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ARCHIVED REPORTS XR0003442
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PR0544595
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ARCHIVED REPORTS XR0003442
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Last modified
6/24/2019 12:11:34 PM
Creation date
6/24/2019 11:13:34 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0003442
RECORD_ID
PR0544595
PE
3528
FACILITY_ID
FA0002048
FACILITY_NAME
TESORO (Shell) 68221(WRR 6290)
STREET_NUMBER
2705
STREET_NAME
COUNTRY CLUB
STREET_TYPE
BLVD
City
STOCKTON
Zip
95204
APN
12121008
CURRENT_STATUS
02
SITE_LOCATION
2705 COUNTRY CLUB BLVD
P_LOCATION
01
P_DISTRICT
003
QC Status
Approved
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EHD - Public
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Ms Marla D Guensler <br /> Exxon Company, U S A <br /> August 20, 1997 <br /> Page 5 <br /> The average vacuum applied to VEW-3 was 70 inches of water column, and the average air flow rate <br /> recorded during the test was 46 5 cubic feet per minute (cfm) The average vacuum applied to VEW-1 <br /> was also 70 inches of water column with a corresponding average air flow rate of 9 4 cfm The air <br /> flow rates from the SVE wells were calculated from measurements of the airstream velocity using an <br /> anemometer located at the discharge stack Calculations of the average air flow rate, average length of <br /> available screen, and the average flow rate per foot of screen are included in Enclosure H <br /> Calculations have been performed to estimate the soil vapor flow rates and soil vapor hydrocarbon <br /> extraction rates from each of the test wells during the pilot testing The mass flow rates from the test <br /> conducted on VEW-3 were not calculated due to nondetectable concentrations The average mass flow <br /> rate from the test conducted on VEW-I was calculated to be 0 25 pounds per day The average mass <br /> flow rate calculation is included in Enclosure H <br /> No measurable vacuums were noted in the surrounding monitoring wells during both tests Based on <br /> the results of the SVE pilot tests, an effective radius of vacuum influence could not be assessed <br /> Discussion of SVE Pilot Test Results <br />. The SVE pilot tests performed on VEW-3 and VEW-1 both reported average vacuums of 70 inches of <br /> water column, average airflow rates of 46 5 and 9 4 cfm, and average flow rates per length of screen of <br /> 10 3 and 10 4 cubic feet per foot of screen, respectively Based on Delta's experience with SVE <br /> systems, a flow rate of 1 cfm per foot of screen is generally considered to be adequate for effective <br /> removal of petroleum hydrocarbons from soil However, based on the low influent TPPH as gasoline <br /> concentrations and the lack of a measurable vacuum in the surrounding monitoring wells, it is <br /> anticipated that a SVE system would not be economically practical for this site at this time Instead, it <br /> is recommended that a low flow bioventing/air sparging system be installed at the site as a remedial <br /> option <br /> Proposed Remedial Alternative <br /> An extended air sparging test was conducted at the site from March 13, to July 17, 1995 The results <br /> of the air sparging test are included in Delta's report dated August 15, 1995 Based on data from the <br /> SVE pilot test performed on June 5, 1997, and the air sparging test conducted in 1995, Delta <br /> recommends that a low flow bioventing/air sparging system be installed as a remedial alternative The <br /> proposed low flow bioventmg/spargmg system would initially consist of a Rotron 454 or equivalent <br /> blower, controls, existing system piping, and vapor extraction wells VEW-1 and VEW-3 Air would <br /> be injected into VEW-1 and VIEW-3 during low ground water elevation periods It is anticipated that <br /> the injected air would increase soil oxygen levels which in turn would enhance natural biological <br /> attenuation in the soil matrix With a low injection flow rate of between approximately 5 and 10 efim <br /> per well, the probability of soil vapor migration would be reduced to a minimum while still delivering <br /> an adequate amount of oxygen to the soil to enhance biological activity Additionally, during seasonal <br />. periods of high ground water elevations, the system would be converted to a low flow sparging; system <br /> by adding a small GAST or equivalent oilless air compressor A drop tube would then be connected to <br /> a KVA or equivalent sparge point which would be installed in VEW-1 and VEW-3 approximately <br /> 3 feet below the surface of the ground water The air compressor would be used to inject air into the <br /> ground water at approximately 3 to 5 cfm per well It is anticipated that this would increase the <br />
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