My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
ARCHIVED REPORTS_2011 REVISED FEASABILITY STUDY
EnvironmentalHealth
>
EHD Program Facility Records by Street Name
>
I
>
INDUSTRIAL
>
230
>
2900 - Site Mitigation Program
>
PR0009051
>
ARCHIVED REPORTS_2011 REVISED FEASABILITY STUDY
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
2/5/2020 2:26:35 PM
Creation date
2/5/2020 10:37:50 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
2011 REVISED FEASABILITY STUDY
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
Scanner
SJGOV\sballwahn
Tags
EHD - Public
Jump to thumbnail
< previous set
next set >
There are no annotations on this page.
Document management portal powered by Laserfiche WebLink 9 © 1998-2015
Laserfiche.
All rights reserved.
/
276
PDF
Print
Pages to print
Enter page numbers and/or page ranges separated by commas. For example, 1,3,5-12.
After downloading, print the document using a PDF reader (e.g. Adobe Reader).
View images
View plain text
Nestle USA, Inc.—Ripon, CA January 28, 2011 <br /> 2011 Revised Feasibility Study <br /> gas surveys, a second SVE system was installed in 1992 at 519 South Stockton <br /> Avenue" The Site SVE system was expanded to include a total of eight vapor <br /> extraction wells in 1992. These additional wells focused on extracting vapors <br /> from TCE- and chloroform-impacted areas near suspected chemical releases on <br /> the eastern portion of the Site. In 1998, four new SVE wells and a new vapor <br /> treatment system were installed to focus vapor extraction activities in the area of <br /> highest remaining TCE concentrations near the former decaffeination building. <br /> The SVE systems removed an estimated 880 pounds of VOCs (primarily TCE <br /> and chloroform) from the subsurface between 1988 until the discontinuation of <br /> SVE prior to 1994. Complete documentation and an assessment of the SVE <br /> activities in the area of the Site are included in Attachment A.3. As indicated in <br /> the attachment, the historical SVE remediation activities resulted in remediation <br /> of the vadose zone (within the upper portion of the B-zone beneath the Site). <br /> 3.4.2 Groundwater Remediation <br /> Groundwater remediation efforts first began in January 1986. Four onsite <br /> production wells (N-1, N-2, N-3 and N-4) supplied water for manufacturing <br /> processes at the former facility. N-1 supported the manufacturing process. N-2 <br /> operated intermittently because of high total dissolved solids (TDS), according to <br /> personal communication with John Meling, former plant engineer. Well N-3 was <br /> used for tea processing from 1962 through 1974, with backup production from <br /> well N-4 (this operating information was also obtained through personal <br /> communication with John Meling). In January 1986, routine sampling and <br /> analysis of N-1 and N-2 revealed TCE in the groundwater samples from these <br /> wells. In May 1986, COCs were detected in groundwater samples obtained from <br /> municipal wells MW-1 and MW-6, located near the Site. Subsequent to these <br /> findings, operation of municipal well MW-1 was terminated and this well was <br /> decommissioned. Following notification to the appropriate regulatory agencies <br /> (Section 3.3), Nestle constructed a GAC system at the northern corner of the Site <br /> in July 1986 to treat groundwater extracted from well N-1. <br /> Expanded groundwater extraction and treatment at the Site incorporated well <br /> EW-1, installed in 1992, and well EI-1, which replaced well N-1 after its closure in <br /> 1994. Both of these wells are screened at approximately 100 to 120 feet below <br /> ground surface (bgs) within the lower portion of the A-zone aquifer. Extraction <br /> from these wells has mitigated plume migration and removed COC mass within <br /> this zone. <br /> Following the 2005 investigation activities (by Geomatrix Consultants, Inc.), ECM <br /> installed wells EU-3 and EU-4 to focus mass removal and hydraulic control <br /> activities within the upper portion of the A-zone beneath the Site. Groundwater <br /> extraction within the upper A-zone also provides hydraulic containment and <br /> influence in the area of well M-1 B (screened within the B-zone (20 to 40 feet <br /> bgs)) beneath the site"' Wells EU-3 and EU-4 began pumping at 30 gpm each <br /> in February 2008. With approval from the RWQCB, groundwater extraction at <br /> well EI-1 was discontinued when well EU-3 and EU-4 began operating. <br /> Additional documentation of IRAP groundwater extraction and treatment system <br /> 5 <br />
The URL can be used to link to this page
Your browser does not support the video tag.