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ALDERWOOD WATER AND
WASTEWATER DISTRICT
OUTFALL UPGRADE
Seattle University Senior Design Team CEE 16.7
Kristin Ramey, Isabella Schwartz, Abbie Lorensen, Larissa
Grundell
Science and Engineering Project Center
College of Science and Engineering
Seattle University
Faculty Advisor: Dr. Michael Marsolek
Sponsor: Alderwood Water and Wastewater District
Acknowledgments
Thank you!
Useful Terms
Outfall: The pipe that conveys treated effluent from
the wastewater treatment plant to the Puget Sound
Diffuser: The last section of pipe that has openings to
distribute effluent into the surrounding water body
3,100 ft - 18” Ductile
Iron
1,300 ft - 18” Reinforced
Concrete
80’
Diffuser
4” Portholes
1972 – CAS
Facility
2013 – MBR Facility
Project Motivation
Structural Condition
Internal condition unknown
External inspections show signs
of corrosion
Pipe Capacity
Expanding Service Area
Corrosion of pipe to flange weld at 12
o’clock position on outfall pipe.
Project Motivation
Q= 8.7
MGD
Q=15.8 MGD
Design Approach
 Preliminary Assessment
Condition Assessment
Hydraulic Analysis
 Design Selection
 Design Considerations
Detention Vault Design
Pipe Replacement
Mixing Zone Analysis
 Cost & Decision
Condition Assessment
Hydraulic Analysis
Preliminary Assessment
Condition Assessment
Hydraulic Analysis
Preliminary Assessment
Condition Assessment
 External Dive Inspection
Determine condition of submerged concrete pipe and diffuser
Results:
Flanged end of diffuser in "poor" condition with heavy corrosion
Indicates a new diffuser should be included in all design options
 Internal Camera Inspection
On hold
Condition Assessment
Hydraulic Analysis
Preliminary Assessment
Hydraulic Modeling
 Purpose:
Determine capacity of the outfall
 Approach:
Use PCSWMM to model dynamic outfall hydraulics
Storm Water Management Model
Constructed by the EPA
Use as-built information to construct model
Input wet weather flow data from December 2015
Apply peaking factor
Hydraulic Modeling
JunctionConduit
Hydraulic Modeling
Max Flow =
11.1 MGD
Hydraulic Modeling
Hand Calculations
 Purpose:
Verify capacity determined in PCSWMM modeling.
 Approach:
Determine the maximum allowable flow rate given the fixed changed
in elevation available.
 𝑧 =
𝑉2
2𝑔
+
𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟
𝜌 𝑒effluent
𝑧 𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
WWTP
ZZ=169’
Hand Calculations
𝑧 =
𝑉2
2𝑔
+
𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟
𝜌 𝑒ffluent
𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
Velocity
Head
Ambient /Effluent Density
Difference
Hand Calculations
𝑧 =
𝑉2
2𝑔
+
𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟
𝜌 𝑒ffluent
𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
Datum
Hand Calculations
𝑧 =
𝑉2
2𝑔
+
𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟
𝜌 𝑒ffluent
𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
Friction Losses
ℎ 𝑓 = 𝑓
𝐿
𝐷
𝑉2
2𝑔
Hand Calculations
𝑧 =
𝑉2
2𝑔
+
𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟
𝜌 𝑒ffluent
𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
Minor
Losses
ℎ 𝑚 = 𝑘
𝑉2
2𝑔
Hand Calculations
 ℎ 𝑚
 Horizontal bends from As-builts
 Radius of curvature to determine K from tabulated values
Bend
Radius of
Curvature
K
𝑽 𝟐
𝟐𝒈
𝒉 𝒎 = 𝑲
𝑽 𝟐
𝟐𝒈
1 48 0.35 1.48’ 0.52’
2 37.3 0.35 1.48’ 0.52’
3 7.26 0.25 1.48’ 0.37’
4 7.16 0.25 1.48’ 0.37’
5 3.87 0.16 1.48’ 0.24’
6 16.26 0.35 1.48’ 0.52’
7 14.67 0.32 1.48’ 0.47’
8 14.67 0.32 1.48’ 0.47’
