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ARCHIVED REPORTS_XR0008363
Environmental Health - Public
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3500 - Local Oversight Program
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PR0545864
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ARCHIVED REPORTS_XR0008363
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Last modified
7/21/2020 9:57:46 AM
Creation date
7/21/2020 9:40:00 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0008363
RECORD_ID
PR0545864
PE
3528
FACILITY_ID
FA0004530
FACILITY_NAME
MARLOWE PROPERTY
STREET_NUMBER
4648
STREET_NAME
WATERLOO
STREET_TYPE
RD
City
STOCKTON
Zip
95215
CURRENT_STATUS
02
SITE_LOCATION
4648 WATERLOO RD
P_LOCATION
99
P_DISTRICT
002
QC Status
Approved
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EHD - Public
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I <br /> 28 April 1995 <br /> AGE-NC-95-0103 <br /> Page G of 1 I <br /> 1 In a carbon-canister system, hydrocarbon vapors are routed through activated carbon filters, <br /> %%,here adsorption of hydrocarbons takes place, removing them from the vapor stream These <br />' systems .%ork- best for low concentrations of hydrocarbons, but become expensive when high <br /> concentrations of hydrocarbon vapors necessitate frequent canister replacement and disposal of <br /> spent carbon <br /> In thermal oxidation ,systems, hydrocarbons are destroyed by open-flame combustion Natural gas <br /> Y <br /> is commonly used as supplemental fuel, heating the extracted vapors to a combustion temperature <br />' of approximately 1400 °F Relative to internal combustion systems, these systems may be slightly <br /> more expensive to purchase and install Ho�%e%er, they can operate at higher air flow rates, and <br /> I therefor remediate sites at a faster rate For this system to be effecti"e, hydrocarbon <br /> concentrations should range f3 om 5,000 ppniv to 30,000 ppmv They also operate at much lower <br /> noise lexels than internal combustion systems <br /> Catalytic oxidation units provide another option for treating vadose-zone contamination, <br /> particularly af3er other extraction systems have reached their effective limits due to lowered <br /> I h)di ocai bon concentrations These systems operate at temperatures of approximately 700 °F, <br /> requii in�tZ less supplemental fuel than either thermal oxidizers or internal combustion engines <br /> Other iequiiements and limitations are similar to those for internal-combustion and thermal <br /> oxidizer sN stems <br /> 5 1 2 REQUIRED SOIL CONDITIONS <br /> Opei anon of the blower in a vapoi extraction system ci eates a vacuum in the subsurface, inducing <br /> Iair "cui i eats" through pore spaces Vapors move by convection toward the area of lowered air <br /> pressuie (the extraction point) The eflicienc\ of this process is proportiopal to soil porosity and <br /> pei meability Qualitative information has been gained through examination of soil samples and the <br /> pei formance of a vapor extraction pilot test The information indicates that soil conditions at the <br /> site ai e adequate for operation of a vapor extraction s)stem <br /> I <br /> 5 1 3 EXTRACTION WELLS <br /> At least one extraction well is required in a tiapor extraction system Well VW-1 was installed for <br /> this pui pose This well was sci eened through the contamination plume (see section 2 2) The <br /> I results of the vapor extraction test indicate that one well should be adequate to reach the <br /> pei imeter of the hydi ocarbon plume (see section 5 1 1 ) <br />
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