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ARCHIVED REPORTS_XR0006750
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0543479
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ARCHIVED REPORTS_XR0006750
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Last modified
5/5/2020 10:31:54 AM
Creation date
5/5/2020 9:54:47 AM
Metadata
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Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0006750
RECORD_ID
PR0543479
PE
2960
FACILITY_ID
FA0024679
FACILITY_NAME
CANEPA'S CAR WASH
STREET_NUMBER
6230
STREET_NAME
PACIFIC
STREET_TYPE
AVE
City
STOCKTON
Zip
95204
APN
081360030
CURRENT_STATUS
01
SITE_LOCATION
6230 PACIFIC AVE
P_LOCATION
01
QC Status
Approved
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EHD - Public
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1 i • <br /> I <br /> E] REACTOR: <br /> The reactor interior shall be constructed of 3041, stainless steel The exterior shell shall be <br /> constructed of hot rolled steel with a single coat of UV resistant polyurethane spatter coating <br />' High density ceramic insulation shall be placed between the uiner and outer shells to maintain <br /> external skin temperature at safe levels The catalyst shall be contained is a fully welded 304L <br /> stainless steel bed configuration with high temperature gasketnng to ensure no VOC bypass <br />' Temperature thermocouples shall be located before and after the catalyst bed for proper control <br /> of temperature within the reactor <br />' F] CATALYST: <br /> The catalyst shall conform to the following specifications to achieve the required 98+% non <br />' methane hydrocarbon (NMHC) destruction efficiency <br /> Catalyst Type Johnson Matthey <br />' Gas Hourly Space Velocity 46,875 hrs-1 <br /> Volume of Catalyst 0 16 ft' <br /> Minimum Catalyst Inlet Temperature 600°F <br /> Maximum Catalyst Outlet Temperature 1,150°F <br /> The catalyst shall be positioned to maintain uniform an-flow and temperature throughout the <br /> catalyst bed The expected catalyst life shall be 30,000 hours of operation Additional catalyst <br /> is available for higher destruction efficiency if required <br /> G] HEAT EXCHANGER: <br /> A heat exchanger shall be supplied to preheat the intoning air stream and reduce awdlnary fuel <br /> consumption The VOC laden air shall pass through the cold side of the exchanger and the hot <br /> purified air shall pass through the hot side <br /> H] EXHAUST STACK: <br /> A stainless steel no-loss type exhaust stack with sampling ports shall be provided for mountmg <br />' to the exhaust port flange atop the VTM The stack discharge height shall be 15 feet above <br /> grade Additional lengths of stack are available for an additional charge, to meet local <br /> miimum height requirements <br /> CONDOR EARTH TECHNOLOGIES <br /> GBL-8585 <br />
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