alternative dewatering technologies gillette 200908 pncwa.pdf

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Improving Efficiency of Dewatering Alternatives to Conventional Dewatering Technologies Robert Gillette, PE, BCEE Steve Swanback, PE Rebecca Overacre, PE 2009 PNCWA Webinar Recent Developments In Biosolids Management Processes

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  • Improving Efficiency of DewateringAlternatives to Conventional Dewatering

    Technologies

    Robert Gillette, PE, BCEESteve Swanback, PE

    Rebecca Overacre, PE

    2009 PNCWA Webinar Recent Developments In

    Biosolids Management Processes

  • sgs809pncwa.ppt/2

    Outline

    1. Screw press technologya. Performance survey resultsb. Pilot testing resultsc. Lifecycle cost evaluation (Class A and Class B)d. Design considerations

    2. Rotary fan press technologya. Performance survey resultsb. Pilot testing resultsc. Lifecycle cost evaluation (Class A and Class B)d. Design considerations

    3. Overview of R&D Technologies

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    Screw Press Technology

  • sgs809pncwa.ppt/4

    Screw Press Manufacturers

    Huber (inclined)

    FKC (horizontal)

  • Screw Press General Description

  • Dewatering by Volume Reduction

  • Screw Press Expanded View

  • Screw Press Expanded ViewClass A Option

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    Flow Schematic

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    Tallahassee, FL, FKC InstallationTallahassee, FL, FKC Installation

    FKC Screw Press

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    FKC Screw Press

    Petaluma, CA, FKC InstallationPetaluma, CA, FKC Installation

  • sgs809pncwa.ppt/12

    Huber Press

    Magna, UT, Huber InstallationMagna, UT, Huber Installation

  • sgs809pncwa.ppt/13

    Huber Press

    Maine, Huber InstallationMaine, Huber Installation

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    Performance Survey

  • sgs809pncwa.ppt/15

    Survey of 22 Full Scale Installations The Cake Solids Concentration Depends on Type of Sludge

    Type of Sludge Screw Press Cake (% solids)FKC 15 20

    FKC (with steam and lime) 20 45Huber 12 20FKC 21 28

    WAS

    Huber 22 25Raw Huber 18 40

    PS+WASFKC > 18

    Huber 19 24Aerobically Digested

    Anaerobically Digested

    FKC 17 25Anaerobically Digested Huber 13 16

    Raw

  • sgs809pncwa.ppt/16

    Survey of 22 Full Scale Installations The Median Cleaning Schedule is Once Per Week

    Manual Cleaning Schedule(times per month)

    0

    5

    10

    15

    20

    25

    30

    1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22Facility Number

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    Case Study St Petersburg, FL

  • sgs809pncwa.ppt/18

    Pilot Results - Projected Full Performance St. Petersburg

    Manufacturers Recommendations

    Screw PressBelt Press CentrifugeClass B Class A

    Minimum Cake Solids Concentration (% solids)

    18 21 16 33

    Maximum Polymer Dosage (lb/DT)

    19 25 30 33

    Minimum Solids Capture (%)

    95 95 90 90

    Parameter

  • sgs809pncwa.ppt/19

    Relative Cost Comparison

    BFP Centrifuge Screw Press

    Capital Cost $ $$$ $$

    Building Modifications $ $$ $$

    Odor Control $$$ $ $

    Power $ $$$ $

    Maintenance $$ $$ $

    Chemical $$ $$$ $$

    Hauling $$ $ $$

    Disposal $$ $ $$

  • sgs809pncwa.ppt/20

    Performance Comparison

    Will Vary Depending on Conditions!!!Will Vary Depending on Conditions!!!

    BFP Centrifuge Screw Press

    % Solids Produced ++ +++ +

    Filtrate/Centrate Quality ++ ++ +

    Reliability ++ ++ +++

    Operator Attention Required + ++ +++

    Ease of startup and shutdown ++ + ++

  • sgs809pncwa.ppt/21

    Design Considerations

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    Design Considerations

    Lead time (from Japan or Germany): prepurchase?

