ASPENTECH TRAINING SCHEDULE
Chennai:
Name of The Course Start Date End Date Place Cost
EHY101 Aspen HYSYS: Process Modeling 27-May-2013 29-May-2013 Chennai, India
INR 24600
X1011 Design and Rate Shell and Tube Heat Exchangers 11-Jun-2013 12-Jun-2013 Chennai, India
INR 16400
EHY2511 Flare Network Design and Rating 13-Jun-2013 14-Jun-2013 Chennai, India
INR 16400
EHX131 Heat Exchanger Mechanical Design using Aspen Shell & Tube Mechanical (Aspen Teams)
17-Jun-2013 17-Jun-2013 Chennai, India
INR 8200
EHY202 Aspen HYSYS: Advanced Process Modeling Topics 24-Oct-2013 25-Oct-2013 Chennai, India
INR 16400
EHY223 Aspen HYSYS Dynamics: Introduction to Dynamic Modeling 28-Oct-2013 30-Oct-2013 Chennai, India
INR 24600
Pune:
Name of The Course Start Date End Date Place Cost
EHY101 Aspen HYSYS: Process Modeling 21-Oct-2013 23-Oct-2013 Pune, India INR 24600
EHY202 Aspen HYSYS: Advanced Process Modeling Topics 24-Oct-2013 25-Oct-2013 Pune, India INR 16400
EHY223 Aspen HYSYS Dynamics: Introduction to Dynamic Modeling 28-Oct-2013 30-Oct-2013 Pune, India INR 24600
EHX1011 Design and Rate Shell and Tube Heat Exchangers 31-Oct-2013 01-Nov-2013 Pune, India INR 16400
EHY101 Aspen HYSYS: Process Modeling
Course Overview
Learn to build, navigate and optimize process simulations using Aspen HYSYS
Learn the efficient use of different HYSYS functions to build steady state process simulations
Course Benefits
Leverage the intuitive bi-directional solver and other key features of Aspen HYSYS that allow for rapid flowsheet construction
Use the Workbook and Process Flow Diagram (PFD) interfaces for quick and effective modeling
Discover how multi-flowsheet integration can streamline and organize simulation efforts
Explore different means of reporting results, including the use of Microsoft Excel VB macros
Evaluate the performance of existing equipment by leveraging the rating capabilities of Aspen HYSYS
Improve the convergence characteristics of columns and flowsheets; troubleshoot common problems
Perform Case studies to determine the optimum operating point for a process
Understand the pipeline hydraulics calculations used to assess the sizing requirements for a gas gathering system
Who Should Attend
New engineering graduates/technologists who will be using Aspen HYSYS in their daily work
Process engineers doing process design and optimization projects and studies
Plant engineers checking plant performance under different operating conditions
R&D engineers and researchers using Aspen HYSYS for process synthesis
Approach
Instruction on basic topics
Experienced instructor will select an appropriate order in which to present the modules
Discussion about the general approach and the key elements for successful simulations
Instructor-guided demonstrations of features
Hands-on workshops using examples from the petroleum processing industry
Detailed course notes
Prerequisites
A background in chemical engineering or industrial chemistry
Suggested Subsequent Courses
EHY121 Aspen HYSYS: Using Aspen Simulation Workbook
EHY202 Aspen HYSYS: Advanced Process Modeling Topics
EHY101 Aspen HYSYS: Process Modeling Course Agenda
Getting Started
Create and define a fluid package
Utilize the built-in expert system to choose an appropriate thermodynamic model
Select components, including hypotheticals
Install streams and attach stream utilities
Customize the Workbook
Workshop: Introduce basic concepts necessary for creating simulations in Aspen HYSYS®.
Propane Refrigeration Loop
Add and connect operations to construct a simple flowsheet
Use the graphic interface to manipulate flowsheet objects and provide a clearer representation of the process
Understand how process information is propagated both forwards-and backwards
Convert simulation cases to templates
Workshop: Build and analyze a propane refrigeration loop simulation
Refrigerated Gas Plant
Install and converge heat exchangers
Use logical operations: Adjust and Balance
Workshop: Model a simplified version of a refrigerated gas plant.