Total 3.48’
Hand Calculations
Expansion
ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 = 𝑘
𝑉2
2𝑔
𝑧 =
𝑉2
2𝑔
+
𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟
𝜌 𝑒ffluent
𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
Hand Calculations
 𝒉 𝒅𝒊𝒇𝒇𝒖𝒔𝒆𝒓
Flow equally distributed at maximum capacity
Conservation of mass at each port
Ports modeled as expansions
ℎ = 𝑘
𝑉2
2𝑔
Friction losses between ports
Hand Calculations
𝑧 =
𝑉2
2𝑔
+
𝜌 𝑎
𝜌 𝑒
𝑧 𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
 Z=169ft
 Iterating with V=Q/A
 𝑄 𝑚𝑎𝑥 = 11 𝑀𝐺𝐷
Z
WWTP
Capacity Conclusions
 Hydraulic modeling capacity = 11.1 MGD
 Hand calculations capacity = 11 MGD
Corroborates modeling results
 11 MGD capacity is less than the projected 15.8 MGD
Design options need to account for flow attenuation
Option 3
Full
Replacement
Extend
Diffuser
Design Selection
Option 1
Partial
Replacement
Detention Vault
Shallow
Diffuser
Option 2
Partial
Replacement
Detention Vault
Extend Diffuser
Detention Vault
Pipe Replacement
Mixing Zone Analysis
Design Considerations
Detention Vault Design
 Purpose:
Flow attenuation is required
 Approach:
Conservation of mass
Inflow – modified wet weather time series
Outflow – 10 MGD (conservative)
Q=10 MGD
Q=10 MGD
Q=15.8 MGD
30,000 gallons
Detention Vault Design
 Constrained by
Max Plan Dimensions: 100ft X 45ft
Pipe diameter of surrounding pipe network: 24in
 Design Plan Dimensions: 45ft X 15ft
Detention Vault Plan View
Vault
Detention Vault Profile Section
Detention Vault Design
 Constrained by:
Allowable depth 22 ft.
 Design depth 10ft
Detention Vault
Pipe Replacement
Mixing Zone Analysis
Design Considerations
Pipe Replacement
 Purpose:
Condition assessment shows concrete is deteriorating
Hydraulic analysis indicates insufficient capacity
 Approach:
Partial Replacement
Replace concrete portion with 24”
pipe
Alleviate structural concerns
Compatible with future upgrades
Full Replacement
Replace entire system with 24” pipe
Alleviate structural concerns
Improves capacity
Pipe Replacement - Capacity Calculations
 Same procedure as existing capacity hand calculations
 𝑧 =
𝑉2
2𝑔
+
𝜌 𝑎
𝜌 𝑒
𝑧 𝑆𝐿 − 𝑧1 + 𝑧1 + ℎ 𝑓 + ℎ 𝑚 + ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
 New Qmax = 20 MGD
Z
WWTP
Pipe Replacement - Material Selection
 Ductile Iron Portion
Replace with 24” DIP
 Concrete Portion
Replace with 24” HDPE
Advantages Disadvantages
Corrosion resistance
Relies on surroundings for
rigidity
Fatigue Resistance Floats
Extended service life
Larger pipes require
heavier/thicker walls
Flexibility
Difficult to verify field joint
Pipe Replacement - Anchor Design
 Anchor Design:
Calculated Weight = 2120 lbs/Anchor
Anchor Detail – Dimensions determined from weight requirement
Detention Vault
Pipe Replacement
Mixing Zone Analysis
Design Considerations
Diffuser Design - Mixing Zone Analysis
 Purpose:
Scope of the project includes a diffuser design
Department of Ecology (DOE) requires a mixing zone analysis to receive
an NPDES permit
 Approach:
Performed analysis on current diffuser
Used the same process for new diffuser design
Diffuser Design - Mixing Zone Analysis
Steps
Wastefield plume
Profile Section
1. Determine mixing zone regions
Define acute and chronic zones boundaries as prescribed by the DOE
Permit Writer’s Manual
2. Calculate dilution factors
3. Calculate pollutant concentrations at mixing zone boundaries
4. Ensure this meets pollutant regulations
Acute Mixing Zone
• 26.4 ft.
• Aquatic criteria
considered
Chronic Mixing Zone
• 264.4 ft.
