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ARCHIVED REPORTS_XR0007874
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0507217
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ARCHIVED REPORTS_XR0007874
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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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Working To Restore Nature <br /> Addendum One to Remedial Action Plan March 1, 1993 <br /> Coca-Cola Former Distribution Facility, Stockton, California 54006.01 <br /> to an area within an approximately 20 foot radius surrounding the former underground <br /> gasoline storage tank, and down to a depth of about 25 feet (USTEC, November 1990 and <br /> ' December 1991) Wells VEW 3 and VEW 7 are screened substantially deeper than the <br /> vertical area of concern, and will be grouted with a cement/bentomte slurry from the <br /> bottom of the well up to 30 feet below the existing grade. <br /> ' Subsurface PVC collection pipe will direct extracted vapors to the remediation compound <br /> where the vapors will be treated prior to discharge through a stack. Process equipment in <br /> the remediation compound includes a skid-mounted condensate separator to remove <br /> particulates and condensed water, a condensate storage tank and double containment tank, <br /> a skid-mounted vacuum blower, a skid-mounted thermal oxidizer and associated equipment <br /> and controls, and a remote monitoring system. The remediation compound will be fenced <br /> to preclude public access. The proposed design flows for the vapor extraction system are <br /> 75 cubic feet per minute (cf n) per well with a total design flow of 225 cfrn, at a design <br /> wellhead vacuum of 60-inches of water. The system will be permitted for the full capacity <br /> of the thermal oxidizer, 600 cfm, in order to increase well flows as soil conditions allow, to <br /> add more wells to the system if needed at a future date, and to add dilution air to the <br /> ` system to maintain the optimum vapor to oxygen ratio for peak efficiency. In addition, it <br /> is recommended that a second PVC pipe be installed in the vapor collection pipe trench for <br /> potential future use as a groundwater double containment pipe. If a groundwater treatment <br /> system is required at a future date, the water collection pipe can be inserted in the double <br /> containment pipe without need to retrench the entire area and disrupt existing commercial <br /> ' operations at the site, and the cost will be reduced since the major cost of laying pipe is due <br /> to the cost of labor rather than the cost of the PVC pipe. <br /> ' The proposed operating plan is to bring well VEW 3, the well located in the former tank <br /> pit, on line first for approximately 30 days in order to prevent lateral and vertical migration <br /> of the vapor plume. Then all three wells will be operated during the second and following <br /> ' months. <br /> Proposed Scope of Work <br /> Based on the results ofP revious work at the site, RESNA proposes the following project <br /> Tasks 1 through 12 listed below to accomplish the engineering design, permitting, <br /> ' construction, and operation of a soil remediation system. The tasks are listed below and <br /> described in detail in this report. <br /> u <br />
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