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生物工程两段式序批式反应器和过滤吸附工艺处理复杂农用化学品废水的可行性。

Feasibility of bioengineered two-stages sequential batch reactor and filtration-adsorption process for complex agrochemical effluent.

机构信息

CSIR-National Environmental Engineering Research Institute, Nagpur 440 020, India.

出版信息

Bioresour Technol. 2013 Nov;148:334-42. doi: 10.1016/j.biortech.2013.08.145. Epub 2013 Sep 3.

Abstract

In the present study, the feasibility of a bioengineered two-stages sequential batch reactor (BTSSBR) followed by filtration-adsorption process was investigated to treat the agrochemical effluent by overcoming factor affecting process stability such as microbial imbalance and substrate sensitivity. An air stripper stripped 90% of toxic ammonia, and combined with other streams for bio-oxidation and filtration-adsorption. The BTSSBR system achieved bio-oxidation at 6 days hydraulic retention time by fending off microbial imbalance and substrate sensitivity. The maximum reduction in COD and BOD by heterotrophic bacteria in the first reactor was 87% and 90%, respectively. Removal of toxic ammoniacal-nitrogen by autotrophic bacteria in a post-second stage bio-oxidation was 97%. The optimum filtration and adsorption of pollutants were achieved at a filtration rate of 10 and 9 m(3)m(-2)h(-1), respectively. The treatment scheme comprising air stripper, BTSSBR and filtration-adsorption process showed a great promise for treating the agrochemical effluent.

摘要

在本研究中,通过克服影响工艺稳定性的因素,如微生物失衡和基质敏感性,考察了生物工程两段序批式反应器(BTSSBR)后过滤-吸附工艺处理农用化学品废水的可行性。空气汽提器去除了 90%的有毒氨,并与其他流股一起进行生物氧化和过滤-吸附。BTSSBR 系统通过抵御微生物失衡和基质敏感性,在 6 天水力停留时间内实现了生物氧化。第一反应器中异养菌对 COD 和 BOD 的最大去除率分别为 87%和 90%。在后段生物氧化中自养菌对有毒氨氮的去除率达到 97%。在过滤速率为 10 和 9 m(3)m(-2)h(-1)时,可实现对污染物的最佳过滤和吸附。包括空气汽提器、BTSSBR 和过滤-吸附工艺的处理方案显示出处理农用化学品废水的巨大潜力。

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