current trends in biosolids management & treatment biosolids... · current trends in biosolids...
TRANSCRIPT
![Page 1: Current Trends in Biosolids Management & Treatment Biosolids... · Current Trends in Biosolids Management & Treatment Jay Kemp, PE, BCEE Bill Marten, PE, BCEE Black & Veatch Donohue](https://reader031.vdocuments.mx/reader031/viewer/2022022002/5a8404117f8b9ac96a8b4856/html5/thumbnails/1.jpg)
Current Trends in Biosolids Management & Treatment
Jay Kemp, PE, BCEE Bill Marten, PE, BCEE Black & Veatch Donohue & Associates
35th Annual Spring Biosolids Symposium March 21, 2017 Stevens Point, WI
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Page 2 | March 21, 2017
35th Annual Spring Biosolids Symposium
Presentation Topics
High Level Overview Discussion of:
Digestion
Aerobic
Anaerobic
Nutrients
Issues, Challenges, Recovery
Takeaways
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Aerobic Digestion Has Been Around a Long Time, What Could be New or Trending?
Operational Mode Cycling
– Cycling Air On (Aerobic) and Off (Anoxic)
Use of Membranes to Enhance Thickening
Aerobic Digestion
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Operational Mode Cycling
Aeration ON – Digestion occurring
– Oxygen is utilized for electron acceptor
– Ammonia is nitrified to nitrate
– Alkalinity is consumed & pH decreases
Aeration OFF – Digestion occurring
– Nitrate is utilized as electron acceptor (Energy Savings)
– Nitrate is denitrified to nitrogen gas
– Alkalinity is recovered & pH increases
Can Accomplish in Dedicated Reactor Zones or Single Reactor (Digester)
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Process Control – Aerobic: D.O. or Time
– Anoxic/Anaerobic: ORP or Time > Experiences Have Shown 50/50 Time Split Works Well
Can Minimize Digested Sludge Production – Long Cycle Times and Multiple Cycles in Each
Operational Mode > Similar to Interchange Reactor Effect of the Cannibal Process
– Enhanced Digestion Due to More Effective Predation > Anaerobic Predation on Aerobic Organisms
> Aerobic Predation on Anaerobic Organisms
Aerobic Digestion Cycling
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Eliminate Decanting, Use Membrane Filters for Solids Separation (Decanting)
Benefits – Cleaner “Decant”
– Ability to Operate Digester at Much Higher TS Concentrations > From Typical 3% TS to 4.5-6% TS
> Increases Treatment & Biosolids Storage Capacity, Possibly Delaying Need for Plant Expansions
Aerobic Digestion: Membrane Thickening
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Example: Kubota PAD-K Aerobic Digestion
Aerobic Digestion: Membrane Thickening
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Maximizing Biogas Production & Energy Use/Value – High Strength Waste Receiving
– Effective Mixing
– Recuperative Thickening
– Staged Digestion
– Pre-Digestion Sludge Treatment
Anaerobic Digestion Trends
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35th Annual Spring Biosolids Symposium
Electrical Pulses
Mechanical Grinding
High Heat – With Pressure
– With Chemical Treatment
Pre-Digestion Raw Sludge Treatment
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Electrical Pulses
Mechanical Grinding
High Heat – With Pressure
– With Chemical Treatment
Pre-Digestion Raw Sludge Treatment
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Heat & Pressure Approach
Cambi Thermal Hydrolysis – Pre-Dewatering
– All Sludge or Just WAS
BioThelys – Pre-Dewatering
– All Sludge or Just WAS
Exelys – Pre-Thickening
– Usually Just WAS
In General:
• Utilize Steam
• Raise Sludge Temperature to 330-350 Deg F
• Raise Pressure to 90-130 psi
• Rapid Depressurization
• All Capable of Class A
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Example Heat & Pressure: Exelys
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Heat & Chemical Approach
Pondus TCHP – Pre-Thickening
– All Sludge or Just WAS
In General:
• Utilize Hot Water
• Raise Sludge Temperature to ~150 Deg F
• Use Caustic to Raise pH to ~11
• Hydrolization Lowers pH
• Capable of Class A
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Example Heat & Chemical: Pondus TCHP
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Process Complication vs Operating Costs – Dewatering vs Heating Water
Total Present Worth Considerations – Capital Cost
– Operating Cost Negatives > Heat, Chemical, Processing Energy
– Operating Cost Positives > Increased VSR of 10-20% Possible
> Potential Class A
Performance characteristics will be highly site specific – pilot testing recommended.
