SIMDEUM: water demand in distribution network modelling Mirjam Blokker 20 November 2009 – ColloquiumTU Delft.

Slides:



Advertisements
Similar presentations
Modelling sustainability in water supply and drainage with SIMDEUM®
Advertisements

Hydrodynamics and Sediment Transport Modelling Ramiro Neves
Irene Seco Manuel Gómez Alma Schellart Simon Tait Erosion resistance and behaviour of highly organic in-sewer sediment 7th International Conference on.
J. A. Elías-Maxil Jan Peter van der Hoek Jan Hofman Luuk Rietveld SPN7.
Surface Water Treatment Plant
Upscaling and effective properties in saturated zone transport Wolfgang Kinzelbach IHW, ETH Zürich.
Transport of bacteria and colloids in intermittent sand filters Maria Auset 1, Arturo A. Keller 1, François Brissaud 2, Valentina Lazarova 3 1 Bren School.
A modified Lagrangian-volumes method to simulate nonlinearly and kinetically adsorbing solute transport in heterogeneous media J.-R. de Dreuzy, Ph. Davy,
VIII. Viscous Flow and Head Loss. Contents 1. Introduction 2. Laminar and Turbulent Flows 3. Friction and Head Losses 4. Head Loss in Laminar Flows 5.
Monroe L. Weber-Shirk S chool of Civil and Environmental Engineering Reactors The Case of the Chlorine Contact Tank.
Applications of Scaling to Regional Flood Analysis Brent M. Troutman U.S. Geological Survey.
Computational simulation of aerosol behaviour Jouni Pyykönen Lectio Praecursoria
Water Distribution Systems Water Quality Modelling for Civil Engineers 1 Helena M Jetmarova, GWMWater Helena M Jetmarova, GWMWater George J Kastl, MWH.
About Estuarine Dynamics
Mass Balances. Fundamental Principle of (Dynamic) Mass Balances The rate at which something accumulates in a region of interest (a “control volume”) equals.
Modeling Water Quality In Drinking Water Distribution Systems: Its Potential for Enhancing Water Security By: Robert Clark.
7/18/05 Interdisciplinary Modeling for Aquatic Ecosystems Curriculum Development Workshop Water Quality Modeling John J. Warwick, Director Division of.
Reactors . ä Reactor: a “container” where a reaction occurs ä Examples: ä Clear well at water treatment plant (chlorine contact) ä Activated sludge tank.
Interdisciplinary Modeling of Aquatic Ecosystems Curriculum Development Workshop July 18, 2005 Groundwater Flow and Transport Modeling Greg Pohll Division.
Flow Produced Noise & Fluid Mechanical Treatment Flow Produced Noise & Fluid Mechanical Treatment Prepared By: Eng. Ashraf Al-Shalalfeh Mechanical Engineering.
Principles of Liquid Flow through Pipelines
Suspended Load Above certain critical shear stress conditions, sediment particles are maintained in suspension by the exchange of momentum from the fluid.
Chapter 4 (continues) Pipe Network.
Distribution System Control Strategies.  Tank Management/Operations  Flushing  Rerouting Water  Others  optimizing existing booster chlorination.
Summary: Results Cumulative Risk from exposure to contaminants Use of household appliances results in emissions of VOCs into indoor air from contaminated.
Age of Potable Water Impacts on DBP’s and Disinfection Residuals.
Fouling Factor: After a period of operation the heat transfer surfaces for a heat exchanger become coated with various deposits present in flow systems,
Reverse Osmosis Feed Treatment, Biofouling, and Membrane Cleaning
BsysE595 Lecture Basic modeling approaches for engineering systems – Summary and Review Shulin Chen January 10, 2013.
General Question Test format: What types of questions should we expect? 7 multiple choice questions (5 points each) Short problems (similar to previous.
Processing, distribution and use of water.
Lesson 21 Laminar and Turbulent Flow
What effects do they have in drinking water
E NVIRONMENTAL E NGINEERING 441 Lecture 5: Water Treatment (3) Sedimentation & filtration Philadelphia University Faculty of Engineering Department of.
Watershed & Water Quality Modeling Technical Support Center WASP7 Course Sediment Transport.
Working With Simple Models to Predict Contaminant Migration Matt Small U.S. EPA, Region 9, Underground Storage Tanks Program Office.
Chapter 11 Heat Exchangers ( ) Heat Exchangers.
REDUCING SCALE DEPOSITION BY PHYSICAL TREATMENT Sungmin Youn and Professor X. Si, Calvin College REDUCING SCALE DEPOSITION BY PHYSICAL TREATMENT Sungmin.
ME 101: Fluids Engineering Chapter 6 ME Two Areas for Mechanical Engineers Fluid Statics –Deals with stationary objects Ships, Tanks, Dams –Common.
Urban Water Global water aspects
Types of Models Marti Blad Northern Arizona University College of Engineering & Technology.
Development, Testing and Application of the Multi-Block LTFATE Hydrodynamic and Sediment Transport Model Earl J. Hayter See instructions for customizing.
ERMSAR 2012, Cologne, Germany, March 21 – 23, 2012 Aerosol Retention in Containment Leak Paths: Indications for a Code Model in the Light of COLIMA Experimental.
Nira L. Salant, Marwan A. Hassan Department of Geography, University of British Columbia Physical effects of streambed periphyton on particle deposition.
Environmental Hydrodynamics Lab. Yonsei University, KOREA RCEM D finite element modeling of bed elevation change in a curved channel S.-U. Choi,
Enrico Da Riva (EN/CV/PJ)
Sedimentology Flow and Sediment Transport (1) Reading Assignment: Boggs, Chapter 2.
8. 1 Mixer Sizing Methods Four different sizing criteria - Velocity - Shear Stress - Yield Stress - Mixing Time.
In  Out  Generation or Removal  Accumulation
Clemson Hydro Project Describing Methods. Clemson Hydro Reactive Transport Silver dichromate forming Leisegang rings in a test tube experiment
Water System Infrastructure
CE 3372 Water Systems design
Hydrotransport 15 Conference,
Project Describing Methods.
Integrating Modeling and Physical Testing for Assessing Filtered Exhaust Stack Sampling Probe Location Xiao-Ying Yu, Kurtis P. Recknagle, John A. Glissmeyer,
FORTH/ICE-HT & U. PATRAS
Sediment Transport Mechanics
Q Chemical Mixers 1. Rapid mixers - for rapid chemical reactions where the reactant needs to be added efficiently 2. Flocculators - when different phases.
Mixing and flocculation
Lecture Objectives Learn about particle dynamics modeling
Treatment – Chlorine Disinfection
Eddy correlation – basic principles
Jos Derksen & Radompon Sungkorn Chemical & Materials Engineering
Lecture Objectives Review for exam Discuss midterm project
The impact of occupants’ behaviour on urban energy demand
Mohr Separations Research, Inc.
Maximum daily demand = 1.8 x average daily demand
SEDIMENTATION Aim - rapid removal of solid material by gravitational settling Drawbacks – colloidal material is slow settling Mustafa Nasser 2012.
Fixed bed Filled with particles Usually not spherical
Acceptability aspects: Taste, odour and appearance  Water should be free of tastes and odours that would be objectionable to the majority of consumers.
Presentation transcript:

