('v%7=:=:K7��8:=`8`xDL�K��3K7=`L�{(8:{,K7�3E�_3=:K7��xDJ48uE���t�%��nx('v%7=��^ ~4y��3^Q�?��abK7'(>T�3�+�¡�KML�+-575�Õ�2

Z �T2*�@>�%717�6{DxFK7EG�&�v���?=:�-t�xv8`%���%7AdA��?�6E��3K7tF><z]K�'v8uK���=:�-{0A�%7' %7_�xv8`af8:�?8:��1<t�%7�nxv'(%�=�%7As����xv=`L@��>}t�%�=`�3a/�{(�3��Ó�%7'v>�{�r3%7_%7�<����xv=`L@��> E�8:{�x(8:=:=:K�x(8:%7�*�3HQ~4H0y9�3~�'v%7�E�r��?8:a<��5��@�?_�24+-575�Õ�2

�¶

Page 81: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Z �T2��@>�%717�6{DxFK7EG���(~���x(%�'(8uK�=8`�nxv'(%�E��3t�x(8:%7�bxv%�=:8:���-K7'saf%�E��?=�_�'v�-E�8ut�xv8`z��Qt?%7�nx('v%7=u���nHI%7'FE�8utI_�'v%�t��6{({&t�%���xv'(%�=3Ó�%7'v>n×{(r�%7_*��ÓáK7E3K�r�=��3HI%�'(J,KML7��+6/�nK���+-5�5n[@2

Z �T23�@>�%71��-{�xvK7E*���v¡}��=`x(8:zMK7'(8uK����?=T'v�?1���=`�-'(8:��1�%�1�%�_�x(8:abK�=:8:{(�?'v8:��1��3�nH0%7'F{�>�;3%7'v�?��8:��1�A�%�'4.I��xv%7abK]xv8:{(�?'v8`�31we�H0;�.Qo&.I'F{(a ��x(�6{��-a/8:�3K7'-�@Ã���x(x('v�7�*+][@2�K�_3'(8:=�+-5�5n[@2Z �T2��>7%71��-{�xvK�EG���(¡}%�E��-=*�3K�{��6E�xv����8:��1�%�A��d�D^ t�%7�nxv'(%�=`=:�?'F{(�3�nH0%7'F{�> �IL�E�'v%��4�-{(�-K7'vtFr}ps�?�nx(�-'-�3��%�'v{(17'v�������@�7 .I�31324+-5�5n[�2

Z �T2I�@>�%717�6{DxFK7EG������af_%�'�xFK��nx 8u{v{����6{�8:� _�'(%�t?�-{v{ {(L�{Dxv�?ab{��-��178:���-�?'v8`��1§�3{(8`��1ÆE�8u{Dxv8`=:=uK]x(8:%7� K7{wK�� ��Ø�K�af_�=:�-�3��@�-a/8:�3K7'-��.0'(8u{Dxv%�xv=`��yI�38`z��?'F{�8`xDL�%�A�~,r��6{({vK�=:%7��8:>@8���à 'v�?�6t��7�375b�@�?_*24+6575@[@2

Z �T2M�@>7%�17�-{�xvK�EG�3��ps%7�nx('v%7=:=uK���8:=`8`xDL0K7�3K�=:L�{�8u{*K��E�t�%7�nxv'(%�=7{Dxv'(�t�x(�3'(�dE��6{�8:17����]�@�?af8:�3K�'6�6^Q�?_K�'(x(af�?�nx�%7A�cY=`�6t�xv'(8ut?K7=cd�3178:���?�-'(8:��13��cY8`�3E�r�%]z7�-� ~��-tFr���8ut?K7=*yI��8:z7�-'v{(8`xDL7��HI�?x(r��-'(=uK��E�{?�G+�+�HI%]zT2,+-575@[@2

Z �T2Y�@>�%71��-{�xvK7E*�������nx('v%�E��3t�xv8`%��qxv%�t?%7�nx('v%7=:=:K7��8:=`8`xDL�K��3K7=`L�{(8:{v���d~�K�_��-E§=`�6t�xv��'(�<K]xb.I'v8:�?%7�K��nxFK]xv�<y0��8:z7�?'F{(8|xDL��~��?af_����+�H0%]z�2,+6575n[�2

Z �T2T�@>7%�17�-{�xvK�EG� ��ps%7�nx('v%7=:=uK���8:=`8`xDL�K7�3K�=:L�{�8u{IK��E<_�=:K7�nxDJ48:E���t�%7�nxv'(%�=:�<�G�@r�%�'�xFt�%7�3'v{(�be� �r3%7��'F{vo,K�x �0%7���-LnJ&�?=:=���dr3%n�-��8`ØT�3�+�HI%]zT2,+-575�\�2

