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Inhibition, kinetic and modeling studies of acetylene and 1-chloro-1-fluoroethene on reductive dechlorination of TCE and vinyl chloride.

机译:乙炔和1-氯-1-氟乙烯对三氯乙烯和氯乙烯还原脱氯的抑制,动力学和模型研究。

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Laboratory and modeling studies were performed with a mixed-anaerobic-culture obtained from the Evanite site in Corvallis, Oregon. The culture completely transforms trichloroethene (TCE) to cis-dichloroethene ( c-DCE), vinyl chloride (VC), and finally to ethene. Acetylene inhibition studies were used to examine the culture's microbial activities. Kinetic studies determined the half-saturated constant (Ks), the maximum utilization rate (kmaxX), and inhibition constants (KI). The kinetic constants were used to model the results of inhibition studies using competitive and uncompetitive inhibition models.; Acetylene was found to function as a reversible inhibitor and was used to probe the activities of reductive dechlorination. Various acetylene concentrations were used to differentiate microbial processes, including methanogenesis, acetogenesis, and halorespiration. Acetylene concentrations of 48, 192, and 12 muM, respectively, were required to achieve 90% inhibition in the rates of methanogenesis, TCE and VC transformation. H2-dependent acetate production was not inhibited by acetylene.; Ks values for TCE and VC were 12 muM and 63 muM, respectively. Model fitting of acetylene inhibition constants ( KIC) for TCE and VC transformations yielded the same value (0.4 muM) for a competitive inhibition model. However, for uncompetitive inhibition the estimated KIU for TCE to c-DCE, TCE to 1,1-DCE and VC to ethene were 13.3, 14.1 and 2.2 muM, respectively. Competitive and uncompetitive inhibition models simulated experimental data equally well for results obtained at high TCE and VC concentrations. The models were further verified to fit transient data of acetylene inhibition at lower TCE and VC concentrations, and competitive inhibition resulted in a better fit to the experimental data.; 1-chloro-1-fluoroethene (1,1-CFE) was found to track the rate of VC transformation well, since VC and 1,1-CFE had similar maximum transformation rates and Ks values. A competitive inhibition model with the measured Ks values, 63 and 87 muM, was used to predict the rates of VC and 1,1-CFE transformation, respectively. The similar rates and results of acetylene and compound inhibition studies indicated VC and 1,1-CFE were transformed by the same enzyme. 1,1-CFE transformation by three different cultures, clearly demonstrate that 1,1-CFE was an excellent surrogate to track rates of VC transformation.
机译:使用从俄勒冈州科瓦利斯的伊万石遗址获得的混合厌氧培养物进行了实验室和模型研究。该培养物将三氯乙烯(TCE)完全转化为顺二氯乙烯(c-DCE),氯乙烯(VC),最后转化为乙烯。乙炔抑制研究用于检查培养物的微生物活性。动力学研究确定了半饱和常数(Ks),最大利用率(kmaxX)和抑制常数(KI)。动力学常数用于使用竞争性和非竞争性抑制模型对抑制研究的结果进行建模。发现乙炔起可逆抑制剂的作用,并被用于探测还原性脱氯的活性。各种乙炔浓度用于区分微生物过程,包括甲烷生成,产乙酸和呼吸困难。要达到90%的甲烷生成率,TCE和VC转化率抑制率,分别需要48、192和12μM的乙炔浓度。 H 2依赖性乙酸盐的产生不受乙炔的抑制。 TCE和VC的Ks值分别为12μM和63μM。对于TCE和VC转化,乙炔抑制常数(KIC)的模型拟合得出竞争抑制模型的相同值(0.4μM)。但是,对于非竞争性抑制,TCE到c-DCE,TCE到1,1-DCE和VC到乙烯的估计KIU分别为13.3、14.1和2.2μM。竞争性和非竞争性抑制模型对于在高TCE和VC浓度下获得的结果同样能很好地模拟实验数据。对模型进行了进一步验证,以拟合在较低TCE和VC浓度下乙炔抑制的瞬态数据,竞争性抑制导致对实验数据的更好拟合。发现1-氯-1-氟乙烯(1,1-CFE)可以很好地跟踪VC的转化速率,因为VC和1,1-CFE具有相似的最大转化速率和Ks值。具有测量的Ks值为63和87μM的竞争性抑制模型分别用于预测VC和1,1-CFE转化的速率。乙炔和化合物抑制研究的相似速率和结果表明VC和1,1-CFE被同一酶转化。通过三种不同的文化进行的1,1-CFE转化清楚地表明1,1-CFE是跟踪VC转化率的绝佳替代品。

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