SIMDEUM: water demand in distribution network modelling Mirjam Blokker 20 November 2009 – ColloquiumTU Delft

2 Watercycle Research Institute From transport model …

3 Watercycle Research Institute … to a more detailed model …

4 Watercycle Research Institute … to an all-pipes model

5 Demand allocation: top-down or bottom-up?

6 Watercycle Research Institute Is a bottom-up demand allocation the future? Practical considerations Is it necessary for specific purposes? Hydraulics influence WQ processes Choice in spatial and temporal aggregation influences hydraulic model results Effect of Bottom-Up or Top-Down demand allocation in real network

7 Watercycle Research Institute Pulse Intensity Flow Intensity Time Time Basic principle of stochastic demand model Source: Buchberger, 2007

8 Watercycle Research Institute SIMDEUM: parameters follow from surveys and information on appliances How often did you flush the toilet? How long did you take a shower for? When did you get up, leave the house, go to bed? Siemens typical patterns  I D No flow measurements

9 Watercycle Research Institute Compare: flows 43 homes Zandvoort, 1000 homes office

10 Watercycle Research Institute compare: travel times

11 Watercycle Research Institute Practical considerations – automatic linking data SIMDEUM Census data Land register Pipe information system connections Customer information

12 Watercycle Research Institute Skeletonize and aggregation

13 Watercycle Research Institute Hydraulics influence water quality processes High flows can re-suspend particles or slough biofilm Dissolved substances move with the water; may also disperse in case of laminar flows Non-conservative substances (chlorine) decrease under influence of contact time and e.g. temperature …

14 Watercycle Research Institute (AOC and dissolved solids) Suspended solids © J.H.G. Vreeburg Regular deposition & resuspension Biofilm formation & sloughing Corrosion Precipitation & flocculation Suspended solids incidental resuspension (AOC and dissolved solids) WQ processes in the distribution network

15 Watercycle Research Institute Suspended solids © J.H.G. Vreeburg Regular deposition & resuspension Biofilm formation & sloughing Suspended solids incidental resuspension hydraulic processes in the distribution network particles / wall interaction Maximum shear stress or velocity

16 Watercycle Research Institute (AOC and dissolved solids) © J.H.G. Vreeburg Biofilm formation Corrosion (AOC and dissolved solids) hydraulic processes in the distribution network dissolved substances / wall interaction Residual chlorine is related to Contact time (travel time) Temperature Biostability (incoming water quality)

17 Watercycle Research Institute (AOC and dissolved solids) hydraulic processes in the distribution network dissolved substances / dispersion v max v Stagnant flow, v = 0 m/s Laminar flow, v max = 2 * v mean = 0,04 m/s Turbulent flow, v max = 1.2 * v mean = 1,0 m/s v max v

