BioWin3 ® – An Introduction Michael D. Doran, P. E. DEE Adjunct Professor of Civil & Environmental Engineering CEE 426.

Slides:



Advertisements
Similar presentations
Desalination Becomes A Reality In Tampa Bay Florida
Advertisements

Newcastle Water Pollution Control Plant
Welcome to American #2 Wastewater Treatment Plant.
CE 370 Sedimentation.
Sewage and Effluent Treatment 2-4 November 2002 Seán Moran -The first few slides.
1000 Friends of Florida Presentation on May 12, 2005 Presenter: Kart Vaith/CDM
Treatment of Slaughterhouse Wastewater
INDUSTRIAL WATER POLLUTION CONTROL Ass. Prof. Dr. Erkan ŞAH İ NKAYA.
Module 1: Introduction to Wastewater Treatment
Oregon’s Methane Project - Experience and Potential Mike Gamroth Oregon State University Dept. of Animal Sciences.
Introduction to Septic Tanks John R. Buchanan, Ph.D., P.E. University of Tennessee.
An-Najah National University Civil Engineering Department
Modeling Suspended Growth Systems – see Grady, Daigger & Lim Environmental Biotechnology CE421/521 Tim Ellis (originally prepared by Dr. Eric Evans) October.
1 CE 548 Analysis and Selection of Wastewater Flowrates and Constituent Loading.
WASTEWATER ENGINEERING
WATER I NNOVATE Pascal Harper Product Manager. 2 Application Areas for Greenfield Sites –Incorporate odour emissions into process selection. Process Upgrades.
Upgrade of Sana'a WWTP1 Upgrade of the Sana‘a Wastewater Treatment Plant Presentation of the Design Implementation of the New Preliminary Wastewater.
MODELING AMMONIA REMOVAL FROM AMMONIA SUPPLEMENTED BREWERY WASTEWATER By Julie E. Smith 1 and Linda A. Figeuroa 2 1 – Coors Brewing Company, 2 – Colorado.
Nitrification and Denitrification
Moving Bed Biofilm Reactor MBBR for Nitrification/Denitrification
Innovations in Oxidation Technologies to treat difficult wastewaters Dr Peter Barratt Business Manager Environmental & Clean Technology Air Products (Europe)
Dave Stropky, Paul Nowak, Suqin Dong Process Simulations Ltd. Konstantin Pougatch, Martha Salcudean University of British Columbia P.S. Pagoria, W.A. Barkley,
Municipal Wastewater Treatment Preliminary Seventh Power Plan Energy Efficiency Estimates November 18, 2014 West Point Wastewater Treatment Plant, Seattle.
Activated Sludge Design (Complete Mix Reactor)
Folklore in Activated Sludge Treatment Plant Operations
Reducing the Amount of Waste Activated Sludge Sara Schmidt CE 479 December 6, 2006.
Biosolids Treatment and Disposal
PROCESS INTEGRATED DESIGN WITHIN A MODEL PREDICTIVE CONTROL FRAMEWORK Mario Francisco, Pastora Vega, Omar Pérez University of Salamanca – Spain University.
WATER I NNOVATE Pascal Harper Product Manager. 2 What is ?
INTEGRATED DESIGN OF WASTEWATER TREATMENT PROCESSES USING MODEL PREDICTIVE CONTROL Mario Francisco, Pastora Vega University of Salamanca – Spain European.
A COMPUTER BASED TOOL FOR THE SIMULATION, INTEGRATED DESIGN, AND CONTROL OF WASTEWATER TREAMENT PROCESSES By P. Vega, F. Alawneh, L. González, M. Francisco,
NORM BASED APPROACHES FOR AUTOMATIC TUNING OF MODEL BASED PREDICTIVE CONTROL Pastora Vega, Mario Francisco, Eladio Sanz University of Salamanca – Spain.
Dr. Martin T. Auer MTU Department of Civil & Environmental Engineering Mass Balance, Kinetics & Reactors.
Obtaining the goals.  Identify realistic future use of all water bodies – drinking water, irrigation water, livestock watering, bathing, fishing, recipient.
Wastewater Treatment. Collection Sewers Collect wastewater and bring it to the wastewater treatment plant – Combined sewer overflows: Take untreated sewage.
Pennsylvania Water Environment Federation PennTEC Annual Technical Conference June 4, 2013 Altoona Westerly Wastewater Treatment Facility BNR Conversion.
