clif bar pretreatment
play

Clif Bar Pretreatment Larry Rupp and Jason King Keller Associates - PowerPoint PPT Presentation

Pacific Northwest Pretreatment Workshop September 12, 2017 Clif Bar Pretreatment Larry Rupp and Jason King Keller Associates Meridian, Idaho 1 CITY OF LEWISTON WWTP 2020 IMPROVEMENTS City of Twin Falls Population: 48,260* Major


  1. Pacific Northwest Pretreatment Workshop September 12, 2017 Clif Bar Pretreatment Larry Rupp and Jason King Keller Associates Meridian, Idaho 1 CITY OF LEWISTON WWTP 2020 IMPROVEMENTS

  2. City of Twin Falls • Population: 48,260* • Major Industries • Glanbia Nutritionals (cheese) • AmeriPride (uniforms) • KapStone (cardboard) • Independent Meat Co. (pork) • Conagra (potato)** • Chobani (dairy)** • WWTP Capacity * City also treats the wastewater for the City of Kimberly (Pop. ~3,700) ** City owns and operates the pretreatment system at this industrial plant

  3. Clif Bar Bakery/Pretreatment Facility • 1st Clif Bar-Owned Bakery • Pretreatment Facility constructed at same time as Bakery • City to own and operate Pretreatment Facility • Clif Bar potentially to own and operate in the future • Intermittent flows with variable concentrations, pH, and temperature • Expansion potential

  4. Preliminary Design Considerations • Process understanding • Sampling • Design criteria • Preliminary discharge permit • Pretreatment options • Pretreatment selection

  5. Process Understanding • Collaboration with Indianapolis Facility and Clif Bar • Historical sampling results • 10-day sampling procedure • Biochemical oxygen demand (BOD) • Total suspended solids (TSS), • Volatile suspended solids (VSS) • Chemical oxygen demand (COD) • Soluble COD • Total Kjeldahl nitrogen (TKN) • Ammonia (NH3-N) • Oil and grease (O&G) • Flow • Temperature

  6. Historical Sampling Results

  7. 10-Day Sampling Results

  8. Design Criteria • Influent Design Criteria • Average Day Flow – 14,800 gpd • Maximum Month Flow – 23,000 gpd • Maximum Day Flow – 38,800 gpd • Peak Hour Design Flow – 240 gpm • Design Influent BOD 5 Concentration – 4,160 mg/L • Design Influent TSS Concentration – 1,100 mg/L • Design Influent O&G Concentration – 90 mg/L • Other considerations • Influent temperature • Influent pH

  9. Pretreatment Options Percentage 1. UASB 2. UAFF 3. UASB/ PMT Factors 4. SBR 5. TF/SC 6. AS 7. MBBR 8. RBC 9. MBR 10. Evaporator UAFF Sustainability 10% 4 4 4 3 3 3 3 3 3 1 Experience 5% 4 4 4 4 4 4 3 1 1 1 Operability 10% 3 3 3 4 3 3 3 2 1 2 Process Stability 10% 3 3 3 3 4 3 4 2 3 4 Ease of Startup 5% 3 3 3 4 4 4 4 3 3 4 Toxic Sensitivity 10% 2 2 2 4 4 4 4 3 3 4 Capital Cost 5% 2 2 2 3 3 3 3 3 2 1 Installation Cost 5% 3 3 3 3 3 3 3 3 2 5 O&M Cost 9% 3 3 3 3 3 3 3 3 1 1 Energy Cost 5% 3 3 3 3 3 3 3 3 2 1 Sewer Fee Cost 9% 4 4 4 4 4 4 3 2 5 5 Dewatering Cost 5% 4 4 4 3 3 3 3 3 3 2 Footprint 2% 4 4 4 3 3 2 3 1 4 5 Expandability 10% 4 4 4 3 3 2 3 1 2 5 Total 100% 3.26 3.26 3.26 3.39 3.39 3.17 3.25 2.37 2.47 2.94

  10. Anaerobic (UASB) EQ TANK WASTE FLOW UASB SBR FROM CLIF BAR TO CITY FACILITY SCREEN Adv. • Effective for high-strength wastewater • Not affected by O&G Disadv. • Microorganisms do not respond quickly to loading changes • Requires heating • Requires gas collection, flaring

  11. TF/SC TRICKLING EQ TANK SOLIDS WASTE FLOW FILTER CONTACT CLARIFIER FROM CLIF BAR TO CITY FACILITY SCREEN Adv. • Effective • Stable • Handles variable loads/ flows well Disadv. • Requires additional pumping and building space • Influenced by temperature and pH changes • High capital cost

  12. SBR EQ TANK WASTE FLOW SBR FROM CLIF BAR TO CITY FACILITY SCREEN Adv. • More stable than anaerobic treatment options • Not sensitive to toxins • Cost effective • Smaller footprint Disadv. • Expensive expansion • Nutrient, pH, and O&G control important • Requires careful solids management • Not as stable as TF/SC or MBBR options

  13. Selected Alternative - MBBR EQ TANK WASTE FLOW MBBR DAF FROM CLIF BAR TO CITY FACILITY SCREEN Adv. • Stable • Cost effective • Not sensitive to toxins • Effective at removing O&G Disadv. • Nutrient, pH, and O&G control important

  14. Industrial Discharge Permit Development • EPA Requirements • WWTP Capacity • Collection System Capacity • Compliance point • Startup/Monitoring

  15. Compliance Point • Influent vs effluent • Design concerns • Flow measurement with intermittent flow • Process concerns • Temperature and pH • Equalization tanks

  16. Compliance • Influent manhole • 24-hour composite sampler for BOD 5 , TSS • FOG grab sample • Influent flow rate (Parshall flume), pH, temperature sensors upstream of EQ – continuous readings • If temperature or pH exceeds criteria, EQ pumps will automatically shut off to protect MBBR • Effluent manhole • 24-hour composite sampler for BOD 5 , TSS • FOG grab sample • Effluent flowmeter (submerged magmeter) downstream of DAF

  17. Discharge Permit

  18. Design Overview

  19. Headworks • Materials of construction • Monitoring • Influent Sampling

  20. Equalization Tanks • Operational Flexibility • Series • Parallel • Isolation • Monitoring • pH/Temperature • Process Control • Chemical Feed Pumps • MBBR Feed Pumps

  21. MBBR Tanks and DAF • Tank Bypass • Recycle effluent • Effluent Monitoring • Composite sampler

  22. Solids Handling • Sludge Disposal • Liquid • Dewatered

  23. Construction • Schedule • Designed in 6 months • Construction in 12 months • Pre-purchase equipment • Pre-qualify contractors • Design review meetings

  24. Construction • Treatment during construction • Temporary tanks • Bypass pumping • Chemical adjustment • Coordination • Clif Bar • City • Contractor • Keller • Temporary discharge permit

  25. Temporary Discharge Permit (Effluent)

  26. Initial Startup • Seed sludge • Recycling effluent • Supplement food source • Foam Control

  27. Monitoring - Flow

  28. Monitoring - BOD

  29. Monitoring - TSS

  30. Questions?

Download Presentation
Download Policy: The content available on the website is offered to you 'AS IS' for your personal information and use only. It cannot be commercialized, licensed, or distributed on other websites without prior consent from the author. To download a presentation, simply click this link. If you encounter any difficulties during the download process, it's possible that the publisher has removed the file from their server.

Recommend


More recommend