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ARCHIVED REPORTS_XR0008002
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0541401
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ARCHIVED REPORTS_XR0008002
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Last modified
4/14/2020 2:57:42 PM
Creation date
4/14/2020 1:19:50 PM
Metadata
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EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0008002
RECORD_ID
PR0541401
PE
2950
FACILITY_ID
FA0006046
FACILITY_NAME
UNION OIL STATION #5098
STREET_NUMBER
5606
STREET_NAME
PACIFIC
STREET_TYPE
AVE
City
STOCKTON
Zip
95207
CURRENT_STATUS
02
SITE_LOCATION
5606 PACIFIC AVE
P_LOCATION
01
P_DISTRICT
002
QC Status
Approved
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EHD - Public
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• not long after the warranty period When removing the pump and motor for motor repair, the pump is <br /> also serviced (wear rings, bearings, etc ) as necessary The pumps themselves have held up well It <br /> costs about $3,000 to pull the pump / motor assembly, about $1,000 to service the pump, about $5,000 <br /> to replace the motor, and about $3,000 to re-install the pump / motor assembly, for a total cost of about <br /> $12,000 <br /> 4 1 5 3 Air Strippers The air strippers are consistently reducing TCE levels to below detection <br /> limits (less than 1 ppb) The strippers were designed to reduce TCE levels from of 250 to 0 78 ppb <br /> However, since 1995 influent TCE levels have been between 20 and 30 ppb SHMP is currently being <br /> fed upstream from the strippers to prevent precipitation in piping and injection wells (see Sec 4 2 3 3 <br /> Sequestration of Inorganic Precipitates) However, even before SHMP was being used, scaling or <br /> fouling of the stripper packing was not found to be a problem And there has not been evidence of <br /> scaling or fouling of the stripper packing since the use of the SHMP was initiated <br /> 4 1 5 4 Piping There have not been recent problems with the piping, however, prior to the <br /> addition of the SHMP, scale collected in the piping near the injection well head, especially at the valves <br /> This accumulation had to be removed by hand <br /> 4 1 5 5 Chemical Peed System A chemical feed system is being used to feed SHMP into the <br /> process stream through injection ports between the transfer pumps and the air strippers The SHMP <br /> being used is a Calgon product (CL-50), and is delivered to the site as a concentrated solution in plastic <br /> containers The feed-rate is not automatically regulated based on the flow rate of water being pumped to <br /> the strippers, but is adjusted manually if there is a significant change in influent flow rate The target <br /> concentration for SHMP in process water is 8 mg/L Although SHMP could be added downstream from <br /> the air strippers, it was more convenient to locate the feed system inside the treatment plant building <br /> 4 1 6 Components or Processes that Account for Majority of Costs <br /> 4 1 6 1 Electricity Electricity costs approximately $500,000 per year (5 1 - 5 2 cents per kW- <br /> hr) <br /> 4 1 6 2 SHMP Costs for SHMP now exceed $200,000 per year <br /> • 4 1 6 3 Labor The staff consists of a manager and a staff of three with an estimated annual cost <br /> exceeding $300,000 <br /> 4 1 6 4 Chemical Analysis Sampling of approximately 45 monitoring wells occurs <br /> semiannually Treatment plant influent/effluent, and individual extraction wells concentrations are <br /> determined quarterly Analysis includes VOCs by methods 8010 aIId 08020 acid l.liromiwri by riicuiou <br /> 6010 Estimated annual cost for these analyses is $15,000-20,000 The existing staff conducts <br /> sampling <br /> 4 1 6 5 Welland Pump Maintenance Pump motors require replacement approximately every <br /> two years At a cost of$12,000 per well and assuming that seven extraction wells require work each <br /> year, the total cost per year is approximately $85,000 <br /> 06/07/99 <br /> Page 7 of 14 <br />
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