Z �T2��>7%71��-{�xvK�EG�q�(�Y=:K7�nxDJ48:E���t�%��nx('v%7=u�������@z@8`x(�-E xFK�=:>�K]xI~���x(�-8`��1���Lnaf_�%�{(8`�3aw��à �?'vafK7�@L7�G+7+�¡�K7'vtFr�+-5�57\�2

Z �T2��@>7%�17�6{DxFK7EG����ps%7�nx('v%7=Y{�x('v�3t�x(��'v��E��6{�8:17�qK7�3E�_�=uK��nxDJ48uE�� t?%7�nx('v%7=�×�~,r��w{��6K�'FtFr�A�%�'�xvr�� {(�?=`Aj×�%�_�x(8:af8`�-8`�31t�%��nx('v%7=�{Dxv'(�t�x(�3'(�6�9�����nz@8`x(�6E9xFK�=:>9K]x4+65757\ �d'v%�t��6{({��@L�{�x(�?ab{�cY��178:���?�-'(8:��1��@�?af8:�3K�'Y���?'v8`�6{?����af_��?'v8:K7=ps%7=:=`�-17���*%��3E�%��*�37/¡�KML}+65757\32

Z �T2��>7%71��-{�xvK�EG���v�@�-=|Aj×Ë%7_�x(8:a/8:�?8:��1bt�%��nx('v%7=u���3�@�-a/8:�3K7'IK]x0.I��x(%7abK�x(8ut9ps%7�nx('v%7=*^Q�?_3K7'�xvaf�?�nx-��cY~4��� �T��'(8utFr*�*+M��������f+-5�57\�2

Z �T23�@>�%71��-{�xvK7E*���F�@�?=`Aj×Ë%7_�xv8`af8:�?8:��1/t?%7�nx('v%7=u�����@�-af8`�3K7'4K]xI^0�-_3K�'(x(af�-��x4%7A�psr��-a/8ut?K7=*cd��1�8`�3�?�?'v8:��13��^ ~4y�� *L@��×17�@L��G+-\f�7�3���f+-575�\�2

Z �T2G�@>7%�17�6{DxFK7EG�s�v�@�-=|Aj×Ë%7_�xv8`af8:�?8:��1 t?%7�nx('v%7=u���T�@�?af8:�3K�'�K]x�^0�-_3K�'(x(af�-��x %�AY.0��x(%�afK�x(8ut/ps%���xv'(%�=��T.0K7=`��%7'v1�y0��8|×z7�-'v{(8`xDL7�T+7+�;��-��'v�3K�'vL}+-5�575�2

Z �T2��@>7%�17�-{�xvK�EG�I�F�@�?=`Aj×�%�_�x(8:af8`�-8`�31�t�%7�nxv'(%�=:�3���d'v�-{(�?�nxvK�x(8:%7�áK]x/p&.Q�Yc�×"! �YcsH J&%7'v>�{�r3%7_*��~�%7�3=`%��3{����s+M�w�7���3�+-5�575�� ��r3K��3E�J4'(8`x�xv�?�wx('FK��3{(_3K7'vK7�3t�8:�-{���2

Z �T2��@>7%�17�6{DxFK7EG�Q�(�d=uK��nxDJ48uE���t?%7�nx('v%7=�)�~,r��w{��6K�'FtFr�A�%7'�xvr�� {(�?=`Aj×Ë%7_�xv8`af8:�?8:��1�t�%��nx('v%7=s{�x('v�3t�x(��'v�-�3���@�-af8`�3K7'�K�xyI�38`z��?'F{�8`xDL�%�A�.Iab{�x(�?'FE�K7aw���5/¡�K�'FtFr<7�7����2

Z �T2Y�@>�%71��-{�xvK7E*���(¡}�3=|xv8`z��-{v{��-=&�K]xvtFrÆE�8u{Dxv8`=:=uK]x(8:%7�§×9c�Ø�_��?'v8`af�-��xFK�=,z7�-'(8`Öt-K]x(8:%7����Y�@�-a/8:�3K7'�K]x�yI��8:z7�-'v{(8`xDL�%�AcY{v{(�?�*�G+- /�������b+65757532

Z �T2��@>7%�17�6{DxFK7EG�*��ps%7�nx('v%7=:=uK���8:=`8`xDL�K7�3K�=:L�{�8u{dK7�3Ef_�=uK��nxDJ48:E��Qt�%��nx('v%7=u���7~�K�=:>/K�xs{(r�%7'(x�×�t�%���'v{(�7��~�'v%7�3E�r��?8:a<�+�+�×F+6! t�x624+-5�575�2

Z �T2��>7%71��-{�xvK�EG�§�v�d=uK��nxDJ48uE�� t?%7�nx('v%7=�)d~,r���{(�-K7'vtFr�A�%7'4xvr���{��-=|Aj×Ë%7_�x(8:a/8:�?8:��1�t?%7�nx('v%7=G{�x('v�3t�xv��'(�6���G2,�@�?af8:�3K�'IK�xyI�38`zT2�%�A�.Iab{�x(�-'vE�K7a<��HI��xvr��?'v=uK��3E�{-�3�5f¡�K7'vtFr}����7�32

