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OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
Water and wastewater systems
in the era of data explosion
Michela Mulas
Water and Environmental Engineering
Dept. of Civil and Environmental Engineering
Aalto University
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
MotivationsWater treatment facilities are continuously challenged to satisfy new constraints interms of quality of the effluents for compliance with stringent environmentalregulations, sustainable reuse and cost optimization.
Data explosion
The facilities are becoming modern with a vast amount ofon-line and off-line measurements collected routinelyand the operators and process engineers are becomingmore experienced in instrumentation and automationconcepts.
Data are used for decision support , for early warning ofdisturbances and process changes , for trackinginteresting and relevant parameters as well as for thebasis of control actions .
ObjectiveDiscuss the potential of encapsulating data-enhanced process knowledge
and modelling capability in automation systems.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
MotivationsWater treatment facilities are continuously challenged to satisfy new constraints interms of quality of the effluents for compliance with stringent environmentalregulations, sustainable reuse and cost optimization.
Data explosion
The facilities are becoming modern with a vast amount ofon-line and off-line measurements collected routinelyand the operators and process engineers are becomingmore experienced in instrumentation and automationconcepts.
Data are used for decision support , for early warning ofdisturbances and process changes , for trackinginteresting and relevant parameters as well as for thebasis of control actions .
ObjectiveDiscuss the potential of encapsulating data-enhanced process knowledge
and modelling capability in automation systems.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
MotivationsWater treatment facilities are continuously challenged to satisfy new constraints interms of quality of the effluents for compliance with stringent environmentalregulations, sustainable reuse and cost optimization.
Data explosion
The facilities are becoming modern with a vast amount ofon-line and off-line measurements collected routinelyand the operators and process engineers are becomingmore experienced in instrumentation and automationconcepts.
Data are used for decision support , for early warning ofdisturbances and process changes , for trackinginteresting and relevant parameters as well as for thebasis of control actions .
ObjectiveDiscuss the potential of encapsulating data-enhanced process knowledge
and modelling capability in automation systems.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
Outline
Introduction
Drinking water networkSävel research project
Sewer networkEfeSus research project
Wastewater treatment plantsDiamond research project
A full-scale exampleThe Viikinmäki WWTP
Conclusion
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
Sävel research project
Water mains managementThe effect of aging on the water distribution network are very ha rd to detect , because pipesare buried below the level of soil frost penetration.
Sävel project
◮ Funded by Tekes◮ Research parties
◮ Aalto UniversityRiku Vahala and Kia Aksela
◮ National Institute of Health and WelfareWater and Health UnitIlkka Miettinen
◮ Water companiesCompanies and associations
◮ Project duration : 1 July 2008 - 30 June 2012
Goals◮ Develop a system that detects network malfunctions more effectively and
respond to them with greater precision.◮ Detect disturbances by analyzing continuous measurements, water-use
forecast and network model.
◮ Improve the management of the network asset.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
EfeSus research project
Sewer network renovationSewer are valuable assets . There is the need to systematic approach to renovation planningas well as for comprehensive data collection and automated t reatment of data .
EfeSus project
◮ Funded by Tekes◮ Research parties
◮ Aalto University:Riku Vahala and Tuija Laakso
◮ Finnish Meteorological Institute:Jarmo Koistinen
◮ University of Exeter (UK): Dragan Savic◮ Companies
Wastewater utilities◮ Project duration : 1 June 2011 - 30 June 2014
Goals◮ Improve the prioritization of renovation and repair activities - what to
renovate and when.◮ Develop the use and the processing of existing data resources.
◮ Create a software prototype for assessing the different network areas.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
Diamond research project
Wastewater treatment plants
The lack of appropriate data management tools is clearly limiting a broader implementation andefficient use of new sensors, monitoring systems and advanced process controllers.
Diamond project
◮ Funded by FP7 Capacities:Research for the benefits of SMEs
◮ RTD performers :◮ CEIT (Spain)◮ Uppsala Universitet (Sweden)◮ IVL Svenska Miljoe Institutet AB (Sweden)◮ Aalto University (Finland)
◮ Small and Medium Enterprises:◮ Mondragón Sistemas de Información (Spain)◮ Cerlic Controls AB (Sweden)◮ Mipro Oy (Finland)
◮ End-Users:◮ Aguas de Gipuzkoa S.A (Spain)◮ Stockholm Vatten AB (Sweden)
◮ Project duration:1 September 2012 - 31 August 2014
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
Diamond research project
Wastewater treatment plants
DIAMOND
AdvanceD data management and InformAtics for the optimuM operatiON anDcontrol of wastewater treatment plants
◮ Processing, centralising, synthesizing, correcting and completing allthe heterogeneous data available in a WWTP.
