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ARCHIVED REPORTS XR0008210
Environmental Health - Public
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EHD Program Facility Records by Street Name
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EL DORADO
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1448
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3500 - Local Oversight Program
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PR0544673
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ARCHIVED REPORTS XR0008210
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Last modified
8/19/2020 5:24:13 AM
Creation date
7/18/2019 3:52:22 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0008210
RECORD_ID
PR0544673
PE
3528
FACILITY_ID
FA0006182
FACILITY_NAME
REGAL STATION #604
STREET_NUMBER
1448
Direction
N
STREET_NAME
EL DORADO
STREET_TYPE
ST
City
STOCKTON
Zip
95202
CURRENT_STATUS
02
SITE_LOCATION
1448 N EL DORADO ST
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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EHD - Public
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ACTIVATED CARBON REGENERATION <br /> Granular activated carbon (GAC) can be used for final "polishing"of the soil-gas <br /> by adsorption of low concentration VOC's being recycled. This is achieved by placing <br /> the GAC in the closed loop flow path of the Cyclo-Purge System The use of the CP in <br /> this arrangement reduces the rdlative humidity of the air entering the GAC. With the <br /> preconditioning of the soil-gases entering the GAC, the adsorption capacity Is greatly <br /> enhanced In the case of highly contaminated soil formations, such as the venting of <br /> the capillary fringe above a water table with floatingF <br /> gasobne product, over 9090 of the <br /> i VOC is eliminated from the soil gas as a condensed liquid before It reaches the GAC. <br /> This feature alone will allow a tremendous reduction in the size of the GAC installation <br /> reqi,..:Z4 during the initial months of remediation With the use of our medium sized <br /> snit, the recovery of up to 24 gallons VOC per day can be achieved The GAC need <br /> only be concerned with the adsorption of solvent vapors remaining after passing <br /> through the colt' heat exchanger, a g. approximately 10% of the raw soil gas. <br /> When saturation of the GAC does occur, regeneration of the GA <br /> � 9 C can be <br /> accomplished, in place, by rerouting the flow path of closed-loop gas (which might be <br /> inert gaseous nitrogen when recovering flammable vapors) to exclude the wells from <br /> the modified closed loop flow path This rearrangement allows the warm air from the <br /> CP to enter the GAC carim'er, where the high temperature encourages desorption of <br /> the VOC from the GAC An auxiliary heat source is beneficial during the GAC <br /> fregeneration phase The VOC saturated vapors leaving the GAC canister are then <br /> i passed into the CI~, where condensation removes the VOC fraction. The recirculated <br /> gas is reheated after "cold drying" and reintroduced into the GAC canister, to strip <br /> i additional VOC, until regeneration is completed The GAC canister is then placed <br /> back on line in the sod venting flow path arrangement The desorption cycle for a 200 T <br /> pound canister of GAC can easily be achieved in less than eight hours, incurring a <br /> total electrical power cost of approximately $6 00 Time and costs will vary with the <br /> ' nature of the VOC material and the size of the GAC canister However, the <br /> regeneration cost ratio of $0 03 per pound of GAC may be considered a conservative <br /> estimate <br /> i <br /> 4 <br />
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