Z �T2��>7%71��-{�xvK�EG�§�v�d=uK��nxDJ48uE�� t?%7�nx('v%7=�)d~,r���{(�-K7'vtFr�A�%7'4xvr���{��-=|Aj×Ë%7_�x(8:a/8:�?8:��1�t?%7�nx('v%7=G{�x('v�3t�xv��'(�6���G2,�@�?af8:�3K�'IK�x^Q%]JÍps%32:��~��?'v���?���-�?�*�HI��xvr��?'v=uK��3E�{-��¶7�f¡�K7'vtFr<����7��2

Z �T2��@>7%�17�-{�xvK�EG�I�v;��?�6E��3K�tF>�)�~,r��bA�%7'v17%7x�xv%7��x('v8:tF>��3��ps%7�nxv'(%�=�17'v%7��_�{(�?af8`�K�'6��~�2 y�2�^0�-=|Ajx6��H0��xvr��?'v=:K7�3E�{-�s+�+^Q�-t�2Y7�7����2

Z �T23�@>�%71��-{�xvK7E*���v�d=uK��nxDJ48:E��0_�'v%�t��-{v{,t�%���xv'(%�=:�3��!Q�3��×�E�KMLb=`�6t�xv��'(��{(�?'v8`�6{s1�8`z��?��A�%7'&x(r���~�K�8:J&K7���-{(���s��cÆà '(%���_K]xIHQK]x(8:%7�K�=*~�K�8:J&K7�wy0��8`z��?'F{�8`xDL�%7A���t?8`�-�3t���K7�3E ~��-tFr3��%7=:%71�L�e�H0~4y ��~Io���~�K78`_��?8��3~�K�8:J&K7�*�T+6/¡�K7'vtFr<��7�3+72

Z �T2*�@>�%717�6{DxFK7EG�&�(;3�?�6E��3K7tF>T)0~,r3�9A�%�'(1�%�x�xv%7�}xv'(8utF>����*�@�-a/8:�3K7' K�x �D~4�4��e����3EG2�~��6tFr*2��4�-{-2����3{�x-2Co����Q{�8:�ápsr@�*�~�K�8:J&K7�*�T+-¶f¡�K�'FtFr}��7�3+72

Z �T2I�@>�%717�6{DxFK7EG���(;��-�-E��K7tF>T)q~,r���A�%7'v17%�x(x(%��Ôx('v8:tF>��3�Q�@�?af8:�3K�'<K]x}.0$,$�ps%�'(_�%7'FK]xv��'(�6{��6K�'FtFr*�0$&8:=`=:8`�31�{�xvK7E*�HI%�'(J,KML7��¶���¡�K7'vtFr}�����+�2

]

Page 82: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Z �T2��@>7%�17�6{DxFK7EG���v;�=:%]JI{(r��?�?x�t�%���xv'(%�=`=uK��38`=:8|xDL�K7{v{��6{({(af�?�nx�xv%n%�=:{v��� ��-t�xv��'v� K]x/cd��'v�-t-K 37p&K�tFr��fÓ�%�'(>�{(r�%7_�%�����nx(�-17'FK]x(8:%7� %�A�E��-{(8:17�<K��3Ewt�%���xv'(%�=��T�3^ ~4y�� *L@��1��nL���^0�-��abK�'v>���7���3��7�7�3+72

Z �T2��@>�%71��-{�xvK7E*�&�v;��-�-E��3K�tF>T)Q~,r��/A�%7'v17%7x�xv%7�}xv'(8utF>������@�-a/8:�3K7'�K�x�yI��8:z7�-'v{(8|xDL<%7A4p&K�=:8`A�%7'v��8:K3� *%n{ .0��17�-=`�6{?��7�HI%]zT2d�����+�2

Z �T2G�@>7%�17�6{DxFK7EG� �(;3�?�-E��3K7tF>T)4~,r���A�%�'(1�%�x(x(%7�<xv'(8utF>������G^0�-_�x-2�{��-af8`�3K7' K�x y0��8`z��?'F{�8`xDLw%�A&ps%7=:%7'FK7E�%3�$&%���=:E��?'6�+6/;3�?�*2Y7�7���2

Z �T23�@>�%71��-{�xvK7E*���v;��-�-E��3K�tF>T)�~,r3�QA�%�'(1�%�x(x(%7��x('v8:tF>��3�@^Q�?_�x-2Y{(�?af8:�3K�'4K]xIy0��8`z��?'F{�8`xDLb%�A�~����K7{-��.I�3{�x(8:�*�*+- f;3�?�*2������2

