My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
ARCHIVED REPORTS_XR0002813
Environmental Health - Public
>
EHD Program Facility Records by Street Name
>
H
>
HARDING
>
719
>
3500 - Local Oversight Program
>
PR0545262
>
ARCHIVED REPORTS_XR0002813
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
2/3/2020 7:45:24 PM
Creation date
2/3/2020 10:29:21 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0002813
RECORD_ID
PR0545262
PE
3528
FACILITY_ID
FA0009940
FACILITY_NAME
SAN JOAQUIN CATHOLIC CEMETERY
STREET_NUMBER
719
Direction
E
STREET_NAME
HARDING
STREET_TYPE
WAY
City
STOCKTON
Zip
95204
APN
12720002
CURRENT_STATUS
02
SITE_LOCATION
719 E HARDING WAY
P_DISTRICT
001
QC Status
Approved
Scanner
SJGOV\sballwahn
Tags
EHD - Public
There are no annotations on this page.
Document management portal powered by Laserfiche WebLink 9 © 1998-2015
Laserfiche.
All rights reserved.
/
33
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
. Mr Harlin Knoll <br /> June 5, 1998 <br /> Page 2 <br /> In-Situ Bioremediation <br /> The design of an in-situ soil bioremediation system typically includes provisions for the injection of air, <br /> water and nutrients into the plume for the purpose of enhancing the biological growth of naturally occurring <br /> microorganisms The proximity of the plume beneath the site,which contacts the groundwater surface, <br /> poses risks associated with the injection of water for bioremediation The leaching of hydrocarbons to <br /> groundwater would likely occur and would necessitate a groundwater treatment system to contain and treat <br /> leached hydrocarbons Groundwater treatment would result in the withdrawal of dissolved hydrocarbons <br /> from beneath the site and would result in prohibitively expensive treatment and disposal costs The risks <br /> and prohibitive cost of in-situ bioremediation,estimated at approximately$200,000,eliminates this option <br /> from further consideration <br /> Soil Vapor Extraction <br /> Vapor extraction pilot test data indicates that SVE has the potential to remove approximately 216 pounds of <br /> hydrocarbons per day SVE has been proven to be an effective method to decontaminate impacted soil,both <br /> from a technical and economic perspective The cost to design, install and operate a 100 cubic foot per <br /> minute SVE system for a period of one year is approximately$100,000 As such, SVE is clearly the most <br /> economic and technically sound remedial option for hydrocarbon source removal at the subject site <br /> AIR SPARGING FOR GROUNDWATER TREATMENT <br /> Due to the increases in groundwater elevation beneath the site in the last 4 years, some of the wells <br /> originally installed between 1990 and 1994, currently have well screens that are completely submerged <br /> below groundwater A review of the construction log for existing well MW-1 indicates that the upper <br /> well screen is approximately 27 feet below groundwater More importantly, the well/borehole seal is <br /> also submerged approximately 23 feet below the groundwater surface Based on the configuration of <br /> well MW-1 as compared to the current groundwater depth,well MW-I can be utilized as an air sparge <br /> well The advantages of adding air sparging via well MW-1 areas follows <br /> a The construction of a new well is not necessary <br /> a Well MW-1 is located within the area of highest groundwater impact <br /> a Air sparge off-gas from the saturated zone will be contained by the SVE system <br /> a Air sparging will effect the removal of dissolved gasoline and BTEX while promoting saturated zone <br /> biodegradation via dissolved oxygen increases <br /> Therefore, Ramage Environmental proposes the inclusion of air sparging using existing well MW-1 as an <br /> air injection well The design effort for the SVE system will be expanded to include I)the addition of <br /> an air compressor to deliver pressurized air to the saturated zone, 2) subsurface piping from the treatment <br /> compound to the MW-1 wellhead and 3)process control provisions to manage the pressure and flowrate <br /> of sparge air <br />
The URL can be used to link to this page
Your browser does not support the video tag.