Pre-Digestion Treatment Considerations
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Nutrient Issues/Challenges
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Nutrient Issues/Challenges: Phosphorus
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NR 217: 20+ Years of Effluent P Limits
Biosolids Impacts – Higher P Content
– Increased Sludge Quantities
Nutrient Issues/Challenges: Phosphorus
Tertiary
Treatment
Effluent Secondary
Treatment
(Bio-P)
Raw WW Primary
Treatment
Chemical Feed
Chemical Feed
P P
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Very Low Water Quality Based Effluent Limits Will Result in: – Higher Levels of Removal Required
– Alternative Compliance Approaches such as Trading, Adaptive Management, Variances
Revisions to NR 217 – A New Pinch on P
More P More P More P
…and Potentially More Restrictions on Biosolids Reuse
Tertiary
Treatment
Effluent Secondary
Treatment
( Bio-P)
Raw WW Primary
Treatment
Chemical Feed Chemical
Feed Chemical
Feed
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…Due to the Required Anaerobic/Aerobic Cycling
Bio-P Presents Some Unique Biosolids Challenges…
Time
Anaerobic AerobicC
on
ce
ntr
ati
on
SolubleBOD
Soluble Orthophosphorus
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Anaerobic Zone => VFA Uptake & SP Release
Bio-P Refresher…
Carbon
Storage
Polyphosphate
VFA’s
Soluble PO4-P (Energy)
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Aerobic Zone => Biometabolism of Carbon (Growth & Oxidation) & Soluble P Uptake
Bio-P Refresher…
O2
CO2 and H2O
and More Cells
(Cell Synthesis)
Soluble PO4
Energy Carbon
Storage
Polyphosphate
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• Soluble PO4-P Release
• Thickening/Dewatering – Increased SPO4-P in Filtrate/Centrate Sidestreams
Increased SPO4-P Also Occurs With Aerobic Digestion, Just Not to Same Extent
Most Bio-P Related Biosolids Challenges Are Associated With Anaerobic Digestion
Carbon
Storage
Polyphosphate
VFA’s
SPO4-P (Energy)
Anaerobic Conditions with
Lots of VFAs
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One (Now Familiar) Bio-P/Anaerobic Digestion Sidestream Issue…Struvite!
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Sidestream Control Strategies Can Also Control Struvite – Or Simple Dilution of Filtrate Can Work Too
Luckily, We Understand Struvite & Controlling It
Anaerobic
Digester
Gravity Belt
Thickener
Thickened SludgeGBT
Filtrate
Polymer
Ferric Chloride Addition
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Such Sidestream/Struvite Control a Standard Component of Our Designs
Eau Claire DSD Thickening Filtrate Line
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The New Bio-P Ugly: Impaired Dewatering of Anaerobically Digested Sludge
8’ Tall Push Walls 3-4 Foot Typical of Unusable Wall Height
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Dewatered Cake “Looks Normal & Dry”
Reduction in Cake Dryness of 5-8% TS
Stacking Height Often Half of Expected
Being Experienced at Many Plants – Beloit, WI
– Sun Prairie, WI
– Marquette, MI
– Hampton Roads Sanitary District Atlantic & Nansemond Plants, VA
– Met Council Environmental Services Empire & Blue Lake Plants, MN
– Metro Denver, CO
Impaired Dewatering of Anaerobically Digested Bio-P Sludge Observations
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Differences in Extra-Cellular Polymeric Substances (EPS)/Soluble P Concentration of Digested Sludge – Evidence that soluble Ortho-P binds water to
solids > Possibly due to increased presence of EPS/EPS binds water
> Lower digested sludge soluble Ortho-P => higher cake TS
Divalent Cation Bridging
Suspected Causative Factors
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Divalent Cation Bridging Theory
Courtesy of Sprouse, 2013
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Prominent Divalent Cations Are Mg2+, Ca2+ and Fe2+
Prominent Monovalent Cations are Na+ and K+
Divalent Cation Bridging Theory
To Help Understand This, Let’s Take a Step Back
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Anaerobic Digestion of Bio-P: Potential Effect on Cation Ratios
Carbon
Storage
Polyphosphate
VFA’s
PO4-
(Energy)
Mg2+
K+
NH4+
Struvite
And What About That Potassium???
Magnesium is Decreasing
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An interesting development is struvite harvesting and claims it can help solve this problem.
The approach involves making struvite intentionally to:
Minimize Impacts on Cation Ratios
Minimize Soluble P Content
Before the digested sludge gets to dewatering.
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Airprex is making struvite before dewatering. But is the improvement due to less soluble P in the sludge, or more divalent cations???
One Example: Airprex
Pilot Testing at Several Wisconsin Plants in 2016 Has Shown Dewatered Cake Gains of 2-5% TS
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Example: Pilot Testing Airprex at Stevens Point May 2016
4-5% TS Increase with Airprex
Highly Site Specific: Pilot Testing Needed
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Nutrient Recovery Discussion Items
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Nitrogen-phosphorus balance in biosolids
P-index
Benefits of phosphorus removal from biosolids
Background on Struvite and Brushite Solubility
Alternatives for phosphorus removal
Nutrient Recovery Discussion Items
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Typical digested sludge – 5 % N; 2% P
Bio-P Sludge – 5% N; 4 % P
Application based on N may apply P in excess of crop requirements
Biosolids are Applied based on nitrogen requirements
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Area of active research – WERF Study
– UW- Madison
– WI Lutheran College
– Penn State
P-index – Considers how P is delivered to surface water
– Considers all sources of P
How much P from biosolids is plant available ?