CSE 425: Industrial Process Control 1. About the course Lect.TuLabTotal Semester work 80Final 125Total Grading Scheme Course webpage:
Wastewater Treatment CE 326 Principles of Environmental Engineering Prof. Tim Ellis Spring 2008.
Landfill Processes. Objectives  Describe the physical, chemical, and biological processes occurring in a landfill  Describe leachate quality (Table.
Increasing Energy Efficiency at the Allegan WWTP MWEA/AWWA Joint Annual Conference August 19, 2010.
McMaster Innovation Park 114A-175 Longwood Road South Hamilton, ON L8P 0A1 Canada Brazil Water and Wastewater Mission.
A New Twist on an Old Test for Activated Sludge Process Control Estes Park PWO Seminar October 22, 2004 Greg Farmer – Littleton / Englewood WWTP.
Co-Generation: Today’s Reality Larry McFall Plant Operations Manager Rock River Water Reclamation District Rockford, IL
August 01, 2008 Performance Modeling John Meisenbacher, MasterCard Worldwide.
Evaluation of alternative technologies for upgrading wastewater treatment plants in Minnesota for new phosphorus limits H. David Stensel University of.
TREATMENT OF A DAIRY FARM WASTEWATER USING A PILOT SCALE UPFLOW ANAEROBIC SLUDGE BLANKET (UASB) PROCESS By Ashveen Deerpaul & Arvinda Kumar RAGEN.
Using the CPE Approach to Optimize Industrial Waste Treatment Facilities Ronald G. Schuyler and Michael Rothberg Rothberg, Tamburini, and Winsor, Inc.
Adjusting N:P ratios in liquid dairy manure through nitrification and chemical phosphorus removal to match crop fertilizer requirements Background Nutrient.
NYWEA ENERGY SPECIALTY CONFERENCE November 20, 2014 Towards Net-Zero Energy in Wastewater Treatment Demonstration of ClearCove’s Enhanced Primary Treatment.
Introduction to Environmental Engineering Dr. Kagan ERYURUK
COMPARISON OF MBBR AND Suspended growth BNR Performance at the HRWTF
A Simpler Approach for Determining Biodegradation of SOCs in Wastewater Treatment Tim Ellis Associate Professor Dept. of Civil and Construction Engineering.
© 2014 Evoqua Water Technologies LLC INTRODUCING THE CAPTIVATOR George Smith; Director of Biological Processes.
Membrane Bioreactors for Wastewater Treatment.
Modeling A Wastewater Plant The Purpose Where does the water you use go? –The waste water from your shower, toilets, sinks, etc. and the water from businesses.
CTC 450 Review WW Collection Systems Types of pipes Installation.
2011 WCW Conference. Fort McMurray James Sacker, Director Environmental Hugh Crawford, Wastewater Supervisor Plant Operations staff Alberta Environment.
Enhanced Biological Nitrogen Removal In PVA-Gel Based MBBR - A Novel Option To Save Dal Lake. J. Singh*, K.M.Gani*, N.K.Singh*, V. Rose**, A.A. Kazmi*
Using PC simulation for flow sensitivity analysis with application to a wastewater treatment plant Panaitescu Ileana-Irina, Panaitescu Mariana, Panaitescu.
 Overview: Wastewater Engineering  Wastewater Characteristics  Wastewater Treatment Considerations  Overview: Wastewater Treatment Plant Design.
BNWRP Biosolids Presentation
Ioannis Markidis WISE CDT PhD Student, University of Bath
Preliminary Treatment Removing Large Solids Material by Raking & Screening REMOVES 1.
Wastewater Treatment.
Performance Analysis of Textile Industry Wastewater Treatment Plant with Physicochemical Characterizations Tadele Assefa Aragaw Faculty of Chemical and.
US Environmental Protection Agency
Individual Household Treatment Systems (Septic Tanks)
Wastewater Treatment Secondary Treatment.
Energy performance and Carbon emissions Assessment and Monitoring tool
City of Janesville Wastewater Facility Plan Amendment Public Hearing
Presentation transcript:

BioWin3 ® – An Introduction Michael D. Doran, P. E. DEE Adjunct Professor of Civil & Environmental Engineering CEE 426

Presentation Outline What is BioWin3 ® ? What can BioWin3 ® be used for? How does BioWin3 ® work? Some Examples Cautions Using BioWin3 ® Class Exercise

BioWin3 ® is Powerful WWTP Process Simulation Software BioWin3 ® is microcomputer-based wastewater treatment plant process software that allows integrated steady state or dynamic unit process simulations. According to EnviroSim Associates, Ltd., BioWin3 ® is the world-wide leader in WWTP simulator software.

BioWin3 ® Is Useful for: Integrated “Mass Balance” Approach, Including Sidestream Impacts Preliminary Analysis of Various Processes for Planning Purposes Detailed Analysis of Unit Process Sizing and Configuration during Design Analysis of Diurnal Loads, Peak Wet Weather, Solids Processing, etc., on Treatment Performance Evaluating SRT, Temperature, Other Factors Estimating Raw Solids Generation, Biosolids Process Loadings, Stabilized Biosolids Generation

BioWin3 ® Includes Robust Models IAWQ Extended (for BNR) Activated Sludge Fermentation Poly P Organisms Anaerobic Autotrophic (methane formers) Clarifier Hindered Settling-Thickening Clarifier Biological Activity Oxygen Transfer e.g.

Model Documentation can be Found in Literature General Model for Biological Nutrient Removal Activated Sludge Systems: Model Presentation, P.S. Barker and P.L. Dold, Water Environment Research, vol. 59, no , p General Model for Biological Nutrient Removal Activated Sludge Systems: Model Application, P.S. Barker and P.L. Dold, Water Environment Research, vol. 59, no , p COD and Nitrogen Mass Balances in Activated Sludge Systems, P.S. Barker and P.L. Dold, Water Research, vol. 29, no. 2, 1995, p An Introduction to Process Modeling for Designers, Water Environment Federation MOP 31, e.g.

BioWin3® Uses an Effective Human Interface Interface Modeling Engine Simulator Output Management Graphs Tables Configuration Kinetic Parameters Influent Characteristics Performance Factors

The Configuration Screen is Used to Describe the Modeled System

BioWin3® Simulation Configured From Elements Influent Element Clarifier Elements Reactor Elements Effluent Elements Mixer Element Anaerobic Digester Element Splitter Element Primary Clarifier Element Pipe Element (typ)

BioWin3 ® Contains Useful Controls and Tools SRT Wasting Control For Act Sldg Can Consider (or not) Clarifier Sludge Blanket, Non-Aerated MLSS, etc., in Biomass Inventory for F/M or SRT Global Temperature (or can be set “locally”) Simulation (Monitoring) and Tabular or Graphical Output Formats; Export Utility “Point and See” Information Documentation Output Report to “WORD” or PDF

Simulations Can Be Simple

Simulations Can Be Complex

Example – How Does the Model Predict Real Plant Performance? Beloit WI WWTP Activated Sludge System ~3.0 hr HRT ~23 hr HRT ~ 8 d SRT

Example – 2008 Monthly Avg Beloit Data Used

Example – BioWin3 Model Predicts Beloit Effluent Pretty Well Default BioWin3 Coefficients Used for Model.

Example – BioWin3 Model Predicts Beloit Effluent Pretty Well Default BioWin3 Coefficients Used for Model.

Example – BioWin3 Model Predicts Beloit Effluent Pretty Well Default BioWIn3 Coefficients Used for Model.

Example – BioWin3 Model Predicts Beloit Effluent Pretty Well Default BioWin3 Coefficients Used for Model.

Example 2 – Final Clarifier Performance vs. Loading Rate Variable Infl Flowrate 500 gpd/sq ft 800 gpd/sq ft 1,000 gpd/sq ft 1,200 gpd/sq ft Average OFR Values:

Example 2 – Flow Input of Typical Diurnal Pattern Used

Example 2 - TSS from Clarifiers

Example 2 - Effluent TSS Deteriorates at OFR above ~1,000 gpd/sq ft

Sludge Blanket “Blooms” at SLR above ~26 lb/d/sq ft

Close-up of Blanket Height Output from Simulation

Example 3 – Plant Mass Balance Recycle Quantities (% of Infl): Q=8.4% CBOD=5.6% TSS=18.3% TKN=19.2% TP=121%

Simulator Can Help Answer Key Design Questions What process, reactor sizings, recycle rates, etc. are best for my application? What Raw Sludge Loading to digestion can I expect During Peak Week and Peak Month Conditions? What Aeration Capacity is needed for Peak Conditions? What is the best Aeration tapering scheme? What SRT is best for different seasonal conditions? What impact do Sidestreams have on performance of other units? How does my proposed design respond to seasonal temperature variations, diurnal and peak loadings? How does the proposed design handle wet weather I/I inputs from severe storms? etc., etc., etc.

BioWin3 ® Should Be Used with Care Study Workbooks and Do Tutorial Examples. Carefully Complete All Input Screens for Element Properties. Think About Information Needed; Construct Graphs or Tables in “Album” for Desired Output. Simulate Critical Cases (e.g., Peak Hr, Peak Day, Peak Week, Critical Temperatures). Keep Log of “Runs” and Save Files with Logical Name. Ask Questions – I Have Found EnviroSim Staff to Be Very Helpful! Default Model Parameters have been Carefully Researched by EnviroSim (for domestic wastewater), but May Not Apply to Your Case; Use Careful and Conservative Approach to Planning and Design; Calibrate model to specific wasteswater if necessary.

Questions-Discussion

Let’s Build This Simple Simulation