My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
SU0002453
Environmental Health - Public
>
EHD Program Facility Records by Street Name
>
A
>
AUSTIN
>
6600
>
2600 - Land Use Program
>
UP-88-13
>
SU0002453
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
5/18/2022 5:21:56 PM
Creation date
4/14/2020 11:41:19 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2600 - Land Use Program
RECORD_ID
SU0002453
PE
2626
FACILITY_NAME
UP-88-13
STREET_NUMBER
6600
Direction
S
STREET_NAME
AUSTIN
STREET_TYPE
RD
City
STOCKTON
ENTERED_DATE
10/26/2001 12:00:00 AM
SITE_LOCATION
6600 S AUSTIN RD
QC Status
Approved
Scanner
SJGOV\sballwahn
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.
/
444
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
rise over time and would be directed to the next Settling Tank by a <br /> piping connection near the top of the tank. Water would be drawn off the <br /> bottom of the cone-shaped tanks until samples indicate increasing <br /> lubricant content. This process of progressive separation would remove <br /> approximately 80 percent of the entrained water droplets. <br /> The contaminated water would be transferred to a Wastewater Holding <br /> Tank of sufficient capacity to allow long-term settling operations. In a <br /> batching operation, the oily water would be skimmed off by a centrifugal <br /> water pump drawing from near the top of the holding tank and transferred <br /> to the Used Lubricant Storage Tanks for reprocessing. The remaining <br /> quantity of relatively uncontaminated water would be pumped to the Reten- <br /> tion Pond or the rotary dryer inlet for evaporation. <br /> The remaining entrained water, in very small droplet form, would be <br /> removed (to specification limits) by a forced-circulation flash evapora- <br /> tion process. Used lubricants would be transferred from the final <br /> Settling Tank into a vertical shell and tube heat exchanger (Feedstock <br /> Heater) to achieve the final evaporation temperature. The heat exchange <br /> vessel would always be maintained full and under pressure to avoid these <br /> changes. The lubricant would then be forced through a spray nozzle into <br /> the evaporator column and against an impingement plate. Recovered lubri- <br /> cant would drain into the lower half of the column where a constant <br /> liquid level would be maintained. Analysis for water content of the <br /> lubricants exiting the column would determine the appropriate amount ofl <br /> recirculation required. <br /> Recovered lubricant, referred to as finished oil , would then be <br /> stored in one of three Finished Oil Storage Tanks. <br /> Steam used for heating of the lubricant at various steps is gener- <br /> ated in a residential -size package boiler (Steam Generator) . <br /> Blending oil for firing on-site equipment would be contained within <br /> a single Blending Tank with hard-piped fill connections from the finished <br /> Oil Storage Tanks and from a diesel Fuel Oil Tank. The Fuel Oil Tank <br /> would be exempt from the San Joaquin Air Pollution Control District <br /> 2-17 <br /> 101-46.R4 4/7/89 <br />
The URL can be used to link to this page
Your browser does not support the video tag.