◮ Interpreting and extracting the maximum information from theseplant data.
◮ Constructing new information from existing measurable variables.◮ Facilitating the decision-making process of the operators of the
WWTP.
◮ Facilitating the design and implementation of plant-wide operationalstrategies and automatic controllers.
Optimize the operation of wastewater systems by adequately managingand using all the information available in the plant.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Wastewater treatment plants: A full-scale example
Viikinmäki project
◮ Funded by MVTT◮ Aalto University :
◮ Water and Environmental Engineering◮ Environmental and Industrial Machine Learning
◮ Viikinmäki’s personnel
The wastewater treatment line consists of:◮ bar screening and grit removal◮ pre-aeration and primary sedimentation◮ activated sludge process (8 lines)◮ secondary sedimentation
◮ biological post-filtration (post-denitrification)
The sludge treatment line has mesophilicdigesters and dewatering systems
Retrieved fromwww.flickr.com/photos/sameli/sets/72157607704932823/
Monitoring nitrate concentrations in the denitrifying pos t-filtration unit.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Wastewater treatment plants: A full-scale example
Viikinmäki project
◮ Funded by MVTT◮ Aalto University :
◮ Water and Environmental Engineering◮ Environmental and Industrial Machine Learning
◮ Viikinmäki’s personnel
The wastewater treatment line consists of:◮ bar screening and grit removal◮ pre-aeration and primary sedimentation◮ activated sludge process (8 lines)◮ secondary sedimentation
◮ biological post-filtration (post-denitrification)
The sludge treatment line has mesophilicdigesters and dewatering systems
Retrieved fromwww.flickr.com/photos/sameli/sets/72157607704932823/
Monitoring nitrate concentrations in the denitrifying pos t-filtration unit.
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Process description: The denitrifying post-filtration unit
◮ Overall a total nitrogen removal of 90%
◮ Ten Biostyr R© filters arranged in parallel
◮ The influent wastewater is equally distributed
◮ Before each cell, the incoming flow is split in two
◮ Attached biomass tends to clog the cell
◮ Periodic backwashes with effluent wastewaterand a counter-current air flow
◮ To favor the removal, methanol is dosed with afeedback loop policy
◮ Dosing according to the nitrate concentration inthe filters, measured on-line with analyticalinstruments
◮ Treated wastewater is discharged into a commoneffluent channel
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Process description: The denitrifying post-filtration unit
◮ Overall a total nitrogen removal of 90%
◮ Ten Biostyr R© filters arranged in parallel
◮ The influent wastewater is equally distributed
◮ Before each cell, the incoming flow is split in two
◮ Attached biomass tends to clog the cell
◮ Periodic backwashes with effluent wastewaterand a counter-current air flow
◮ To favor the removal, methanol is dosed with afeedback loop policy
◮ Dosing according to the nitrate concentration inthe filters, measured on-line with analyticalinstruments
◮ Treated wastewater is discharged into a commoneffluent channel
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Process description: The denitrifying post-filtration unit
◮ Overall a total nitrogen removal of 90%
◮ Ten Biostyr R© filters arranged in parallel
◮ The influent wastewater is equally distributed
◮ Before each cell, the incoming flow is split in two
◮ Attached biomass tends to clog the cell
◮ Periodic backwashes with effluent wastewaterand a counter-current air flow
◮ To favor the removal, methanol is dosed with afeedback loop policy
◮ Dosing according to the nitrate concentration inthe filters, measured on-line with analyticalinstruments
◮ Treated wastewater is discharged into a commoneffluent channel
