My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
FIELD DOCUMENTS CASE 2
EnvironmentalHealth
>
EHD Program Facility Records by Street Name
>
L
>
LATHROP
>
1250
>
2900 - Site Mitigation Program
>
PR0521881
>
FIELD DOCUMENTS CASE 2
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
8/5/2019 1:01:39 PM
Creation date
8/5/2019 10:49:45 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
FIELD DOCUMENTS
FileName_PostFix
CASE 2
RECORD_ID
PR0521881
PE
2960
FACILITY_ID
FA0014865
FACILITY_NAME
CALIFORNIA NATURAL PRODUCTS
STREET_NUMBER
1250
Direction
E
STREET_NAME
LATHROP
STREET_TYPE
RD
City
LATHROP
Zip
95330
APN
19804001
CURRENT_STATUS
01
SITE_LOCATION
1250 E LATHROP RD
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.
/
202
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
• The remediation system will include a 5 hp compressor/blower to provide vacuum on the <br /> • well points set in the ground, twin carbon beds containing a total of about 800 pounds of <br /> carbon, a steam boiler, condenser and gasoline/water separator. The soil venting process <br /> will continue until breakthrough occurs within the carbon beds. At this point the <br /> concentration of gasoline in the effluent air stream from the carbon beds will have <br /> exceeded one percent of the influent concentration and the bed will be shut down to <br /> remove accumulated gasoline. Regeneration will be accomplished by generating steam at <br /> 10-15 PSI from an on-site steam boiler and passing the steam through the carbon beds <br /> where at evaporates off the gasoline. The gasoline and steam vapor mixture would then <br /> pass through a water cooled condenser and then to a separator where pure gasoline would <br /> be removed. The clear water would be recycled to the boiler after passing through <br /> another activated carbon bed to remove any residual gasoline. The equipment to be used <br /> would be trailer mounted and operated manually. <br /> Design of the Venting System <br /> i� <br /> The design and layout of well points for placing a vacuum on the ground is shown in <br /> Figure 1-1. Since site conditions consist of 10 feet of fine sand underlain by 5 feet of silty <br /> clay, it is proposed that 2 sets of well points be installed. The first set will penetrate only <br /> the upper 10 feet of sand while the second will be sealed through the sand and will be <br /> perforated only within the lower clay zone (Figure 1-2). Each separate series of well <br /> points will be manifolded together with the extracted vapors sent to separate compressors <br /> and carbon beds. Flush threaded 4 inch perforated and blank PVC pipe will be used for <br /> the well points which will be manifolded together via 4 inch pipe into a 4 or 6 inch trunk <br /> line leading to each compressor. <br /> Operation of the Venting System <br /> Operation of the soil venting system will begin once all regulatory permits and approval <br /> • have been obtained. Operations will start with 9 well points into each soil layer at an air <br />
The URL can be used to link to this page
Your browser does not support the video tag.