cwea hydraulics presentation.pptle tour de hydraulics andle tour de hydraulics and control at...
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LE TOUR DE HYDRAULICS ANDLE TOUR DE HYDRAULICS AND CONTROL AT OCSD’S PLANT NO. 1
Rich ten Bosch, PE
April 2007
Overview
Orange County Sanitation District (OCSD)
Secondary Activated Sludge Facility 2 at Plant No. 1 Project (P1-102)
Hydraulic Analysis
Flow Control StrategyFlow Control Strategy
April 2007
Orange County Sanitation District Plant Nos 1 & 2 Vicinity MapPlant Nos. 1 & 2 Vicinity Map
Plant No. 1 –Plant No. 1 Reclamation PlantFountain Valley
Plant No. 2 –Treatment PlantHuntington Beach
April 2007
Huntington Beach
Orange County Sanitation District Key Statistics
Service area includes:
Key Statistics
471 square miles
21 cities
3 special districts
2.5 million residents
625 miles of collection system pipeline
245 MGD average daily flow received
120-inch diameter 5 mile long ocean outfall
301h Waiver
April 2007
Orange County Sanitation District Flow and CapacityFlow and Capacity
Plant No. 1 2006 Capacity
Primary 88 MGD 204 MGD
Secondary 71 MGD 105 MGD
Plant No. 2
Primary 155 MGD 168 MGD
Secondary 90 MGD 90 MGD
66% of the flow receives secondary treatment
April 2007
Secondary Activated Sludge Treatment Facility 2 at Plant No 1 (Project P1 102)at Plant No. 1 (Project P1-102)
Objectivesj
Increase the secondary treatment capacity at Plant No. 1
Current: 105 MGD (30 MGD TF + 75 MGD AS1)
Future: 165 MGD (60 MGD AS2)Future: 165 MGD (60 MGD AS2)
Provide flow to Groundwater Replenishment System (GWRS)(GWRS)
Quantity: Phase 1 – 128 MGD; Phase 3 – 185 MGD
April 2007
Quality: 5 NTU Monthly / 10 NTU Instantaneous
Secondary Activated Sludge Facility 2 atPlant No 1 Site PlanPlant No. 1 – Site Plan
Blower Building
Aeration Basins Secondary Clarifiers
Blower Building
SC GalleryTunnels
April 2007
Secondary Activated Sludge Treatment Facility 2 at Plant No 1 (Project P1 102)at Plant No. 1 (Project P1-102)
Trickling Filter Facility (P1-76)
30 MGDN
Secondary ActivatedSecondary Activated Sludge Facility 1
(P1-82) 75 MGDNew Secondary
P1-102
yActivated Sludge
Facility 2(Project P1-102)
60 MGD
April 2007
60 MGD
Hydraulic AnalysisOverviewOverview
Issues and ConstraintsIssues and Constraints
Hydraulic Analysis Goals
Hydraulic Model
Model DiscoveriesModel Discoveries
Hydraulic Analysis Results
April 2007
Hydraulic Analysis– Issues and ConstraintsPlant Wide HydraulicsPlant Wide Hydraulics
Existing Secondary Activated
Existing Trickling Filters (P1-76)
Existing Secondary Activated Sludge Facility 1 (P1-82)
April 2007
New Secondary Activated Sludge Facility 2 (P1-102)
Hydraulic Analysis – Issues and Constraints 15 Flow Scenarios15 Flow Scenarios
Scenarios divided intoScenarios divided into three main categories
-Average Dry WeatherWeather
-Maximum Hydraulic Capacity
-Storm
Divided into subcategories based upon treated effluent distribution options
-Groundwater Replenishment System
O O tf ll
April 2007
-Ocean Outfall
Hydraulic Analysis – Issues and Constraints Secondary Influent Feed
Primary Effluent
Secondary Influent Feed
Primary Effluent Pump Station 1
Trickling Filter Pump FM
dPrimary Effluent Distribution Box
Pump Station
Primary Effluent Pump Station 2 (Future)
FM
FM
April 2007
Throttling BFVFM
Hydraulic Analysis – Issues and ConstraintsSecondary Effluent DischargeSecondary Effluent Discharge
To Plant No. 2 / Ocean Outfall
Plant Water Pump Station
OCOCWD Pump
Station
Groundwater Recharge System
April 2007
Hydraulic Analysis - Goalsy y
Maximize gravity flow capacityMaximize gravity flow capacity
Establish weir elevations
Avoid flooding of secondary weirs
Ensure flow quantity to GWRS PWPS etcEnsure flow quantity to GWRS, PWPS, etc
Identify required control devices
Minimize active controls
Id tif f t i tIdentify future improvements
Hydraulic Analysis – Hydraulic ModelNodesNodes
April 2007
Hydraulic Analysis – Hydraulic ModelDetailed Hydraulic CalculationsDetailed Hydraulic Calculations
April 2007
Hydraulic Analysis – Hydraulic ModelThe Ultimate Balancing ActThe Ultimate Balancing Act
April 2007
Hydraulic Analysis - DiscoveriesControl Structures
To Plant No. 2 / Ocean Outfall
Control Structures
Plant Water Pump Station
OCWD
SEJB NO.1
OCWD Pump
Station
SEJB NO.2 `
Groundwater Recharge System
PEDB
SEJB NO.6
April 2007
Hydraulic Analysis – ResultsSummarySummary
