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SITE INFORMATION AND CORRESPONDENCE
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Last modified
2/5/2020 12:26:47 PM
Creation date
2/5/2020 10:23:06 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
SITE INFORMATION AND CORRESPONDENCE
RECORD_ID
PR0009051
PE
2960
FACILITY_ID
FA0000649
FACILITY_NAME
FORMER NESTLE USA INC FACILITY
STREET_NUMBER
230
STREET_NAME
INDUSTRIAL
STREET_TYPE
DR
City
RIPON
Zip
95366
APN
25938001
CURRENT_STATUS
01
SITE_LOCATION
230 INDUSTRIAL DR
P_LOCATION
05
P_DISTRICT
005
QC Status
Approved
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CALIFORNIA REGIONAL WATER QUALITY CONTROL BOARD <br /> CENTRAL VALLEY REGION <br /> ORDER NO. 93-712 <br /> CLEANUP AND ABATEMENT ORDER <br /> FOR <br /> NESTLE BEVERAGE COMPANY <br /> SAN JOAQUIN COUNTY <br /> The California Regional Water Quality Control Board, Central Valley Region, (hereinafter <br /> Board) finds that: <br /> 1. Nestle Beverage Company (hereinafter Discharger) is a wholly owned subsidiary of the <br /> Nestle Holdings, Incorporated. The Discharger owns and operates a manufacturing plant <br /> in Ripon, San Joaquin County. The plant is in the NW-'/4 of Section 29, T2S, R8E, <br /> MDB&M and is approximately three quarters of a mile north of the Stanislaus River, as <br /> shown on Attachment A. <br /> 2. The facility was built in the 1930's and was used for the production and processing of <br /> dairy products. Since 1948, the plant has manufactured instant coffee. Beginning in <br /> 1957, trichloroethylene (TCE) was used to extract caffeine in the decaffeination process. <br /> Beginning in 1970, the use of TCE was discontinued and methylene chloride was used for <br /> this process. Since April 1986, decaffeination using volatile organic constituents (VOCs) <br /> has not occurred at this facility. The facility continues to process coffee beans. <br /> 3. The decaffeination processes used "closed loop" systems where solvents were distilled and <br /> recycled. The solvents (TCE and methylene chloride) were stored in above-ground tanks <br /> nearby the decaffeination building as shown on Attachment B. In 1986, the decaffeination <br /> plant was removed. <br /> 4. There are two on-site production supply wells, NI and N2, as shown on Attachment B. <br /> The Discharger uses approximately 0.3 million gallons per day (mgd) of water in its <br /> manufacturing process. Water is primarily supplied from N1 which pumps about 200 <br /> gallons per minute (gpm). Supply well N2 is not used. City water is used as a backup. <br /> 5. Wastewaters from the manufacturing process have historically and are currently disposed <br /> of to the industrial sewer line to the City of Ripon publicly operated treatment works <br /> (POTW) which are regulated by Waste Discharge Requirements (WDRs) Order No. 85- <br /> 120. The industrial sewer line is in the center of Industrial Avenue, off of the Nestle <br /> property. <br /> 6. In October 1985 and January 1986, the Discharger conducted sampling of NI and N2. <br /> The analytical results revealed that trichloroethylene (TCE) was present in the ground <br /> water samples. By July 1986, the Discharger had installed a granular activated carbon <br /> (GAC) system for the treatment of the production water. This action has performed as <br /> an interim remedial measure (IRM) since that time. <br />
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