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Last modified
5/5/2020 9:46:00 AM
Creation date
5/5/2020 9:07:43 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
FIELD DOCUMENTS
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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Remedial Action Plan <br /> Canepa's Car Wash. 6230 Pacific Avenue. Stockton. California <br /> March 3, 2003 <br /> Page t <br /> 2.0 SUMMARY OF SITE ASSESSMENT <br /> lCanepa' s Car Wash is located in a heavily urbanized area of Stockton (Figure 1 ). The business consists of <br /> an automated car wash, a gasoline/diesel fuel station, and a convenience store. The business area is paved <br /> with either concrete or asphalt. <br /> - � 2.1 INVESTIGATION HISTORY <br /> In early 1993, three underground fuel (gasoline and diesel) storage tanks (USTs), fuel lines, and dispensers <br /> were removed and replaced with a doubled walled system. Multiple samples were collected at the site with <br /> - maximum total of petroleum hydrocarbons as gasoline (TPH-G) concentrations in soil samples collected <br /> from under the dispenser island [(3 ,800 milligrams per kilogram (mg/kg)] . Soil boring B-1 , installed in <br /> 1 March 1993, encountered groundwater approximately 56 feet below the ground surface (bgs). <br /> In September 1993 , monitoring wells MW- 1 through MW-4 were installed at the site (Figure 2). In March <br /> 1994, monitoring wells MW-5 through MW-8 were installed. Quarterly groundwater monitoring was <br /> conducted at the site from March 1994 through June 1995, and from August 1996 through the present. <br /> i` A 24-hour pump test was conducted at the site in December 1994. The results indicated an optimum pumping <br /> rate of 5 gallons per minute (gpm) with an effective radius of 140 feet. Aquifer permeability for a 20-foot <br /> screen length was estimated at 126 gallons per day per feet squared (gpd /ft), <br /> JAdditional soil borings were installed in 1998 and were described in Report — Soil and Groundwater <br /> Investigation, dated June 12, 1998. Additional soil boring installation, cone penetrometer boring installation, <br /> hydropunch sampling, and the installation of three additional wells were conducted in December 2001 and <br /> r, were described in the Additional Soil and Groundwater Investigation Report dated January 21 , 2002. <br /> In August 2001 , a sensitive receptor survey was conducted within a 2,000-foot radius of the site. The <br /> i results described in the Quarterly Groundwater Monitoring (Third Quarter 2001) and Sensitive Receptor <br /> Survey Report dated August 16, 2001 indicated the presence of several domestic and municipal wells, two <br /> schools, three child-care facilities, and three leaking underground storage tank (LUST) sites within the <br /> .i study area. No actively pumped drinking water wells were identified within 500 feet of the site. <br /> 2.2 REMEDIATION HISTORY <br /> At the time of UST removal, approximately 600 cubic yards of contaminated soil was removed. Shortly after <br /> - the new USTs were installed in 1993 , nine soil vapor extraction (SVE) wells were installed in the area of the <br /> Riel dispenser islands. An internal combustion unit (ICU) was installed for vapor extraction and treatment. <br /> I,I I The ICU operated from March 1994 through June 10, 1995 . Average influent organic vapor concentrations, <br /> measured with a photo ionization detector (PID), exceeded 2,200 parts per million (ppm). <br /> j I An evaluation of the SVE system was conducted and reported in the Soil Vapor Extraction (SVE) System <br /> Evaluation, dated September 23, 1996. That report recommended that the ICU operations be suspended <br /> because the system did not appear to meet permit conditions (95% destruction efficiency). The configuration <br /> of the existing SVE wells appeared to be sufficient to remove a majority of the remaining contaminants in the <br /> vadose zone. <br /> A larger thermal oxidizing SVE system began operation in March 1999. Initial concentrations of total volatile <br /> organics up to 1 ,050 ppm were reduced to approximately 50 ppm by February 2001 . SVE operation was <br /> stopped on February 6, 2001 as a result in a drop in the SVE efficiency below 95%. The SVE system was <br /> 4 <br /> CONDOR <br /> i <br />
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