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ARCHIVED REPORTS_XR0007874
Environmental Health - Public
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EHD Program Facility Records by Street Name
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WILSON
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2900 - Site Mitigation Program
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PR0507217
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ARCHIVED REPORTS_XR0007874
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Entry Properties
Last modified
10/8/2020 10:09:58 PM
Creation date
6/23/2020 2:52:44 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0007874
RECORD_ID
PR0507217
PE
2950
FACILITY_ID
FA0007741
FACILITY_NAME
AUTO ZONE INC
STREET_NUMBER
1100
Direction
N
STREET_NAME
WILSON
STREET_TYPE
WAY
City
STOCKTON
Zip
95202
APN
11733035
CURRENT_STATUS
02
SITE_LOCATION
1100 N WILSON WAY
P_LOCATION
01
QC Status
Approved
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EHD - Public
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i <br /> f MANUFACTURER DATA ON THERMAL OXIDIZER <br /> (REFERENCE: USTEC, September 20, 199 1) <br /> . f , <br /> �k <br /> ` 5.4 THERMAL OXIDATION UNIT <br /> The thermal oxidation unit is illustrated on Figure lb. A detailed description of the unit is <br /> presented in the following paragraphs. <br /> L � <br /> �. 3.4.1 Regenerative Oxidation Process <br /> The oxidizer bed consists of a reinforced, insulated, fabricated-steel chamber filled with silica <br /> gravel. Electrical heating elements are distributed in the bed. Passages are Iocated above and <br /> ! below the oxidizer bed to allow the process gas flow to be reversed through the bed. In order <br /> to avoid an uneven temperature distribution throughout the bed, the gas flow is controlled by <br /> an automatic valve that changes the direction of the gas flow at regular intervals typically <br /> i ranging from 50 to 480 seconds. This maintains a uniform temperature distribution throughout <br /> ' i <br /> the entire bed. Maximum heat recovery is obtained when incoming process gas is preheated <br /> ! through the exchange of exhaust gas heat energy within the silica-based oxidizer bed. <br /> 1 ?0 <br /> r <br /> 3 <br /> L <br />
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