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Optimization for Centrifuge Dewatering
WEFTEC New Orleans, Louisiana
Rashi Gupta, P.E.
Steve Walker, CWP
Carollo Engineers
September 28, 2016
Filename.ppt/2
Questions to Answer Today…
• Why is optimization important?
• What should I consider within my dewatering
process?
• How do I systematically optimize the process?
Filename.ppt/3
Dewatering Costs a Lot
Annual Dewatering Cost = $3.7M
Case Study 1
Filename.ppt/4
Increasing Dryness Can Save on Hauling $
~$80,000 between 20% and 22%
per centrifuge at 250 gpm; 2% feed
Case Study 1
Filename.ppt/5
Reducing Polymer Can Save on Chemical $
~$20,000 between 38 lb act/DT
and 40 lb act/DT per centrifuge at
250 gpm; 2% feed
Case Study 1
Filename.ppt/6
Maximizing Dryness Not Always the Answer
Case Study 2
Filename.ppt/7
Dewatering Costs – Case Study 1B from July
2011 to September 2014
Filename.ppt/8
Dewatering Performance – Case Study 1B
Averages:
22.0% Cake
99% Capture
38.3 lb act/DT
Filename.ppt/9
Case Study 1B Dewatering Costs – Before and
After
• 2011-2014 Monthly Costs
− $33,000 Hauling
− $19,000 Polymer
− $52,000 Total
• 2015 Monthly Costs
− $29,500 Hauling
− $15,600 Polymer
− $45,100 Total
Filename.ppt/10
DEWATERING SYSTEM
CONSIDERATIONS
Filename.ppt/11
Centrifuge Features
Polymer
Addition
Sludge Feed
Cake
Discharge
Centrate
Discharge
Centrifuge Main
Drive
Scroll Back
Drive
Ref: Centrisys
Filename.ppt/12
• Dewatered cake
• Centrate
• Sludge:
− Anaerobically or
aerobically digested
− Primary sludge
− Thickened waste
activated sludge
− Chemically enhanced
• Polymer solution
Centrifuge Inputs and Outputs
Inputs Outputs
Filename.ppt/13
Operational Targets to Track Performance
Criteria Units Importance
Cake dryness %TS • Disposal costs
• Water equals weight and takes up
volume
Centrate
quality
%TS
or
TSS, mg/L
• Impact on liquid treatment
processes
• Re-treatment of solids (thickening,
digestion and dewatering)
• Impact of inert solids on activated
sludge mass calculations
Throughput lb/hr and gpm • Centrifuge capacity
• Operations and hauling logistics
Polymer dose Active pounds
per dry ton
• Operating costs
Filename.ppt/14
Dewatering Feed Characteristics Matter
• Important Sludge Feed Characteristics
− PS:TWAS ratio in digester feed, by mass
 Important because PS is MUCH easier to digest and
dewater than TWAS
 The higher the PS:TWAS ratio, the better the
dewaterability
− Volatile solids content
 Generally, higher VS = More difficult to dewater
− Biological phosphorous removal
− Divalent cations (Ca2+, Mg2+) vs Monovalent (Na+, K+)
− Sludge feed temperature
Filename.ppt/15
PS:TWAS Ratio Matters a Lot
Case Study 1A Case Study 1B Case Study 1C Case Study 1D
Highest PS:TWAS
Lowest Polymer
Most Dry
Filename.ppt/16
Understanding Polymer Basics Necessary to
Assess Effectiveness
• “Neat” polymer
− Oil, surfactants, water, and polymer
(emulsion as delivered)
• “Active”
− What’s doing the work
− 40-50% typical for emulsion
− 90%+ typical for dry
Filename.ppt/17
Many Pieces to the Polymer Puzzle
• Procure the right polymer
• Select right dilution concentration
for polymer solution
• Produce fully activated solution
• Find best polymer injection location
• Maintain req’d water pressure
• Check water characteristics (chlorine,
hardness, temperature)
• Optimize polymer dose
Filename.ppt/18
• Loading rates (throughput)
• Bowl speed (G-force)
• Conveyor/scroll speed (differential
speed) and torque
− Newer centrifuges are controlled using
a % torque or pressure setpoint
− To achieve the desired
torque/pressure, the PLC adjusts the
scroll speed
• Weir plates
− Set the pool depth within the bowl
Centrifuge Parameters that Affect
Performance
Filename.ppt/19
Throughput
• Need to stay within loading capacity
• Changing solids concentration impacts loading
Filename.ppt/20
Throughput
Case Study 1A: Data from January 2015 – April 2015
Filename.ppt/21
OPTIMIZATION APPROACH
Filename.ppt/22
Process Optimization
