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ARCHIVED REPORTS_XR0007731
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0507153
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ARCHIVED REPORTS_XR0007731
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Last modified
10/8/2020 10:45:45 PM
Creation date
6/23/2020 11:02:51 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0007731
RECORD_ID
PR0507153
PE
2950
FACILITY_ID
FA0007717
FACILITY_NAME
THRIFTY OIL #171
STREET_NUMBER
1250
Direction
N
STREET_NAME
WILSON
STREET_TYPE
WAY
City
STOCKTON
Zip
95205
APN
11731001
CURRENT_STATUS
02
SITE_LOCATION
1250 N WILSON WAY
QC Status
Approved
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EHD - Public
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• zone and lowers the level of static groundwater Three components must be considered in <br /> implementing vapor extraction technology, the vapor collection system, the air moving device, <br /> and the vapor treatment system <br /> The air collection system will consist of several vertical well points that currently exist on the <br /> property The western soil contarunation area will be treated by vapor extraction using wells <br /> TB4, TB6, and MW5 Each of these wells is accessible to a pre-installed vapor recovery line <br /> that extends to the proposed treatment area The eastern soil contamination area will be <br /> similarly treated using wells TB9, TB7, TB 12, and MW2, which are also connected to the <br /> mainline vapor piping Currently, there are no lines extending to the third area of <br /> contamination, near TB3 A separate line may be run to this well if necessary Also in an <br /> attempt to mitigate the downgradient portion of the dissolved plume, wells MW3R, TB8, and <br /> MW6 will be connected to the vapor extraction system The individual wells will be equipped <br /> with a ball valve to control flow from each well <br /> Based on the available information, a positive displacement blower capable of moving air at <br /> 200 cubic feet per minute(cfin) at about 75 inches of water vacuum will be sufficient for use at <br /> this site However, because of the high vacuums encountered with the low flow rates of the <br /> test, the blower should be capable of a wide range of flow performance so that it can be <br /> adjusted if necessary The actual operating flow rate of the system will likely be 100-150 cfn <br /> After removal from the subsurface, vapors will be treated by an appropriate medium Several <br /> technologies exist for treatment of hydrocarbon vapors These include activated carbon, <br /> catalytic oxidation, and thermal oxidation In determining which is most cost effective for any <br /> particular site, two important factors need to be considered The first is the volume and type of <br /> contaminant to be removed, the second is the contaminant removal rate and corresponding <br /> concentration of vapors in the air stream <br /> Page 9 <br />
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