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Process description: The denitrifying post-filtration unit
Proper functioning of the nitrate sensorsis of crucial importance
from an environmental and aneconomical point of view
but harsh environmental conditionsexpose these instruments to malfunction
One big problem is vicinity of the analyzersto the effluent channel
◮ Methanol control is compromised◮ Need for a back-up instrument
Retrieved fromwww.flickr.com/photos/sameli/sets/72157607704932823/
Main goalDevelop an array of soft-sensors that estimatein real-time the nitrate concentration in the cells
◮ Accurate and computationally lightmodels are the priority
◮ Starting from easy to measureprocess variables
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Process description: The denitrifying post-filtration unit
Proper functioning of the nitrate sensorsis of crucial importance
from an environmental and aneconomical point of view
but harsh environmental conditionsexpose these instruments to malfunction
One big problem is vicinity of the analyzersto the effluent channel
◮ Methanol control is compromised◮ Need for a back-up instrument
Retrieved fromwww.flickr.com/photos/sameli/sets/72157607704932823/
Main goalDevelop an array of soft-sensors that estimatein real-time the nitrate concentration in the cells
◮ Accurate and computationally lightmodels are the priority
◮ Starting from easy to measureprocess variables
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Soft-sensors based on unstructured modelsBased on a more-or-less accurate description of relationsh ips between data
An unstructured software sensor is often seen as input-output model
◮ the inputs X are easy to measure
◮ the output y are hard to measure
Assuming the existence of a functional relationshipbetween the inputs and the outputs (y = f (X)+ ε),
the model is calibrated to reconstruct it (̂f )
Unstructured models rely on methods for dataanalysis:
◮ Techniques for sample selection◮ Techniques for variable selection
◮ Techniques for regression
KISS: Start with a simple model type
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Soft-sensor design
A set of process measurements hasbeen collected:
◮ 3 years of continuous operations(2008 - 2010), hourly averages
Sample selection
The overall number of available processvariable relevant to the task is 142:
◮ 7 for the influent◮ 5 for the effluent
◮ (12+1)×10 for the filters
Variable selection
TAG Description UnitsI-NO3-1 Influent Nitrate-Nitrogen (sensor 1) mg/lI-NO3-2 Influent Nitrate-Nitrogen (sensor 2) mg/lI-SS-1 Influent Suspended Solids (sensor 1) mg/lI-SS-2 Influent Suspended Solids (sensor 2) mg/lI-O2 Influent Dissolved Oxygen mg/lI-PO Influent Phosphate-Phosphorus mg/lI-TP Influent Total Phosphorus mg/lE -NO3 Effluent Nitrate-Nitrogen mg/l
E -TOC Effluent Total Organic Carbon mg/lE -PO Effluent Phosphate-Phosphorus mg/lE -TP Effluent Total Phosphorus mg/lE -T Effluent Temperature ◦C
Fi-QWW i-th Filter Backwashing water flowrate m3/sFi-QWA i-th Filter Backwashing air flowrate m3/s
Fi-QW -1 i-th Filter Wastewater flowrate (line 1) m3/s
Fi-QW -2 i-th Filter Wastewater flowrate (line 2) m3/sFi-QM-1 i-th Filter Methanol flowrate (line 1) m3/h
Fi-QM-2 i-th Filter Methanol flowrate (line 2) m3/hFi-P-1 i-th Filter Pressure at the bottom kPaFi-P-2 i-th Filter Pressure at the top kPaFi-NO3 i-th Filter Nitrate-Nitrogen mg/lFi-HL i-th Filter Head-Loss mFi-CR i-th Filter Clogging rate %Fi-HRU i-th Filter Hour in use −
Fi-ITW i-th Filter Intermediate time of backwash −
Simplicity is on of the main requirements to allow adirect implementation in the plant’s control system. Regression models
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Soft-sensor design
A set of process measurements hasbeen collected:
◮ 3 years of continuous operations(2008 - 2010), hourly averages
Sample selection
The overall number of available processvariable relevant to the task is 142:
◮ 7 for the influent◮ 5 for the effluent
◮ (12+1)×10 for the filters
Variable selection
TAG Description UnitsI-NO3-1 Influent Nitrate-Nitrogen (sensor 1) mg/lI-NO3-2 Influent Nitrate-Nitrogen (sensor 2) mg/lI-SS-1 Influent Suspended Solids (sensor 1) mg/lI-SS-2 Influent Suspended Solids (sensor 2) mg/lI-O2 Influent Dissolved Oxygen mg/lI-PO Influent Phosphate-Phosphorus mg/lI-TP Influent Total Phosphorus mg/lE -NO3 Effluent Nitrate-Nitrogen mg/l
E -TOC Effluent Total Organic Carbon mg/lE -PO Effluent Phosphate-Phosphorus mg/lE -TP Effluent Total Phosphorus mg/lE -T Effluent Temperature ◦C
Fi-QWW i-th Filter Backwashing water flowrate m3/sFi-QWA i-th Filter Backwashing air flowrate m3/s
Fi-QW -1 i-th Filter Wastewater flowrate (line 1) m3/s
Fi-QW -2 i-th Filter Wastewater flowrate (line 2) m3/sFi-QM-1 i-th Filter Methanol flowrate (line 1) m3/h
Fi-QM-2 i-th Filter Methanol flowrate (line 2) m3/hFi-P-1 i-th Filter Pressure at the bottom kPaFi-P-2 i-th Filter Pressure at the top kPaFi-NO3 i-th Filter Nitrate-Nitrogen mg/lFi-HL i-th Filter Head-Loss mFi-CR i-th Filter Clogging rate %Fi-HRU i-th Filter Hour in use −
Fi-ITW i-th Filter Intermediate time of backwash −
Simplicity is on of the main requirements to allow adirect implementation in the plant’s control system. Regression models
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Soft-sensor design
A set of process measurements hasbeen collected:
◮ 3 years of continuous operations(2008 - 2010), hourly averages
Sample selection
The overall number of available processvariable relevant to the task is 142:
◮ 7 for the influent◮ 5 for the effluent
◮ (12+1)×10 for the filters
Variable selection
TAG Description UnitsI-NO3-1 Influent Nitrate-Nitrogen (sensor 1) mg/lI-NO3-2 Influent Nitrate-Nitrogen (sensor 2) mg/lI-SS-1 Influent Suspended Solids (sensor 1) mg/lI-SS-2 Influent Suspended Solids (sensor 2) mg/lI-O2 Influent Dissolved Oxygen mg/lI-PO Influent Phosphate-Phosphorus mg/lI-TP Influent Total Phosphorus mg/lE -NO3 Effluent Nitrate-Nitrogen mg/l
E -TOC Effluent Total Organic Carbon mg/lE -PO Effluent Phosphate-Phosphorus mg/lE -TP Effluent Total Phosphorus mg/lE -T Effluent Temperature ◦C
Fi-QWW i-th Filter Backwashing water flowrate m3/sFi-QWA i-th Filter Backwashing air flowrate m3/s
Fi-QW -1 i-th Filter Wastewater flowrate (line 1) m3/s
Fi-QW -2 i-th Filter Wastewater flowrate (line 2) m3/sFi-QM-1 i-th Filter Methanol flowrate (line 1) m3/h
Fi-QM-2 i-th Filter Methanol flowrate (line 2) m3/hFi-P-1 i-th Filter Pressure at the bottom kPaFi-P-2 i-th Filter Pressure at the top kPaFi-NO3 i-th Filter Nitrate-Nitrogen mg/lFi-HL i-th Filter Head-Loss mFi-CR i-th Filter Clogging rate %Fi-HRU i-th Filter Hour in use −
Fi-ITW i-th Filter Intermediate time of backwash −
Simplicity is on of the main requirements to allow adirect implementation in the plant’s control system. Regression models
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Soft-sensor design
A set of process measurements hasbeen collected:
◮ 3 years of continuous operations(2008 - 2010), hourly averages
Sample selection
The overall number of available processvariable relevant to the task is 142:
◮ 7 for the influent◮ 5 for the effluent
◮ (12+1)×10 for the filters
Variable selection
TAG Description UnitsI-NO3-1 Influent Nitrate-Nitrogen (sensor 1) mg/lI-NO3-2 Influent Nitrate-Nitrogen (sensor 2) mg/lI-SS-1 Influent Suspended Solids (sensor 1) mg/lI-SS-2 Influent Suspended Solids (sensor 2) mg/lI-O2 Influent Dissolved Oxygen mg/lI-PO Influent Phosphate-Phosphorus mg/lI-TP Influent Total Phosphorus mg/lE -NO3 Effluent Nitrate-Nitrogen mg/l
E -TOC Effluent Total Organic Carbon mg/lE -PO Effluent Phosphate-Phosphorus mg/lE -TP Effluent Total Phosphorus mg/lE -T Effluent Temperature ◦C
Fi-QWW i-th Filter Backwashing water flowrate m3/sFi-QWA i-th Filter Backwashing air flowrate m3/s
