My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
FIELD DOCUMENTS AND WORK PLANS 1992-1999
Environmental Health - Public
>
EHD Program Facility Records by Street Name
>
W
>
WAGNER
>
200
>
2900 - Site Mitigation Program
>
PR0009002
>
FIELD DOCUMENTS AND WORK PLANS 1992-1999
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
2/22/2019 9:57:43 PM
Creation date
2/22/2019 2:55:03 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
FIELD DOCUMENTS
FileName_PostFix
AND WORK PLANS 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
01
SITE_LOCATION
200 N WAGNER AVE
P_LOCATION
99
P_DISTRICT
002
QC Status
Approved
Scanner
TMorelli
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.
/
373
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
WASTE DISCHARGE REQUIREMENTS -3- <br /> MARLEY COOLING TOWER COMPANY <br /> SAN JOAQUIN COUNTY <br /> the existing ion exchange treatment system, identified in Attachment B, <br /> incorporated herein and made part of this Order. The new system was placed <br /> in operation in January 1992. <br /> 12. The new treatment plant consists of an electrochemical reduction (Andco) <br /> and precipitation process which uses iron as the reducing agent for the <br /> hexavalent chromium followed by iron co-precipitation using pH adjustments. <br /> The addition of polymers and further pH adjustments are used to optimize <br /> settling. The effluent is then filtered prior to discharge. The solids <br /> from the clarifier are pumped and accumulated in a filter press. The filter <br /> press filtrate and mixed media filter backwash are returned to the <br /> treatment plant for further treatment. <br /> 13. The ground water extraction system is scheduled to operate in a cyclical <br /> fashion with each cycle lasting 48 hours. During one cycle, water will be <br /> extracted primarily from the north zone near the site. During the next <br /> cycle, ground water extraction will be from the area south of the site. <br /> Water extracted from the north zone will have higher chemical <br /> concentrations. During south zone pumping, the capacity of the treatment <br /> plant will not be utilized fully unless supplemental waste sources are <br /> added. In either mode, when sufficient storm water is accumulated on the <br /> North Yard to justify treatment, the operator will manually initiate storm <br /> water treatment through the Andco system. Ground water from selected wells <br /> will simultaneously be delivered to the ion exchange treatment system. A <br /> third mode of operation entails continuous extraction of ground water from <br /> wells throughout the extraction network. Flushing water may be added to <br /> supplement the ground water concentrations. <br /> 14. The Report of Waste Discharge describes the combined storm water and ground <br /> water characteristics prior to treatment as follows: <br /> Average Flow: Existing Plant - 0.374 million gallons per day (mgd) <br /> Expanded Plant - 0.716 million gallons per day (mgd) <br /> Expanded Plant Hydraulic Capacity: 1.008 mgd <br /> Expanded Plant Treatment Capacity: 0.716 mgd <br /> Average Temperature: Storm water - ambient <br /> Ground water - 68° F <br /> pH: Ground water - 7.0 to 7.5 <br />
The URL can be used to link to this page
Your browser does not support the video tag.