• Aquatic criteria
considered
• Human health criteria
considered for:
• Carcinogenic
pollutants
• Non-carcinogenic
pollutants
Plan View
Diffuser Design - Dilution Calculations
 Input
Ambient water specifications
current velocity and direction
ambient water density
Discharge characteristics
 flow rates
 effluent density
 diffuser depth
 port size
 port spacing
 Visual Plumes will calculate the dilution ratio of the effluent to
the water at specific distances from the diffuser
Diffuser Design - Pollutant Concentrations
 Divide effluent pollutant concentration by DF to get diluted
concentration at boundary
 Compare against regulation value
 Example:
Pollutant: Zinc
Effluent concentration = 820 µg/L
DF (Acute, Aquatic Life Criteria ) = 32
Diluted Concentration=
820 µg/L
32
= 25.6 µg/L
Regulation (Acute, Aquatic) = 90 µg/L
25.6 µg/L < 90 µg/L
PASS
Diffuser Design - Diffuser Selection
 Replaces open port diffuser with duckbill diffuser
 Duckbill valve remains closed under low flow preventing
seawater intrusion and sediment buildup
Duckbill Valve Profile
View
Diffuser Design - Plume Depth
Considerations
 To protect shellfish the plume boundary should be below -70 ft.
MLLW
-70 ft
-115 ft
PROPOSED SYSTEM
DESIGNS
Replace with 24” HDPE
Option 1
Replace with 24” HDPE
Option 2
Upsize to 24”
Option 3
Cost Estimate
Option 3
Better Effluent
Mixing
Longest Potential
Lifespan
Most Expensive
Option Summary
Option 1
Least
Expensive
Option 2
Better
Effluent
Mixing
Option 3
Better Effluent
Mixing
Longest Potential
Lifespan
Most Expensive
Option Summary
Option 1
Least
Expensive
Option 2
Better
Effluent
Mixing
Option 3
Better Effluent
Mixing
Longest Potential
Lifespan
Most Expensive
Option Summary
Option 1
Least
Expensive
Option 2
Better
Effluent
Mixing
Conclusion
Recommendation: Option 3
Highest score in matrix
Longest lifecycle
Minimal O&M
Minimal Impacts over lifespan
AWWD Response
Incorporated Option 3 design into
plant assessment project
Option 3
Full
Replaceme
nt
Extend
Diffuser
QUESTIONS?
Diffuser Design - Dilution Calculations
At 26.4 ft.
the DF is 45
Dilution with Acute Zone, Aquatic Life Criteria
Centerline
dilutionAverage
dilution

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PNCWA Presentation Final_Alderwood

  • 1. ALDERWOOD WATER AND WASTEWATER DISTRICT OUTFALL UPGRADE Seattle University Senior Design Team CEE 16.7 Kristin Ramey, Isabella Schwartz, Abbie Lorensen, Larissa Grundell
  • 2. Science and Engineering Project Center College of Science and Engineering Seattle University Faculty Advisor: Dr. Michael Marsolek Sponsor: Alderwood Water and Wastewater District
  • 4. Useful Terms Outfall: The pipe that conveys treated effluent from the wastewater treatment plant to the Puget Sound Diffuser: The last section of pipe that has openings to distribute effluent into the surrounding water body
  • 5.
  • 6. 3,100 ft - 18” Ductile Iron 1,300 ft - 18” Reinforced Concrete 80’ Diffuser 4” Portholes 1972 – CAS Facility 2013 – MBR Facility
  • 7. Project Motivation Structural Condition Internal condition unknown External inspections show signs of corrosion Pipe Capacity Expanding Service Area Corrosion of pipe to flange weld at 12 o’clock position on outfall pipe.
