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Last modified
2/14/2019 6:16:53 PM
Creation date
2/14/2019 2:56:21 PM
Metadata
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Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
WORK PLANS
RECORD_ID
PR0544148
PE
3526
FACILITY_ID
FA0005937
FACILITY_NAME
NEAL STALLWORTH AUTO DETAIL
STREET_NUMBER
602
Direction
N
STREET_NAME
CALIFORNIA
STREET_TYPE
ST
City
STOCKTON
Zip
95202
APN
13916509
CURRENT_STATUS
02
SITE_LOCATION
602 N CALIFORNIA ST
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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EHD - Public
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i <br /> 3.2 COC Removal <br /> The concentrations of GRO in the aqueous phase and in the off-gases are shown in Table <br /> 5 . All of the treatments significantly reduced the amount of GRO in the aqueous phase: <br /> in most cases, < 2 % of the GRO present in the Control remained after treatment and <br /> complete removal was seen in the tests employing H2O2, iron, and acid. However, most <br /> (34- 119%) of the GRO lost was volatilized rather than destroyed. Better GRO <br /> destruction was achieved using a lower dose of H202, probably because the reaction was <br /> less vigorous, resulting in a greater contact time between the oxidant and the GRO. <br /> Treatment with H202only resulted in very little (0-23 %) GRO destruction. Treatment <br /> with H2O2 and acid (with or with out iron) enhanced destruction to 63 -66% when the <br /> initial concentration of H2O2 was 2%. <br /> Treatment with chelated iron was probably the least effective treatment. Use of 2% H2O2 <br /> did not destroy any of the GRO . Although the 5% H2O2/FeEDTA test results suggest that <br /> 91 % of the GRO was destroyed, this number is probably significantly overestimated. <br /> Both the 2% H2O2/FeEDTA and the %5 H202/FeEDTA reactions were vigorous and <br /> nearly instantaneous. However, the effect was much greater for the 5%H2O2FeEDTA <br /> tests and a large volume of off-gases were not collected because the reactor could not be <br /> capped fast enough to capture them. Thus, the volume of the collected off-gases is low <br /> and the concentration of GRO in the off-gases may also be low, both of which imply that <br /> % Volatilized reported in Table 5 isartificially low and that the %Destroyed is artificially <br /> high. <br /> The %5 H2O2/FeEDTA test became very warm to the touch. None of the other tests had <br /> a noticeable change in temperature. <br /> 3.3 Effect of Treatment on Secondary Water Quality <br /> The effect of each oxidant system on secondary water quality parameters is shown in <br /> Table 6. All of the treatments increased the concentration of Cr(VI) relative to the <br /> controls and most also affected the concentrations of several metals. ORP and pH were <br /> not significantly affected in most cases. <br /> Cr(VI) was formed in all cases, in concentrations ranging from 0.027 mg/L to 0. 139 <br /> mg/L. The Cr(VI) concentrations are consistent with the concentrations of total dissolved <br /> chromium. The amount of Cr(VI) observed in these tests corresponds to the oxidation of <br /> 0. 14-0 .69 mg Cr(VI)/kg soil. It is unclear whether all of this Cr would be oxidized in a <br /> field application because of differences in field and laboratory conditions. <br /> Treatment with H202only (Tests 2 and 3) affected only Cr(VI), total Cr, vanadium, and <br /> pH. Cr(VI) increased from < 0.001 mg/L in the control test to 0. 0858 mg/L and 0. 111 <br /> mg/L in the 2% H202 Only and 5% H202 Only tests, respectively. The concentrations of <br /> total Cr were 0.079 mg/L and 0. 11 mg/L, respectively. Vanadium increased by an order <br /> of magnitude: from about 0.0061 mg/L in the control to 0.062-0.065 mg/L in the H2O2 <br /> i <br /> PRIMA Environmental, Inc. 12 Eval of Peroxide <br /> February 8, 2007 Cambria--G Street, Davis <br />
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