Fi-QW -1 i-th Filter Wastewater flowrate (line 1) m3/s
Fi-QW -2 i-th Filter Wastewater flowrate (line 2) m3/sFi-QM-1 i-th Filter Methanol flowrate (line 1) m3/h
Fi-QM-2 i-th Filter Methanol flowrate (line 2) m3/hFi-P-1 i-th Filter Pressure at the bottom kPaFi-P-2 i-th Filter Pressure at the top kPaFi-NO3 i-th Filter Nitrate-Nitrogen mg/lFi-HL i-th Filter Head-Loss mFi-CR i-th Filter Clogging rate %Fi-HRU i-th Filter Hour in use −
Fi-ITW i-th Filter Intermediate time of backwash −
Simplicity is on of the main requirements to allow adirect implementation in the plant’s control system. Regression models
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Soft-sensor design
A set of process measurements hasbeen collected:
◮ 3 years of continuous operations(2008 - 2010), hourly averages
Sample selection
The overall number of available processvariable relevant to the task is 142:
◮ 7 for the influent◮ 5 for the effluent
◮ (12+1)×10 for the filters
Variable selection
TAG Description UnitsI-NO3-1 Influent Nitrate-Nitrogen (sensor 1) mg/lI-NO3-2 Influent Nitrate-Nitrogen (sensor 2) mg/lI-SS-1 Influent Suspended Solids (sensor 1) mg/lI-SS-2 Influent Suspended Solids (sensor 2) mg/lI-O2 Influent Dissolved Oxygen mg/lI-PO Influent Phosphate-Phosphorus mg/lI-TP Influent Total Phosphorus mg/lE -NO3 Effluent Nitrate-Nitrogen mg/l
E -TOC Effluent Total Organic Carbon mg/lE -PO Effluent Phosphate-Phosphorus mg/lE -TP Effluent Total Phosphorus mg/lE -T Effluent Temperature ◦C
Fi-QWW i-th Filter Backwashing water flowrate m3/sFi-QWA i-th Filter Backwashing air flowrate m3/s
Fi-QW -1 i-th Filter Wastewater flowrate (line 1) m3/s
Fi-QW -2 i-th Filter Wastewater flowrate (line 2) m3/sFi-QM-1 i-th Filter Methanol flowrate (line 1) m3/h
Fi-QM-2 i-th Filter Methanol flowrate (line 2) m3/hFi-P-1 i-th Filter Pressure at the bottom kPaFi-P-2 i-th Filter Pressure at the top kPaFi-NO3 i-th Filter Nitrate-Nitrogen mg/lFi-HL i-th Filter Head-Loss mFi-CR i-th Filter Clogging rate %Fi-HRU i-th Filter Hour in use −
Fi-ITW i-th Filter Intermediate time of backwash −
Simplicity is on of the main requirements to allow adirect implementation in the plant’s control system. Regression models
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Soft-sensor design
A set of process measurements hasbeen collected:
◮ 3 years of continuous operations(2008 - 2010), hourly averages
Sample selection
The overall number of available processvariable relevant to the task is 142:
◮ 7 for the influent◮ 5 for the effluent
◮ (12+1)×10 for the filters
Variable selection
TAG Description UnitsI-NO3-1 Influent Nitrate-Nitrogen (sensor 1) mg/lI-NO3-2 Influent Nitrate-Nitrogen (sensor 2) mg/lI-SS-1 Influent Suspended Solids (sensor 1) mg/lI-SS-2 Influent Suspended Solids (sensor 2) mg/lI-O2 Influent Dissolved Oxygen mg/lI-PO Influent Phosphate-Phosphorus mg/lI-TP Influent Total Phosphorus mg/lE -NO3 Effluent Nitrate-Nitrogen mg/l
E -TOC Effluent Total Organic Carbon mg/lE -PO Effluent Phosphate-Phosphorus mg/lE -TP Effluent Total Phosphorus mg/lE -T Effluent Temperature ◦C
Fi-QWW i-th Filter Backwashing water flowrate m3/sFi-QWA i-th Filter Backwashing air flowrate m3/s
Fi-QW -1 i-th Filter Wastewater flowrate (line 1) m3/s
Fi-QW -2 i-th Filter Wastewater flowrate (line 2) m3/sFi-QM-1 i-th Filter Methanol flowrate (line 1) m3/h
Fi-QM-2 i-th Filter Methanol flowrate (line 2) m3/hFi-P-1 i-th Filter Pressure at the bottom kPaFi-P-2 i-th Filter Pressure at the top kPaFi-NO3 i-th Filter Nitrate-Nitrogen mg/lFi-HL i-th Filter Head-Loss mFi-CR i-th Filter Clogging rate %Fi-HRU i-th Filter Hour in use −
Fi-ITW i-th Filter Intermediate time of backwash −
Simplicity is on of the main requirements to allow adirect implementation in the plant’s control system. Regression models
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Estimation performanceThe hardware sensor in Filter 9 is not returning any measurement.
