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ARCHIVED REPORTS XR0010889
EnvironmentalHealth
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EHD Program Facility Records by Street Name
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ELKHORN
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1050
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2900 - Site Mitigation Program
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PR0505234
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ARCHIVED REPORTS XR0010889
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Last modified
8/1/2019 3:25:51 PM
Creation date
8/1/2019 2:23:45 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0010889
RECORD_ID
PR0505234
PE
2951
FACILITY_ID
FA0001103
FACILITY_NAME
Elkhorn Golf Club
STREET_NUMBER
1050
STREET_NAME
ELKHORN
STREET_TYPE
DR
City
STOCKTON
Zip
95209
CURRENT_STATUS
02
SITE_LOCATION
1050 ELKHORN DR
P_LOCATION
99
P_DISTRICT
003
QC Status
Approved
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EHD - Public
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.. 27 June 1996 <br /> AGE-NC Project No. 95-0118 <br /> Page l I of 23 <br /> expensive when high concentrations of hydrocarbon vapors necessitate frequent canister replacement <br /> ,., and disposal of spent carbon. <br /> f Thermal oxidation systems destroy hydrocarbons by open-flame combustion. Natural gas is <br /> +1 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 /> 1;=� be slightly more expensive to purchase and install. However, they can operate at higher air flow <br /> rates, and can 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. These systems also operate at much <br /> 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 /> 7.1.2. 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 soil pore spaces. Vapors move by convection toward the area of <br /> lowered air pressure (the extraction point). The efficiency of this process is.proportional to soil <br /> -; porosity and permeability. Qualitative infonnation has been gained through examination of soil <br /> =� samples and the performance of a vapor extraction pilot test. Soil at this.site has a high sand content, <br /> which should make vapor extraction an effective and rapid process. <br /> I <br /> 7.1,3. MONITORING ACTIVITIES <br /> t.�a <br /> Monitoring of vapor extraction systems involves weekly measurement of vapor concentrations at <br /> the inlet to the destruction unit and periodic service and repair. Systems can be equipped with an <br /> t .? automatic telecommunication system to alert the operator of system malfunction or failure. Vapor <br /> samples should be collected monthly for laboratory analysis to monitor the efficiency of the <br /> remediation program. When the concentration of extracted vapors decreases and stabilizes after <br /> .-J <br /> _. several months of operation, confirmation borings are drilled to collect soil samples for quantitative <br /> analysis in the laboratory to document the degree of clean-up obtained. <br /> 4 <br />
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