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FIELD DOCUMENTS AND WORK PLANS 1987
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0009002
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FIELD DOCUMENTS AND WORK PLANS 1987
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Last modified
2/22/2019 5:04:55 PM
Creation date
2/22/2019 2:32:33 PM
Metadata
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EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
FIELD DOCUMENTS
FileName_PostFix
AND WORK PLANS 1987
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
01
SITE_LOCATION
200 N WAGNER AVE
P_LOCATION
99
P_DISTRICT
002
QC Status
Approved
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over groundwater to minimize the time storm water will remain on the <br /> site. Therefore, in the course of a rain storm, the water treatment <br /> plant may treat all groundwater, a mix of ground- and storm water, all <br /> storm water, and back to all groundwater in sequence. The expected <br /> system performance of the ion exchange process in treating storm water <br /> is presented in Table 4. <br /> OBJECTIVES OF STARTUP PROGRAM <br /> The objectives of the startup program are as follows: <br /> I. Confirm treatment plant capacity for all wood treating <br /> chemicals. <br /> 2. Correlate chromate analyzer readings and system totalizer <br /> readings with concentrations of other wood treating chemicals <br /> in treatment plant effluent. <br /> These objectives have been defined to confirm that the available auto- <br /> matic system monitoring devices are adequate to assure treatment. The <br /> two automatic monitoring devices that will be relied upon during system <br /> operation are the automatic totalizer of water treated and the automatic <br /> hexavalent chromium or chromate analyzer. <br /> The automatic totalizer will be the primary monitoring device used <br /> to automatically control system shutdown and annunciate the need for <br /> system regeneration. As described in other sections of this report, the <br /> operating characteristics of the anion and cation resins are predictable <br /> and the influent characteristics of the water to be treated are also <br /> predictable or controllable. Based on the calculations presented in the <br /> previous sections, the potential throughput can be predetermined for the <br /> various waters to be treated. <br /> The influent characteristics of storm water are different than <br /> those of the groundwater. Storm water with its high cation load will <br /> place greater demands on the cation exchanger than an equal volume of <br /> groundwater. In order to balance the run length of the anion exchangers <br /> 6 <br />
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