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3500 - Local Oversight Program
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PR0544465
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Entry Properties
Last modified
5/16/2019 11:54:59 AM
Creation date
5/16/2019 11:30:23 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
WORK PLANS
RECORD_ID
PR0544465
PE
3528
FACILITY_ID
FA0005837
FACILITY_NAME
STEFANOS GASOLINE*
STREET_NUMBER
1419
Direction
E
STREET_NAME
CHARTER
STREET_TYPE
WAY
City
STOCKTON
Zip
95205
APN
15137016
CURRENT_STATUS
02
SITE_LOCATION
1419 E CHARTER WAY
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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4-5j..Oxidation ,. _ r . Page ] of 5 <br /> 4.57 Oxidation <br /> mediation Technologies Screening Matrix (Off-Gas Treatment Technology) <br /> and Reference Guide, Version 4.0 <br /> Description Synonyms Applicability Limitations Site Information Points of Contact <br /> Data Needs Performance Cost References Vendor Info. Health&Safety <br /> Technology>> Air Emissions/Off-Gas Treatment <br /> of Contents <br /> >>3.14 Air Emissions/Off-Gas Treatment <br /> Introduclion <br /> »4.57 Oxidation <br /> Introduction>> Organic contaminants are destroyed in a high temperature 1,000°C (' <br /> combustor. Trace organics in contaminated air streams are destroyec <br /> temperatures, 450 °C (842 °F), than conventional combustion by pas, <br /> mixture through a catalyst. <br /> j, Appendices <br /> Description. <br /> Figure_4-57: <br /> TV ical Oxidation Diagram <br /> Oxidation equipment(thermal or catalytic) is used for destroying contaminants in the <br /> exhaust gas from air strippers and SVE systems. Thermal oxidation units are typically <br /> single chamber, refractory-lined oxidizers equipped with a propane or natural gas burner <br /> and a stack. Lightweight ceramic blanket refractory is used because many of these units <br /> are mounted on skids or trailers. If gasoline is the contaminant, heat exchanger efficiencies <br /> are limited to 25 to 35%, and preheat temperatures are maintained below 180 °C (530 °F) <br /> to minimize the possibility of ignition occurring in the heat exchanger. Flame arrestors are <br /> always installed between the vapor source and the thermal oxidizer. Burner capacities in <br /> the combustion chamber range from 0.5 to 2 million Btus per hour. Operating temperatures <br /> range from 760 to 870 °C (1,400 OC to 1,600 °F), and gas residence times are typically 1 <br /> second or less. <br /> J. <br /> Catalytic oxidation is a relatively recently applied alternative for the treatment of VOCs in <br /> air streams resulting from remedial operations. The addition of a catalyst accelerates the <br /> rate of oxidation by adsorbing the oxygen and the contaminant on the catalyst surface <br /> where they react to form carbon dioxide, water, and hydrochloric gas. The catalyst enables <br /> the oxidation reaction to occur at much lower temperatures than required by a conventional <br /> thermal oxidation. VOCs are thermally destroyed at temperatures typically ranging from <br /> 320° to 540° C (600° to 1,000° F) by using a solid catalyst. First, the contaminated air is <br /> directly preheated (electrically or, more frequently, using natural gas or propane)to reach a <br /> temperature necessary to initiate the catalytic oxidation [310 °C to 370 OC (600 °C to 700 ° <br /> F)] of the VOCs. Then the preheated VOC-laden air is passed through a bed of solid <br /> catalysts where the VOCs are rapidly oxidized. Thermal oxidizers can often be converted <br /> to catalytic units after initially high influent contaminant concentrations decrease to less <br /> than 1,000 to 5,000 ppmv. <br /> > CataVic Oxidation <br /> Catalyst systems used to oxidize VOCs typically use metal oxides such as nickel oxide, <br /> copper oxide, manganese dioxide, or chromium oxide. Noble metals such as platinum and <br /> palladium may also be used. Most commercially available catalysts are proprietary. <br /> http://w-ww.frtr.gov/matrix2/section4/4-59.htmi 10/22/2004 <br />
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