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Application of Process Simulators and CFD to Optimize Process Capacity of WRRFs November 13, 2017.

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Presentation on theme: "Application of Process Simulators and CFD to Optimize Process Capacity of WRRFs November 13, 2017."— Presentation transcript:

1 Application of Process Simulators and CFD to Optimize Process Capacity of WRRFs
November 13, 2017

2 DRAFT: Icon is Optional
Date or speaker or subtitle

3 BC SmartArt Color Sequence
Blue 158 209 Green 118 176 67 Light Gray 192 202 199 Orange 245 130 32 Gray 149 157 147 Purple 51 42 134 Brown and Caldwell

4 Subsection Title or Presenters Name
Name of Presentation or Other Text Subsection Title or Presenters Name Brown and Caldwell

5 Modeling Platforms inCTRL SIMBA# EnviroSim BioWin 2Dc and 2Dr
ANSYS Fluent Dynamita SUMO Hydromantis GPS-X MIKE WEST FLOW Science FLOW-3D Hydraulic Modeling ??? Brown and Caldwell

6 Case Study #1: Lynchburg, VA
Date or speaker or subtitle

7 Intro Sentence Before Bullets
To change the slide layout (grid) or to change the color of the top bar: Select the slide thumbnail along the left side. Right Click and go to “Layout” Choose the corresponding color and/or layout to apply to the slide. Avoid using the Design tab to change layouts or color themes, there is an application bug that causes PowerPoint to crash. Brown and Caldwell

8 Case Study #2: HRSD, Williamsburg, VA
Date or speaker or subtitle

9 Process Flow Diagram Brown and Caldwell

10 Brown and Caldwell

11 Can pass 55 MGD peak hour flow
Do not need to consider plant expansion as part of Regional Wet-weather Management Plan Brown and Caldwell

12 Case Study #3: Pueblo, CO SIMBA#

13 Process Flow Diagram Parameter Annual Median 95th Percentile TP
Pueblo is an AS plant in a Johannesburg BNR configuration. The main features are: Primary clarifier for TSS and BOD removal Anaerobic and Anoxic zones for both N and P removal (I am missing acetic acid addition) Secondary clarification followed by UV disinfection before the final discharge Solids are managed through anaerobic digestion. Digested sludge is either dried or centrifuged and stored before being hauled to the landfill. Parameter Annual Median 95th Percentile TP 1.0 mg/L 2.5 mg/L TIN 15 mg/L 20 mg/L

14 Existing Biological Reactor Configuration
DO Probes NH4 and NOx Probes

15 Existing DO Control Loops Proposed AvN Control Loop

16 AvN and DO Control Loops

17 Modeling Aeration Control
AvN Modeling Summary Parameters Eff. TIN Eff. TAN DO TP Annual Median 5.2 2.6 0.4 0.6 Max Day 10.8 4.9 0.8 1.6 Min Day 1.84 0.92 0.22 0.25

18 Case Study #4: MWS, Nashville, TN
Date or speaker or subtitle

19 Table Sample South Grit Facility South Primary Clarifiers (13)
Tertiary Filters (abandoned) and South Chlorine Contact Tanks North Chlorine Contact Tanks North Primary Clarifiers (6) Aeration Tanks(8) North Secondary Clarifiers (8) Intermediate Screw Pumping Station North Grit Facility South Grit Facility South Primary Clarifiers (13) South Secondary Clarifiers (6) Excess Flow Treatment Brown and Caldwell

20 Brown and Caldwell

21 Secondary Clarifier Testing
MODEL INPUTS - Sludge Settling Characteristics Discrete Settling Fractions Brown and Caldwell | 8/2/2012

22 Comparison of Baffling Alternatives
WWF vane baffle No baffle No baffle WWF 5x5 conduit with 10” openings 5x10 chimney 5x10 chimney Higher surface vel and roll RAS RAS RAS

23 Title Page: Icon is Optional
Date or speaker or subtitle

24 Fun new elements to incorporate in your slides
Callout for emphasis Brown and Caldwell

25 Callout for emphasis

26 Brown and Caldwell


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