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Thermochemical Conversion Technologies
Combustion Types
Incineration (energy recovery through complete oxidation)– Mass Burn– Refuse Derived Fuel
PyrolysisGasificationPlasma arc (advanced thermal
conversion)
Gasification
Partial oxidation process using air, pure oxygen, oxygen enriched air, hydrogen, or steam
Produces electricity, fules (methane, hydrogen, ethanol, synthetic diesel), and chemical products
Temperature > 1300oFMore flexible than incineration, more
technologically complex than incineration or pyrolysis, more public acceptance
Flexibility of Gasification
Pyrolysis
Thermal degradation of carbonaceous materials Lower temperature than gasification (750 – 1500oF) Absence or limited oxygen Products are pyrolitic oils and gas, solid char Distribution of products depends on temperature Pyrolysis oil used for (after appropriate post-
treatment): liquid fuels, chemicals, adhesives, and other products.
A number of processes directly combust pyrolysis gases, oils, and char
Pyrolyzer—Mitsui R21
Thermoselect (Gasification and Pyrolysis) Recovers a synthesis gas, utilizable glass-like
minerals, metals rich in iron and sulfur from municipal solid waste, commercial waste, industrial waste and hazardous waste
High temperature gasification of the organic waste constituents and direct fusion of the inorganic components.
Water, salt and zinc concentrate are produced as usable raw materials during the process water treatment.
No ashes, slag or filter dusts 100,000 tpd plant in Japan operating since
1999
Thermoselect (http://www.thermoselect.com/index.cfm)
Fulcrum Bioenergy MSW to Ethanol Plant
Plasma Arc Heating Technique using electrical arc Used for combustion, pyrolysis, gasification, metals
processing Originally developed by SKF Steel in Sweden for
reducing gas foriron manufacturing Plasma direct melting reactor developed by
Westinghouse Plasma Corp. Further developed for treating hazardous feedstocks
(Contaminated soils, Low-level radioactive waste, Medical waste)
Temperatures (> 1400oC) sufficient to slag ash Plasma power consumption 200-400 kWh/ton Commercial scale facilities for treating MSW in Japan
Plasma Arc Technology in FloridaGreen Power Systems is proposing to build
and operate a plasma arc facility to process 1,000 tons per day of municipal solid waste (garbage) in Tallahassee, Florida.
Geoplasma is proposing to build a similar facility for up to 3,000 tons of solid waste per day in St. Lucie County, claims 120 MW will be produced
Health risks, economics, and technical issues still remain
Process
Heated using – direct current arc plasma for high T
organic waste destruction and gasification and
– Alternating current powered, resistance hearing to maintain more even T distribution in molten bath
Waste Incineration - Advantages• Volume and weight reduced (approx. 90% vol. and
75% wt reduction)• Waste reduction is immediate, no long term
residency required• Destruction in seconds where LF requires 100s of
years• Incineration can be done at generation site • Air discharges can be controlled • Ash residue is usually non-putrescible, sterile,
inert• Small disposal area required• Cost can be offset by heat recovery/ sale of energy
Waste Incineration - DisadvantagesHigh capital costSkilled operators are required
(particularly for boiler operations)
Some materials are noncombustible
Some material require supplemental fuel
Waste Incineration - Disadvantages Air contaminant potential (MACT standards
have substantially reduced dioxin, WTE 19% of Hg emissions in 1995 – 90% reduction since then)
Volume of gas from incineration is 10 x as great as other thermochemical conversion processes, greater cost for gas cleanup/pollution control
Public disapprovalRisk imposed rather than voluntaryIncineration will decrease property value
(perceived not necessarily true)Distrust of government/industry ability to
regulate
Carbon and Energy Considerations Tonne of waste creates 3.5 MW of
energy during incineration (eq. to 300 kg of fuel oil) powers 70 homes
Biogenic portion of waste is considered CO2 neutral (tree uses more CO2 during its lifecycle than released during combustion)
Unlike biochemical conversion processes, nonbiogenic CO2 is generated
Should not displace recycling
WTE Process
Three Ts
TimeTemperatureTurbulence
System Components
Refuse receipt/storageRefuse feedingGrate systemAir supplyFurnaceBoiler
Energy/Mass Balance
Waste Flue Gas
Energy Loss (Radiation)
Mass Loss (unburnedC in Ash)
Flue Gas Pollutants
ParticulatesAcid GasesNOx
COOrganic Hazardous Air PollutantsMetal Hazardous Air Pollutants
Particulates
Solid Condensable Causes
– Too low of a comb T (incomplete comb) – Insufficient oxygen or overabundant EA (too high T) – Insufficient mixing or residence time – Too much turbulence, entrainment of particulates
Control– Cyclones - not effective for removal of small
particulates – Electrostatic precipitator – Fabric Filters (baghouses)
Metals
Removed with particulates Mercury remains volatilized Tough to remove from flue gas Remove source or use activated
carbon (along with dioxins)
Acid Gases
From Cl, S, N, Fl in refuse (in plastics, textiles, rubber, yd waste, paper)
Uncontrolled incineration - 18-20% HCl with pH 2
Acid gas scrubber (SO2, HCl, HFl) usually ahead of ESP or baghouse – Wet scrubber – Spray dryer – Dry scrubber injectors
Nitrogen removal
Source removal to avoid fuel NOx production
T < 1500 F to avoid thermal NOx
Denox sytems - selective catalytic reaction via injection of ammonia
Air Pollution Control
Remove certain waste componentsGood Combustion PracticesEmission Control Devices
Devices
Electrostatic PrecipitatorBaghousesAcid Gas Scrubbers
– Wet scrubber– Dry scrubber– Chemicals added in slurry to neutralize
acids
Activated CarbonSelective Non-catalytic Reduction
Role of Excess Air – Control Three Ts
Amount of Air Added
Insufficient O2
Stoichiometric
Excess Air
T
Role of Excess Air – Cont’d
Insufficient O2
Stoichiometric
Excess Air
Increasing Moisture
Amount of Air Added
Role of Excess Air – Cont’d
Insufficient O2
Stoichiometric
Excess Air
PICs/Particulates
NOxT
Optimum T Range
(1500 – 1800 oF)
Amount of Air Added
Ash
Bottom Ash – recovered from combustion chamber
Heat Recovery Ash – collected in the heat recovery system (boiler, economizer, superheater)
Fly Ash – Particulate matter removed prior to sorbents
Air Pollution Control Residues – usually combined with fly ash
Combined Ash – most US facilities combine all ashes
Schematic Presentation of Bottom Ash Treatment
Ash Reuse Options
Construction fillRoad constructionLandfill daily cover Cement block productionTreatment of acid mine drainage
StackRefuse Boiler
TippingFloor
Fabric FilterSpray Dryer
Metal Recovery
Ash Conveyer
Mass Burn Facility – Pinellas County
Overhead Crane
Turbine Generator
Fabric Filter
Conclusions
Combustion remains predominant thermal technology for MSW conversion with realized improvements in emissions
Gasification and pyrolysis systems now in commercial scale operation but industry still emerging
Improved environmental data needed on operating systems
Comprehensive environmental or life cycle assessments should be completed