livestock waste technologies for energy production and...
TRANSCRIPT
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Livestock Waste Technologies for Energy Production and Pollution Control
A Global PerspectiveKurt F. Roos
AgSTAR ProgramU.S. Environmental Protection Agency
BioEnergy and Sustainable Technology SocietyUniversity of Florida – January 18, 2006
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AgSTAR Program
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Introduction: Farm ProcessesLAND
APPLICATION
Combined Treatment & Storage Lagoon
LiquidSlurry
Semisolid
Above/below ground storageponds, tanks, basins, pits
Surface or Injection
BUILDING TREATMENT/STABILIZATION
PRE-TREATMENT
Open Treatment Lagoon
Storage Pond
STORAGE
Anaerobic Digesters
Storage Pond
Separation
GravityMechanicalChemical
Aeration Storage Pond
Evaporation Pond
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Waste System Considerations
• Livestock waste are high strength materials, comparatively 10-100 times stronger than sewage
• Wastes can pollute and cause disease when improperly disposed• Main polluting elements:
– High organic fraction (BOD and COD)• Fish kills – competes for dissolved oxygen• Odor attracts fly and other disease transmission vectors• Emits methane - greenhouse gas
– Contain nutrients – nitrogen phosphorus and other• Causes eutrophication in surface waters• Can mutate plants when over applied or volatilized
– Contain an array of bacteria, pathogens and other disease causing organisms• E. coli, Staph., Strep, Ascaris, etc.
- Livestock wastes are agricultural resources -Challenge is to cost effectively manage wastes with consideration to human, water, air, and land impacts
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Wastes are Handled in DifferentWays
Liquid, slurry, and semi-solids offer the bestmethane reduction opportunities because they create
anaerobic environments that feed methanogenic bacteria
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Methane Emissions areDependent on Waste System
AMWS Systems and Methane Emission Factor by Climate Type Manure Management System
Climate Lagoon Liquid and
Slurry
Solid Storage
Dry lot Pit <1
month
Pit >1
month
Daily Spread
Digester Other
Cool 90% 10% 1% 1% 5% 10% 0.10% 10% 1% Temperate 90% 35% 1.50% 1.50% 18% 35% 0.50% 10% 1% Warm 90% 65% 2% 5% 33% 65% 1% 10% 1%
Factors effecting methane emissions:1) Manure type
2) Manure handling (liquid, slurry, semi-solid, solid)
3) Temperature and time
Lagoons Liquid/Slurry storage
ponds, pits, tanks
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Calculating Methane Reductions
Example: 500 cow dairy with varying baseline waste management systems in a warm climate
Daily Spread Liquid/Slurry LagoonStorage
(A) Baseline Farm - MCF 1% 65% 90%Baseline Methane Emission - MT/yr 1.9 120.3 166.6
(B) MT Combusted CH4/Year1 185 185 185(C) MT CO2 Utility Emission Offset (as CH4) 32 32 32(D) Refractory Emission2 @1% biodegradable VS 1.9 1.9 1.9
MT Methane Reduction/Year3 0.0 -118.5 -164.8as CO2 0 -2,488 -3,460
as Carbon Equivalent 0 -679 -944Notes:1 For this farm energy capacity is about 80 kW. Energy output is about 69 kWh/hr.2 Remaining biodegradale VS results in refractory emissions, assumed3 Positive value indicates increase in emission
Waste System Types
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Overview: Potential MethaneReducing Options
• Aeration – energy is used to provide oxygen to meet oxygen demand of waste (1 lbs. BOD requires 1 HP)
• energy intensive and very expensive• used as tertiary treatment in sewage to meet
discharge requirement• residual solids become problematic • Can produce nitrous oxide - much higher GWP
• Shifting liquid/slurry handling to solid manure handling• very limited because of scale• more economical to flush manure from confined
production systems (pigs and dairy)• Anaerobic digesters
• consistent with farm waste handling objectives• oxygen demand satisfied anaerobically• produces biogas providing farm energy
opportunities
Aeration
Anaerobic Digester
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What are Anaerobic Digesters?
Biological treatment/stabilization systems that collect and combust off-gases.Offer Air Quality benefits
-Control odors from storage and field application-Reduces Greenhouse gases (methane)-Controls other emissions (H2S, ammonia)
Offer Water Quality benefits-Stabilize manure organics (BOD)-Significantly reduce pathogens-Provide nutrient management predictability and flexibility
Offer return on Investment…….Energy revenues
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Anaerobic Digester Components
Digesters separate manure treatment from storage functions which can result in lower initial installation costs for new or expanding farms
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What Makes Digesters work?
