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FIELD DOCUMENTS_1992-1999
Environmental Health - Public
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EHD Program Facility Records by Street Name
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2900 - Site Mitigation Program
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PR0009002
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FIELD DOCUMENTS_1992-1999
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Last modified
6/17/2020 2:56:57 PM
Creation date
6/17/2020 1:38:57 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
FIELD DOCUMENTS
FileName_PostFix
1992-1999
RECORD_ID
PR0009002
PE
2960
FACILITY_ID
FA0004040
FACILITY_NAME
SPX COOLING TECHNOLOGIES INC
STREET_NUMBER
200
Direction
N
STREET_NAME
WAGNER
STREET_TYPE
AVE
City
STOCKTON
Zip
95215
APN
14331007
CURRENT_STATUS
02
SITE_LOCATION
200 N WAGNER AVE
P_LOCATION
99
P_DISTRICT
002
QC Status
Approved
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EHD - Public
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-A • MEMORANDUM . <br /> CALIFORNIA REGIONAL WATER QUALITY CONTROL BOARD • CENTRAL VALLEY REGION <br /> 3443 Routier Road, Suite A Phone: (916) 255-3000 <br /> Sacramento, CA 95827-3098 CALNET: 8-494-3000 <br /> TO: Antonia K.J. Vorster FROM: Cori Condon <br /> Senior WRC Engineer Assoc. Engineering Geologist <br /> DATE: 23 March 1994 SIGNATURE: <br /> SUBJECT: SITE INSPECTION AND MEETING, MARLEY COOLING TOWER COMPANY, <br /> STOCKTON, SAN JOAQUIN COUNTY <br /> On 10 November 1993 I did a site inspection of the Marley Cooling Tower Company's Stockton <br /> facility. The purpose of this meeting was to clarify the sampling objectives set forth in the newly <br /> adopted NPDES permit no. 93-221, adopted by the Board on 22 October 1993. The inspection was <br /> preceeded with a meeting at which Mr. David Bates presented a letter from GeoAnalytical <br /> Laboratories stating that arsenic analyzed by EPA Method 206.2, using graphite furnace is the <br /> preferred method of analysis for arsenic, as opposed to the method 206.3 hydride generation <br /> specified in the NPDES permit. As both of these methods will produce results within acceptable <br /> detection limits, either of the methods will be acceptable. <br /> The second issue discussed pertained to evaluation of the total dissolved solids from the treatment <br /> plant. The permit specifies that influent samples shall be collected from the flow equalization basin <br /> and the influent holding tank. The permit further specifies that these samples shall be combined into <br /> a single sample which is representative of the volume and nature of the inflow to the plant. The <br /> influent sample is to be collected at approximately the same time as the effluent so that the increase <br /> in TDS from the treatment system can be monitored. The influent and the effluent samples are to <br /> be weekly composite samples. Marley has been collecting a grab sample from each system on the <br /> influent in order to comply with the permit requirement of taking the influent and effluent samples <br /> at approximately the same time. In addition to this set of samples, a weekly composite sample is <br /> being collectd on the effluent to satisfy the effluent monitoring requirement. At the present, the <br /> treatment systems are not equipped to collect composite samples on the influent lines. In the <br /> meeting Marley proposed to move the composite sampler formerly on one of the effluent streams <br /> and setting it up on one of the influent streams and purchasing the necessary equipment to conduct <br /> composite sampling on the remaining influent line. This way a composite of the weekly ion <br /> exchange influent, a weekly composite on the andco influent and a weekly composite on the <br /> combined effluent will be collected. This will deviate from the permit in that the influent samples <br /> will not be combined however, it will meet the intentions of the permit to evaluate the change in <br /> concentration of TDS from the treatment system and what the total concentration is being discharged <br /> in the Stockton Diverting Canal, and is therefore acceptable. <br /> Marley will be reporting the volume of flow through the ion exchange, the volume of flow through <br /> the andco system and total flow processed. Flow through each system is being recorded in order to <br /> weight the concentration of the effluent if necessary. The system generally processes approximately <br /> half of the contaminated water through the andco system and half through the ion exchange system. <br />
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