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ARCHIVED REPORTS_XR0005629
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ARCHIVED REPORTS_XR0005629
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Last modified
11/19/2024 1:50:29 PM
Creation date
4/29/2020 2:26:09 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0005629
RECORD_ID
PR0545626
PE
3528
FACILITY_ID
FA0000957
FACILITY_NAME
LATHROP GAS & FOOD MART*
STREET_NUMBER
14800
Direction
S
STREET_NAME
STATE ROUTE 99
STREET_TYPE
RD
City
MANTECA
Zip
95336
APN
19702004
CURRENT_STATUS
02
SITE_LOCATION
14800 S HWY 99 RD
P_LOCATION
99
P_DISTRICT
005
QC Status
Approved
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SJGOV\sballwahn
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EHD - Public
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Fourth Quarter 1995 Groundwater Monitoring&Remediation Status Report <br /> Moore Petroleum, 14800 W Frontage Rd,Manteca,CA <br /> January 19, 1996 <br /> Page 3 <br /> On September 19, 1995, the vapor extraction rate was 43 standard cubic feet per minute(SCFM) <br /> Based on the vapor sample analytical results for this date the system extraction rate was 3 5 pounds <br /> per day(Ib/day) of TPA as gasoline Benzene was not detected in the influent to the vapor <br /> extraction system On November 27, 1995,the vapor extraction rate was 43 SCFM Based on the <br /> vapor sample analytical results for this date the system extraction rate was 7 01b/day of TPH, as <br /> t gasoline Benzene was not detected m the influent to the vapor extraction system. On December 5, <br /> 1995, the vapor extraction rate was 43 SCFM Based on the vapor sample analytical results for <br /> this date the system extraction rate was 5 81b/day of TPH, as gasoline Benzene was not detected <br /> in the influent to the vapor extraction system Air analytical results and cham-of-custody forms are <br /> contained in Attachment 3 As of December 5, 1995, the vapor extraction system has extracted <br /> approximately 2,090 lbs of TPH, as gasoline, and 7 6 lbs of benzene <br /> System operating data are contained in Table 3 Mass extraction rates to date, based on laboratory <br /> analytical results, are contained in Table 4 Example calculations are contained in Attachment 4 <br /> Groundwater Remediation System <br /> On January 23, 1995, Emcon started a groundwater treatment system at the subject site The <br />' groundwater treatment system is pneumatically operated via compressed air supplied from the <br /> RS I unit and extracts groundwater from monitoring wells MW 1, MW-2, MW-3 and MW-4 <br /> Once the groundwater arrives in the remediation compound via V diameter PVC piping, it is <br /> filtered through two m-line particulate filters and then through two m-line, 400 lb carbon vessels <br /> Upon discharging from the carbon vessels, it is reinjected through two remjection wells, RW-1 and <br />' RW-2, located to the west of the remediation compound (Figure 2) <br /> During this reporting period, water flow through the treatment system has ranged from 1 0 gallon <br />' per minute (g p m.) on November 29 to 3 0 g p in. on November 21, 1995 Groundwater samples <br /> were collected from the system mfluent and effluent on September 26 and November 29, 1995 to <br /> demonstrate compliance with Land Discharge Permit Order No 91-25013 The system was not <br />' sampled during the month of October or December due to a system malfiwction <br /> On September 26, 1995, the groundwater extraction rate was 1 5 g p m. Based on water sample <br />' analytical results for this date, concentrations of both TPH, as gasoline, and benzene were below <br /> laboratory detection limits, therefore system extraction rates were zero for this sampling event On <br /> November 29, 1995,the groundwater extraction rate was 10 g p m. Based on water sample <br />' analytical results for this date, concentrations of both TPR as gasoline, and benzene were below <br /> laboratory detection hunts, therefore system extraction rates were zero for this sampling event <br /> As of November 29, 1995 the groundwater treatment system has extracted approximately 18 lbs. <br /> of TPI, as gasoline, and 0 37 Ibs. of benzene <br /> 1 <br />
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