18 Watercycle Research Institute SIMDEUM: SIMulation of Demand, an End-Use Model SIMDEUM was developed and validated with flows and travel times Conclusion: SIMDEUM generates realistic demand patterns, and thus a proper BU model can be constructed. Next step: Determine difference between current (TD) method and new (BU) method

19 Watercycle Research Institute Choice in spatial and temporal aggregation influences hydraulic model results

20 Watercycle Research Institute Correlation – level pumping station R = 0.99 Auto correlation (5 min) R = 1

21 Watercycle Research Institute Correlation – level 150 homes R = 0.68 Auto correlation (5 min) R = 0.84 R = 0.80

22 Watercycle Research Institute R = 0.26 Auto correlation (5 min) R = 0.66 R = 0.44 Correlation – level single home

23 Watercycle Research Institute Effect of Bottom-Up or Top-Down demand allocation in real network (Purmerend) Two network models: BU: model + SIMDEUM demand patterns Each connection has unique demand pattern Time step is 0.01 h (36 s) TD: model + sum demand pattern Sum pattern is the total flow of BU model Time step is 5 min

24 Watercycle Research Institute Purmerend network

25 Watercycle Research Institute Effect of Bottom-Up or Top-Down demand allocation in real network (Purmerend) 1.Cross correlation with respect to incoming flow 2.Flow direction reversals 3.Flow regime: stagnant, laminar, turbulent flow 4.Travel time 5.Maximum velocity

26 Watercycle Research Institute 1. Cross correlation BU TD=1

27 Watercycle Research Institute 2. Flow direction reversals BU TD =0: no reversals =1: 50% reversals

28 Watercycle Research Institute 3.a Stagnant flow BU TD Mainly at connection lines

29 Watercycle Research Institute 3.b Laminar flow BU TD Also at connection lines

30 Watercycle Research Institute 3.c Turbulent flow BU TD

31 Watercycle Research Institute 4. Travel times BU TD At 0:00 h (simulation run 48 h)

32 Watercycle Research Institute Travel times, average or accounting? …the longer water is in contact with the fabric of the distribution system, the higher the propensity for water quality problems to occur, and it is feasible that a small volume of poor quality water could conceivably harbor enough bacteria to cause failed regulatory samples and pose a public health risk.

33 Watercycle Research Institute 5. Max flow velocities BU TD

34 Watercycle Research Institute Quantifying effect of Bottom-Up or Top-Down demand allocation in real network 1.Cross correlation 2.Flow direction reversals 3.Flow regime: a.Stagnant flow b.Laminar flow c.Turbulent flow 4.Travel time 5.Maximum velocity 1.Large effect on diameter < 200 mm 2.Large effect 3. a.Effect in branch ends b.Effect in branch ends c.Limited effect 4.Limited effect on average travel times, more effect on variation 5.Effect especially noticeable on smaller pipe diameters and in branch ends

35 Watercycle Research Institute When is a BU model required? Tracing contaminants: when is the water save again, including for customers at the outskirts of the network? Id. for residual chlorine Hydraulics and water quality in branched networks Dispersion Flow direction reversals Maximum velocities Network fouling

36 Watercycle Research Institute Is a bottom-up demand allocation the future? Practical considerations Yes – automatic demand generation and allocation Possibly followed by skeletonization / aggregation step Is it necessary for specific WQ purposes? Self-cleaning network design: yes, in simplified form (uni-directional only) Tracing dissolved substances: yes in the outskirts (dispersion, flow direction reversals); yes in case maximum travel time is important (non-conservative substances)

SIMDEUM: water demand in distribution network modelling Mirjam Blokker 20 November 2009 – Colloquium

38 Watercycle Research Institute WQ in DWDS contamination propagation corrosion sedimentation and re-suspension coagulation, flocculation, precipitation disinfectant decay DBP formation bacterial re-growth Biofilm formation nitrification taste and odour Advection flows dispersion mixing at junctions inertia compressibility water / pipe Reaction initial WQ residence time / contact time temperature shear stress interaction with wall or other processes Water demand model temporal scale spatial scale stochastic / deterministic Accuracy auto (temporal) correlation cross (spatial) correlation probability of stagnation probability of laminar flow probability of turbulent flow Field data flow measurements tracer test monitoring WQ process water-use related surveys

39 Watercycle Research Institute WQ – an ADR model Advection Dispersion Reaction The concentration (C) of a dissolved or particulate substance changes through the network by (plug) flow, through dispersion (esp. laminar flow) and reaction (with pipe wall or other substances)

40 Watercycle Research Institute Water demand influences water quality Water demand determines flow, which influences Advection (plug flow, flow direction reversal) Dispersion (flow regime: stagnant / laminar / turbulent) Reaction Contact time (travel time) Temperature (travel time, flow velocity) Wall interaction (flow regime) Shear stress (maximum velocity) …?