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ARCHIVED REPORTS_XR0012262
EnvironmentalHealth
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2900 - Site Mitigation Program
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PR0541653
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ARCHIVED REPORTS_XR0012262
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Last modified
10/10/2020 11:25:10 PM
Creation date
7/9/2020 8:59:06 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0012262
RECORD_ID
PR0541653
PE
2965
FACILITY_ID
FA0023871
FACILITY_NAME
TOP FILLING STATION
STREET_NUMBER
101
Direction
S
STREET_NAME
WILSON
STREET_TYPE
WAY
City
STOCKTON
Zip
95205
APN
15125307
CURRENT_STATUS
01
SITE_LOCATION
101 S WILSON WAY
P_LOCATION
01
QC Status
Approved
Scanner
LSauers
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EHD - Public
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7 <br /> 20 March 1996 <br /> AGE-NC Project No 95-0130 <br /> Page 10 of 23 <br /> 611 PRINCIPLES <br />' For most SVE systems, a vacuum blower is used to volatilize hydrocarbons and draw the vapors into <br /> extraction wells installed and screened within the contaminant plume The vapors are drawn from the <br /> wells and treated in one of several possible treatment units (carbon canisters, internal combustion <br /> engines, thermal oxidizers, and catalytic oxidizers) Air infection wells may be installed outside the <br /> contaminant plume to increase air flow to the extraction unit <br />` An internal-combustion(IC) system draw vapors into a carburetor system of an engine and mixes the <br /> vapors with air prior to combustion Exhaust gasses (oxides of carbon and hydrogen) are broken <br /> down further in a catalytic converter before being emitted to the atmosphere IC systems require <br /> supplemental fuel, such as propane or natural gas, which can become increasingly expensive as vapor <br /> concentrations decrease below levels required for combustion Typically, internal combustion engines <br /> work effectively where in-situ hydrocarbon vapor concentrations approach the 40,000 ppmv required <br /> for peak performance of the engine As vapor 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, the noise can be mitigated by placing the unit inside an <br /> enclosure, such as a building <br /> Hydrocarbon vapors are routed through activated carbon filters in a carbon-canister system, where <br /> adsorption of the hydrocarbons onto activated carbon removes the hydrocarbons from the vapor <br /> stream These systems work best for soil impacted by low concentrations of hydrocarbons, but <br /> become 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 vapors to a combustion temperature of <br /> 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 /> 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 /> I <br />
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