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ARCHIVED REPORTS XR0008636
Environmental Health - Public
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EHD Program Facility Records by Street Name
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EL DORADO
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1605
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3500 - Local Oversight Program
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PR0544687
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ARCHIVED REPORTS XR0008636
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Last modified
7/24/2019 8:47:32 AM
Creation date
7/24/2019 8:31:17 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0008636
RECORD_ID
PR0544687
PE
3528
FACILITY_ID
FA0006185
FACILITY_NAME
El Dorado Gas & Mart
STREET_NUMBER
1605
Direction
S
STREET_NAME
EL DORADO
STREET_TYPE
ST
City
STOCKTON
Zip
95206
APN
16703101
CURRENT_STATUS
02
SITE_LOCATION
1605 S EL DORADO ST
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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stripping, cascading, or waterfall aeration, diffuser striping, and surface aeration <br /> To <br /> remove compounds that are volatile at higher than ambient groundwater temperature, <br /> the air stripping system can be designed to preheat the water or is used in conjunction <br /> with a secondary treatment or polisher system, such as activated carbon <br /> Prior to choosing this method of treatment, flow rates, contaminant types and <br /> concentrations, groundwater chemistry, permitting requirements, and space and power <br /> requirements must be considered <br /> The air containing organic compounds is typically discharged from the system The <br />' air discharge should be modeled and permuted where required. Similarly, treatment <br /> of the air used to strip compounds from the water may be required by the permitting <br /> agencies. <br /> 2 2.2 Bioremediation <br /> Extracted groundwater may also be treated by use of an aboveground bioreactor <br /> Bioreactors utilize natural or specialized bacteria to remove organic contaminants <br /> through aerobic and anaerobic consumption and digestion processes Digested <br /> organic compounds are converted to biomass and harmless by-products such as <br /> methane, carbon dioxide, and inorganic salts The bioreactor design depends on <br /> contaminant concentration and type, flow rates, and groundwater chemistry <br /> Groundwater is pumped from the subsurface and enters a container that contains a <br /> sludge or film with a high microbe population that is exposed to the liquid The <br /> reactor capacity is large enough to allow both sufficient surface area for the <br /> introduction of the microbes into the groundwater and a sufficient residence time for <br /> the microbes to metabolize the organic compounds. The water may be pre-treated to <br />' adjust the pH and temperature, and to remove inorganic materials that may clog the <br /> reactor system or harm the microbes <br />' 2 2 3 Ultraviolet Degradation <br /> Ultraviolet (UV) degradation involves pumping extracted water through a UV light <br />' source Two methods of destruction of organic compounds utilizing UV light have <br /> been developed The first method utilizes either a natural or introduced hydroxyl <br /> radical source and a UV energy source to destroy organic compounds The UV light <br /> source frees hydroxyl radicals, usually from hydrogen peroxide or ozone, which then <br /> react with the organic compound to form carbon dioxide and a secondary by-product <br /> The second method of UV light destruction involves utilizing a plasma type UV light <br />' source with a focused wavelength This focused energy is absorbed by the organic <br /> compound, breaking the molecular bonds This reaction also produces carbon dioxide <br /> and a secondary by-product Depending on the type of organic compound being <br />' destroyed, the secondary by-product can potentially be hazardous and may need to <br /> be disposed of or treated <br />' Before utilizing this treatment alternative, groundwater chemistry, contaminant type <br /> and concentration, and flow rates must be evaluated <br /> r <br /> i <br />
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