  • 9. Design Approach  Preliminary Assessment Condition Assessment Hydraulic Analysis  Design Selection  Design Considerations Detention Vault Design Pipe Replacement Mixing Zone Analysis  Cost & Decision
  • 12. Condition Assessment  External Dive Inspection Determine condition of submerged concrete pipe and diffuser Results: Flanged end of diffuser in "poor" condition with heavy corrosion Indicates a new diffuser should be included in all design options  Internal Camera Inspection On hold
  • 14. Hydraulic Modeling  Purpose: Determine capacity of the outfall  Approach: Use PCSWMM to model dynamic outfall hydraulics Storm Water Management Model Constructed by the EPA Use as-built information to construct model Input wet weather flow data from December 2015 Apply peaking factor
  • 17. Max Flow = 11.1 MGD Hydraulic Modeling
  • 18. Hand Calculations  Purpose: Verify capacity determined in PCSWMM modeling.  Approach: Determine the maximum allowable flow rate given the fixed changed in elevation available.  𝑧 = 𝑉2 2𝑔 + 𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟 𝜌 𝑒effluent 𝑧 𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 WWTP ZZ=169’
  • 19. Hand Calculations 𝑧 = 𝑉2 2𝑔 + 𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟 𝜌 𝑒ffluent 𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 Velocity Head Ambient /Effluent Density Difference
  • 20. Hand Calculations 𝑧 = 𝑉2 2𝑔 + 𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟 𝜌 𝑒ffluent 𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 Datum
  • 21. Hand Calculations 𝑧 = 𝑉2 2𝑔 + 𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟 𝜌 𝑒ffluent 𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 Friction Losses ℎ 𝑓 = 𝑓 𝐿 𝐷 𝑉2 2𝑔
  • 22. Hand Calculations 𝑧 = 𝑉2 2𝑔 + 𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟 𝜌 𝑒ffluent 𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 Minor Losses ℎ 𝑚 = 𝑘 𝑉2 2𝑔
  • 23. Hand Calculations  ℎ 𝑚  Horizontal bends from As-builts  Radius of curvature to determine K from tabulated values Bend Radius of Curvature K 𝑽 𝟐 𝟐𝒈 𝒉 𝒎 = 𝑲 𝑽 𝟐 𝟐𝒈 1 48 0.35 1.48’ 0.52’ 2 37.3 0.35 1.48’ 0.52’ 3 7.26 0.25 1.48’ 0.37’ 4 7.16 0.25 1.48’ 0.37’ 5 3.87 0.16 1.48’ 0.24’ 6 16.26 0.35 1.48’ 0.52’ 7 14.67 0.32 1.48’ 0.47’ 8 14.67 0.32 1.48’ 0.47’ Total 3.48’
  • 24. Hand Calculations Expansion ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 = 𝑘 𝑉2 2𝑔 𝑧 = 𝑉2 2𝑔 + 𝜌 𝑠𝑎𝑙𝑡𝑤𝑎𝑡𝑒𝑟 𝜌 𝑒ffluent 𝑧𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟
  • 25. Hand Calculations  𝒉 𝒅𝒊𝒇𝒇𝒖𝒔𝒆𝒓 Flow equally distributed at maximum capacity Conservation of mass at each port Ports modeled as expansions ℎ = 𝑘 𝑉2 2𝑔 Friction losses between ports
  • 26. Hand Calculations 𝑧 = 𝑉2 2𝑔 + 𝜌 𝑎 𝜌 𝑒 𝑧 𝑆𝐿 − 𝑧1 +𝑧1 +ℎ 𝑓 +ℎ 𝑚 +ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟  Z=169ft  Iterating with V=Q/A  𝑄 𝑚𝑎𝑥 = 11 𝑀𝐺𝐷 Z WWTP
  • 27. Capacity Conclusions  Hydraulic modeling capacity = 11.1 MGD  Hand calculations capacity = 11 MGD Corroborates modeling results  11 MGD capacity is less than the projected 15.8 MGD Design options need to account for flow attenuation
  • 28. Option 3 Full Replacement Extend Diffuser Design Selection Option 1 Partial Replacement Detention Vault Shallow Diffuser Option 2 Partial Replacement Detention Vault Extend Diffuser
  • 29. Detention Vault Pipe Replacement Mixing Zone Analysis Design Considerations
  • 30. Detention Vault Design  Purpose: Flow attenuation is required  Approach: Conservation of mass Inflow – modified wet weather time series Outflow – 10 MGD (conservative) Q=10 MGD Q=10 MGD Q=15.8 MGD 30,000 gallons
  • 31. Detention Vault Design  Constrained by Max Plan Dimensions: 100ft X 45ft Pipe diameter of surrounding pipe network: 24in  Design Plan Dimensions: 45ft X 15ft Detention Vault Plan View Vault
