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Full Scale and Demonstration Primary Filter Projects Demonstrate Great Promise Presented at North Texas Section WEAT Seminar| February 13, 2018 Presented by Onder Caliskaner, Ph.D., P.E. Co-authors George Tchobanoglous, Ph.D., P.E., Terry Reid, P.E., Brian Davis, P.E., Zoe Wu, Ryan Young, P.E., Eassie Miller, P.E., Ryan Atterbury, P.E., Catrina Paez

Full Scale and Demonstration Primary Filter Projects ... · 5 142-360 213 89-210 122 43% CBOD 5 170 170 99 99 42% Soluble BOD 5 81 81 71 71 13% Ammonia 49-81 66 28-83 62 6% TKN 64-110

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  • Full Scale and Demonstration Primary Filter Projects Demonstrate Great Promise

    Presented atNorth Texas Section WEAT Seminar| February 13, 2018

    Presented byOnder Caliskaner, Ph.D., P.E.

    Co-authorsGeorge Tchobanoglous, Ph.D., P.E., Terry Reid, P.E., Brian Davis, P.E. , Zoe Wu, Ryan Young, P.E., Eassie Miller, P.E., Ryan Atterbury, P.E., Catrina Paez

  • Acknowledgements

    • California Energy Commission

    • Full scale installation - Linda County Water District

    • Pilot / Demonstration Sites - Los Angeles County Sanitation District, City and County of Honolulu, Rockford (IL), Oak Hill (WV)

    • Peer Review - Prof. Emeritus George Tchobanoglous / UC Davis

    • Primary Filter System: Aqua Aerobics Systems, Inc.

    • Thickening System: Process Wastewater Technologies, Inc.

    • Third party verification - Base Energy

    • Kennedy Jenks CA and HI offices

    2

  • Topics

    • Primary Filtration for Carbon Diversion • Background

    • Objectives

    • Pilot and Demonstration Projects

    • First Full Scale Installation

    • Conclusions

    • Questions / Discussion

    3

  • Conventional and Modified Wastewater Treatment Flow Diagrams - Primary Filtration

    4

    Modified Wastewater Treatment Flow Diagrams

    Conventional Wastewater Treatment Flow Diagrams

    Tertiary Effluent Filter

    FilteredPrimary Effluent

    Primary Filter

    Aerated Activated

    Sludge Basin (Reduced Size)

    Smaller Blower (Reduced Air Demand)

    Increased Digester Gas

    Tertiary Effluent Filter

  • 5

    Primary Filtration

    Primary filtration is another emerging technology based on successful demonstration of primary effluent filtration for 2 years

    • Similar objectives (as PEF) for energy savings and plant capacity increase

    • Replaces primary clarifiers with primary filters• 50 – 60% higher TSS/VSS removal efficiency

    • 40 – 50% higher BOD/COD removal efficiency

    • 70 – 80% reduction in footprint

  • Primary Filter Comparison

    6

    Tertiary Filter Primary Filter

  • 7

  • Operational simplicity / flexibility

    Treatment performance

    Footprint

    Capital and operational costs

    Carbon management / diversion

    What is the most important criteria for design and operation of a primary

    treatment system?

    8

  • Primary Filtration Main Objectives and Advantages✓Higher removal of organic load (BOD):

    Secondary treatment capacity

    Aeration power consumption

    Secondary treatment volume requirement

    ✓Reduction in primary treatment area

    ✓Higher removal of volatile suspended solids (VSS)

    Digester biogas energy production

    ✓Particle size modification: biological treatment efficiency

    9

  • City and County of HonoluluSand Island Primary Filtration Testing (August 2016 – May 2017)

    10

    Average Flow Design Capacity: 90 MGD

    Testing of Filtration for 3 MGD Sidestream Treatment System

    Testing of Primary Filtration

  • City and County of Honolulu Sand Island Sidestream Filtration Testing Results

    11

    Combined Sidestream Filtration System Concentration Ranges and Average Removal Performances

    Constituent

    Sidestream, mg/L

    Filtered Sidestream, mg/L

    Typical Average Removal Efficiency

    Range Average Range Average Percent

    VSS 100-510 223 10-140 75 66%

    TSS 240-590 325 81-170 123 62%

    COD 400-820 557 130-500 300 46%

    BOD5 142-360 213 89-210 122 43%

    CBOD5 170 170 99 99 42%

    Soluble BOD5 81 81 71 71 13%

    Ammonia 49-81 66 28-83 62 6%

    TKN 64-110 91 35-91 71 21%

  • City and County of Honolulu Sand Island Primary Filtration Testing Results

    12

    Primary Influent Filtration System Concentration Ranges and Average Removal Performances

    Constituent Primary Filter Influent, mg/L Primary Filter Effluent, mg/LConstituent Average Removal Efficiency

    Range Average Range Average Percent

    VSS 110-190 155 17-40 27 82%

    TSS 120-260 188 24-62 41 78%

    COD 230-1000 389 67-270 178 54%

    BOD5 110-210 154 55-86 73 53%

    Soluble BOD5 47-63 55 38-56 47 15%

    Soluble COD 100 100 96 96 4%

    TKN 22-27 24 20-26 22 8%

  • City and County of Honolulu - Sand Island Primary Filtration Particle Size Distribution Results

    13

    Percentage of particles smaller than the indicated size

    Particle size

    Date Sample Type 2 µm 5 µm 10 µm 20 µm

    5/4/2017 Influent 1.3 2.2 5.2 12.8

    5/4/2017 Effluent 12.4 17.2 30.2 52.2

    DateMean particle size

    (volumetric), Influent (µm)