• Achieve:
− Desired cake dryness and
centrate quality
− Lowest polymer cost
− Maximum throughput and
efficiency
• Balancing act: Maximize one or
more of the process
parameters, while keeping all
others within their constraints
Filename.ppt/23
Parameters used for Optimization
• Type of polymer
• Polymer dose
• Polymer dilution/solution concentration
• Polymer injection point
• Centrifuge torque/pressure
• Centrifuge pond depth
• Centrifuge bowl speed
• Sludge feed (throughput)
• Sludge characteristics
Filename.ppt/24
Process Optimization – Polymer Selection
• Selecting the right polymer:
− Site specific jar testing by different
suppliers
 High molecular weight for
centrifuge dewatering
 High charge density helps with
dewatering of secondary sludges
 Cationic
− Site specific full scale tests with
promising polymers
• Full scale tests can identify more
effective polymers
• Polymer effectiveness can be
gauged through viscosity
Filename.ppt/25
Polymer Contract Flexibility
• Establish Primary and Alternate supplies
− Use two different suppliers rather than two different
products from the same supplier
• Determine if seasonal constraints support
alternatives. For example:
− An emulsion polymer may be more cost effective in
winter months
− A dry polymer may be more cost effective in the
other months
Filename.ppt/26
Test Methodology – Phase 1 (Polymer Dose)
• Batch polymer at preferred solution strength
• Set sludge feed rate
• Enter typical torque setpoint and bowl speed
• Set lowest polymer feed rate
• Run for a standard time (i.e., 45 minutes)
• Sample feed, centrate and cake for TS/TSS.
− Feed solids concentration used to calculate throughput
• Run through sequence for at least 5 polymer feed
rates
• Calculate associated dose and plot results
Filename.ppt/27
Polymer Optimization
Filename.ppt/28
Performance Curve - Polymer
80
82
84
86
88
90
92
94
96
98
100
10
15
20
25
30
35
1 2 3 4 5 6
lb/tonor%TS
Dose v. % Recovery
Dose, lb/ton Cake Recovery
24
Filename.ppt/29
Test Methodology – Phase 2 (Torque)
• Set sludge feed rate
• Set polymer solution feed rate for the “ideal” polymer
dose
• With sludge and polymer feed rates “locked in”,
adjust % torque setpoint
• Run for a standard time (i.e., 45 minutes)
• Sample feed, centrate and cake for TS/TSS.
• Run through sequence for at least 5 torque setpoint
• Plot results
Filename.ppt/30
Performance Curve - Torque
80
82
84
86
88
90
92
94
96
98
100
10
15
20
25
30
35
40
45
50
1 2 3 4 5 6
%TSorTorque
Torque v. % Recovery
Torque Cake Recovery
39% Torque
Filename.ppt/31
Further Optimization
• Choose variable to test
− Polymer solution concentration or injection point
− Throughput
− Centrate weir location
− Etc.
• Run through same process as above, holding
other parameters constant
• Run through sequence with incremental changes
to variable
• Plot results
Filename.ppt/32
Optimize Upstream Processes
• PS:TWAS ratio
− If possible, modify upstream
operations to favor PS in the
digester feed
• Dewatering feed temperature
− Try minimizing storage or
feeding from digesters
• Track VS in dewatering feed
• Plot these parameters and
compare to performance
Case Study 1A Case Study 1B Case Study 1C Case Study 1D
Filename.ppt/33
Outcomes of Regular Optimization
• Determine what dose is effective under what conditions
• Determine what torque is effective at what throughput
• Determine impacts of upstream processes on dewatering
• Provide general guidelines to dial in centrifuges and
understand impacts of changes
• If using more than one polymer, determine under what
conditions each is most effective
• Forecast usage to establish purchasing frequency and
budget projections
Consider a full range of testing at least every 6 months
Filename.ppt/34
Track Performance and Publish Results
Relative to Targets
Filename.ppt/35
Continually Optimize to Address Changes
Filename.ppt/36
Optimization for Centrifuge
Dewatering
Thank you for being a wastewater treatment professional.
