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2900 - Site Mitigation Program
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PR0527799
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Last modified
3/4/2019 2:43:14 PM
Creation date
3/4/2019 1:26:48 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
WORK PLANS
RECORD_ID
PR0527799
PE
2960
FACILITY_ID
FA0018844
FACILITY_NAME
TRANSMISSION STORE
STREET_NUMBER
515
Direction
W
STREET_NAME
CHARTER
STREET_TYPE
WAY
City
STOCKTON
Zip
95206
APN
14707408
CURRENT_STATUS
01
SITE_LOCATION
515 W CHARTER WAY
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
Scanner
WNg
Tags
EHD - Public
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11 <br />4.2 Air Spar in with SVE <br />g g <br />Air sparging and SVE are two technologies that have been proven successful in their application <br />to in-situ treatment of subsurface soil and groundwater contaminated with TPH-g and BTEX. <br />Air sparging is primarily used for groundwater remediation, while SVE is used for vadose zone <br />soil treatment. Integrated together, these two technologies form an alternative that is considered <br />potentially applicable for the site. <br />' In principle, the air sparging process involves the use of pressurized air to remove volatile <br />contaminants from groundwater by means of "stripping" (as in air stripping). To implement air <br />sparging at this site, air would be injected under pressure into the saturated zone to enhance <br />volatilization of TPH-g and BTEX. An air compressor would be used to provide the pressurized <br />air. Under the pressure gradient, the hydrocarbons "stripped" from the water phase into vapor <br />phase would be driven, along with the air, from the saturated zone into the vadose zone. With a <br />SVE system running simultaneously, the hydrocarbons in the vadose zone would then be drawn <br />into the vapor extraction wells by the moving soil air under vacuum. <br />In addition to 1- to 2 -inch diameter air sparge wells or points, the air sparging system would <br />consist of an air compressor and probably a receiving tank of 120 gallons in capacity or <br />equivalent. Steel piping would be used to convey compressed air from the compressor tank to <br />the injection wells. The SVE system, on the other hand, would require 2- to 4 -inch diameter <br />vapor extraction wells and include a blower or vacuum pump, a liquid -vapor separator, and an <br />offgas emission control unit such as a catalytic thermal oxidizer. The emission control <br />requirement would be essentially the same as in the case of pump -and -treat where an air stripper <br />would be used. Plastic piping would usually be used to convey captured soil vapor from the <br />vapor extraction wells to the blower or vacuum pump. <br />Since SVE had previously been conducted at the site to remove TPH-g and BTEX from the <br />vadose zone, an SVE test would not be necessary. A field pilot test of air sparging would, <br />however, be recommended for proper sizing of the air sparge system for full-scale treatment. <br />The test data would also be used to further assess if the site subsurface conditions would favor <br />the implementation of air sparging for groundwater treatment. <br />4.2.1 Technical Effectiveness <br />Air sparging coupled with SVE has the capability of reducing the dissolved phase mass of <br />TPH-g and BTEX in groundwater at the site — meeting the primary treatment objective in bulk <br />mass reduction. However, as in the case of pump -and -treat, its effectiveness will be limited due <br />to the presence of the relatively low permeable silty to clayey soils within the treatment area. <br />Even though the TPH-g and BTEX in the gravelly, sandy soil layers would be "stripped" out <br />L <br />I <br />FS Onsite Petroleum Hydrocarbon Remediation.doc 4-4 Shaw Environmental, Inc. <br />
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