Z �@8:17��'FE���>7%71��-{�xvK�EG���v�d=uK��nxDJ48:E��st�%��nx('v%7=�)�~�%]J,K�'FE�{�KQ{(L�{Dxv�?abK]xv8:ts_�'v%@t?�-E��3'(�6���7�Y=`�-�3K�'vL�=`�6t�xv��'(�,K]x�cd�3'(%�_�6K���@L@af_%n{�8:��a %7�wps%�af_���x(�-'s.08:E��6E��d'v%�t��6{({�cY��178:���?�-'(8:��1b+M���E��?���QK7K�1��H0��x(r3�?'v=:K7�3E�{-�n�Õ�×�75�¡�KMLf7�7�n��7K7�3EK�=u{(%�_�'v�-{(�?�nxv�-EwK]x0�Y�4!���~ .I���@�3K7=�¡}�?�?x(8:��13�~�'v%7�3E�r��?8:a<�G+7+��7�3������7�n�2

Z �T27�@>�%71��-{�xvK7E*� �v;��?�6E��3K�tF>�t�%7�nxv'(%�=�xvr��?%�'(LT)�.0�f%]z7�?'vz@8`�-JqK��3E/t�%������6t�x(8:%7�{�xv%���8`%�tFr��-af8:t-K�=�{(L@{�x(�-ab{�xvr��?%�'(L��3������@z@8`x(�-E�=:�-t�xv��'v�fK�x�Ã0�(�Ëx(rá���nx(�?'v�3K�x(8:%7�3K7=Y�@L@a/_�%�{(8:��a#%7��$&8:%@tFr3�?af8:t-K�=d�@L�{�x(�?ab{�~,r��-%7'vL�.Iz��?'vL7��H0%7'vJ&KML��+M[M×�7�9�������97�7��

Z ~,r�����K717���Y�3tF>@=`�?xfps%7=:=`%��n��8uK<8`��_�'(%�t?�-{v{�E�L@�3K�af8ut?{�K��3E�t?%7�nx('v%7=���^Q�3��%���x6��ÓÔ8:=:a/8:��17x(%7���d�7\}HI%]zT2�7�7�����7�Y=:K7�nxDJ48:E���t�%��nx('v%7=�)�ÓÔrK]xI{�r3%7��=uEwJs��t�%��nx('v%7= ,-�

Z �s��c�×�{��-a/8:�3K7'QK]x9ps'FK���Ö3�-=:E�yI��8:z7�-'v{(8|xDL��G��+/���?_*297�7�7¶3����. =:%]J,×�E�8`af�-�3{�8:%7�K�=�af%�E��-=�%7As{(�?z7�-'(�/{�=:��1�178:��1�A�%�'t�%��nx('v%7=GE��-{(8:17�<K��3E<K��K�=:L@{(8u{(�

Z �@�-'(z�%7a/x(�?x-�3�¶32�%7>nx-2d����7¶3�@~�'v�?�3E�{,8:�<_�'v%@t?�-{v{4t�%���xv'(%�=

Z ������K7��7�7�� �*�@%7��xvrápsr�8:�3K<yI�38`z��?'F{�8`xDL<%�A&~��-tFr3��%7=:%71�L7�Gà �3K���1��?r�%��*��psr�8:�3K��*��;��-�-E��3K�tF>T)Q.I_3_�=`8ut?K�x(8:%7�3{Qxv%{(�?=`Aj×�%�_�x(8:af8`�-8`��1bt?%7�nx('v%7=GK��Ew{�xvK7��8:=`8:�-K�x(8:%7�w%�A�{(=:��171�8`��1n�

Z �[�.I_3'(8:=s����� �G�DcYcYc .0E�z]K7�3t��6E��Y'(%�t?�-{v{�ps%��nx('v%7=�Ó�%�'(>�{(r�%7_��GÃdK��3t?%7��z��?'6��p&K��3K�E�K�2f¶wr�%7��'F{�_�=:�?�3K7'(L}%���nps%��nx('v%7=G{Dxv'(�t�x(�3'(��E��6{�8:17�3�32

Z �5f.0_�'(8:=�7�7�� �ny0��8:z7�?'F{(8|xDL�%7A�.0=`���?'(xvK3�3cYE�a/%��nx(%7���p&K��3K�E�K�2�^Q�?_3K7'�xva/�-�nxI%�A�psr3�?af8:t-K�=�cY��178:���-�?'v8`��1b�@�-a�×8:�3K�'6���7;3�?�-E��3K7tF>�t?%7�nx('v%7=�)�~,r���{�8:af_�=`��K7�3Ew��6{Dx0{(%7=:��xv8`%��3��2

7�

Page 83: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV – B.A.Foss

May 2004 1 of 2

CV - Professor Bjarne A. Foss Name: Bjarne Anton Foss Date and place of birth: July 31, 1957 in Tønsberg, Norway Nationality: Norwegian Present position: Department head and Professor of systems and optimization

theory, The Department of Engineering Cybernetics, The Norwegian University of Science and Technology

