Slurry-Phase Biological Treatment of 2,4 Diitrotoluene and 2,6 Dinitrotoluene: Role of Bioaugmentation and Effects of High Dinitrotoluene Concentration

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dc.contributor.authorZhang, Carl
dc.date.accessioned2020-04-06T15:57:56Z
dc.date.available2020-04-06T15:57:56Z
dc.date.issued2000
dc.description.abstractA pilot-scale study was conducted to evaluate the use of aerobic slurry reactors to treat soils that were highly contaminated with 2,4-dinitrotoluene (2,4-DNT) and 2,6-dinitrotoluene (2,6-DNT). Contaminated soils were obtained from Volunteer Army Ammunition Plant (VAAP; Chattanooga, TN) and Badger Army Ammunition Plant (BAAP; Baraboo, WI). Concentrations of 2,4-DNT and 2,6-DNT were 19 000 and 1380 mg/kg in VAAP soil and 8900 and 480 mg/kg in BAAP soil. Soils were homogenized and subjected to a soil washing process; the resulting soil slurry was subsequently fed to an Eimco bioreactor (70-L) operated in a draw-and-fill mode. Degradation of either isomer required augmentation with a DNT-mineralizing culture. Stable performance and essentially complete degradation of 2,4-DNT (within ∼2 days) was demonstrated for both soils at slurry concentration (sum of aqueous, sorbed, and crystalline phases) exceeding 11 000 μM. Incomplete degradation of 2,6-DNT was observed after inoculation, and low-level degradation activity could not be sustained without repeated bioaugmentation. Changing reactor operation to maintain low slurry-phase concentrations of 2,4-DNTthrough continuous feeding or by reducing the volume of soil slurry fed during draw-and-fillimproved the ability to sustain 2,6-DNT degradation activity. Complementary studies conducted in shake flasks demonstrated that the high concentrations of 2,4-DNT resulted in an inhibition of 2,6-DNT degradation. The impact of 2,4-DNT on 2,6-DNT degradation required a dual-stage approach to achieve complete treatment of both contaminants. Operating two reactors in series, where 2,4-DNT was degraded in the first reactor and 2,6-DNT was degraded in the second reactor, allowed for stable draw-and-fill operation. High nitrite concentrations resulting from 2,4-DNT degradation in the first reactor had no apparent impact on subsequent 2,6-DNT degradation.en_US
dc.identifier.citationZhang C, Hughes JB, Nishino SF, Spain J (2000), Slurry-Phase Biological Treatment of 2,4-Dinitrotoluene and 2,6-Dinitrotoluene: Role of Bioaugmentation and Effects of High Dinitrotoluene Concentrations, Environmental Science and Technology, 34(13):2810-2816. 45en_US
dc.identifier.urihttps://hdl.handle.net/10657.1/2231
dc.publisherEnvironmental Science and Technologyen_US
dc.subjectDegradation Soils Anions Animal feed Molecular structureen_US
dc.titleSlurry-Phase Biological Treatment of 2,4 Diitrotoluene and 2,6 Dinitrotoluene: Role of Bioaugmentation and Effects of High Dinitrotoluene Concentrationen_US
dc.typeArticleen_US

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College of Science and Engineering
Chunlong (Carl) Zhang