    Custom design varying dimensions until shop drawing

    Performance guarantee and penalty for non-compliance

    Basis of design Loading & capacity: pilot test Run time, unattended operation

    Effect of rising steel costs units all SST

  • sgs809pncwa.ppt/23

    Design Considerations, Continued

    Need headroom if RST on mezzanine Monorail/overhead crane Building considerations footprint

    requirement or outside Provision for Class A in future Cake conveyance options affects layout

  • sgs809pncwa.ppt/24

    Design Parameters

    Range of Capacity: Up to 8.5 DT/day At nominal speed

    RST output (% Solids): around 4% Screw Press output (% Solids): 15 28% Polymer consumption: 20 40 lb/DT Detention time: approximately 4 hours Motor speed: as low as 0.3 rpm Motor HP largest unit is 7.5 HP

  • sgs809pncwa.ppt/25

    Rotary Press Technology

  • sgs809pncwa.ppt/26

    Rotary Press Manufacturers

    Fournier

    Prime Solutions

  • sgs809pncwa.ppt/27

    Rotary Press Schematic

  • sgs809pncwa.ppt/28

    Process Cutaway

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    Design Parameters

    Range of Capacity: 7-250 gpm Cake % Solids: 12 28% Detention time: N/A Motor speed: as low as 1-3 rpm Motor HP: 5-20 HP

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    Fournier Rotary Press

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    Size Compared to Other Technologies

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    Multiple Channels on Single Drive

  • sgs809pncwa.ppt/33

    Fournier Rotary Press Pilot Test

  • sgs809pncwa.ppt/34

    Prime Solutions Rotary Fan Press

  • sgs809pncwa.ppt/35

    Performance Survey

  • sgs809pncwa.ppt/36

    Survey Results

    Facility EquipmentFacility

    Size (mgd)

    Solids Type Incoming % TS

    Discharge % TS

    Raiford, FL Prison WWTP

    Rotary fan press 1.1 Extended aeration

    1.6-2.5 19-22

    Front Royal, VAMunicipal WWTP

    Rotary fan press 3.3 Thermophilic Anaerobic Digestion

    3.5 25

    Fairfield, CAMunicipal WWTP

    Rotary fan press 15.5 Conventional Anaerobic Digestion

    2 17

    Lafayette, TNMunicipal WWTP

    Rotary press 0.5 Conventional Anaerobic Digestion

    1.0-1.5 25

    Portland, MEMunicipal WWTP

    Rotary press 19.8 Thickened PS/WAS

    3-6 19-25

    Hampton, NHMunicipal WWTP

    Rotary press 2.5 Septage/PS/WAS

    6-8 26-28

    Murfreesboro, TNMunicipal WWTP

    Rotary press 15 PS/WAS 0.8-1 12-14

    Scarborough, MEMunicipal WWTP

    Rotary press 1.4 Thickened PS/WAS

    3 28

  • sgs809pncwa.ppt/37

    Rotary Dewatering Features

    Low speed, low vibration, low shear Uses less energy than centrifuges or BFPs Modular Small footprint Minimal start-up and shutdown time Minimal moving parts Odors contained

  • Questions?

    Bob [email protected]

    916-565-4888

  • sgs809pncwa.ppt/39

    R&D Technologies

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    EKG Technologies

    Electrokinetic Geosynthetics (EKG) Technology Theory Electro-osmotic principle

  • sgs809pncwa.ppt/41

    Uses of EKG Technology

    Ashbrook Product Anaerobically/Aerobically Digested

    Sludge Fresno England

    Alternative to conventional dewatering

    Siemens Product Secondary dewatering process Alternative to sludge drying

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    Siemens ELODE Technology

  • sgs809pncwa.ppt/43

    Siemens ELODE Technology

  • sgs809pncwa.ppt/44

    Siemens ELODE Technology

  • Questions?

    Bob [email protected]

    916-565-4888

    Improving Efficiency of DewateringAlternatives to Conventional Dewatering TechnologiesOutlineScrew Press ManufacturersScrew Press General DescriptionDewatering by Volume ReductionScrew Press Expanded View Screw Press Expanded ViewClass A OptionFlow SchematicFKC Screw PressFKC Screw PressHuber PressHuber PressSurvey of 22 Full Scale Installations The Cake Solids Concentration Depends on Type of SludgeSurvey of 22 Full Scale Installations The Median Cleaning Schedule is Once Per WeekPilot Results - Projected Full Performance St. PetersburgRelative Cost ComparisonPerformance ComparisonDesign ConsiderationsDesign Considerations, ContinuedDesign ParametersRotary Press ManufacturersRotary Press SchematicProcess CutawayDesign ParametersFournier Rotary PressMultiple Channels on Single DriveFournier Rotary Press Pilot TestPrime Solutions Rotary Fan PressSurvey ResultsRotary Dewatering FeaturesQuestions?Bob [email protected] TechnologiesUses of EKG TechnologySiemens ELODE TechnologySiemens ELODE TechnologySiemens ELODE TechnologyQuestions?Bob [email protected]