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ARCHIVED REPORTS_1979
EnvironmentalHealth
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4400 - Solid Waste Program
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PR0440014
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ARCHIVED REPORTS_1979
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Last modified
7/17/2020 2:15:59 PM
Creation date
7/3/2020 11:16:16 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
4400 - Solid Waste Program
File Section
ARCHIVED REPORTS
FileName_PostFix
1979
RECORD_ID
PR0440014
PE
4445
FACILITY_ID
FA0001304
FACILITY_NAME
STOCKTON SCAVENGERS ASSOCIATION
STREET_NUMBER
1240
STREET_NAME
NAVY
STREET_TYPE
DR
City
STOCKTON
Zip
95206
CURRENT_STATUS
02
SITE_LOCATION
1240 NAVY DR
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
Scanner
CField
Supplemental fields
FilePath
\MIGRATIONS\SW\SW_4445_PR0440014_1240 NAVY_1979.tif
Tags
EHD - Public
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The trommel through-put, the majority of which is combustible, is <br /> transferred to another inclined steel pan, cleated conveyor, which <br /> deposits the fuel product on the incinerator feed storage floor. <br /> At this point, a front-end loader either stockpiles the fuel prod- <br /> uct or feeds the incinerator charge boxes. The incinerator feed <br /> storage area has a minimum capacity of 4 days of processed refuse. <br /> The steam or electric power generating section is designed to <br /> operate 24 hours per day, 7 days per week. <br /> From their charging boxes, the fuel product is fed into a primary <br /> chamber where it is burned under controlled air conditions. The <br /> resulting; gases are passed through a second chamber, where excess <br /> air is injected to complete combustion. Auxiliary fuel is required <br /> in minimal quantities to maintain proper combustion temperatures. <br /> Combustible particulate matter burns off, and the hot cases are <br /> passed through a waste heat boiler to produce steam, which may be <br /> sold directly or, if electricity is to be produced, piped to a <br /> turbogenerator, then through a condenser in which heat transfer <br /> is accomplished by cooling tower water. The condensate is then <br /> piped back to the boiler. Makeup water is required for the boiler <br /> because of blowdown and evaporation losses and is also required <br /> for the cooling tower because of evaporation losses. Cooling tower <br /> makeup water is subjected to chlorination. The flue gas train in- <br /> cludes fans and a baghouse. <br /> Residue remainingafter combustion soon is dropped into an ash pit where <br /> it is water-quenched and mechanically conveyed to a storage bin to <br /> await truck transport to a landfill. <br /> Electricity, if generated, will be produced at a maximum of 13 , 800 <br /> volts, 3 phase, 60 Hz. Generated electricity is used for both in- <br /> plant processing and export as an energy product. Power will be <br /> provided at 13 , 800 volts to the electrical distribution network <br /> for transformation (if required) and transmission. <br /> The package incinerator units utilize No. 2 fuel oil for start-up, <br /> temperature maintenance and as a back-up fuel should the supply of <br /> refuse be cut off. Sufficient on-site storage has been provided <br /> for a minimum of 5 days of operating only on fuel oil. The capa- <br /> bility to transfer wastes directly to long-haul vehicles for deliv- <br /> ery to the landfill will be maintained as a back-up in the event <br /> of a total process shutdown. <br /> Basic Design Parameters <br /> Parameters used to design the package incinerator/power plants are <br /> listed below in Table 5-1. <br /> 20, <br />
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