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ARCHIVED REPORTS_XR0005088
EnvironmentalHealth
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3500 - Local Oversight Program
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PR0545571
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ARCHIVED REPORTS_XR0005088
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Last modified
9/16/2020 1:42:05 AM
Creation date
3/18/2020 4:03:36 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0005088
RECORD_ID
PR0545571
PE
3528
FACILITY_ID
FA0003570
FACILITY_NAME
BOBS MUFFLER & RADIATOR
STREET_NUMBER
466
STREET_NAME
MOFFAT
STREET_TYPE
BLVD
City
MANTECA
Zip
95336
APN
22104019
CURRENT_STATUS
02
SITE_LOCATION
466 MOFFAT BLVD
P_LOCATION
04
P_DISTRICT
005
QC Status
Approved
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SJGOV\sballwahn
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EHD - Public
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11 February 2003 <br /> AGE-NC Project No. 98-0520 <br /> ' Page 8 of 21 <br /> concentrations approach the 40,000 parts per million - volume (ppmv) required for peak <br /> r perfoi=mance of the engine. As concentrations decrease below 20,000 ppmv, supplemental fuel <br /> requirements become burdensome..Another disadvantage of these systems is the noise generated by ; <br /> ' the engine; however, this can be mitigated by placing the unit inside do enclosure, such as a <br /> building. <br /> In a carbon-canister system, hydrocarbon vapor is routed.through activated carbon filters where <br /> adsorption of hydrocarbons onto carbon takes place, removing the hydrocarbons from the vapor <br /> stream. This type of system works best for low concentrations of hydrocarbons, but becomes <br /> expensive when high concentrations- of hydrocarbon vapors necessitate frequent canister <br /> replacement and disposal of spent carbon. <br /> Thermal oxidation systems destroy hydrocarbons by open-flame combustion. Natural gas is <br /> commonly used as supplemental fuel, heating the extracted vapor stream to a combustion <br /> temperature of approximately 1400°F. Relative to-internal combustion systems, these systems may <br /> be slightly more expensive to purchase-and install. However, they can operate at higher air flow <br /> rates, and therefore remediate sites at,a faster rate_ For this system to be effective, hydrocarbon, <br /> '• concentrations should range from 5,000 ppmv to 30,000 ppmv.Thermal oxidation systems operate <br /> at much.lower noise levels than internal combustion systems. <br /> 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 />' 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 />' 6.2.2. Required Soil Conditions <br />' Operation of the blower in a vapor extraction system creates a partial vacuum in the subsurface, <br /> inducing air "currents" through the soil pore spaces. Vapors move by convection toward the area <br /> of lowered air pressure (the extraction point). The efficiency of this process is proportional to soil <br />' porosity and permeability.Qualitative information has been gained through the examination of soil <br /> samples collected at the site. Soil above 20 feet and in the vadoze zone consists of sand,rendering <br /> vapor extraction as an effective remediation method. Soil between 20 and 35 feet has a relatively <br />' high clay and silt content, potentially making vapor extraction less effective for this zone. Figures <br /> 3A and 4A show subsurface soil types at the site. <br /> Advanced GeoEnvironmentat,Inc. <br />
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