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ARCHIVED REPORTS_XR0008316
EnvironmentalHealth
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EHD Program Facility Records by Street Name
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S
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SCHOOL
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3500 - Local Oversight Program
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PR0545674
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ARCHIVED REPORTS_XR0008316
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Entry Properties
Last modified
5/20/2020 10:15:38 AM
Creation date
5/20/2020 10:02:47 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0008316
RECORD_ID
PR0545674
PE
3528
FACILITY_ID
FA0006039
FACILITY_NAME
MARK NEWFIELD
STREET_NUMBER
107
Direction
N
STREET_NAME
SCHOOL
STREET_TYPE
ST
City
LODI
Zip
95240
CURRENT_STATUS
02
SITE_LOCATION
107 N SCHOOL ST
P_DISTRICT
004
QC Status
Approved
Scanner
LSauers
标签
EHD - Public
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10 June 1999 <br /> S AGE-NC Project No 97-0290 <br />' Page 10 of 26 <br /> I unit <br /> An internal-combustion(IC) system draws the vapor stream into the carburetor system of the engine <br />' and mixes the vapor with air prior to combustion Exhaust gasses (oxides of carbon and hydrogen) <br /> are further broken down in a catalytic converter before being emitted to the atmosphere These <br /> systems require supplemental fuel, such as propane or natural gas, which can greatly increase <br /> expenses as vapor concentrations decrease below levels normally required for combustion <br /> Typically, internal combustion engines work effectively where in-situ hydrocarbon concentrations <br /> approach the 40,000 parts per million- volume,(ppmv)required for peak performance of the engine <br /> IAs concentratibns decrease below 20,000-ppmv, supplemental fuel requirements, and therefore <br /> expenses, become burdensome Another disadvantage of these systems is the noise generated by the <br /> Iengine, however, this can be mitigated by placing the unit inside an enclosure, such as a building <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 rates, <br /> 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 They also operate at much lower <br /> 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 /> A carbon-canister system operates by routing hydrocarbon vapor through activated carbon filters <br /> I where adsorption of hydrocarbons onto carbon takes place, removing the hydrocarbons from the <br /> vapor stream This type of system works best for low concentrations of hydrocarbons, but becomes <br /> expensive when high concentrations of hydrocarbon vapor necessitate frequent canister replacement <br /> and disposal of spent carbon <br /> I7 12 Required Soil Conditions <br /> Operation of the blower in a vapor extraction system creates an induced vacuum in the subsurface, <br /> generating vapor flow towards the area of lowered air pressure (the extraction point) through the soil <br /> pore spaces The efficiency of this process is proportional to soil porosity and intrinsic permeability <br /> Intrinsic permeability is the measure of the ability of soils to transmit fluids, porosity is the <br /> Advanced GeoEn%ironmental,Inc <br /> I <br />
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