  • 32. Detention Vault Profile Section Detention Vault Design  Constrained by: Allowable depth 22 ft.  Design depth 10ft
  • 33. Detention Vault Pipe Replacement Mixing Zone Analysis Design Considerations
  • 34. Pipe Replacement  Purpose: Condition assessment shows concrete is deteriorating Hydraulic analysis indicates insufficient capacity  Approach: Partial Replacement Replace concrete portion with 24” pipe Alleviate structural concerns Compatible with future upgrades Full Replacement Replace entire system with 24” pipe Alleviate structural concerns Improves capacity
  • 35. Pipe Replacement - Capacity Calculations  Same procedure as existing capacity hand calculations  𝑧 = 𝑉2 2𝑔 + 𝜌 𝑎 𝜌 𝑒 𝑧 𝑆𝐿 − 𝑧1 + 𝑧1 + ℎ 𝑓 + ℎ 𝑚 + ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟  New Qmax = 20 MGD Z WWTP
  • 36. Pipe Replacement - Material Selection  Ductile Iron Portion Replace with 24” DIP  Concrete Portion Replace with 24” HDPE Advantages Disadvantages Corrosion resistance Relies on surroundings for rigidity Fatigue Resistance Floats Extended service life Larger pipes require heavier/thicker walls Flexibility Difficult to verify field joint
  • 37. Pipe Replacement - Anchor Design  Anchor Design: Calculated Weight = 2120 lbs/Anchor Anchor Detail – Dimensions determined from weight requirement
  • 38. Detention Vault Pipe Replacement Mixing Zone Analysis Design Considerations
  • 39. Diffuser Design - Mixing Zone Analysis  Purpose: Scope of the project includes a diffuser design Department of Ecology (DOE) requires a mixing zone analysis to receive an NPDES permit  Approach: Performed analysis on current diffuser Used the same process for new diffuser design
  • 40. Diffuser Design - Mixing Zone Analysis Steps Wastefield plume Profile Section 1. Determine mixing zone regions Define acute and chronic zones boundaries as prescribed by the DOE Permit Writer’s Manual 2. Calculate dilution factors 3. Calculate pollutant concentrations at mixing zone boundaries 4. Ensure this meets pollutant regulations
  • 41. Acute Mixing Zone • 26.4 ft. • Aquatic criteria considered Chronic Mixing Zone • 264.4 ft. • Aquatic criteria considered • Human health criteria considered for: • Carcinogenic pollutants • Non-carcinogenic pollutants Plan View
  • 42. Diffuser Design - Dilution Calculations  Input Ambient water specifications current velocity and direction ambient water density Discharge characteristics  flow rates  effluent density  diffuser depth  port size  port spacing  Visual Plumes will calculate the dilution ratio of the effluent to the water at specific distances from the diffuser
  • 43. Diffuser Design - Pollutant Concentrations  Divide effluent pollutant concentration by DF to get diluted concentration at boundary  Compare against regulation value  Example: Pollutant: Zinc Effluent concentration = 820 µg/L DF (Acute, Aquatic Life Criteria ) = 32 Diluted Concentration= 820 µg/L 32 = 25.6 µg/L Regulation (Acute, Aquatic) = 90 µg/L 25.6 µg/L < 90 µg/L PASS
  • 44. Diffuser Design - Diffuser Selection  Replaces open port diffuser with duckbill diffuser  Duckbill valve remains closed under low flow preventing seawater intrusion and sediment buildup Duckbill Valve Profile View
  • 45. Diffuser Design - Plume Depth Considerations  To protect shellfish the plume boundary should be below -70 ft. MLLW -70 ft -115 ft
  • 47. Replace with 24” HDPE Option 1
  • 48. Replace with 24” HDPE Option 2
  • 51. Option 3 Better Effluent Mixing Longest Potential Lifespan Most Expensive Option Summary Option 1 Least Expensive Option 2 Better Effluent Mixing
  • 52. Option 3 Better Effluent Mixing Longest Potential Lifespan Most Expensive Option Summary Option 1 Least Expensive Option 2 Better Effluent Mixing
  • 53. Option 3 Better Effluent Mixing Longest Potential Lifespan Most Expensive Option Summary Option 1 Least Expensive Option 2 Better Effluent Mixing
  • 54.
