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ARCHIVED REPORTS_XR0008461
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0537118
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ARCHIVED REPORTS_XR0008461
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Last modified
7/7/2020 9:48:50 AM
Creation date
7/7/2020 9:28:46 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0008461
RECORD_ID
PR0537118
PE
2957
FACILITY_ID
FA0021303
FACILITY_NAME
WATERLOO FOOD & FUEL
STREET_NUMBER
3032
STREET_NAME
WATERLOO
STREET_TYPE
RD
City
STOCKTON
Zip
95205
CURRENT_STATUS
01
SITE_LOCATION
3032 WATERLOO RD
QC Status
Approved
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EHD - Public
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. 25 January 2001 <br /> AGE-NC Project No 99-0559 <br /> Page 5 of 14 <br /> 42 TREATMENT SYSTEM DESIGN <br /> AGE proposes the use of a closed-loop, three-chamber air stripper to address TPH-g, BTEX and <br /> MTBE, and a 1,000-pound granular activated carbon (GAC) absorption vessel to ensure treatment <br /> of MTBE in the extracted ground water <br /> Prior to chemical processing, extracted ground water will be routed into a 750-gallon poly holding <br /> tank used to store extracted water and sediment This tank is equipped with upper and lower level <br /> control switches that serve to control the rate at which extracted water is introduced into the closed- <br /> loop air stripper to provide safety shutoff capabilities and to allow coarse sediment to settle out prior <br /> to treatment An emergency shut-off switch will be located Immediately below the top of the raw <br /> holding tank <br /> A "low" float control switch will be placed approximately 8 inches above the base of the holding <br /> tank to activate the process pump, located within the holding tank The raw water will pass through <br /> to the closed-loop air stripper <br /> The closed-loop air stripper circulates water through a series of aeration chambers Diffusers within <br /> each chamber release air bubbles providing an air-to-water interface that facilitates volatile <br /> hydrocarbon removal from the water to the bubbled air The air exhaust system of the air-stripper <br /> is designed to remove volatilized hydrocarbons through carbon adsorption Two 55-gallon capacity <br /> vapor vessels or the equivalent will receive the exhaust from the air-stripper The second stage of <br /> treatment media will consist of a 1 000-pound GAC absorption vessel The GAC vessel is designed <br /> to adsorb TPH-g, volatile organic compounds (VOCs) and MTBE <br /> The estimated ground water extraction flow rate will be between two and four GPM AGE <br /> anticipates the total ground water extraction flow rate to be four GPM from the individual well, <br /> therefore active ground water extraction may need to be alternated between wells to control the <br /> volume of produced water Sample collection ports will be located in appropriate positions <br /> downstream of the air-stripper, the GAC vessel and the air-stripper exhaust to allow raw water <br /> sampling to detect potential process break through and to obtain final discharge samples <br /> Electricity is readily available to the site, a dedicated electricity meter will be installed by <br /> representatives of AGE, that will connect directly to the pump and treat system The location of the <br /> ground water pump and treat system is proposed to be at the east corner of the site (Figure 4) The <br /> proposed location of the pump and treat system will allow the site to conduct day-to-day business <br /> without interference by operation of the remediation system The pump and treat system will be <br /> secured in a chain-linked, gated enclosure approximately 15 feet wide, 15 feet long and six feet high <br /> A generalized design of the treatment system is depicted in Figure 4 <br /> • <br /> Aduntc�rt GcaLnvironmcntal,Inc <br />
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