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F9−QW
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F3−QW
The missing measurements can be replaced by the soft-sensor estimates
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Estimation performanceThe hardware sensor in Filter 9 is not returning any measurement.
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F9−QW
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F9−
NO
3
Measured
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F3−QW
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F3−
NO
3
Measured
The missing measurements can be replaced by the soft-sensor estimates
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Estimation performanceThe hardware sensor in Filter 9 is not returning any measurement.
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F9−QW
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F9−
NO
3
Measured
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F9−
NO
3
k−NN LLROLSR
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F3−QW
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F3−
NO
3
Measured
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F3−
NO
3
k−NN LLROLSRMeasured
The missing measurements can be replaced by the soft-sensor estimates
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Estimation performanceThe hardware sensor in Filter 9 is not returning any measurement.
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F9−QW
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F9−
NO
3
Measured
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F9−
NO
3
k−NN LLROLSR
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.09
0.2
0.4
0.6
0.8
F3−QW
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F3−
NO
3
Measured
02.Oct.09 03.Oct.09 04.Oct.09 06.Oct.09 07.Oct.090
0.5
1
1.5
2
F3−
NO
3
k−NN LLROLSRMeasured
The missing measurements can be replaced by the soft-sensor estimates
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Estimation performanceErroneous measurements are returned by the hardware sensor in Filter 6.
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.10
0.1
0.2
0.3
0.4
F6−
QW
F6−QW
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.10
0.1
0.2
0.3
0.4
F3−
QW
F3−QW
The soft-sensor is capable of recovering the nitrate concen tration
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Estimation performanceErroneous measurements are returned by the hardware sensor in Filter 6.
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.10
0.1
0.2
0.3
0.4
F6−
QW
F6−QW
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.100
0.5
1
F6−
NO
3
Measured
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.10
0.1
0.2
0.3
0.4
F3−
QW
F3−QW
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.100
0.5
1
F3−
NO
3
Measured
The soft-sensor is capable of recovering the nitrate concen tration
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
The Viikinmäki WWTP
Estimation performanceErroneous measurements are returned by the hardware sensor in Filter 6.
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.10
0.1
0.2
0.3
0.4
F6−
QW
F6−QW
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.100
0.5
1
F6−
NO
3
Measured
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.100
0.5
1
F6−
NO
3
k−NN LLROLSRMeasured
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.10
0.1
0.2
0.3
0.4
F3−
QW
F3−QW
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.100
0.5
1
F3−
NO
3
Measured
16.Mar.10 17.Mar.10 18.Mar.10 19.Mar.100
0.5
1
F3−
NO
3
k−NN LLROLSRMeasured
The soft-sensor is capable of recovering the nitrate concen tration
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
Conclusion
Viikinmäki project
Potential benefits for the WWTP supervisionand monitoring
◮ Back-up system to conventional analyticalequipment for replacing out-of-order components.
◮ Validation tools for existing field measurements.
We discussed the potential of encapsulating data-enhanced process knowledge and modell ingcapability in automation systems through different project examples:
◮ Sävel : Water supply real-time management◮ Efesus : Effective sewer condition management using online sensor information
◮ Diamond : Advanced data management and informatics for the optimum operation and controlof wastewater treatment plants
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion
OutlineDrinking water network
Sewer networkWastewater treatment plants
A full-scale exampleConclusion
Conclusion
Viikinmäki project
Potential benefits for the WWTP supervisionand monitoring
◮ Back-up system to conventional analyticalequipment for replacing out-of-order components.
◮ Validation tools for existing field measurements.
We discussed the potential of encapsulating data-enhanced process knowledge and modell ingcapability in automation systems through different project examples:
◮ Sävel : Water supply real-time management◮ Efesus : Effective sewer condition management using online sensor information
◮ Diamond : Advanced data management and informatics for the optimum operation and controlof wastewater treatment plants
BioRefine and Vesi - Final seminar 2012 Water and wastewater systems in the era of data explosion