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ARCHIVED REPORTS_XR0005502
EnvironmentalHealth
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EHD Program Facility Records by Street Name
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N
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99 (STATE ROUTE 99)
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14800
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3500 - Local Oversight Program
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PR0545626
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ARCHIVED REPORTS_XR0005502
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Entry Properties
Last modified
11/19/2024 1:50:28 PM
Creation date
4/29/2020 1:37:23 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0005502
RECORD_ID
PR0545626
PE
3528
FACILITY_ID
FA0000957
FACILITY_NAME
LATHROP GAS & FOOD MART*
STREET_NUMBER
14800
Direction
S
STREET_NAME
STATE ROUTE 99
STREET_TYPE
RD
City
MANTECA
Zip
95336
APN
19702004
CURRENT_STATUS
02
SITE_LOCATION
14800 S HWY 99 RD
P_LOCATION
99
P_DISTRICT
005
QC Status
Approved
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SJGOV\sballwahn
Tags
EHD - Public
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1 <br /> significant -'iffcrence between spray aeration and air stripping is that <br /> no oacking material is present in the aeration process which may <br /> become ;o,:ied and require subsequent replacement The RSI system <br /> further enhances the separation of hydrocarbons from water by using <br /> vacuum ana heat The pressure is reduced so the temperature at which <br /> the hydrocarbons vaporize drops An increase in the temperature from <br /> the addition of heat further increases the potential for hydrocarbon <br /> ' vaporization. The RSI spray aerator takes advantage of both of these <br /> principles oy spraying heated water in a vacuum To ensure sufficient <br /> hydrocarbon removal, the water is recirculated through a second set of <br /> spray nozzles In geographic areas where benzene becomes a governing <br /> factor, carbon canisters for water polishing may be required. <br /> ' A vacuum up to 15 inches of mercury may be placed on the tank <br /> and the water heated to 100 degrees F There are limits to the level o f <br /> ' vacuum on the tank and the water temperature must be monitored <br /> carefully to avoid evaporating a large quantity of water along with <br /> hydrocarbons. For example, at 110 degrees F and 27 inches of mercury, <br /> ' all the water would evaporate and be passed to the engine <br /> The soil vacuum extraction system consists of a vacuum pump <br /> driven by the internal combustion engine. The vacuum on the <br /> extraction well causes the hydrocarbons to volatilize and flow with <br /> the air into the well and up to the vacuum pump. The vapors drawn by <br /> ' the vacuum are combined with the hydrocarbon vapors which have been <br /> stripped from the ground water and are directed to the intake of the <br /> engine where they are mixed with the auxiliary fuel (if required) and <br /> then burned in the engine through the process of thermal oxidation <br /> where temperatures can exceed 5000° F, thus consuming the total <br /> hydrocarbon mixture. The engine's air to fuel ratio is adjusted to <br /> ' maintain efficient combustion when the vapor from the wells is <br /> combined with the fuel from the carburetor, thus resulting in minimum <br /> ' emissions from the engine. The exhaust from the engine is passed <br /> through an automobile catalytic converter to ensure a maximum <br /> destruction of the hydrocarbons. These catalytic converters meet EPA <br /> ' requirements and the CARR Executive Order D-193-2 allowing their <br /> use in California. The temperature at the catalyst exit ranges between <br /> 800 and 1400 degrees Fahrenheit ('F). The system is under a vacuum <br /> from the extraction wells to the engine cylinders, so leaks at the <br /> seals or connections are into the system, with no loss of hydrocarbons <br /> to the atmosohere <br /> SAFETY OF OPERATION <br /> The engine is the power source for all other equipment so all <br /> systems stop operating when the engine stops This eliminates any <br /> ' 3 <br />
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