Email and telephone: [email protected]/+47-73594376

Education: 1980: Diploma engineer (siv.ing.) in Electrical engineering, The Norwegian Institute of Technology. 1987: Dr.ing. in Engineering Cybernetics, The Norwegian Institute of Technology. Work experience: 1980 Research assistant at The Norwegian Institute of Technology. 1981-82: Military Service at Gråkallen Air Force Radar Station. Work task: System

Programming 1982-85: Research Scientist at SINTEF Automatic Control (non-profit research

organization) 1985-87: Graduate student (doctorate degree), partly on leave from SINTEF 1988-90: Head of System Control Group at SINTEF Automatic Control 1989 : Full professor at The Norwegian Institute of Technology (later The Norwegian

University of Science and Technology) 1995-96: Visiting professor at The University of Texas at Austin 1999-2001: Department head 2002- : Member of the University Senate at NTNU 2003- : Co-leader of Gas Technology Center NTNU-SINTEF Other positions and activities: 1989- : Scientific advisor for SINTEF (www.sintef.no) 1997- : Scientific advisor for Elkem ASA (producer of light metal - www.elkem.com) 1998- : Co-founder and board member of Cyberlab.Org AS

(internet-based company for remote experimentation - www.cyberlab.org) 1999- : Co-founder and board member of Cybernetica AS

(company for application of advanced control - www.cybernetica.no) 2000-02: Co-founder and board member of FIRST Scandinavia

(non-profit organization to inspire children's interest in science and technology - www.hjernekraft.org)

2001-03: Board member of SINTEF Electronics and Cybernetics Publications: (for details see: www.itk.ntnu.no/ansatte/Foss_Bjarne) More than 100 refereed journal papers, conference publications and book-chapters. Co-author of one book. Guest editor Int.J.Control. A large number of restricted technical reports and international guest lectures. Research projects: Supervised 14 completed dr.ing. degrees. Lead several national industry development projects.

Page 84: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

CV – B.A.Foss

May 2004 2 of 2

Co-lead in two international development projects (for ESA and EU). Professional activities: Member The Norwegian Academy of Technical Sciences (1993), Senior Member IEEE (1997), Member IFAC Technical Committee on Chemical Process Control (1996), Associate editor, Journal of Process Control (1996), Member editorial board - Mathematical Modelling (1996), Co-chair and member several IPCs (International Program Comittees), Review of a large number of scientific papers, Organized two international workshops. Awards: 1980: Innstilling awarded for the siv.ing. degree (ie., the result was communicated to the Norwegian King). 1995: The Karl Diesel Best Paper Award from Society of Design & Process Science. (www.sdpsnet.org)

Page 85: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

Publication list – Professor Bjarne A. Foss

1994-2004

Book J. G. Balchen, T. Andresen and B. A. Foss. Control Engineering (in Norwegian). Tapir forlag, 1999.

International Journals and book chapters 1. T. A. Johansen and B. A. Foss. Identification of non-linear system structure

and parameters using regime decomposition. Automatica, 31:321--326, 1995. Also in Preprints 10th IFAC Symposium on Identification and System Parameter Estimation, Copenhagen (SYSID '94), Vol.1 ,pp.131-7.

2. B. A. Foss, T. A. Johansen, and Aa. V. Sørensen. Nonlinear predictive control using local models - applied to a batch process. Control Engineering Practice, 3:389--396, 1995.

3. B.A. Foss and S.O. Wasbø. Benchmark IFAC 93: Adaptive predictive PI-control of an unknown plant. Automatica, 30(4), 1994.

4. K.Uhlen, B.A.Foss, and O.B.Gjøsæter. Robust control and analysis of a wind-diesel hybrid power plant. IEEE Trans. on Energy Conversion, 9(4), 1994.

5. T.A. Johansen and B.A. Foss. Advances in Neural Networks for Control Systems, chapter Semi-Empirical Modeling of Non-Linear Dynamic Systems through Identification of Operating Regimes and Local Models Springer Verlag, 1995.

6. B. A. Foss and T. A. Johansen. Neural Networks for Chemical Engineers, chapter Local modelling as a tool for semi-empirical or semi-mechanistic process modeling. Elsevier, Amsterdam, 1995.

7. F.A. Michelsen and B.A. Foss. A comprehensive mechanistic model of the continuous kamyr digester. Applied Mathematical Modelling, 20:523--533, 1996.

8. F.A. Michelsen and B.A. Foss. A dynamic model of the interaction between the chemical reactions and the residence time in the continuous kamyr digester. Tappi Journal, 79:170--176, 1996.

9. B. A. Foss and S. J. Qin. Interpolating optimizing control. J. of Process Control, 7(2):129--138, 1997.

10. T. A. Johansen and B. A. Foss. Operating regime based process modelling and identification Computers and Chemical Engineering, 21:159--176, 1997.

