Gerritse J, Kloetstra G, Borger A, Dalstra G, Alphenaar A, Gottschal J C
Department of Microbiology, University of Groningen, The Netherlands.
Appl Microbiol Biotechnol. 1997 Oct;48(4):553-62. doi: 10.1007/s002530051096.
Anaerobic tetrachloroethene (C2Cl4)-dechlorinating bacteria were enriched in slurries from chloroethene-contaminated soil. With methanol as electron donor, C2Cl4 and trichloroethene (C2HCl3) were reductively dechlorinated to cis-1,2-dichloroethene (cis-C2H2Cl2), whereas, with L-lactate or formate, complete dechlorination of C2Cl4 via C2HCl3, cis-C2H2Cl2 and chloroethene (C2H3Cl) to ethene was obtained. In oxic soil slurries with methane as a substrate, complete co-metabolic degradation of cis-C2H2Cl2 was obtained, whereas C2HCl3 was partially degraded. With toluene or phenol both of the above were readily co-metabolized. Complete degradation of C2Cl4 was obtained in sequentially coupled anoxic and oxic chemostats, which were inoculated with the slurry enrichments. Apparent steady states were obtained at various dilution rates (0.02-0.4 h-1) and influent C2Cl4-concentrations (100-1000 microM). In anoxic chemostats with a mixture of formate and glucose as the carbon and electron source, C2Cl4 was transformed at high rates (above 140 micromol 1-1 h-1, corresponding to 145 nmol Cl- min-1 mg protein-1), into cis-C2H2Cl2 and C2H3Cl. Reductive dechlorination was not affected by addition of 5 mM sulphate, but strongly inhibited after addition of 5 mM nitrate. Our results (high specific dechlorination rates and loss of dechlorination capacity in the absence of C2Cl4) suggest that C2Cl4-dechlorination in the anoxic chemostat was catalysed by specialized dechlorinating bacteria. The partially dechlorinated intermediates, cis-C2H2Cl2 and C2H3Cl, were further degraded by aerobic phenol-metaboizing bacteria. The maximum capacity for chloroethene (the sum of tri-, di- and monochloro derivatives removed) degradation in the oxic chemostat was 95 micromol 1-1 h-1 (20 nmol min-1 mg protein-1), and that of the combined anoxic --> oxic reactor system was 43.4 micromol 1-1 h-1. This is significantly higher than reported thus far.
在受氯乙烯污染的土壤泥浆中富集了厌氧四氯乙烯(C2Cl4)脱氯细菌。以甲醇作为电子供体时,C2Cl4和三氯乙烯(C2HCl3)被还原脱氯为顺式-1,2-二氯乙烯(cis-C2H2Cl2),而以L-乳酸盐或甲酸盐为电子供体时,C2Cl4可通过C2HCl3、顺式-C2H2Cl2和氯乙烯(C2H3Cl)完全脱氯为乙烯。在以甲烷为底物的好氧土壤泥浆中,顺式-C2H2Cl2可实现完全的共代谢降解,而C2HCl3则部分降解。以甲苯或苯酚为底物时,上述两种物质都易于共代谢。在依次连接的缺氧和好氧恒化器中实现了C2Cl4的完全降解,该恒化器接种了泥浆富集物。在不同的稀释率(0.02 - 0.4 h-1)和进水C2Cl4浓度(100 - 1000 microM)下获得了明显的稳态。在以甲酸盐和葡萄糖的混合物作为碳源和电子源的缺氧恒化器中,C2Cl4以高速率(高于140 micromol 1-1 h-1,相当于145 nmol Cl- min-1 mg蛋白质-1)转化为顺式-C2H2Cl2和C2H3Cl。添加5 mM硫酸盐不会影响还原脱氯,但添加5 mM硝酸盐后会强烈抑制。我们的结果(高比脱氯速率以及在不存在C2Cl4时脱氯能力丧失)表明,缺氧恒化器中的C2Cl4脱氯是由专门的脱氯细菌催化的。部分脱氯中间体,顺式-C2H2Cl2和C2H3Cl,被好氧苯酚代谢细菌进一步降解。好氧恒化器中氯乙烯(去除的三氯、二氯和一氯衍生物的总和)降解的最大能力为95 micromol 1-1 h-1(20 nmol min-1 mg蛋白质-1),而组合的缺氧→好氧反应器系统的最大能力为43.4 micromol 1-1 h-1。这明显高于迄今为止报道的数值。