BIODEGRADABLE FRACTION
ProteinCarbohydrateHemicellulose
VOLATILE ACIDSProprionic
Acetic
(Intermediate Odor Producing (Compounds)
BIOGAS
70% CH430% CO2Trace H2S
Acitogenic Phase
Acid Forming BacteriaAcitogens
Methanogenic Phase
Methane Forming BacteriaMethanogens
Anaerobic digestion is a biological process. It occurs in an oxygen free environment.
Methanogens
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Appropriate Digester Selection?
- Hog and Dairy industry constitute >90% of market potential
Attached Film
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Unheated Digesters
Covered Lagoon Digester Attached MediaBank-to-Bank Cover
Modular Cover
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More Unheated Digesters
Small - Intermediate Scale Digesters
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Heated (Mesophilic) MixedDigesters
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Heated (Mesophilic) Plug FlowDigesters
Used for Dairy only w/ Separation
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Gas Use: Electrical GenerationGas Handling and TransmissionRecip. Engines 40-150kW
C
O
M
P
O
N
E
N
T
S
Engine ControllerElectric Metering
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Gas Use: Heat
Boilers Forced Air
Hot Water Storage Hot Water Use
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Gas Use: Flares
Odor Control and Greenhouse Gas Mitigation
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Other Gas Use Options Cooking Wood and Coal
Pumps
Cooking PropaneHeat lamps and light
Shaft Power
Pumps
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Environmental RetrofitRetrofit Plan
Before After
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Covered Lagoon
CoveredAnaerobic
Lagoon
StorageLagoon
Biogas
Electricity
Electric Generator
Hot WaterHeater
ExhaustGas
Was
te C
olle
ctio
n
Was
tew
ater
HeatExchange
Hot Water
Pits
Swine House
Fig. 1. A Schematic of Covered Anaerobic Lagoon System for Manure Management at Barham Farm.
To Irrigation RecycleSampling location
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Project Types
• On-Farm or Farm Scale: System is owned and operated by farm owner/manager– Currently the predominant project type in the U.S.
• Regional or Centralized Digesters: Off farm management and operation with a third party– Ideally located at a large energy (electric or heat) consuming
source or interconnection point (feed mills or utility substation)
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General Costs: Livestock Basis
Digester Type Cost per Cow (1,400 lbs.)Attached Media $500-800Complete Mix $400-700Covered Lagoon $300-1,000Plug Flow $400-700
Swine equivalents: 4 sows = cow;10 feeder pigs = cow
Note: Cost assumes all manure is collected
Costs include engine gensets and separator (dairy systems)
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Caution - Digesters Can Fail!
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Organic Stabilization and Odor
Covered lagoon w/ separate storageReductions, %
Combined treatment storage lagoonReductions, %PARAMETER
Coveredlagoon
Storagepond
Total Total
Total solids 90.1 7.7 97.8 95.6Total volatilesolids
95.4 3.7 99.1 98.9
Fixed solids 76.9 18 94.9 91.5Chemical oxygendemand
97 2.8 99.8 99
Martin J.H. Jr., A Comparison of the Performance of Three Swine Waste Stabilization Systems, AgSTAR Program deliverable under contract #68-W7-0068, Draft March 2002
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Pathogen Performance
Comparative Health Indicator Performance
0.0
1.0
2.0
3.0
4.0
Covered Multiple CellLagoon
Single Cell LagoonLog
redu
ctio
n, c
fu/g
TS
Fecal coliform
Salmonella
Martin J.H. Jr., A Comparison of the Performance of Three Swine Waste Stabilization Systems, AgSTAR Program deliverable under contract #68-W7-0068, Draft March 2002
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Nitrogen Performance
Comparative Nitrogen Distribution
0%10%20%30%
40%50%60%70%
Covered Multiple CellLagoon
Single Cell LagoonPerc
ent o
f Inf
luen
t Nitr
ogen
SludgeVolatilzedLand Applied
- Comparative reductions of Phosphorus (Total & Ortho) were @97% for each system
Martin J.H. Jr., A Comparison of the Performance of Three Swine Waste Stabilization Systems, AgSTAR Program deliverable under contract #68-W7-0068, Draft March 2002