    Mean particle size (volumetric), Effluent

    (µm)Relative change, percent

    5/4/2017 96.6 20.4 79%

    Mean particle size reduced by approximately 80 percent

  • Los Angeles County Sanitation District - City of Lancaster Primary Filtration Demonstration Project (November 2016 - November 2017)

    14

    Tertiary Treatment – 18 MGD

    Serves approximately 160,000 people

  • Los Angeles County Sanitation District - City of Lancaster - Primary Filtration Demonstration Project

    15

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    mo

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    S (

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    /L)

    Lancaster Primary Filter Daily Average TSS

    TSS Removal (%) Filter Influent TSS Filter Effluent TSS

    Avg Influent TSS Avg Effluent TSS Avg Removal (%)

    Avg Inf TSS: 392 mg/L

    Avg Eff TSS: 56 mg/L

    Avg Removal: 86%

  • Los Angeles County Sanitation District - City of Lancaster - Primary Filtration Demonstration Project

    16

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    11/8/16 12/28/16 2/16/17 4/7/17 5/27/17 7/16/17 9/4/17

    Wa

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    er

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    Lancaster Primary Filter Waste Ratios

    Waste Ratio (%) Filtered Effluent (gal/d) BW Volume (gal/d) SW Volume (gal/d)

    Average Volumes

    Effluent: 35,527 gal

    BW: 3,713 gal

    SW: 1,852 gal

    BW+SW: 5,430 gal

  • First Full Scale InstallationLinda County Water District WWTP

    17

    Average Flow : 1.2 MGD (2016-2017)

    2.5 MGD (2018-2019)

    Downstream Process:

    Nitrogen Removal, Tertiary Filtration

    LCWD WWTP

    Sacramento

  • First Full Scale InstallationLinda County Water District WWTP

    18

    Primary Filter Capacity:

    Average Flow - 1.5 MGD

    Peak Flow - 3 MGD

  • First Full Scale Installation –Linda County Water District WWTP

    19

    Design Completed in June 2016

    Construction Started in October 2016

    Started-up in August 2017

  • First Full Scale Installation Linda County Water District WWTP

    20

  • First Full Scale InstallationLinda County Water District WWTP

    21

    Primary Clarifier –average flow capacity 5 MGD

    Primary Filter – average flow capacity 1.5 MGD

  • First Full Scale InstallationLinda County Water District WWTP

    22

  • First Full Scale Installation Primary Filter – Cloth Depth Filter

    23

  • First Full Scale Installation Primary Filter – Cloth Depth Filter

    24

    Filter Influent Filter Effluent

    Influent Effluent

  • First Full Scale Installation Thickening System - Volute Thickener

    25

  • First Full Scale Installation Thickening System – Phase Separator

    26

  • Flow Diagram– Linda County Water District WWTP

    27

  • Primary Filter System Initial PerformanceLinda County Water District

    28

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    Re

    mo

    va

    l (%

    )

    TS

    S (

    mg/L

    )

    LCWD Primary Filter Daily Average TSS

    TSS Removal (%) Filter Influent TSS Filter Effluent TSS

    Avg Influent TSS Avg Effluent TSS Avg Removal (%)

    Avg Inf TSS: 276 mg/L

    Avg Eff TSS: 48 mg/L

    Avg Removal: 83%

  • Summary of Average Wastewater Characteristics (Linda County Water District)

    29

    * Based on historical data at LCWD WWTP

    Parameter

    Primary Clarifier

    Influent

    Primary Clarifier

    Effluent Primary Filter

    Avg Value (mg/L) % Removal * Avg Value (mg/L) % Removal

    BOD5 220 26% 106 52%

    Soluble BOD5 51 0% 51 0%

    COD 501 24% 254 49%

    TSS 200 50% 40 80%

    VSS 188 47% 38 80%

    TKN 46 0% 41 11%

  • Conclusions

    30

    Primary filtration is an emerging advanced primary treatment technology for increased carbon diversion

    Replaces primary clarifiers with primary filters:

    TSS/VSS removal efficiency 50-70 percent

    BOD/COD removal efficiency 40-55 percent

    Footprint 80 to 85 percent

  • Conclusions

    Actual performance/feasibility will be site specific

    • Plant size

    • Influent characteristics

    • Efficiency of existing aeration system

    • Available capacity

    • Power cost

    • Use of digester gas

    31

  • Conclusions

    Observed/expected side benefits:

    • Response to upset conditions

    • Load equalization

    • Overall improvement in downstream biological treatment

    Other considerations:

    • Impact on denitrification

    • Comparison with other technologies with similar concept

    • Material/enclosure considerations compared to tertiary filters

    • Digester design considerations

    32

  • ConclusionsPrimary Filtration Potential Benefits

    25-30 % in aeration costs

    20-25 % in secondary treatment capacity

    30-40 % in digester gas energy production

    80 - 85 % Primary treatment footprint

  • Estimated Savings

    34

    Savings Per MGD

    Construction Cost Saving $600,000

    Annual O&M Costs Saving $30,000

    Net Present Value $1,100,000

    Assuming a 10% implementation of the (primary filtration technology) in US, the estimated present value of the savings will be approximately $5B

    Wastewater Treatment System Cost Savings Resulting from Primary Filtration

  • QUESTIONS & COMMENTS

    35

    Onder Caliskaner

    E-mail: [email protected]

    Phone: (916)-858-2738