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ARCHIVED REPORTS XR0001108
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3500 - Local Oversight Program
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PR0544231
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ARCHIVED REPORTS XR0001108
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Entry Properties
Last modified
3/6/2019 4:31:32 PM
Creation date
3/6/2019 2:12:18 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0001108
RECORD_ID
PR0544231
PE
3526
FACILITY_ID
FA0023968
FACILITY_NAME
NOMELLINI CONSTRUCTION CO
STREET_NUMBER
1045
Direction
W
STREET_NAME
CHARTER
STREET_TYPE
WAY
City
STOCKTON
Zip
95206
APN
16323040
CURRENT_STATUS
02
SITE_LOCATION
1045 W CHARTER WAY
P_LOCATION
01
QC Status
Approved
Scanner
WNg
Tags
EHD - Public
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14 November 1995 `r <br /> AGE-NC Project No 95-0121 <br />' Page 8 of 20 <br /> , <br /> concentrations decrease below levels normally required for combustion Typically, internal <br />' combustion engines work effectively where m-situ hydrocarbon concentrations approach the 40,000 <br /> ppmv required for peak performance ofthe engine As concentrations decrease below 20,000 ppmv, <br />' supplemental fuel requirements become burdensome Another disadvantage of these systems is the <br /> noise generated by the engine, however, tins can be mitigated by placing the unit inside an enclosure, <br /> such as a building T <br /> In a carbon-canister system, hydrocarbon vapors are routed through activated carbon filters, where <br /> adsorption of the hydrocarbons takes place, removing them from the vapor stream These systems <br />' work best for low concentrations of hydrocarbons, but become expensive when high concentrations <br /> „ of hydrocarbon vapors necessitate frequent canister replacement and disposal of spent carbon ' <br /> 1 r ! <br />' In thermal oxidation systems, hydrocarbons are destroyed by open-flame combustion Natural gas is <br /> commonly used as supplemental fuel, heating the extracted vapors to a combustion temperature of <br /> r approximately 1400°F Relative to internal combustion systems, these systems may be slightly more <br /> expensive to purchase and install However, they can operate at higher air flow rates, and therefore <br /> remediate sites at a faster rate For this system to be effective, hydrocarbon concentrations should <br /> range from 5,000 ppmv to 30,000 ppmv They also operate at much lower noise levels than internal <br /> combustion systems <br /> r Catalytic oxidation units provide another option for treating vadose-zone contamination, particularly <br /> after other extraction systems have reached their effective limits due to lowered hydrocarbon <br /> concentrations These systems operate at temperatures of approximately 700°F, requiring less <br /> r supplemental fuel than either thermal oxidizers or internal combustion engines Other requirements <br /> and limitations are similar to those for internal-combustion and thermal oxidizer systems ' <br /> 6 12, EFFECTIVE SOIL CONDITIONS <br /> t 1 <br /> Operation of the blower in a vapor extraction system creates a vacuum in the subsurface, inducing <br /> air flow through the soil,pore spaces Vapors move by convection toward the area of lowered air 1 } <br /> pressure (the extraction point) The efficiency of this process is proportional to soil porosity and <br /> rpermeability Qualitative information has been gained through examination of soil samples and the <br /> perforance of a vapor extraction pilot test Soil at this <br /> msite has a high clay content, making vapor <br /> extraction a more difficult and slow process i <br /> r <br /> y4 i <br /> 6 1 3 MONITORING ACTIVITIES <br /> Monitoring of vapor extraction systems involves weekly measurement of vapor hydrocarbon <br /> r <br /> r <br />
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