11. O.B.Gjøsæter and B.A.Foss. On the use of diagonal control vs. decoupling for ill-conditioned plants. Automatica, 33(3), 1997.

Page 86: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

12. A. Mjaavatten and B. A. Foss. A modular system for estimation and diagnosis Computers and Chemical Engineering, 21:1203--18, 1997.

13. S.O.Wasbø and B. A. Foss. Modelling unit processes using formal language description and object orientation. Mathematical Modelling, 4: 185--206, 1998.

14. T. Drengstig and D. Ljungquist and B.A. Foss. On AlF3 and temperature control of an aluminum electrolysis cell. IEEE Trans. on Control System Techn., 6:157--171, 1998.

15. B.A.Foss, B. Lohmann and W. Marquardt. A Field Study of the Industrial Modeling. J. of Process Control, 8(6):325--338, 1998. Also in Modeling, Identification, and Control, 19(3):153-174, 1998.

16. T. A. Johansen and B.A.Foss, ORBIT - Operating Regime Based Modeling and Identification Toolkit , Control Engineering Practice, Vol. 6, pp. 1277-1286, 1998.

17. O. Slupphaug and B. A. Foss, Constrained quadratic Stabilization of Discrete-Time Uncertain Multi-Model Systems using Piecewise Affine State-Feedback. International Journal of Control, Vol.72, pp.686-701, 1999 and in Modeling, Identification, and Control, Vol.20, pp.137-164, 1999.

18. O. Slupphaug and B. A. Foss, Robust stabilization of discrete-time multi-model systems using piecewise affine state-feedback, Journal of Process Control, Vol.10, pp.269-274, 2000.

19. O. Slupphaug, L.Imsland and B. A. Foss, Uncertatinty Modeling and Robust Output Feedback Control of Nonlinear Discrete Systems: A Mathematical Programming Approach, Int. Journal of Robust and Nonlinear Control Vol.10, pp.1129-1152, 2000

20. J.Vada, O. Slupphaug, T.A.Johansen and B. A. Foss, Linear MPC with optimal prioritized infeasibility handling: Application, computational issues and stability, Automatica 37 (11), 2001.

21. B. A. Foss and S.O.Wasbø, An integration scheme for stiff solid-gas reactor models, Computer Methods in Applied Mechanics and Engineering, Vol.190/45, pp 6009-6021, 2001. Also in Modeling, Identification, and Control, 22(2):103-118, 2001.

22. L. Imsland, R. Findeisen, E. Bullinger, F. Allgöwer, B. A. Foss, A note on Stability, Robustness and Performance of Output Feedback Nonlinear Model Predictive Control. Journal of Process Control, Vol.13,pp.633-644, 2003.

23. R. Findeisen, L. Imsland, F. Allgöwer, B. A. Foss, Output feedback stabilization of constrained systems with nonlinear predictive control, Int. Journal of Robust and Nonlinear Control Vol.13, pp.211-227, 2003.

24. R. Findeisen, L. Imsland, F. Allgöwer, B. A. Foss, Towards a sampled-data theory for nonlinear model predictive control, In W. Kang, C. Borges, and M. Xiao, editors, New Trends in Nonlinear Dynamics and Control, and their Applications, Lecture Notes in Control and Information Sciences, 295, pages 295-313, New York, 2003. Springer-Verlag.

25. R. Findeisen, L. Imsland, F. Allgöwer, B. A. Foss, State and Output Feedback Nonlinear Model Predictive Control: An Overview, Europ. J. Contr., Vol.9, 2003.

Page 87: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

26. F. Martinsen, L. Biegler, B.A. Foss, A new optimization algorithm with application to MPC, J. of Process Control (in press), 2004.

International Refereed Conference Papers 1. B.A. Foss and O. Øgård. On structural models for fault detection and isolation

in complex plants. In Proc. Process System Engineering (PSE '94), Korea, pages 1147--1151, 1994.

2. B.A. Foss, T.A. Johansen, and Å. Sørensen. Nonlinear predictive control using local models - applied to a batch process. In Preprints Advanced Control of Chemical Processes (ADCHEM '94), Japan, pages 225--230, 1994.

3. F.A. Michelsen and B.A. Foss. Modelling of a continuous digester for supervision and prediction. In Preprints Advanced Control of Chemical Processes (ADCHEM '94), Japan, pages 552--557, 1994.

4. B.A. Foss, R. Klev, M. Levin, and K. Lien. Integrated production systems for the process industries. In Proc. The First World Congress on Integrated Design and Process Technology, Austin, USA, pages 276--282, 1995.

5. T. A. Johansen and Bjarne A. Foss. Empirical modeling of a heat transfer process using local models and interpolation. In Proc. The 1995 American Control Conference, Seattle, Wa., 1995.

