首页> 外文期刊>Transactions of The Institution of Chemical Engineers. Process Safety and Environmental Protection, Part B >Enhancing biodegradation of toxic industrial wastewaters in a continuous two-phase partitioning bioreactor operated with effluent recycle
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Enhancing biodegradation of toxic industrial wastewaters in a continuous two-phase partitioning bioreactor operated with effluent recycle

机译:用流出物回收的连续两相分区生物反应器增强毒性工业废水的生物降解

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In this study, we propose the application of a Continuous Two-Phase Partitioning Bioreactor (C-TPPB) operated with the tubing effluent recycle to enhance the biodegradation of toxic substrates in industrial wastewaters under severe loading conditions. Stepwise increasing influent concentrations (from 200 to 900 mg L-1) of 2,4-dichlorophenol (2,4-DCP) were fed to a C-TPPB operated with Hytrel G3548 tubing to simulate phenolic wastewater. Practically complete 2,4-DCP removal has been achieved during the entire experimental period, but the increased load reduced biodegradation efficiency. At influent concentration of 700 mg L-1, the first effluent recycle (recycle /influent flow rate ratio = 0.3) was applied: biodegradation efficiency doubled from 40 to 80% and was maintained until influent concentrations of 800 mg L-1. Higher influent concentrations caused a decrease in 2,4-DCP biodegradation, so the effluent recycle ratio was increased to 0.5 at 900 mg L-1 and, also in this case, the bioreactor showed a fast recovery (similar to 24 h) of the biodegradation efficiency at 80%. Mass transfer data analysis showed that the effluent recycle resulted in an increase of the mass transfer coefficient. This positive effect, joined with the reduction of the influent concentrations, demonstrated the feasibility of recycle application in enhancing the C-TPPB performance. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:在该研究中,我们提出了使用管道流出物再循环操作的连续两相分配的生物反应器(C-TPPB),以在严重的负载条件下增强工业废水中有毒基材的生物降解。将2,4-二氯苯酚(2,4-DCP)的进水浓度(从200至900mg L-1)逐步加入到用Hytrel G3548管操作的C-TPPB中,以模拟酚醛废水。实际上在整个实验期间已经实现了2,4-DCP去除,但增加了负荷降低了生物降解效率。在水中浓度为700mg L-1,施加第一污水再循环(再循环/进入流速比率= 0.3):生物降解效率从40〜80%加倍,并保持直至800mg L-1的流动浓度。较高的进水浓度导致2,4-DCP生物降解的降低,因此流出物再循环比在900mg L-1下增加至0.5,并且在这种情况下,生物反应器显示出快速恢复(类似于24小时)生物降解效率为80%。传质数据分析表明,流出物再循环导致传质系数的增加。这种积极效果加入了流入的浓度的减少,证明了循环应用在提高C-TPPB性能方面的可行性。 (c)2019化学工程师机构。 elsevier b.v出版。保留所有权利。

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