NGL Fractionation Train
Model distillation columns with the assistance of the Column Input Expert
Manipulate column specifications to better represent process constraints
Evaluate utility requirements using the Process Utility Manager
Workshop: Model a two column natural gas liquid (NGL) recovery plant
Oil Characterization and HP Separation
Introduce Oil Characterization in Aspen HYSYS
Use the Aspen HYSYS Spreadsheet and Case Study functionality
Workshop: Use the Oil Environment to characterize a crude assay and then employ the Case
Natural Gas Dehydration with TEG
Review the recommended methods to saturate single phase and two phase hydrocarbon streams
Discuss the implications of hydrate formation and the different means available to avoid hydrate problems
Model a typical TEG dehydration unit
Workshop: Model a typical TEG dehydration unit and determine water dew point for the dry gas; use the hydrate utility to investigate the effects of methanol injection on hydrate inhibition.
Rating Heat Exchangers
Review heat transfer calculation models in Aspen HYSYS
Configure a shell and tube heat exchanger to use a built-in Rating model
Integrate rigorous Exchanger Design and Rating (EDR) calculations into an Aspen HYSYS flowsheet
Workshop: Use a Rating model to determine if an existing heat exchanger will meet process specifications; design and rate a heat exchanger using the EDR interface inside Aspen HYSYS.
Troubleshooting / Best Practices
Introduce best practices for product integration and automation
Investigate reasons why a simulation may produce poor results, consistency errors, etc.
Identify appropriate thermodynamic models for common processes
Use suggested tips to debug simulations and columns
Workshop: Troubleshoot existing Aspen HYSYS cases; recognize common problem areas in an Aspen HYSYS case.
Reporting in Aspen HYSYS
Create a variety of customized reports using newly added functionality in the Report Manager
Access free Excel utilities designed to extract simulation data
Use Aspen Simulation Workbook to deploy models in Microsoft Excel
Workshop: Use the Report Manager, Excel
Study and Spreadsheet operation to determine how the Gas Oil Ratio (GOR) varies with pressure.
Gas Gathering System
Simulate a gas gathering system located on varied terrain using the steady state capabilities of Aspen HYSYS
Workshop: Use the pipe segment and the Hydraulics subflowsheet to model a piping network in Aspen HYSYS.
Two Stage Compression
Introduce the use of the recycle operation
Recognize suitable recycle locations
Implement performance curves for rotating equipment
Workshop: Utilize the recycle operation to build a two stage compression flowsheet; define and activate compressor curves.
utilities and Aspen Simulation Workbook to obtain custom reports.
Optional Topics Per Request
Optional Topic: Acid Gas Sweetening
Simulate amine towers; supply tray dimensions
Discuss efficiencies for amine towers
Use the Set operation and the Spreadsheet
Workshop: Simulate a typical acid gas treating facility.
Optional Topic: Liquid Natural Gas (LNG)
Use the LNG Exchanger operation to simulate multi-pass heat exchangers
Utilize the Sub-Flowsheet to build a modularized PFD
Model an LNG production process
Workshop: Simulate a typical LNG facility
Appendix A: What’s New in Aspen HYSYS
Review the latest features introduced in Aspen HYSYS V7.3.
Appendix B: Pro/II Converter
Describe the key features of the new Pro/II file converter
Demonstrate workflow and identify existing limitations of the file conversion tool
Workshop: Use the new Pro/II Converter to create an Aspen HYSYS simulation based on an existing keyword file.
Aspen Technology, Inc.® awards Continuing Education Units (CEUs) for training and development activities conducted by our organization in accordance with the definition established by the International Association of Continuing Education & Training (IACET). One CEU is granted for every 10 hours of class participation.
EHY202 Aspen HYSYS: Advanced Process Modeling Topics
Course Overview
Learn how to use and apply advanced modeling techniques to enhance existing Aspen HYSYS flowsheets
Course Benefits
This course is designed to show you how to:
Create custom column templates, including non-standard configurations
Perform complex calculations on flowsheet variables using the Spreadsheet
Realistically simulate separator carryover
Optimize process conditions to meet one or more process constraints
Integrate rigorous heat exchanger models into a standard flowsheet
Define reaction sets and utilize different types of reactors
Who Should Attend
Process engineers who need advanced skills for more complex modeling tasks
R&D engineers and researchers using Aspen HYSYS for process synthesis, upgrade or modifications
Approach
Instruction on basic topics
Discussion about the general approach and the key elements for successful simulations
Instructor-guided demonstrations of features
A full set of detailed course notes on all topics is provided
Prerequisites
Attend EHY101 Aspen HYSYS: Process Modeling training course or have equivalent modeling experience
Familiarity with Aspen HYSYS steady-state modeling concepts
Subsequent Courses
EHY221 Aspen HYSYS Dynamics: Dynamic Modeling
EHY261 Aspen HYSYS: Heat Exchangers for Process Engineers
EHY2102 Aspen HYSYS Petroleum Refining: Refinery Process Modeling and Optimization for Refinery Unit Operations
EHY202 Aspen HYSYS: Advanced Process Modeling Topics Course Agenda
Getting Started
Use core flowsheeting functionality to build a Turbo Expander plant flowsheet with a multi-pass exchanger and other key unit operations (heater, separator, column, set).