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Nitrogen Performance (cont)
Land Applied Nitrogen Profile
6%
12%
2% 2%
4%
10%
0%
5%
10%
15%
Covered MultipleCell Lagoon
Single CellLagoon
Perc
ent o
f Inf
luen
t N
itrog
en TKN
Organic N
Ammonia N
- Comparative reductions of Phosphorus (Total & Ortho) were @97% for each system
Martin J.H. Jr., A Comparison of the Performance of Three Swine Waste Stabilization Systems, AgSTAR Program deliverable under contract #68-W7-0068, Draft March 2002
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Swine Biogas Profile
Parameter % by volumeMethane 67.9
Carbon Dioxide 32.1Hydrogen Sulfide .05
Martin J.H. Jr., An Assessment of the Performance of the Colorado Pork, LLC. Anaerobic Digestion and Biogas Utilization System, AgSTAR Program deliverable under contract #68-W7-0068, Draft March 2003
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Greenhouse Gas Performance
Greenhouse Gas Emissions Profile
-200,000
-150,000
-100,000
-50,000
0
50,000
100,000
150,000
200,000
1
Met
hane
redu
cito
n, m
^3/y
ear
Covered Multiple CellLagoon
Single Cell Lagoon
Martin J.H. Jr., A Comparison of the Performance of Three Swine Waste Stabilization Systems, AgSTAR Program deliverable under contract #68-W7-0068, Draft March 2002
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Comparative: Fecal ColiFecal Coli data for digested and non-digested dairy manure
1
10
100
1,000
10,000
100,000
1,000,000
10,000,000
Raw ManureFarm P
Non DigestedSeparated
Liquid
Non DigestedSeparated
Solids
Raw ManureFarm A
DigestedDigester Effluent
DigestedSeparated
Liquid
DigestedSeparated
Solids
Feca
l Col
iform
(log
sca
le)
With Anaerobic DigestionBaseline
Martin J.H. Jr., A Comparison of Dairy Cattle Manure with and without Anaerobic Digestion and Biogas Utilization, AgSTAR Program deliverable under contract #68-W7-0068, March 2003
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Comparative: PathogensJohnes content in separated digested manure vs separated non-digested manure
1
10
100
1000
10000
P Raw Manure P Separated Liquid P Separated Solids A Raw Manure A Digester Effluent A Separated Liquid A Separated Solids
John
es (c
fu/g
ram
man
ure)
Baseline With Anaerobic Digestion
Martin J.H. Jr., A Comparison of Dairy Cattle Manure with and without Anaerobic Digestion and Biogas Utilization, AgSTAR Program deliverable under contract #68-W7-0068, March 2003
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Livestock in East Asia ProjectPollution Control for Pig Waste
Kurt Roosfor
Weiguo Zhou – Team LeadRural Development & Natural Resources Sector Unit
East Asia and Pacific RegionThe World Bank
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Project Background
• Purpose: Reduce negative environmental and health impacts caused by confined livestock in region
– Discharge to surface waters main issue
• Three country areas involved:– China, Guangdong Province– Thailand, Racthuburi and Chonburi
province– Vietnam, Ho Chi Minh City and Hanoi
• Project implemented over a 5 year period
• Japan PHRD Grant Fund for Climate Change includes a Greenhouse Gas project component
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Project Country Profiles
Standing Pig Methane
Population Emissions
(millions) (Gg)
China+ 47 1,197
Thailand 7 1,786
Vietnam 25 123
Total 79 3,106
as % of World >50% >25
• Opportunities– Pig waste handled as liquids and slurries– Appropriate candidate for anaerobic
treatment and gas recovery– All countries desire gas recovery
technologies
• Project Benefits:– Organic (BOD) stabilization – Pathogen reduction– Nutrient conversion– Odor control– Greenhouse Gas reduction– Energy - adds additional revenue stream
to farm
+ China is a current Methane to MarketsParticipant
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Large Range in Farm Scale
• Thailand– Very large corporate type farms
>20,000 and very small family farms 10-50 pigs
• Vietnam– Very small family farms 10 – 200 pigs
• China– Moderate scale farm 100 – 2,000
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Waste Handling and Collection
All countries solids collection and hose flush
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Waste Management
Fish Ponds
Lagoons
Direct Discharge
Fish Ponds
