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ARCHIVED REPORTS UIC PERMIT APP
Environmental Health - Public
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EHD Program Facility Records by Street Name
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THORNTON
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2900 - Site Mitigation Program
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PR0528038
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ARCHIVED REPORTS UIC PERMIT APP
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Last modified
9/26/2019 9:59:35 AM
Creation date
9/26/2019 9:22:35 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
UIC PERMIT APP
RECORD_ID
PR0528038
PE
2950
FACILITY_ID
FA0018998
FACILITY_NAME
NCPA LODI ENERGY CENTER
STREET_NUMBER
12751
Direction
N
STREET_NAME
THORNTON
STREET_TYPE
RD
City
LODI
Zip
95242
APN
05513016
CURRENT_STATUS
01
SITE_LOCATION
12751 N THORNTON RD
P_LOCATION
02
P_DISTRICT
004
QC Status
Approved
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STIG PROJECT -- EVALUATION OF WATER FOR INJECTION -- 28 March 1994 7 <br /> Similarly, silica which threatens the RO membrane also threatens the injection well. In <br /> normal operations, waste from the RO units becomes mildly diluted in the mixture of waste <br /> streams which is eventually directed to the well. Chemicals added to prevent silica deposition in <br /> the RO membrane will appear as residuals in the injectate mixture. Whether or not those residuals <br /> are effective for preventing solids from forming in the waste mixture is an important factor not <br /> currently resolved. Even their effectiveness at the membrane, based on limited experimental <br /> testing, contains ambiguities. <br /> Those uncertainties could appear acceptable to in-plant operations, but are of greater <br /> concern for injections. Consequently this review assigns no effect to the residual dispersants. <br /> Cooling Tower <br /> The effect of evaporation on the concentrations of residual salts in cooling tower liquid is <br /> aimed at a factor of two. In that case, silica will not become a problem there. Nominal <br /> concentrations in blowdown from the cooling tower will be intermediate between those of <br /> ultrafilter waste and RO waste.Cooling tower blowdown carries residuals of corrosion inhibitors, <br /> algacides, and bactericides to mixtures in the waste receiver tank. <br /> Demineralizer <br /> The product stream from the RO unit goes to the demineralizer where remaining salts are removed <br /> by ion exchange.Output from the demineralizer is approximately as free of salts as distilled water, <br /> suitable as input for the boiler.Silica, at fractional mg/kg concentrations,leaves the demineralizer <br /> in product which feeds the boiler. <br /> Boiler Blowdown <br /> Additives to the boiler water contribute more to the its composition than do effects of <br /> evapo-concentration on the fluid's initial contents. Inflow water to the boiler contains very low <br /> levels of dissolved materials, mainly trace levels of silica. Corrosion inhibitors, etc., operate to <br /> maintain pH in the alkaline range, >9, nominally 10.4. This contrasts with the other waters which <br /> are maintained slightly acid, near pH 6.2. Higher pH strongly inhibits corrosion while enhancing <br /> solubility of silica. <br /> Normal liquid waste discharge rate from the boiler is continuous at 3 gpm(--4300 gal/day). <br /> In a steady-state that would result in about a 120-fold concentration effect between inflow and <br /> liquid discharge, but steady state is not expected. The low concentrations and generally low rate <br /> of contribution to the waste mixture cause this part of boiler blowdown to be an insignificant <br /> contribution to the overall waste composition and amount4. <br /> In addition to the continuous discharge, the boiler also will be discharged at a rate of 250 <br /> gpm two or three times per day for a few minutes each time (^-5000 to 7000 gal/day). Discharge <br /> at boiler temperature, (268°F, s�s25 psig) is associated with steam flashing which is controlled in <br /> a surge tank. Residual liquid at boiling temperature then enters the 60,000 gallon waste receiver <br /> tank. This inflow causes transients of temperature and concentration that cannot be readily <br /> modelled. Details of the transients depend on actual level of liquid in the tank, manner by which <br /> hot water enters the pool, and current inflow rates of other waste steams. <br /> DON MICHELS ASSOCIATES -Missoula,Montana USA <br />
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