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一种将还原脱氯与共代谢氧化相结合以实现四氯乙烯完全降解的反应器系统。

A reactor system combining reductive dechlorination with co-metabolic oxidation for complete degradation of tetrachloroentylene.

作者信息

Lee Tae Ho, Ike Michihiko, Fujita Masanori

机构信息

Department of Environmental Engineering, Osaka University, 2-1 Yamadaoka, Suita, Osaka 565-0871, Japan.

出版信息

J Environ Sci (China). 2002 Oct;14(4):445-50.

Abstract

A laboratory sequential anaerobic-aerobic bioreactor system, which consisted of an anaerobic fixed film reactor and two aerobic chemostats, was set up to degrade tetrachloroethylene (PCE) without accumulating highly toxic degradation intermediates. A soil enrichment culture, which could reductively dechlorinate 900 microM (ca. 150 mg/L) of PCE stoichiometrically into cis-1,2-dichloroethylene (cis-DCE), was attached to ceramic media in the anaerobic fixed film reactor. A phenol degrading strain, Alcaligenes sp. R5, which can efficiently degrade cis-DCE by co-metabolic oxidation, was used as inoculum for the aerobic chemostats consisted of a transformation reactor and a growth reactor. The anaerobic fixed film bioreactor showed more than 99% of PCE transformation into cis-DCE in the range of influent PCE concentration from 5 microM to 35 microM at hydraulic retention time of 48 h. On the other hand, efficient degradation of the resultant cis-DCE by strain R5 in the following aerobic system could not be achieved due to oxygen limitation. However, 54% of the maximum cis-DCE degradation was obtained when 10 mumol of hydrogen peroxide (H2O2) was supplemented to the transformation reactor as an additional oxygen source. Further studies are needed to achieve more efficient co-metabolic degradation of cis-DCE in the aerobic reactor.

摘要

搭建了一套实验室序批式厌氧-好氧生物反应器系统,该系统由一个厌氧固定膜反应器和两个好氧恒化器组成,用于降解四氯乙烯(PCE),且不会积累高毒性的降解中间体。一种土壤富集培养物附着在厌氧固定膜反应器的陶瓷介质上,该培养物可将900微摩尔(约150毫克/升)的PCE按化学计量比还原脱氯为顺式-1,2-二氯乙烯(cis-DCE)。一种苯酚降解菌株,即产碱杆菌属R5,它能通过共代谢氧化有效降解cis-DCE,被用作由一个转化反应器和一个生长反应器组成的好氧恒化器的接种物。在水力停留时间为48小时、进水PCE浓度为5微摩尔至35微摩尔的范围内,厌氧固定膜生物反应器显示出超过99%的PCE转化为cis-DCE。另一方面,由于氧气限制,后续好氧系统中的菌株R5无法有效降解生成的cis-DCE。然而,当向转化反应器中补充10微摩尔过氧化氢(H2O2)作为额外的氧源时,可实现cis-DCE最大降解量的54%。需要进一步研究以在好氧反应器中实现更高效的cis-DCE共代谢降解。

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