Municipal Solid Waste Incineration
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Transcript Municipal Solid Waste Incineration
Municipal Solid Waste
Incineration
Combustion Types
Incineration (energy recovery through
complete oxidation)
– Mass Burn
– Refuse Derived Fuel
Pyrolysis
Gasification
Plasma arc (advanced thermal
conversion)
Gasification
Partial oxidation process using air, pure
oxygen, oxygen enriched air, or steam
Carbon converted into syngas
More flexible than incineration
More public acceptance
Flexibility of Gasification
Pyrolysis
Thermal degradation of carbonaceous
materials
Lower temperature than gasification
Absence or limited oxygen
Products are gas, liquid, solid char
Distribution of products depends on
temperature
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
Environmental Considerations
Tonne of waste creates 3.5 MW of
energy (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)
Should not displace recycling
Waste Incineration Disadvantages
• High capital cost
• Skilled operators are required (particularly for boiler
operations)
• Some materials are noncombustible
• Some material require supplemental fuel
• Public disapproval
Risk imposed rather than voluntary
Incineration will decrease property value (perceived not
necessarily true)
Distrust of government/industry ability to regulate
Three Ts
Time
Temperature
Turbulence
System Components
Refuse receipt/storage
Refuse feeding
Grate system
Air supply
Furnace
Boiler
Energy/Mass Balance
Energy Loss (Radiation)
Waste
Flue Gas
Mass Loss (unburned
C in Ash)
Flue Gas Pollutants
Particulates
Acid Gases
NOx
CO
Organic Hazardous Air Pollutants
Metal 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 components
Good Combustion Practices
Emission Control Devices
Devices
Electrostatic Precipitator
Baghouses
Acid Gas Scrubbers
– Wet scrubber
– Dry scrubber
– Chemicals added in slurry to neutralize acids
Activated Carbon
Selective Non-catalytic Reduction
Role of Excess Air – Control
Three Ts
Stoichiometric
T
Insufficient O2
Excess Air
Amount of Air Added
Role of Excess Air – Cont’d
Stoichiometric
Increasing Moisture
Insufficient O2
Excess Air
Amount of Air Added
Role of Excess Air – Cont’d
Stoichiometric
NOx
T
Optimum T
Range
(1500 – 1800 oF)
PICs/Particulates
Insufficient O2
Excess Air
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 fill
Road construction
Landfill daily cover
Cement block production
Treatment of acid mine drainage
Refuse Boiler
Stack
Fabric Filter
Spray Dryer
Ash Conveyer
Metal Recovery
Mass Burn Facility – Pinellas County
Tipping
Floor
Overhead Crane
Turbine Generator
Fabric Filter
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Updated August 2005