6. A. Mjaavatten, B.A. Foss, and K. Fjalestad. Operator support for diagnosis in a fertilizer plant. In Proc. ISPE'95, Colorado, USA, 1995.

7. S.O.Wasbø and B.A.Foss. An object-oriented method for process modelling. In Preprints DYCORD'95, Lyngby, Denmark, pages 117--122, 1995.

8. S.O.Wasbø and B.A.Foss. Object-oriented model of a ferromanganese furnace. In Proc. INFACON 7, Trondheim, Norway, pages 545--554, 1995.

9. G. Tangen and B.A. Foss. Decision support for planning upgrading of a hydro power plant. In Proc. IEEE International Conf. on Systems, Man and Cybernetics, Vancouver, Canada, volume 2, pages 1562--1567, 1995.

10. J. Simensen and B.A. Foss. A concept for modelling batch plant operation. In Preprints ESCAPE-6, Rhodes, Greece, 1996.

11. B.A.Foss and T.A.Johansen. Identification and convexity in optimizing control. In Proc. SYSID'97, Fukuoka, Japan, pages 691--6, 1997.

12. T.A.Johansen and B.A.Foss. ORBIT - Operating Regime Based Modeling and Identification Toolkit. In Proc. SYSID'97, Fukuoka, Japan, pages 961--7, 1997.

13. B.A.Foss, B.Lohmann and W.Marquardt. A Field Study of the Industrial Modeling Process. In Proc. ADCHEM'97, Banff, Canada, pages 581--7, 1997. Keynote lecture.

14. K. Støle Hansen and B.A.Foss. Controlling pH in a precipitation process. In Proc. ADCHEM'97, Banff, Canada, pages 249--54, 1997.

15. O.Slupphaug and B.A.Foss. Model predictive control for a class of hybrid systems. In Proc. European Control Conference, Brussels, 1997.

Page 88: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

16. O.Slupphaug and J.Vada and B.A.Foss. MPC in systems with continuous and discrete control inputs. In Proc. American Control Conference, Alberquerque, NM, 1997.

17. T.Drengstig, S.Wasbø and B.A.Foss. A formal graphical based process modeling methodology. In Proc. PSE/Escape7, Trondheim, Norway, pages 835--40, 1997.

18. S.J.Qin, V.M.Martinez, and B.A.Foss. An Interpolating Model Predictive Control Strategy with Application to a Waste Treatment Plant. In Proc. PSE/Escape7, Trondheim, Norway, pages 881--6, 1997.

19. S.O.Wasbø, B.A.Foss, and R.Tronstad. Object-oriented ferromanganese furnace model. In Proc. ADCHEM'97, Banff, Canada, pages 345--50, 1997.

20. O.Slupphaug and B.A.Foss. Bilinear Matrix Inequalities and Robust Stability of Nonlinear Multi-Model MPC. In Proc. American Control Conference, 1998.

21. O.Slupphaug and B.A.Foss, Robust Stabilization of Discrete-Time Multi-Model Systems using Piecewise Affine State-Feedback, In Preprints DYCOPS-5, Corfu, Greece, 1998.

22. J.Vada, O.Slupphaug and B.A.Foss, Infeasibility handling in linear MPC subject to prioritized constraints, In Preprints IFAC World Congress, Beijing , 1999.

23. B.A.Foss and S.B. Cong, Nonlinear MPC based on Multi-model for Distillation Columns, In Preprints IFAC World Congress, Beijing , 1999.

24. F.Martinsen, B.A.Foss and T.A:Johansen, A control relevant dynamic model of grate sinterering, In Proc. IEEE CCA Conference, Hawaii , 1999.

25. R.K.Pearson and B.A.Foss, Some Relations between Stability and Smoothness in Discrete-Time Dynamic Models, In Proc. American Control Conference, Chicago, pages 1385--1389, 2000.

26. B.A.Foss, Tor I. Eikaas and M. Hovd, Merging Physical Experiments back into the Learning Arena, In Proc. American Control Conference, Chicago , pages 2944--2948, 2000.

27. J. Vada, O. Slupphaug, T.A. Johansen and B.A.Foss, Stabilizing Linear MPC with Efficient Prioritized Infeasibility Handling, In Proc. ADCHEM'2000, Pisa, Italy , 2000.

28. O. Slupphaug and B.A.Foss, Multi-model based uncertatinty and robust control design (postscript-file), In ADCHEM'2000, Pisa, Italy, 2000.

29. D. diRuscio and B.A.Foss, On state space model based predictive control (postscript-file), In Preprints DYCOPS-5, Corfu, Greece, 1998, pp.304-9.

30. L. Imsland, R. Findeisen, E. Bullinger, F. Allgöwer and B. A. Foss: On output feedback nonlinear model predictive control using high gain observers for a class of systems. In Proc. DYCOPS-6 2001, Cheju Island, Korea, 2001.

