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ARCHIVED REPORTS_SITE CONCEPTUAL MODEL 2009
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0009051
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ARCHIVED REPORTS_SITE CONCEPTUAL MODEL 2009
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Last modified
2/5/2020 2:25:32 PM
Creation date
2/5/2020 10:56:03 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
SITE CONCEPTUAL MODEL 2009
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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EHD - Public
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amec— <br /> Other <br /> industries have operated and continue to operate in the vicinity of the former plant. <br /> These include Regal Almond (now the Site of a building materials company), Ripon Milling, <br /> Guntert Steel, Nulaid Foods, Ripon Manufacturing and Ripon Canning. <br /> 3.1.1 Chemical Use <br /> The decaffeination process included the use of chemicals. The decaffeination occurred at the <br /> "Old Decaf" (Decaffeination Building) and "Decaf Penthouse" locations shown in Figure 2 <br /> (personal communication with John Meling, former Nestle factory engineer). Decaffeination <br /> was performed in a closed, batch process as follows: <br /> 1. Green coffee beans (unroasted) were placed in a rotating vessel filled with water to <br /> hydrate the beans, causing them to swell (swelling allowed the chlorinated solvent <br /> to penetrate the beans more easily). <br /> 2. After the beans had swelled, the water was drained and the vessel was partially <br /> filled with chlorinated solvent and rotated for several hours to extract the caffeine. <br /> 3. The solvent was then drained to a solution tank while the beans were retained in <br /> the vessel with a screen. <br /> 4. Steam was used to extract residual solvent from the beans, and the steam and <br /> solvent vapor was condensed and returned to the solution tank. <br /> 5. The solution tank drained to a gravity separator for recovery of non-aqueous-phase <br /> chlorinated solvent; water from the gravity separator was drained to an onsite <br /> sewer lateral located north of the Decaffeination Building and south of the <br /> warehouse that connected to the industrial sewer along Industrial Avenue. <br /> Between approximately 1957 and 1970, TCE was used as the chlorinated solvent for <br /> decaffeination in the Decaffeination Building area. Annual TCE use was estimated to be <br /> approximately 8,000 gallons (RUST, 1994a); TCE was transported to the Site by truck and <br /> was stored in aboveground tanks south of the Decaffeination Building (Figure 2). Between <br /> 1970 and 1986, methylene chloride (dichloromethane) was used for the decaffeination <br /> process, and an additional step was added, in which water from the gravity separator was sent <br /> to a stripping column to remove the chlorinated solvent before it was sent to the industrial <br /> sewer. Chloroform was also used as a solvent for laboratory-scale decaffeination processes <br /> (the location of the laboratory is shown in Figure 2). Other chemicals used at the Site include <br /> caustics and water softening agents (calcium and magnesium oxides) and perhaps small <br /> quantities of cleaning solvents such as 1,1,1-trichloroethane (1,1,1-TCA) for equipment <br /> maintenance. Hazardous chemicals (caustics and perhaps solvents) were stored in small <br /> quantities (drums and bottles) in the chemical storage building (Building 38; Figure 2); paint <br /> thinners and paints were stored in Building 36 (Figure 2) (personal communication with John <br /> Meling). <br /> AMEC Geomatrix, Inc. <br /> hDoc_Safe\9000s\9837.005\4000 REGULATORY\SCM_01.30.09\1_text\SCM Report Final.doc 8 <br />
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