Validated Plant No. 1 hydraulicsy
Determined maximum gravity capacity of 120 MGD for the P1-102 facilityMGD for the P1-102 facility
Established P1-102 weir elevations
Identified control structure weir elevations
E t bli h l i t & BFV itiEstablish sluice gate & BFV positions
Minimized active controls
April 2007
Identified future improvements
Hydraulic Analysis - ResultsFuture ImprovementsFuture Improvements
Upsize Secondary
Install
p yEffluent Pipeline
Install Adjustable
Weirs at Critical Flow DiversionFlow Diversion
Structures
Lower the GWRS Screenings Weir
Install Parallel
April 2007
Install Parallel Flowmeter
Flow Control StrategyOperational Philosophy
Base Loaded Scenarios
Operational Philosophy
Base Loaded Scenarios
P-82 Base Load Scenario
P1-102 Base Load Scenario
P1 76 Base Load ScenarioP1-76 Base Load Scenario
Free Floating Scenario
Recycle Flows
April 2007
Flow Control StrategyGoalsGoals
Maintain Quantity and Quality of Flow to GWRSMaintain Quantity and Quality of Flow to GWRS
Maintain Flow to PWPS and OCWD PS
Optimize Treatment
Maintain Simple Control StrategyMaintain Simple Control Strategy
April 2007
Flow Control StrategySetpointsSetpoints
P1-102 Facilityy
40 MGD Side
Minimum Flowrate 1 MGD
Average Design Flowrate
Maximum Hydraulic Flowrate
40 MGD
80 MGD
20 MGD Side
Minimum Flowrate
Average Design Flowrate
1 MGD
20 MGDAverage Design Flowrate
Maximum Hydraulic Flowrate
20 MGD
40 MGD
April 2007
Flow Control StrategyP1 82 Base Loaded Low FlowP1-82 Base Loaded – Low Flow
P1-82D = 75 mgdH = 110 mgdA = < 75 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 0 dP1-102
OCWD
A = 0 mgd (40 mgd)D = 40 mgdH = 80 mgdA = 0 mgd
GWRS
P1-102 (20 mgd)
D = 20 mgd
Recycle
April 2007
D = 20 mgdH = 40 mgdA = 0 mgd
Flow Control StrategyP1 82 Base Loaded 75 mgdP1-82 Base Loaded – 75 mgd
P1-82D = 75 mgdH = 110 mgdA = 75 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 0 dP1-102
(40 d)
OCWD
A = 0 mgd (40 mgd)D = 40 mgdH = 80 mgdA = < 40 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = 0 mgd
Flow Control StrategyP1 82 Base Loaded 115 mgdP1-82 Base Loaded – 115 mgd
P1-82D = 75 mgdH = 110 mgdA = 75 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A < 30 dP1-102
(40 d)
OCWD
A = < 30mgd (40 mgd)D = 40 mgdH = 80 mgdA = 40 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = < 20 mgd
Flow Control StrategyP1 82 Base Loaded 165 mgdP1-82 Base Loaded – 165 mgd
P1-82D = 75 mgdH = 110 mgdA = 75 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 30 dP1-102
(40 d)
OCWD
A = 30 mgd (40 mgd)D = 40 mgdH = 80 mgdA = 40 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = 20 mgd
Flow Control StrategyP1 82 Base Loaded 210 mgdP1-82 Base Loaded – 210 mgd
P1-82D = 75 mgdH = 110 mgdA = 75 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 75 dP1-102
(40 d)
OCWD
A = 75 mgd (40 mgd)D = 40 mgdH = 80 mgdA = 40 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = 20 mgd
Flow Control StrategyP1 82 Base Loaded 230 mgdP1-82 Base Loaded – 230 mgd
P1-82D = 75 mgdH = 110 mgdA = 75 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 75 dP1-102
(40 d)
OCWD
A = 75 mgd (40 mgd)D = 40 mgdH = 80 mgdA = 40 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = 40 mgd
Flow Control StrategyP1 82 Base Loaded 270 mgdP1-82 Base Loaded – 270 mgd
P1-82D = 75 mgdH = 110 mgdA = 75 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 75 dP1-102
(40 d)
OCWD
A = 75 mgd (40 mgd)D = 40 mgdH = 80 mgdA = 80 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = 40 mgd
Flow Control StrategyP1 82 Base Loaded 305 mgdP1-82 Base Loaded – 305 mgd
P1-82D = 75 mgdH = 110 mgdA = 110 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 75 dP1-102
(40 d)
OCWD
A = 75 mgd (40 mgd)D = 40 mgdH = 80 mgdA = 80 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = 40 mgd
Flow Control StrategyP1 82 Base Loaded 444 mgdP1-82 Base Loaded – 444 mgd
P1-82Blending
D = 75 mgdH = 110 mgdA = 110 mgd PWPS
P1-76D = 30 mgd
H = 75 mgd
A 75 dP1-102
(40 d)
OCWDBlending
A = 75 mgd (40 mgd)D = 40 mgdH = 80 mgdA = 80 mgd
GWRS
P1-102(20 mgd)
D = 20 mgd
Recycle
April 2007
D 20 mgdH = 40 mgdA = 40 mgd
Flow Control StrategyFree Floating ScenarioFree Floating Scenario
P1-82D = 75 mgdH = 110 mgd
PWPS
P1-76D = 30 mgd
H = 75 mgdP1-102
OCWD
(40 mgd)D = 40 mgdH = 80 mgd
GWRS
P1-102 (20 mgd)
D = 20 mgd
April 2007
D = 20 mgdH = 40 mgd
QUESTIONSQUESTIONS
April 2007