Workshop: Use the Aspen HYSYS LNG Exchanger to simulate multi-pass exchangers. Add Columns using the Input Expert. Customize the Workbook and PFD. Use stream property correlations.
Extending HYSYS Functionality
Demonstrate how automation can be used to increase the capabilities of Aspen HYSYS.
Workshop: Create a User Variable to report user defined quantities. Use Aspen Simulation Workbook to create a custom interface.
Advanced Columns
Simulate columns that do not adhere to the usual configurations.
Workshop: Customize a column with a sizable heat exchanger. Perform tray sizing and Rating calculations using the Tray Sizing utility.
Spreadsheets and Case Studies
Use a spreadsheet to calculate a simplified profit for the Turbo Expander plant.
Workshop: Import and export variables to and from the Spreadsheet; add complex formulas. Use the Case Study to evaluate flowsheet scenarios.
Optimization
Use the optimization feature in Aspen HYSYS to identify optimal operating conditions.
Workshop: Use the available optimization methods to maximize profit in a Turbo Expander plant flowsheet.
Modeling Real Separators
Model liquid/vapor carryover so that your model matches your process mass balance or separator design specification.
Workshop: Estimate carryover based on vessel geometry and inlet conditions. Model an exit device to reduce liquid carryover.
Dynamic Depressurization
Size and rate pressure safety valves to safely meet plant conditions using the Dynamic Depressuring utility.
Workshop: Use the Dynamic Depressuring utility to size a blowdown valve for a vessel and size a PSV for a fire case.
Reactions
Specify equilibrium and conversion reactors using reaction sets defined in the simulation basis.
Workshop: Model a simplified synthesis gas flowsheet using a variety of reactor types.
Heat Exchanger Rating
Convert an existing heat exchanger from a simple design model to a rigorous rating model.
Workshop: Use Aspen Shell and Tube Exchanger as the rating engine for a heat exchanger inside Aspen HYSYS.
EHY223 Aspen HYSYS Dynamics: Introduction to Dynamic Modeling
Course Overview
Develop the skills and techniques required for creating and running dynamic simulations
Study items of interest in dynamic modeling such as vessel relief scenarios, compressor surge control, distillation column control, and pipeline hydraulics
Learn the best practices for transitioning from steady-state to dynamic modeling and discover shortcuts for efficient use of HYSYS Dynamics
Study the effectiveness of process safety measures for the implementation of ESD (Emergency Shutdown systems) through implementation of the Event Scheduler
Help justify operational changes and counter regulatory concerns to comply with regulations and product quality constraints for process operations
Course Benefits
Explore your Dynamics model to introduce various real-life disturbances to a simulation and discover how different control strategies can mitigate these disturbance
Automate actions within a HYSYS Dynamics simulation by using the Event Scheduler tool
Learn pressure flow theory, column dynamics concepts, pipeline hydraulics, and process control theory
Properly define and adjust pressure flow specifications, strip charts, and controller parameters
Discover techniques and “rules of thumb” for controller tuning
Who Should Attend
Engineers with Aspen HYSYS experience
Engineers with no or limited previous experience in dynamic simulation
Approach
Instruction on basic topics through presentation
Discussion about the general approach and the key elements for successful dynamic simulations
Instructor-guided demonstrations of features
Hands-on workshops
Detailed course notes
Prerequisites
Familiarity with Aspen HYSYS steady-state modeling concepts and Aspen Simulation workbook or have attended EHY101 Aspen HYSYS: Process Modeling and EHY121 Building MS Excel User Interfaces for Aspen HYSYS Simulations Using Aspen Simulation Workbook
EHY223 Aspen HYSYS Dynamics: Introduction to Dynamic Modeling -Course Agenda Getting Started in Steady State
Define a fluid package
Add streams and operations
Converge and analyze steady state results
Learn the flow sheet shortcuts to rapidly build a steady state model to establish a functioning dynamic model
Workshop: Introduction to the basic concepts necessary for creating, solving and analyzing simulations in Aspen HYSYS®
Transitioning from Steady State to Dynamics
Define dynamic pressure/flow specifications and equipment sizing data
Add controllers and build strip charts to capture key results and operating data to analyze the process variables