Storage/Direct Discharge
Digesters/Direct Discharge
1) Land application of nutrients limited to solids fraction only
2) Have discharge standards
3) Pollution load is catastrophic
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Project Design
Technical TrainingTrian-the-trainor
Demonstration Component
Appropriate Technologies
MonitoringProcess Characterization
Methodology
Tools DevelopmentWorksheetsDVD/VideoHandbooksSoftware
CAPACITY BUILDING OVER TIME
National StandardsAccepted Technologies
Policy Development: Energy; Regulatory; Voluntary/Market Mechanisms (Code of Practice)
Replication
Other/ExtensionTraining
Certified Technology Providers
(option)
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Demonstration Overview
• Purpose is to demonstrate an array of systems that prevent water pollution– Greenhouse gas and air quality are not primary project objectives– Systems must be affordable – gas recovery component does this
• All countries desire systems with gas recovery• Many system types
– Cost implications– Gas use options vary
• Projects are on-farm and communal• Other processes also in technology mix
– Two cell open lagoons• Land application and nutrient management planning approaches are being
introduced.– Long term implications for project– Some countries limited opportunity i.e., fish pond feed resource
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On-Farm Demonstrations
Covered Lagoon
Polyethylene Bag
Fixed Dome
Two Phase Digestion
Two cell open Lagoon
Polypro Bags
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Communal Digester N. Vietnam
Lagoon site integrated into fish pond
Village Waste Canal System
Bank-to-bank covered lagoon type
• Social structure allows for communal development, operation, and management of covered lagoon• 200 families• @1,500 pigs
• Village waste canal to be constructed • Designed for rainfall exclusion
• Gas purchased and used as cook fuel for families• Distributed and measured in
refillable bags
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Gas Use Options
Heat lamps and light
Shaft Power
Cooking Wood and Coal
Cooking Propane
FlaresPumpsElectric/Cogen
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Nutrient Management – TropicalClimate Options
• Land application relative to crop need (N and P)
– Most common approach includes temperate climate approaches – US, Europe
• Wetland– Aquatic crops remove nutrients
• Fish ponds– Waste used as fish feed resource –
China, Vietnam, Thailand• Treat and discharge - sewage
– Livestock waste comparatively high strength very expensive
– Understanding mass loading critical
Irrigated Rice
Tank hauling of liquid effluent
Fish Pond
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Affordability = Replication
• Demonstration has wide range in installed cost– $7-15 per pig (poly bags, fixed domes, covered lagoons)– China two phase system– $55-100 per pig
• Cost will effect replication potential– Project focused on @$15/pig or less
• Policy component– Energy financial incentives– Meat market pricing structure (Code of Practice)– GHG off-sets– Regulatory
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Renewable Energy Costs kWh Output
PROJECT PARAMETERS
ENERGY OUTPUT
COSTInstalled Cost Capacity Operational kWh/hr Total kWh
Renewabl Energy Sources $/kW Total kW Factor Available kWh/yearWind Energy a --- --- --- --- --- --- Wind-Small (1-100kW) $4,000 50 30% 15 131,400 $0.15 Wind- Utiltity Scale (> 500 kW) $1,200 500 30% 150 1,314,000 $0.05Solar - PV b --- --- --- --- --- --- .1 - 5 kW (Grid Connected) $7,500 3 50% 1.5 13,140 $0.17 20 - 30 kW (Grid Connected) $6,200 25 50% 12.5 109,500 $0.14 .1 - 5 kW (Non-Grid Connected) $14,000 3 50% 1.5 13,140 $0.32 20 - 30 kW (Non-Grid Connected) $14,000 25 50% 12.5 109,500 $0.32Anaerobic Digesters c --- --- --- --- --- --- Covered Anaerobic Lagoons (Meso. & Ambient) $6,500 100 85% 85 744,600 $0.09 Complete Mix (mesophilic) $6,000 100 85% 85 744,600 $0.08 Plug Flow (mesophilic) $5,500 100 85% 85 744,600 $0.07 Attached Media (unheated) $7,500 100 85% 85 744,600 $0.10
Sources:a USDA-RUS from DOE Wind Powering Americab USDA-RUS from NREL/TP.620.29649c AgSTAR Program
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And that’s all for now...
See the AgSTAR Website at www.EPA.GOV/AGSTAR
Thank You