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Field
Annual P delivery to stream
(P Index)
Annual “field-edge” runoff losses estimated for each crop year:
Sediment-bound P Dissolved P from soil Dissolved P from manure and fertilizer
Total P field to stream delivery
ratio applied to account for P deposition and infiltration:
assumes channelized flow similar to a grassed waterway
=
Stream
x
Runoff
Wisconsin P Index
P Index estimates delivery to nearest surface water; Accounts for sources and transport based on long-term average weather
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Sources of Phosphorus in Runoff
Soil P – Biosolids may increase soil P
– Bound P- may solubilize over time
Manure P on surface
Fertilizer P on surface
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Total runoff P losses are a function of amount of P in soil and surface amendments and the amount of runoff and erosion
P Index: Field-Specific Estimate of Total Average Annual Runoff P by Source and Transport Pathway
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Decrease P content of biosolids
Improve biosolids dewaterability
Minimize nuisance scaling and deposits
Reduce P & N recycle loads
Recover fertilizer product
Benefits of phosphorus removal
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35th Annual Spring Biosolids Symposium
Iron salts ( ferric chloride) do not produce a recoverable product
Struvite and brushite recover P as useable fertilizer – Struvite Mg-NH3-P
– Brushite CaHPO4
Divert a valuable resource to where it can be used
P must be insoluble to remove or recover
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Struvite less soluble above and below 35 °C
Struvite Solubility
MD. IQBAL HOSSAIN BHUIYAN
M.Sc, UENSCO-IHE Institute for Water Education, 2002
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High PO4-P and Ca in acid phase digestion
Brushite Solubility
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CaHPO4-2H2O Precipitates at acid conditions
Brushite Solubility
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Ostara
Multiform Harvest
AirPrex
NuReSys
Nutrient Recovery & Upcycling (Brushite) – Now part of CNP
Alternatives for phosphorus removal & recovery
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Reference Installations
Technology Number of Municipal Installations
Date of First Municipal
Installation
AirPrex TM 6 Operational (Europe) 3 In final design (US)
2009
NuReSys TM 3 Operational (Europe) 2013 (first industrial 2006)
Ostara TM 10 Operational (US) 6 In construction/design
2007
Multiform Harvest TM
2 Operational (US) 1 In construction
2012
Brushite (CalPrex) 0 0
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Ostara
P recovered from
dewatering
filtrate/centrate
WASSTRIP
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Maximizes P recovery potential – Less struvite precipitation in digesters
Reduces struvite scaling potential, but does not eliminate it
Reduces impacts to dewatering?
More complex process than recovering from dewatering centrate/filtrate. Need for additional WAS thickening process.
Ostara - WASSTRIP
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Treat filtrate/centrate for recovery of struvite Pearls
MultiWAS – Similar to WASSTRIP – Need to add ammonia to
thickening filtrate reactor
Reactor configured to make struvite crystals, not pearls
–No recycle flow
Multiform Harvest
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MultiWAS maximizes P recovery
Multiform Harvest
P recovered from
dewatering
filtrate/centrate
MultiWAS
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Treat digested sludge to precipitate phosphate as struvite (MgNH4PO4•6H2O) crystals – Sequestration: crystals remain in biosolids
– Recovery: crystals separated from biosolids
AirPrex
• Air added to strip CO2 and raise pH
• MgCl2 is added to control effluent phosphate
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AirPrex
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May be configured on digestate, centrate/filtrate, or “hybrid”
Air Stripper used to raise pH and precipitate Mg remaining after digestion
Crystallizer used to precipitate additional ortho-P
NuReSys
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Hybrid addresses
struvite scaling
downstream of digester
NuReSys
Centrate – WASSTRIP
Hybrid
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Brushite Recovery
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Advantages & Disadvantages
Technology Advantages Disadvantages
Ostara Pearl™ • Proven technology • High Ortho-P Recovery
(90% of reactive P)
• WASSTRIP process increases complexity
MHI Multiform Harvest™
• Proven technology • High Ortho-P Recovery
(90% of reactive P) • Smaller reactor than Ostara
• MultiWAS process increases complexity
• Requires additional chemical (NH4OH)
CNP AirPrex™ • Easy to operate • Lower P recovery potential (<50% of reactive P)
• No US installations
NuReSys Process™ • Easy to operate • Lower P recovery potential (<50% of reactive P)
• No US installations
Brushite Recovery • Highest potential for P recovery, recovers reactive and organically bound P
• Emerging technology, no full scale installations
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Reducing P in biosolids will reduce the impact of P on land application and nutrient management.
P removal/recovery has in-plant benefits – Improved dewatering
– Reduced scaling
Recovered P fertilizers have market value – Recovers a limited but misplaced resource
Many options available
Nutrient Recovery take home message(s)
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Current Trends in Biosolids Management & Treatment
Jay Kemp, PE, BCEE Bill Marten, PE, BCEE Black & Veatch Donohue & Associates
35th Annual Spring
Biosolids Symposium March 21, 2017
Stevens Point, WI
Thank You For Your Attention!