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2900 - Site Mitigation Program
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PR0508450
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SITE INFORMATION AND CORRESPONDENCE
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Last modified
5/29/2019 11:58:23 AM
Creation date
5/29/2019 11:10:41 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
SITE INFORMATION AND CORRESPONDENCE
RECORD_ID
PR0508450
PE
2960
FACILITY_ID
FA0008087
FACILITY_NAME
DDJC-TRACY
STREET_NUMBER
25700
STREET_NAME
CHRISMAN
STREET_TYPE
RD
City
TRACY
Zip
95376
APN
25207002
CURRENT_STATUS
01
SITE_LOCATION
25700 CHRISMAN RD
P_LOCATION
99
P_DISTRICT
005
QC Status
Approved
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EHD - Public
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6 <br /> �® <br /> Unsaturated soil Remedial Description of the Preferred Extraction and <br /> Alternatives Treatment Technologies <br /> Current data indicate that two <br /> areas require unsaturated soil <br /> cleanup: (1)the Gasoline Spill Area <br /> where the contaminants are FHCs For Ground Water <br /> and VOCs,and(2)the Building 518 <br /> Area,where only VOCs are present. ■ Extraction <br /> A third area,the East Taxi Strip Area Pumping <br /> where VOCs and tritium are pre- This is the most common method of removing ground water for treatment <br /> sent,may also require cleanup.All <br /> three areas are in the southeastern above ground. Extraction wells are drilled at strategic locations throughout <br /> part of LLNL.Two remedial altema- the area of the ground water contamination. The locations of the wells,the <br /> fives were developed for the unsatu- pumping rates,and the amount of pumped water vary with the subsurface <br /> rated soil. characteristics. The extracted water is then piped to a treatment facility. <br /> Soil Alternative No.l(The Preferred ■ Treatment <br /> Alternative) Air Stripping(with granular activated carbon treatment of the vapors) <br /> Under this alternative,the unsatu- Air stripping is a commonly used process in which VOCs and FHCs are <br /> rated soil would be cleaned up using removed from water(Figure 3). Extracted ground water is transported via <br /> vacuum-induced venting to extract pipes to a tower,where it is sprayed into the top of the tower. As the water <br /> the FHC and VOC vapors. The cascades down through packing material within the tower,a high-powered <br /> vapors would then be treated at the blower forces air upward <br /> surface by catalytic oxidation to <br /> destroy t_.e contaminants. Any water through the water. This <br /> vapor cont-,ining tritium following causes the contaminants Treated air out <br /> the treatment process will be evaluat- to come out of the water t <br /> ed using the EPA AIRDOS Model to and into the air. Thus,the <br /> determine its health impact. If a sig- flow by air cleans or aeration filet air <br /> nificant health risk is established,fur- "strips" the water of tower <br /> =L? <br /> ther treatment of the tritium in the air volatile contaminants. rf <br /> stream will be done to assure that the The air containing the <br /> risk is reduced to an acceptable level. contaminants is then <br /> Packing Discharge <br /> Estimated Cleanup Time: It may passed through GAC fil- material pumps <br /> take up to 10 years to clean up the ters prior to release to the Air In <br /> unsaturated soil using this alternative. atmosphere. This virtual- r <br /> Cost: The present-worth cost of ly eliminates measurable <br /> this alternative is$1.1 million. air emissions of VOCs Clean water out <br /> and FHCs. <br /> Soil Alternative No.2 f. Extraction well <br /> Under this alternative,contami- GAC has a strong <br /> nants in the unsaturated soil would attraction for VOCs(such water level <br /> be left in place and allowed to as TCE)and FHCs. As air <br /> degrade,volatilize,or possibly flows through the filter, Contaminated ground water <br /> migrate to ground water under nat- the contaminants cling to <br /> ural conditions. If any contamina- the carbon,thereby <br /> tion of ground water above removing them. The Figure 3. Air Stripping. <br /> drinking water standards occurs,it GAC must be replaced <br /> would be detected by periodic periodically because the filter eventually reaches its maximum ability to <br /> monitoring and remedied by absorb the contaminants. The used filters are subsequently treated offsite to <br /> pumping the water to a surface destroy or recycle both the filters and the contaminants. <br /> treatment facility. <br /> Estimated Cleanup Time: It <br /> may take 90 years to clean up the <br /> contamination in the unsaturated <br /> soils using this alternative. <br /> Cost: The present-worth cost of <br /> this alternative is$0.9 million. Note: See sect ons 5.2.4 and 5.3.3 of the PRAP for a discussion of the relative <br /> ti costs of the treatment technologies. <br />
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