Steve Walker swalker@carollo.com 303-635-1220
Rashi Gupta rgupta@carollo.com 714-593-5100

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Dewatering Optimization_Gupta

  • 1. Optimization for Centrifuge Dewatering WEFTEC New Orleans, Louisiana Rashi Gupta, P.E. Steve Walker, CWP Carollo Engineers September 28, 2016
  • 2. Filename.ppt/2 Questions to Answer Today… • Why is optimization important? • What should I consider within my dewatering process? • How do I systematically optimize the process?
  • 3. Filename.ppt/3 Dewatering Costs a Lot Annual Dewatering Cost = $3.7M Case Study 1
  • 4. Filename.ppt/4 Increasing Dryness Can Save on Hauling $ ~$80,000 between 20% and 22% per centrifuge at 250 gpm; 2% feed Case Study 1
  • 5. Filename.ppt/5 Reducing Polymer Can Save on Chemical $ ~$20,000 between 38 lb act/DT and 40 lb act/DT per centrifuge at 250 gpm; 2% feed Case Study 1
  • 6. Filename.ppt/6 Maximizing Dryness Not Always the Answer Case Study 2
  • 7. Filename.ppt/7 Dewatering Costs – Case Study 1B from July 2011 to September 2014
  • 8. Filename.ppt/8 Dewatering Performance – Case Study 1B Averages: 22.0% Cake 99% Capture 38.3 lb act/DT
  • 9. Filename.ppt/9 Case Study 1B Dewatering Costs – Before and After • 2011-2014 Monthly Costs − $33,000 Hauling − $19,000 Polymer − $52,000 Total • 2015 Monthly Costs − $29,500 Hauling − $15,600 Polymer − $45,100 Total
  • 12. Filename.ppt/12 • Dewatered cake • Centrate • Sludge: − Anaerobically or aerobically digested − Primary sludge − Thickened waste activated sludge − Chemically enhanced • Polymer solution Centrifuge Inputs and Outputs Inputs Outputs
  • 13. Filename.ppt/13 Operational Targets to Track Performance Criteria Units Importance Cake dryness %TS • Disposal costs • Water equals weight and takes up volume Centrate quality %TS or TSS, mg/L • Impact on liquid treatment processes • Re-treatment of solids (thickening, digestion and dewatering) • Impact of inert solids on activated sludge mass calculations Throughput lb/hr and gpm • Centrifuge capacity • Operations and hauling logistics Polymer dose Active pounds per dry ton • Operating costs
  • 14. Filename.ppt/14 Dewatering Feed Characteristics Matter • Important Sludge Feed Characteristics − PS:TWAS ratio in digester feed, by mass  Important because PS is MUCH easier to digest and dewater than TWAS  The higher the PS:TWAS ratio, the better the dewaterability − Volatile solids content  Generally, higher VS = More difficult to dewater − Biological phosphorous removal − Divalent cations (Ca2+, Mg2+) vs Monovalent (Na+, K+) − Sludge feed temperature
  • 15. Filename.ppt/15 PS:TWAS Ratio Matters a Lot Case Study 1A Case Study 1B Case Study 1C Case Study 1D Highest PS:TWAS Lowest Polymer Most Dry
  • 16. Filename.ppt/16 Understanding Polymer Basics Necessary to Assess Effectiveness • “Neat” polymer − Oil, surfactants, water, and polymer (emulsion as delivered) • “Active” − What’s doing the work − 40-50% typical for emulsion − 90%+ typical for dry
  • 17. Filename.ppt/17 Many Pieces to the Polymer Puzzle • Procure the right polymer • Select right dilution concentration for polymer solution • Produce fully activated solution • Find best polymer injection location • Maintain req’d water pressure • Check water characteristics (chlorine, hardness, temperature) • Optimize polymer dose
  • 18. Filename.ppt/18 • Loading rates (throughput) • Bowl speed (G-force) • Conveyor/scroll speed (differential speed) and torque − Newer centrifuges are controlled using a % torque or pressure setpoint − To achieve the desired torque/pressure, the PLC adjusts the scroll speed • Weir plates − Set the pool depth within the bowl Centrifuge Parameters that Affect Performance
  • 19. Filename.ppt/19 Throughput • Need to stay within loading capacity • Changing solids concentration impacts loading
  • 20. Filename.ppt/20 Throughput Case Study 1A: Data from January 2015 – April 2015