Explore flow sheet summary table to enter inputs and review preference settings to maintain file backup and data size
Workshop: Review the basic concepts of steady state modeling in HYSYS, then convert the simulation into HYSYS Dynamics
Pressure-Flow Theory
More detailed investigation of the required inputs for a HYSYS Dynamics simulation
Learn about dynamic pressure/flow specifications for various unit operations
Review the solving strategy and
Dynamic Column Modeling
Configure LNG column model in HYSYS Dynamics
Prepare the column for dynamic simulation using tray sizing utility to calculate the tray holdup volume details
Develop an appropriate control strategy for the column reflux, tray temperature and condenser pressure
Explore the workflow to replace the column default kettle reboiler with a shell and tube heat exchanger
Workshop: Set up a distillation column in steady state mode and transition back into dynamics
Column Pressure Relief
Replace the standard condenser unit operation with a detailed overhead system including an air cooled exchanger
Make necessary P/F (Pressure / Flow) specs for the overhead system
Further develop model-building techniques and best practices by adding operations and controllers in the dynamic mode
Install a relief valve for protection of the column overhead system
Workshop: Set up a customized distillation column overhead condenser system
The Event Scheduler, Cause & Effect Matrix, and Spreadsheet
Introduction to Event Scheduler manager
degrees of freedom analysis of HYSYS Dynamics
Learn about the HYSYS Dynamics Assistant, flow sheet color scheme and key shortcuts for building dynamic models
Workshop: Vary the pressure flow spec around vessels and valves to perform backflow flow calculation for flow profile
Dynamic Details
Study valve characteristics and actuator parameters
Implement heat loss models for process vessels
Introduce nozzle location and hydrostatic head calculations
Discuss the dynamics Integrator settings
Workshop: Add operational details to an existing dynamic simulation to more accurately model real equipment
Expanding the Model
Follow best practices for adding dynamic specifications, unit operations and controllers in the dynamic mode
Develop appropriate control strategies using split range and on-off controllers
Install a relief valve for vessel overpressure protection
Workshop: Add equipment, modify the control system and add a pressure relief valve to a simulation directly in Dynamic mode
Compressor Curves and Surge Control
Specify head and efficiency curves for compressors
Use multiple curves to model compressor performance
Add Schedules and Build Sequences
Implement cause-and-event matrix
Create event conditions to activate valve actions
Workshop: Set up a fire scenario for a vessel and implement process safety measures
Basic Control Theory
Learn the basics of process control theory including feedback and feed forward control
Discuss PID control action and options for tuning PID parameters
Examine general guidelines for implementing appropriate control strategies
Workshop: Basic discussion on control Theory for Dynamic Simulations
Dynamic User Variables and Profile Tables in excel
Learn how to work with user variables in HYSYS Dynamics to accumulate the flow passing through a process stream
Add Profile Tables in excel to integrate HYSYS Dynamics simulations
Workshop: Accumulate flow passing through relief valve
Workshop: Create profile table using ASW for reporting
Pipeline Hydraulics
Basics of Modeling Multiphase Flow in Pipelines
Pipeline Modeling Options in HYSYS
Review pipeline hydraulics calculation options in Aspen HYSYS
Make changes and additions in Dynamic mode
Move Pressure-Flow specs when required
Accurately model existing plant equipment with Aspen HYSYS
Add anti-surge control to a compressor
Workshop: Apply performance curves to better represent the dynamic behavior of a compressor model. Implement a compressor surge control strategy to protect the equipment from potential damage
Explore Aspen Hydraulics to model pipeline hydraulics
Pig launching, generating pipeline profiles and identifying slug regions
Workshop: Configure and use the pigging operations, and launch pig using ASW
EHX1011 Design and Rate Shell and Tube Heat Exchangers
Course Overview
Learn the thermal design of shell and tube heat exchangers and how to use simulation to solve real process problems.
Learn how to optimize work processes using Aspen Shell & Tube Exchanger software.
Learn the fundamentals of producing a cost optimized exchanger design.
