Sedran Marie A, Pruden Amy, Wilson Gregory J, Suidan Makram T, Venosa Albert D
Department of Civil and Environmental Engineering, University of Cincinnati, Ohio 45221-0071, USA.
Water Environ Res. 2004 Jan-Feb;76(1):47-55. doi: 10.2175/106143004x141573.
The feasibility of biologically degrading methyl tert-butyl ether (MTBE)-contaminated groundwater is dependent on the ability to degrade MTBE and its byproducts in the presence of other gasoline contaminants. This study investigates a mixed culture degrading both MTBE and benzene-toluene-ethylbenzene-xylene (BTEX) in a continuous-flow reactor with a biomass retention system (porous pot) at varying hydraulic retention times (HRTs). The reactor degraded both MTBE and BTEX simultaneously to less than the U.S. Environmental Protection Agency's drinking water standards and recommendations at an HRT of 3.76 days. Methyl tert-butyl ether was degraded from 75 mg/L to less than 1 microg/L and each BTEX compound was degraded from 17 mg/L to less than 1 microg/L. Effluent concentrations of MTBE and BTEX increased as the HRT was decreased from 3.76 to 0.52 days, but remained lower than drinking water limits. The highest MTBE effluent concentration was at 0.52 days and continued to average less than 10 microg/L. Although tert-butyl alcohol (TBA) is commonly sited as a degradation byproduct of MTBE, it remained lower than 1 microg/L throughout all reactor operation periods. The MTBE and BTEX observed yield coefficients for the reactor ranged from 0.11 to 0.16 mg biomass/mg MTBE and BTEX, with the rate increasing with increased HRT. Degradation rates from the reactor were compared to results from batch studies with the same culture on MTBE and TBA alone and in the presence of BTEX. Results of batch studies showed that BTEX was not required for this culture to degrade MTBE. The presence of BTEX only had an effect on the rate of MTBE degradation at the highest concentration, while BTEX significantly delayed the degradation of TBA at all concentrations. Batch studies also showed that the rate of degradation of TBA was higher with and without BTEX than the rate of degradation of MTBE, explaining the lack of high levels of TBA in the reactor.
生物降解受甲基叔丁基醚(MTBE)污染的地下水的可行性,取决于在存在其他汽油污染物的情况下降解MTBE及其副产物的能力。本研究在具有生物质保留系统(多孔罐)的连续流反应器中,于不同水力停留时间(HRT)下,研究了一种能同时降解MTBE和苯 - 甲苯 - 乙苯 - 二甲苯(BTEX)的混合培养物。在水力停留时间为3.76天的情况下,该反应器能同时将MTBE和BTEX降解至低于美国环境保护局的饮用水标准和建议值。甲基叔丁基醚从75毫克/升降至低于1微克/升,每种BTEX化合物从17毫克/升降至低于1微克/升。当水力停留时间从3.76天降至0.52天时,MTBE和BTEX的出水浓度增加,但仍低于饮用水限值。MTBE的最高出水浓度出现在0.52天时,且持续平均低于10微克/升。尽管叔丁醇(TBA)通常被认为是MTBE的降解副产物,但在整个反应器运行期间其含量均低于1微克/升。该反应器中MTBE和BTEX的观察产率系数范围为0.11至0.16毫克生物量/毫克MTBE和BTEX,速率随水力停留时间的增加而提高。将该反应器的降解速率与使用相同培养物对MTBE和TBA单独以及在BTEX存在下进行的批次研究结果进行了比较。批次研究结果表明,该培养物降解MTBE不需要BTEX。BTEX的存在仅在最高浓度时对MTBE的降解速率有影响,而在所有浓度下BTEX均显著延迟了TBA的降解。批次研究还表明,无论有无BTEX,TBA的降解速率均高于MTBE的降解速率,这解释了反应器中TBA含量不高的原因。