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ARCHIVED REPORTS XR0009894
EnvironmentalHealth
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3500 - Local Oversight Program
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PR0544710
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ARCHIVED REPORTS XR0009894
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Entry Properties
Last modified
7/30/2019 1:52:52 PM
Creation date
7/30/2019 1:19:51 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0009894
RECORD_ID
PR0544710
PE
3528
FACILITY_ID
FA0006247
FACILITY_NAME
Western Lift
STREET_NUMBER
3430
Direction
S
STREET_NAME
EL DORADO
STREET_TYPE
ST
City
STOCKTON
Zip
95206
APN
17525063
CURRENT_STATUS
02
SITE_LOCATION
3430 S EL DORADO ST
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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EHD - Public
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i <br /> ' Report—Vapor Extraction 1 Air Sparge Remedial System Page 8 <br /> Former Bank of Stockton/Western Lift Site <br /> 1 Project No. 102.3 <br /> March 25, 2005 <br /> 4.3 Vapor Extraction System <br /> The surface machinery is mounted on a covered, steel equipment skid designed to protect <br /> the equipment from the elements while allowing easy access for servicing and monitoring. <br /> The skid is located next to the electrical service that powers it, and is also adjacent to the <br /> vapor extraction manifold. <br /> The process air is extracted from the ground using a Fuji 7-HP regenerative blower or ring <br /> compressor capable of producing 250 SCFM at 10 inches of water vacuum, or 195 SCFM <br /> at 40 inches of water. It is expected that at any given time only one extraction well will be <br /> operated. This will allow the wells to be "cycled" to maximize the overall efficiency of the <br /> vapor extraction. In essence, as a given well's gasoline production declines to a low level, <br /> it will be taken off-line and replaced with another well. As the first extractor is allowed to <br /> be idle, the gasoline-impacted soil that it serves will be partially recharged, and eventually <br /> the well will be returned to production. Using this system, and assuming equal duty <br /> ' cycles, each well will be in a recharging state for about 85 percent of the time and will be <br /> in active production for 15 percent of the time. This method should allow the maximum <br /> feasible recovery of gasoline hydrocarbons. <br /> 1 <br /> 4.5 Air Sparge System <br /> �. A 5 horsepower SpeedAire sparge compressor with an 80-gallon reserve tank was <br /> installed on the equipment skid. This compressor is capable of delivering up to least 5 <br /> scfm to the face of 4 sparge wells simultaneously. The normal operating manifold <br /> pressure is between 20 and 25 psig, which should result in pressure at the operating face <br /> of 5 to 10 psig. The compressor was equipped with a new pressure regulator and <br /> accumulator and secondary filters. <br /> ' 4.6 Carbon Filtration System <br /> The exhaust gas from the regenerative blower is directed to a battery of two, 2,000 carbon <br /> filters connected in parallel, and the exhaust from these filters is directed to a third 2,000 <br /> carbon filter connected in series. It is expected that each carbon unit will become <br /> saturated with about 500 to 700 pounds of gasoline. Sample ports were installed at points <br /> ' between the primary and secondary carbon units. A sample port was also installed at the <br /> base of the 10-foot-high exhaust stack. <br /> 1 <br /> • <br /> 2937 Veneman Ave., #B240 Geo-Phase Environmental Inc. Phone(209) 569-0293 <br /> Modesto, CA 95356 Fax(209) 569-0295 <br /> r <br />
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