Understand the basic geometric selections required to establish a practical exchanger design and find out how to avoid tube vibration at the design phase.
Demonstration using AspenTech’s integrated heat exchanger software in conjunction with Aspen HYSYS and Aspen Plus to improve the performance of heat exchangers in the overall process
Learn how to embed a rigorous heat exchanger model into Aspen Simulation Workbook (Demonstration)
Course Benefits
Learn the fundamentals of producing a cost optimized exchanger design
Understand the requirements for design of boilers and condensers. Integrate Aspen Shell & Tube Exchanger with Aspen HYSYS® or Aspen Plus®
Optimize for both mechanical and thermal design requirements through the integration of Aspen Shell & Tube Mechanical (Aspen Teams® ) with Aspen Shell & Tube Exchanger (demonstration)
Who Should Attend
Thermal and process design professionals wishing to enhance their understanding of thermal design and simulation
New engineers wishing to gain experience in heat transfer and heat exchanger design
Approach
Instruction on basic heat transfer and heat exchanger design topics
Discussion about the general approach and the key elements for successful simulations
Use of Aspen Shell & Tube Exchanger in design and simulation exercises covering typical examples in condensing and boiling
Application of Aspen Shell & Tube Exchanger to exercises for thermal design, checks and simulation of shell and tube exchangers
Detailed course notes
This course assumes that Aspen Shell & Tube Exchanger product is in use
Prerequisites
Working knowledge of heat exchangers and heat transfer phenomena.
EHX1011 Design and Rate Shell and Tube Heat Exchangers Course Agenda
Introduction
Introductions and course contents
Workshop session descriptions
Training objectives and benefits
Aspen Shell and Tube Exchanger, What can it Do?
Recognize the features and functional capability of the Aspen Shell & Tube Exchanger application
Design optimum exchanger configurations
Design processes which make effective use of heat exchangers
Operate processes effectively
Trouble-shoot processes with problems
Demonstration on Aspen Shell & Tube Exchanger operation
Workshop: Design Mode and Rate/Checking - Run Design mode and look at different designs, transfer a Design to a Rating/Checking case, look at the tube layout.
Workshop: Checking an Oil Heater - Check an existing heat exchanger to determine if the area ratio is capable of performing the specified heat transfer.
Shell & Tube Heat Exchanger Geometry
Understand the TEMA Standards
Analyze the Performance of Kettle Reboiler
Simulate a K shell.
Enter liquid vapour only outlet nozzles.
Workshop: Analyze the Performance of Kettle Reboiler
Study the Performance of Thermosiphon Reboiler
Simulate a thermosiphon reboiler.
Set up the external inlet/outlet circuit.
Add data at different pressure levels
Workshop: Study the Performance of Thermosiphon Reboiler
Rating of the Falling Film Evaporator
Setup a falling film evaporator case
Workshop: Rating of the Falling Film Evaporator
Design of a Reflux Condenser
Use Aspen Shell&Tube to design a reflux condenser.
Take steps to increase the flooding velocity to improve the design
Workshop: Design of a Reflux Condenser
Monitoring Fouling Rate on a Shell and Tube Exchanger
Link a Maximum Fouling case to run a
Review different Shell and head types
Efficiently use the Aspen Shell & Tube Exchanger application to evaluate Singe phase exchangers, Condensers and Reboilers/vaporisers
Workshop: HP Boiler Feedwater Heater - Design a single-phase heat exchanger. Input data using the Shell & Tube Exchanger interface. Enter physical properties using multiple property options
Workshop: Debutanizer Overhead Condenser - Design a condenser. Enter two phase conditions for stream data using property tables. Specify fluid from component databank.
Design of Multiple Shell Exchanger
Design a large heat exchanger, requiring multiple shells.
Use the detailed geometry input items.
Import property data from a Process Simulator Interface File (PSF).
Workshop: Design of Multiple Shell Exchanger
scenario table in ASW
Workshop: Monitoring Fouling Rate on a Shell and Tube Exchanger
Checking Double Pipe and Multitube Hairpin Performance
Model Double Pipe Heat Exchanger
Model Mulitube Hair Pin Exchanger
Workshop: Checking Double Pipe and Multitube Hairpin Performance
Integration of Aspen Shell & Tube with Aspen HYSYS and Aspen Plus
Demonstration includes linking to the Aspen HYSYS® and Aspen Plus® process simulators
Integrate Aspen HYSYS with Aspen Shell and Tube - Switch from a simple end point or weighted model to a rigorous Aspen Shell & Tube Exchanger model
Integrate Aspen Plus with Aspen Shell and Tube - Rigorously design a heat exchanger to meet process requirements using the integration of Aspen Plus and Aspen Shell & Tube Exchanger
Aspen Technology, Inc. awards Continuing Education Units (CEUs) for training and development activities conducted by our organization in accordance with the definition established by the International Association of Continuing Education & Training (IACET). One CEU is granted for every 10 ho
EHY2511 Flare Network Design and Rating
Course Overview
Learn the fundamental flare network modeling techniques for pipeline design.