  • 55. Conclusion Recommendation: Option 3 Highest score in matrix Longest lifecycle Minimal O&M Minimal Impacts over lifespan AWWD Response Incorporated Option 3 design into plant assessment project Option 3 Full Replaceme nt Extend Diffuser
  • 57. Diffuser Design - Dilution Calculations At 26.4 ft. the DF is 45 Dilution with Acute Zone, Aquatic Life Criteria Centerline dilutionAverage dilution

Editor's Notes

  1. LG
  2. LG
  3. LG
  4. LG Picture from http://discoverycwa.org/Columbia_River_Outfall_Project.html
  5. Need a zoomed out map for WEFTEC – probably improve these screenshots
  6. LG
  7. LG 20 miles north of Seattle
  8. LG Outfall has design capacity of 13.2
  9. LG
  10. LG Current and future Qmax
  11. LG
  12. LG
  13. LG
  14. AL
  15. AL
  16. AL Define PCSWMM: used for x made by EPA, private model company that…
  17. AL
  18. AL Arrows, zoom in on red box
  19. AL
  20. AL
  21. AL
  22. AL
  23. AL
  24. AL
  25. AL
  26. AL
  27. AL
  28. AL
  29. AL
  30. Based on the inspection, hydraulic modeling, and results of literature review the team chose 4 options to bring to 30% design Conceptual level drawings Bulk cost estimations Justification of each design option
  31. KR
  32. Arrows on the plan view, where the outfall is Add zoom out view from report
  33. KR
  34. Include map (profile) of concrete section, show what part of the pipe we are focused on (context for audience) This material is most commonly used now
  35. KR 𝑉 2 2𝑔 , ℎ 𝑓 , and ℎ 𝑚 changed due to the increased diameter. Determined ℎ 𝑑𝑖𝑓𝑓𝑢𝑠𝑒𝑟 using empirical formulas and charts reported in the Journal of Hydraulic Engineering for duckbill diffusers.
  36. Concrete portion offshore
  37. KR Simplification- saying anchors support 80% 0.8 is a correction factor due to float in place
  38. IS
  39. Average dilution over the wastefield plume
  40. The aquatic life criteria is based on the time of exposure that the organisms are being exposed to a certain pollutant concentration. Human health criteria is based off of daily exposures, ingestion rate, and cancer risk for carcinogenic chemicals.
  41. The design flow, current speed, and density stratification must be chosen from the conditions set by the DOE Permit Writer’s Manual, Appendix C
  42. Mention that I calibrated with hand calculations, showed agreement That concludes option 1, option 1 includes (Reiterate option 1), now we will talk about option 2
  43. “It is best practice to ensure that the plume boundary is 70 feet below the water surface in order to protect shellfish habitats.” Geoduck, hard-shell clam, and Dungeness crab reside within the mixing zones of our outfall. In order to ensure plume depth below 70 ft. with 8 portholes at 12 ft. spacing the diffuser needs to be at a depth of 115 ft. which means extending pipe 120 ft.
  44. IS Summarize option 2, replace concrete…. Same as option 1, extended outfall deeper to protect shellfish Next Option is.
  45. KR
  46. KR Outfall has design capacity of 13.2
  47. KR Outfall has design capacity of 13.2
  48. KR Outfall has design capacity of 13.2
  49. LG Show one detail cost, for each option we included material cost and construction costs Figure out which costs are the right ones
  50. LG Based on the inspection, hydraulic modeling, and results of literature review the team chose 4 options to bring to 30% design Conceptual level drawings Bulk cost estimations Justification of each design option
  51. LG Based on the inspection, hydraulic modeling, and results of literature review the team chose 4 options to bring to 30% design Conceptual level drawings Bulk cost estimations Justification of each design option
  52. Based on the inspection, hydraulic modeling, and results of literature review the team chose 4 options to bring to 30% design Conceptual level drawings Bulk cost estimations Justification of each design option
  53. LG
  54. LG
  55. Add picture
  56. Based on the inspection, hydraulic modeling, and results of literature review the team chose 4 options to bring to 30% design Conceptual level drawings Bulk cost estimations Justification of each design option
  57. Based on the inspection, hydraulic modeling, and results of literature review the team chose 3options to bring to 30% design Conceptual level drawings Bulk cost estimations Justification of each design option
  58. Based on the inspection, hydraulic modeling, and results of literature review the team chose 4 options to bring to 30% design Conceptual level drawings Bulk cost estimations Justification of each design option
  59. Option 1: Least Expensive since not replacing onshore section or extending diffuser Option 2: Better effluent mixing due to extending diffuser
  60. What about this research affects the design
  61. Animation where one row pops up, or just have one row