  • 22. Filename.ppt/22 Process Optimization • Achieve: − Desired cake dryness and centrate quality − Lowest polymer cost − Maximum throughput and efficiency • Balancing act: Maximize one or more of the process parameters, while keeping all others within their constraints
  • 23. Filename.ppt/23 Parameters used for Optimization • Type of polymer • Polymer dose • Polymer dilution/solution concentration • Polymer injection point • Centrifuge torque/pressure • Centrifuge pond depth • Centrifuge bowl speed • Sludge feed (throughput) • Sludge characteristics
  • 24. Filename.ppt/24 Process Optimization – Polymer Selection • Selecting the right polymer: − Site specific jar testing by different suppliers  High molecular weight for centrifuge dewatering  High charge density helps with dewatering of secondary sludges  Cationic − Site specific full scale tests with promising polymers • Full scale tests can identify more effective polymers • Polymer effectiveness can be gauged through viscosity
  • 25. Filename.ppt/25 Polymer Contract Flexibility • Establish Primary and Alternate supplies − Use two different suppliers rather than two different products from the same supplier • Determine if seasonal constraints support alternatives. For example: − An emulsion polymer may be more cost effective in winter months − A dry polymer may be more cost effective in the other months
  • 26. Filename.ppt/26 Test Methodology – Phase 1 (Polymer Dose) • Batch polymer at preferred solution strength • Set sludge feed rate • Enter typical torque setpoint and bowl speed • Set lowest polymer feed rate • Run for a standard time (i.e., 45 minutes) • Sample feed, centrate and cake for TS/TSS. − Feed solids concentration used to calculate throughput • Run through sequence for at least 5 polymer feed rates • Calculate associated dose and plot results
  • 28. Filename.ppt/28 Performance Curve - Polymer 80 82 84 86 88 90 92 94 96 98 100 10 15 20 25 30 35 1 2 3 4 5 6 lb/tonor%TS Dose v. % Recovery Dose, lb/ton Cake Recovery 24
  • 29. Filename.ppt/29 Test Methodology – Phase 2 (Torque) • Set sludge feed rate • Set polymer solution feed rate for the “ideal” polymer dose • With sludge and polymer feed rates “locked in”, adjust % torque setpoint • Run for a standard time (i.e., 45 minutes) • Sample feed, centrate and cake for TS/TSS. • Run through sequence for at least 5 torque setpoint • Plot results
  • 30. Filename.ppt/30 Performance Curve - Torque 80 82 84 86 88 90 92 94 96 98 100 10 15 20 25 30 35 40 45 50 1 2 3 4 5 6 %TSorTorque Torque v. % Recovery Torque Cake Recovery 39% Torque
  • 31. Filename.ppt/31 Further Optimization • Choose variable to test − Polymer solution concentration or injection point − Throughput − Centrate weir location − Etc. • Run through same process as above, holding other parameters constant • Run through sequence with incremental changes to variable • Plot results
  • 32. Filename.ppt/32 Optimize Upstream Processes • PS:TWAS ratio − If possible, modify upstream operations to favor PS in the digester feed • Dewatering feed temperature − Try minimizing storage or feeding from digesters • Track VS in dewatering feed • Plot these parameters and compare to performance Case Study 1A Case Study 1B Case Study 1C Case Study 1D
  • 33. Filename.ppt/33 Outcomes of Regular Optimization • Determine what dose is effective under what conditions • Determine what torque is effective at what throughput • Determine impacts of upstream processes on dewatering • Provide general guidelines to dial in centrifuges and understand impacts of changes • If using more than one polymer, determine under what conditions each is most effective • Forecast usage to establish purchasing frequency and budget projections Consider a full range of testing at least every 6 months
  • 34. Filename.ppt/34 Track Performance and Publish Results Relative to Targets
  • 36. Filename.ppt/36 Optimization for Centrifuge Dewatering Thank you for being a wastewater treatment professional. Steve Walker swalker@carollo.com 303-635-1220 Rashi Gupta rgupta@carollo.com 714-593-5100