Learn the basics for rating a flare convergent, divergent and looped network for the constraint violations (Mach number, MABP, Noise, velocity, RhoV2) & for pressure, temperature and flow profile throughout the network.
Understand the solver messages to analyze the flow network problems and review options to take corrective measures.
Review results to perform process safety studies for pressure & temperature beyond allowable range and erosion problems (RhoV2) for healthiness of the flow network in the real plant.
Review flare network simulation computation convergence problems and examine solver solution methods.
Customize reports using MS excel macro
Import sources from Aspen Plus / Aspen HYSYS®, Export and import data from the MS access and MS excel
Course Benefits
Enables the attendees to develop flare network models for convergent, divergent and looped systems.
Approach
Course notes containing lecture materials, examples, and workshops are distributed
Lecture topics are reinforced with workshops throughout the day
Questions relating the course material to real life problems are encouraged
Prerequisites
A background in Refinery, upstream or petroleum engineering.
Familiarity with the Aspen HYSYS graphical user interface or attended the ‘EHY101 Aspen HYSYS: Process Modeling
Who Should Attend
Engineers new to Aspen Flare System Analyzer who need training to model flow networks
Engineers modeling flare systems and equipment
EHY2511 Flare Network Design and Rating
Introduction to Aspen Flare System Analyzer
Review the Aspen Flare System Analyzer program capabilities
Identify typical uses and benefits of the program
Demonstration of design methods using the program Review the requirements for building a simple Aspen Flare System Analyzer simulation model Implementing System Design Constraints
Workshop: Designing a Flare System - Sizing and building the pipe network.
Perform Rigorous Rating and Redesign
Rigorous Rating and Redesign - Implementing a rating check and improving the accuracy of the calculations. Debottlenecking - Identifying and removing pipe constraints. Add Flare Tip Curves and Invoke Heat Transfer calculation Workshop: Rigorous Rating and Redesign - Implementing a rating check and improving the accuracy of the calculations. Workshop: Add Flare Tip Curves and Invoke Heat Transfer calculation.
Study PSV Sizing Options and Inlet Pipe Pressure Drop
Calculate the rated flow for the PSV using API’s methods Setup the Orifice Size for PSVs
Calculate the Critical Pressure for PSVs
Study the effect of back pressure on PSV sizing
Calculate inlet pipe pressure drop for PSVs
Workshop: Setup the inlet piping pressure drop and sizing calculation for PSV
Troubleshooting Models
Review flow sheet variables for messages
Cleanup the components and correct selection of methods Review error messages for flash failure and make corrective actions Review error messages for the flow problems due to high flow rate or flow restrictions Review constraints and make sound engineering judgment Workshop: Take corrective action to resolve solver messages
Using the Export/Import Functions
Merge multiple Aspen Flare System Analyzer files in to one single file Importing Data from Aspen HYSYS
Workshop: Using the Export/Import Wizards - Merging two or more models or sections of a model into a larger model.
Reporting in Aspen Flare System Analyzer
Evaluate ways to customize and format results reporting Use VB automation to customize model reports for pressure flow summary Become familiar with common Aspen Flare System Analyzer and Excel objects Customize report using Excel Macro
Workshop: Add customized reports to a flow sheet simulation model
Discussion on Additional Topics
Learn the best practices
Understand Static Pressure and Total pressure
Review energy balance crossing the valve
Evaluate the effect of Kinetic Energy term on enthalpy calculation Review Mach number, Noise and RhoV2 calculations
Workshop: Group Discussion on Student’s Query,
Add New Plant to an Existing Design
Determine if a new plant flare header can be tied into an existing flare system Use Aspen Flare System Analyzer to evaluate the feasibility of a combined flare option. Workshop: Modifying an Existing Design - Evaluating the tie in feasibility of a new plant to an existing flare system.
conclusion and wrap up