My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
ARCHIVED REPORTS UIC PERMIT APP
Environmental Health - Public
>
EHD Program Facility Records by Street Name
>
T
>
THORNTON
>
12751
>
2900 - Site Mitigation Program
>
PR0528038
>
ARCHIVED REPORTS UIC PERMIT APP
Metadata
Thumbnails
Annotations
Entry Properties
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
Scanner
SJGOV\wng
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.
/
1019
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
STIG PROJECT -- EVALUATION OF WATER FOR INJECTION -- 28 March 1994 17 <br /> and between injectate and formation minerals appear to be of negligible likelihood or significance. <br /> The use of water from WSWPCF for the STIG project will yield waste water mixtures that <br /> are variably suitable for injection/disposal, but only one component, silica, is critical in that <br /> regard. Diversion of the waste stream to the injection well or return to WSWPCF can be based on <br /> monitoring silica. <br /> NOTES AND REFERENCES <br /> 1. Russell Associates, Supplementary Environmental Impact Report, STIG Project, Northern <br /> California Power Agency. <br /> 2.The earliest plotted points in Figure 2B represent the averages of points plotted in Figure 2A. <br /> 3. Testing of polyacrylate materials from two suppliers was reported in March 1994 (Al <br /> Benenati,Nalco).Concentrations to twice the natural solubility of amorphous silica(240 vs. 120 <br /> mg/kg) were reached in waste streams. However, chemical data provided to this reviewer was <br /> ambiguous for showing whether or not silica deposition occurred in the membrane. <br /> Three of five tests with two chemicals at two levels of addition showed that some silica <br /> was not accounted for.Specifically,mass balance verification was possible from measured silica <br /> concentrations in input, concentrate, and permeate. The discrepancy is plausibly explained by <br /> deposition in the membrane. However, the amounts indicated were at about the level of <br /> resolution of the chemical analyses.If analytical results are to be accepted,it must be concluded <br /> that silica deposited in the membrane. Alternatively, if the analyses are not accepted, which <br /> may also be reasonable, the tests must be judged as too insensitive for a conclusion to be made. <br /> Comments about pressures associated with the test suggest that no deposition occurred. <br /> Also,analyses of the membranes were said to not show silica. No pressure records or membrane <br /> data were provided.Thus,chemical data are compelling for this review.Accordingly, no credit <br /> for chemical stabilization of silica is accepted here, regarding injection, when silica <br /> concentrations exceed the nominal solubility limit of 120 mg/kg. <br /> 4. The standard deviations for concentrations of liquid components are mostly in the range of <br /> 10 to 15 percent of the concentration values. That describes a normal variation of input water <br /> composition. Factors causing changes smaller than the range of natural variation may be <br /> regarded as negligible for many aspects of this review. <br /> 5. Normal input rate for the three main waste streams is about 406 gpm. If discharge from the <br /> tank is the same rate, so that a stable liquid level is maintained, then clearance of the tank <br /> occurs at(406/V) [working volumes per minute], where V is the liquid(working) volume held <br /> in the tank. The tank will be operated at less than its 60,000 gallon capacity in order to <br /> accommodate surges and minor upsets in the system. Thus, V could be nominally 30,000 <br /> gallons, but an engineeringly practical range could be from 5000 to 40,000 gallons. A 30,000 <br /> gallon level yields a clearance rate of 0.0135 volumes/minute. <br /> 6. That clearance rate can be recast into the concept of a time to clear half of a parcel of liquid <br /> initially in the tank. Numerically, a clearance rate of 0.0135/min is equivalent to a clearance <br /> half-time of t1/2=0.853 hours.Lower(winter)rates involve average discharges nearer 314 gpm <br /> which have correspondingly longer clearance half-times for the same fill levels of the tank.On <br /> the other hand, if the operating level of the tank is less than 30,000 gallons, clearance half- <br /> DON MICHELS ASSOCIATES -Missoula,Montana USA <br />
The URL can be used to link to this page
Your browser does not support the video tag.