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ARCHIVED REPORTS_XR0011009
Environmental Health - Public
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3500 - Local Oversight Program
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PR0545039
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ARCHIVED REPORTS_XR0011009
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Last modified
12/10/2019 7:32:18 PM
Creation date
12/10/2019 11:28:03 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0011009
RECORD_ID
PR0545039
PE
3528
FACILITY_ID
FA0010186
FACILITY_NAME
DEL MONTE FOODS PLNT #33 - DISCO WH
STREET_NUMBER
110
Direction
N
STREET_NAME
FILBERT
STREET_TYPE
ST
City
STOCKTON
Zip
95205
APN
15702009
CURRENT_STATUS
02
SITE_LOCATION
110 N FILBERT ST
P_DISTRICT
001
QC Status
Approved
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EHD - Public
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k4 KLEINFELDER <br /> f <br /> { 0 DIPE by EPA Method 8260B [non-detect<0.50 µg111; <br /> • ETBE by EPA Method 8260B [non-detect<0.50 µg111; and <br /> TAME by EPA Method 8260B [non-detect<0.50 µg/1]. <br /> For a summary of analytical data for the analytes listed above, please see Table 2 behind the <br /> "Tables" tab of this report. <br /> 5.3 SOIL GAS MONITORING <br /> The soil vapor extraction system installed by CH2M Hill was replaced by Kleinfelder during <br /> 2003 with an air sparging (AS)/high vacuum soil vapor extraction (SVE)/ozone injection system. <br /> The AS/SVE system consists of a network of two air sparging wells (shallow/deep) and a vapor <br /> extraction well positioned at five distinct locations, totaling fifteen wells. The ozone injection <br /> system consists of a horizontally directional drilled (HDD) conduit for ozone/air transmitted to a <br /> ( system of wells triple-nested at three different depths below groundwater, at five separate <br /> } locations, equaling fifteen wells. Active remediation began in May 2003 in the source area <br /> (actual Disco site) by means of AS/SVE utilizing a thermal/catalytic oxidizer unit. Continual <br /> operation of the thermal oxidizer began in June 2003. In July 2003, the AS/SVE unit was <br /> converted from a thermal oxidizer to catalytic oxidizer thereby optimizing the efficiency through <br /> fuel uptake. The ozone injection system began consistent operation within the downgradient <br /> portion of the plume in September 2003. The system has only been inoperable during periods of <br /> system maintenance and enhancements. <br /> During this quarter, the groundwater remediation system has undergone extensive upgrades. <br /> Flounnated Ethylene Propylene (FEP) tubing was installed within the HDD conduit and replaced <br /> the former tubing due to slight failures. The FEP tubing is even more conducive to ozone <br /> applications. A venturi injector system was also designed and installed to help reduce ozone <br /> pump pressures needed to inject the ozone in the air stream. <br /> During the fourth quarter the vapor extraction operation was shut off at wells (VE-2 —VE-5) due <br /> to the high concentrations found at VE-1 (centrally located over the former UST locations). <br /> Photo-ionization detector (PID) samples were collected from VE-1 each month during the Fourth <br /> Quarter 2004 and ranged in concentrations of 950 to 1500 ppm (before PID termination). Air <br /> inlet sampling was conducted at the main manifold of the catalytic oxidizer on November 11 and <br /> December 21, 2004. TPH-G was detected at a concentration of 310 ppmv and 730 ppmv <br /> respectively. The destruction efficiency of the thermo/catalytic oxidizer was calculated at 98%. <br /> ! I <br /> � 1 <br /> ! t <br /> 12280.M0N/ST05RI73/JZ:1v Page 9 of I I <br /> 02005,Kleinfelder, Inc. February 11,2005 <br />
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