School of Chemical, Biological, and Environmental Engineering, 102 Gleeson Hall, Oregon State University, Corvallis, OR 97331, United States.
School of Chemical, Biological, and Environmental Engineering, 102 Gleeson Hall, Oregon State University, Corvallis, OR 97331, United States.
Chemosphere. 2017 Sep;182:65-75. doi: 10.1016/j.chemosphere.2017.04.139. Epub 2017 Apr 29.
Carbon tetrachloride (CT) and chloroform (CF) were transformed in batch reactor experiments conducted with anaerobic dechlorinating cultures and supernatant (ADC + S) harvested from continuous flow reactors. The Evanite (EV) and Victoria/Stanford (VS) cultures, capable of respiring trichloroethene (TCE), 1,2-cis-dichloroethene (cDCE), and vinyl chloride (VC) to ethene (ETH), were grown in continuous flow reactors receiving an influent feed of saturated TCE (10 mM; 60 mEq) and formate (45 mM; 90 mEq) but no CT or CF. Cells and supernatant were harvested from the chemostats and inoculated into batch reactors at the onset of each experiment. CT transformation was complete following first order kinetics with CF, DCM and CS as the measurable transformation products, representing 20-40% of the original mass of CT, with CO likely the unknown transformation product. CF was transformed to DCM and likely CO at an order of magnitude rate lower than CT, while DCM was not further transformed. An analytical first order model including multiple key reactions effectively simulated CT transformation, product formation and transformation, and provided reasonable estimates of transformation rate coefficients. Biotic and abiotic treatments indicated that CT was mainly transformed via abiotic processes. However, the presence of live cells was associated with the transformation of CF to DCM. In biotic tests both TCE and CT were simultaneously transformed, with TCE transformed to ETH and approximately 15-53% less CF formed via CT transformation. A 14-day exposure to CF (CF = 1.4 μM) reduced all rates of chlorinated ethene respiration by a factor of 10 or greater.
四氯化碳(CT)和氯仿(CF)在采用厌氧脱氯培养物和连续流反应器中收获的上清液(ADC+S)进行的批量反应器实验中被转化。Evanite(EV)和 Victoria/Stanford(VS)培养物能够将三氯乙烯(TCE)、1,2-顺式-二氯乙烯(cDCE)和氯乙烯(VC)呼吸转化为乙烯(ETH),在连续流反应器中生长,接受饱和 TCE(10 mM;60 mEq)和甲酸盐(45 mM;90 mEq)的进料,但没有 CT 或 CF。细胞和上清液从恒化器中收获,并在每个实验开始时接种到批量反应器中。CT 转化遵循一级动力学,CF、DCM 和 CS 是可测量的转化产物,代表原始 CT 质量的 20-40%,CO 可能是未知的转化产物。CF 转化为 DCM 和可能的 CO 的速度比 CT 低一个数量级,而 DCM 没有进一步转化。一个包含多个关键反应的分析一级模型有效地模拟了 CT 的转化、产物形成和转化,并对转化速率系数提供了合理的估计。生物和非生物处理表明,CT 主要通过非生物过程转化。然而,活细胞的存在与 CF 转化为 DCM 有关。在生物测试中,TCE 和 CT 同时被转化,TCE 转化为 ETH,通过 CT 转化形成的 CF 减少了 15-53%。14 天接触 CF(CF=1.4 μM)会使所有氯化乙烯呼吸速率降低 10 倍或更多。