31. L. Imsland, O. Slupphaug and B. A. Foss. Robust observer-based output feedback for nonlinear discrete-time systems with constraints. In Prepr. NOLCOS 2001 St. Petersburg, Russia, 2001.

32. L. Imsland, O. Slupphaug and B. A. Foss. Piecewise affine observer-based robust controllers for constrained nonlinear systems. In ECC 2001, Porto, Portugal, 2001.

Page 89: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

33. T.S.Schei, H.Ludvigsen, P. Singstad. Operator Support System for Optimization of Suspension PVC Batch Polymerization Reactors, In ECC 2001 (Industry Day), Porto, Portugal, 2001.

34. B.A. Foss, K. Malvig and T.I. Eikaas. Remote experimentation – new content in distance learning, In ICEE (Int. Conf. On Engn. Educ.) 2001, Oslo, Norway, 2001.

35. C. Schmid, T.I. Eikaas, B.A. Foss and D. Gillet. A Remote Laboratory Experimentation Network., In 1st IFAC conference on Telelematics Applications in Automation and Robotics, Weingarten, Germany, 2001

36. T.I. Eikaas, C. Schmid, B.A. Foss and D. Gillet. A Global Remote Laboratory Experimentation Network and the Experiment Service Provider Business Model, In e2002 Conference on eWork and eCommerce, Prague, 2002.

37. R.Findeisen, L. Imsland, F.Allgower and B. A. Foss. Output feedback nonlinear predictive control - a separation principle approach. In IFAC World Congress, Barcelona, 2002.

38. G.O.Eikrem, B. A. Foss, L.Imsland, B.Hu and M.Golan. Stabilization of gas-lifted wells. In IFAC World Congress, Barcelona, 2002.

39. F.Martinsen, L.Biegler and B. A. Foss. Application of optimization algorithms to nonlinear MPC. In IFAC World Congress, Barcelona, 2002.

40. B.A.Foss, H.Ludvigsen and S.O.Wasbø. Optimization-based control - Some critical issues. In MMAR'02, Szscecin, Poland, 2002.

41. L. Imsland, R.Findeisen, Allgower and B. A. Foss. Output feedback stabilization with nonlinear predictive control: Asymptotic properties. In ACC03, Denver, 2003.

42. R.Findeisen, L.Imsland, F.Allgower, B.A. Foss. Stability Conditions for Observer Based Output Feedback Stabilization with Nonlinear Model Predictive Control. In CDC’03, Hawaii, 2003.

43. S.Drageset, L.Imsland, and B. A. Foss. Efficient model predictive control with prediction dynamics. In ECC03, Cambridge,UK, 2003.

44. L.Imsland, B.A. Foss and G.O.Eikrem. State feedback control of a class of positive systems – Application to gaslift stabilization. In ECC03, Cambridge,UK, 2003.

45. R.Findeisen, L.Imsland, F.Allgower, B.A. Foss. Output-feedback nonlinear model predictive control using high-gain observers in original coordinates. In ECC03, Cambridge,UK, 2003.

46. B.F.Lund, B.A. Foss, K.R:Løvåsen and B.E.Ydstie. Sensitivity analysis of a dynamic model for submerged arc silicon furnaces. In INFACONX, Cape Town, South Africa, 2004.

47. L.Imsland and B.A. Foss. State feedback set stabilization for a class of positive systems. In IFAC POSTA, Rome, 2003.

48. L.Imsland and B.A. Foss. Set stabilization of a class of positive systems. In ADCHEM’2003, Hong Kong, 2004.

49. G.O.Eikrem, L.Imsland and B.A. Foss. Stabilization of gas-lifted wells based on state estimation. In ADCHEM’2003, Hong Kong, 2004.

Page 90: Curriculum Vitae EducationArjun Singh Model-based predictive control of heat exchangers for production of liquefied natural gas (LNG) Jan. 2004 Courses taught: Modelling of contiuous-time

50. G.S.Landsverk, T.Mejdell and B.A. Foss. Modelling and simulation og an unsaturated polyester process. In Polymer Reaction Engineering: Modelling, Optimisation and Control, Lyon, 2003.

51. B.F.Lund, B.A. Foss, K.R:Løvåsen and B.E.Ydstie. System analysis of complex reactor behavior – A case study. Accepted for DYCOPS-7, Boston, 2004.

52. L.Imsland, D.Snarheim, R.Ulfsnes, O.Bolland and B.A.Foss. Modelling and control of a O2/CO2 gas turbine cycle for CO2 capture. Accepted for DYCOPS-7, Boston, 2004.

53. L.Imsland, N.Bar and B.A.Foss. A new algorithm for efficient MPC and a comparison with other schemes. Accepted for ACC, Boston, 2004. .

54. O.M.Aamo, G.O.Eikrem, H.Siahaan and B.A.Foss. Observer design for gas lifted oil wells. Accepted for ACC, Boston, 2004.