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ARCHIVED REPORTS_2011 REVISED FEASABILITY STUDY
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ARCHIVED REPORTS_2011 REVISED FEASABILITY STUDY
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Last modified
2/5/2020 2:26:35 PM
Creation date
2/5/2020 10:37:50 AM
Metadata
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Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
2011 REVISED FEASABILITY STUDY
RECORD_ID
PR0009051
PE
2960
FACILITY_ID
FA0000649
FACILITY_NAME
FORMER NESTLE USA INC FACILITY
STREET_NUMBER
230
STREET_NAME
INDUSTRIAL
STREET_TYPE
DR
City
RIPON
Zip
95366
APN
25938001
CURRENT_STATUS
01
SITE_LOCATION
230 INDUSTRIAL DR
P_LOCATION
05
P_DISTRICT
005
QC Status
Approved
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• IAS does not result in a uniform distribution of air bubbles around the injection point, <br /> but rather in a limited number of discrete air channels that are heterogeneously <br /> distributed and difficult to control. <br /> • There is a small mass transfer zone in the immediate vicinity of the air channels where <br /> dissolved oxygen concentrations are greatest. <br /> • The delivery of oxygen to water saturated zones located between the air channels is <br /> limited by diffusion (a slow process). <br /> Because aerobic degradation rates for biosparging applications are dependent on oxygen <br /> delivery, contaminant removal rates are highest adjacent to and near the air channels. For <br /> enhanced rates of aerobic biodegradation to occur outside the immediate vicinity of the air <br /> channels, oxygen must diffuse into the saturated zones located between the air channels (a <br /> slow process). The rate at which the saturated zones between the air channels can be <br /> supplied with oxygen can become the limiting process for aerobic biodegradation (Braids and <br /> Ong, 2001; Johnson, 1998). It would also be very difficult to maintain aerobic conditions in <br /> groundwater near the WWTP based on the highly reducing groundwater conditions in this area <br /> as discussed in Technical Attachment B.4. <br /> These delivery issues are important considerations for the design of biosparge systems <br /> discussed in Section 2.3. <br /> 2.2 TREATMENT PROCESSES <br /> With the exception of vinyl chloride (VC), chlorinated ethenes (i.e. tetrachloroethylene [PCE], <br /> trichloroethylene [TCE], cis-1,2-dichloroethylene [cDCE]) are not readily degradable by direct <br /> aerobic oxidation reactions. Some studies have indicated cDCE can be degraded aerobically. <br /> TCE and PCE have not been shown to be degraded aerobically (EPA, 1998; ITRC 1998; EPA, <br /> 2000). <br /> A variation of aerobically based biosparging applications is aerobic cometabolism where an <br /> electron donor such as toluene, phenol, methane, or propane is co-injected with oxygen (the <br /> electron acceptor). Bacteria produce non-specific oxygenase enzymes to metabolize the <br /> injected substrate (e.g. toluene). The production of oxygenase enzymes can facilitate oxidation <br /> of TCE, cDCE, and VC. These oxidation reactions are considered fortuitous with the microbes <br /> deriving no net benefit from the oxidation of chlorinated ethenes (EPA, 1998; ITRC 1998; EPA, <br /> 2000). <br /> Research conducted in the 1980s and 1990s indicated chlorinated ethenes (with the exception <br /> of PCE) were degradable cometabolically (Wilson and Wilson, 1985; Semprini et al., 1990; <br /> Munkatta-Marr et al., 1997; Bradley at al., 1998; McCarty et al., 1998). Field implementation of <br /> AMEC Geomatrix, Inc. <br /> \\oad-fs1\doc_safe\9000s\9837.006\4000 REGULATORYTS Assessment_Apx B_012711\Attachment B.1\Attach B1.doc 131-3 <br />
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