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ARCHIVED REPORTS LEC APPLICATION FOR CERTIFICATION
Environmental Health - Public
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2900 - Site Mitigation Program
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PR0516806
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ARCHIVED REPORTS LEC APPLICATION FOR CERTIFICATION
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Last modified
9/26/2019 8:41:30 AM
Creation date
9/25/2019 4:52:39 PM
Metadata
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Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
LEC APPLICATION FOR CERTIFICATION
RECORD_ID
PR0516806
PE
2965
FACILITY_ID
FA0012817
FACILITY_NAME
WHITE SLOUGH WATER POLLUTION CONTRO
STREET_NUMBER
12751
Direction
N
STREET_NAME
THORNTON
STREET_TYPE
RD
City
LODI
Zip
95241
APN
05513016
CURRENT_STATUS
01
SITE_LOCATION
12751 N THORNTON RD
P_LOCATION
02
P_DISTRICT
004
QC Status
Approved
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SECTION 2.0:PROJECT DESCRIPTION <br /> 2.1.10.1 Water Requirements <br /> On an annual average basis,recycled water use would be about 856 gallons per minute <br /> (gpm) or 1,380 acre-feet per year (afy), assuming full-time operation at 8,760 hours per year <br /> (Table 2.1-2). Water used for makeup in the circulating water system will be treated using a <br /> cold lime softener and a microfiltration unit before being fed into the cooling tower <br /> collection basin. The micro-filtration feed water storage tank and the micro-filtration <br /> product water storage tank will provide approximately 2 hours of operational storage in the <br /> event there is a disruption in the supply. Water supply reliability is ensured by the WPCF's <br /> recycled water storage capabilities. There will be approximately 5 cycles of concentration of <br /> the reclaimed water through the cooling system before being discharged to the UIW. <br /> TABLE 2.1-2 <br /> Estimated Daily and Annual Water Use for LEC Operations,"Rapid Response"GE Energy Frame 7FA Natural Gas-fired <br /> Turbine Generator <br /> Maximum Annual <br /> Daily Use Maximum Daily Use <br /> Water Use (gpm) Use(mgpd) (afy) <br /> Process and cooling water: Average annual 856 1.23 1,381 <br /> (unfired) <br /> Maximum annual 1,528 2.2 2,464 <br /> (fired) <br /> Sanitary and domestic water: 5 50 8.1 <br /> aFor the GE 7FA values using other operating scenarios,see Appendix 2A. <br /> bThis assumes full-time operation all year(8,760 hours),which is the maximum operation possible; however,the <br /> facility will be periodically taken out of operation for maintenance and will not operate all the time. <br /> 2.1.10.2 Water Treatment <br /> Water treatment will be provided on site using reverse osmosis (RO) and demineralizer <br /> systems. High-purity water will be stored in an approximately 200,000-gallon demineralized <br /> water storage tank.Water quality is described further in Section 5.15,Water Resources. <br /> 2.1.10.3 Cooling Tower System <br /> Makeup water from the WPCF will be pre-treated prior to feeding the cooling tower basins to <br /> replace water lost from evaporation, drift,and blowdown. A chemical feed system will <br /> supply water-conditioning chemicals to the circulating water to minimize corrosion and <br /> control the formation of mineral scale and biofouling. Sulfuric acid will be fed into the <br /> circulating water system to maintain a target pH to control the scaling tendency of the <br /> circulating water. The acid feed equipment will consist of a bulk sulfuric acid storage tank <br /> and full-capacity sulfuric acid metering pumps. <br /> To further inhibit scale formation,a polyacrylate solution will be fed into the circulating <br /> water system as a sequestering agent in an amount proportional to the circulating water <br /> blowdown flow. The scale inhibitor feed equipment will consist of a chemical solution bulk <br /> storage tank and two full-capacity scale inhibitor metering pumps. <br /> 2-22 SAC/371322/082340003(LEC_2.0_PROJECT_DESC.DOC) <br />
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