首页> 外文期刊>Journal of Environmental Engineering >Hybrid-Hollow-Fiber Membrane Bioreactor for Cometabolic Transformation of 4-Chlorophenol in the Presence of Phenol
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Hybrid-Hollow-Fiber Membrane Bioreactor for Cometabolic Transformation of 4-Chlorophenol in the Presence of Phenol

机译:苯酚存在下混合空心纤维膜生物反应器对4-氯苯酚的代谢转化

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Hybrid-hollow-fiber membrane bioreactors were developed for the enhanced cometabolic biotransformation of phenol and 4-chlorophenol (4-cp) by Pseudomonas putida ATCC49451. Bioreactor performance was investigated, compared, and analyzed under batch and continuous operating modes. The spinning solutions contained polysulfone (PS), N-methyl-2-pyrrolidone, and various weight ratios of granular activated carbon (GAC) (GAC: PS of 0, 1:4, and 1:2). The bioreactor fabricated with 1:2 GAC hybrid-hollow-fiber membranes demonstrated the best performance for the removal of phenol and 4-cp, both under batch and continuous operations. Under batch operation, 500 mg L-1 phenol and 4-cp were completely removed within 23 h in the bioreactor, compared with 26 and 30 h for the 1:4 GAC and GAC free bioreactors. Sorption, biotransformation, desorption, and bioregeneration were identified as the four steps for substrate removal during batch operation. The 1:2 GAC hollow-fiber membrane bioreactor also manifested superiority over the other two during continuous operation for start up and the transient phase after shock loadings of the feed. 300 mg L-1 phenol and 4-cp were completely removed in the 1:2 GAC hybrid-hollow-fiber membrane bioreactor whereas 4-cp was not completely removed in the other two bioreactors at a feed rate of 30 mL h?1. From the experimental results, it was inferred that at steady state, biotransformation was achieved through the dynamic equilibrium among sorption, desorption, and biotransformation rates established within the bioreactors.
机译:开发了混合中空纤维膜生物反应器,以通过恶臭假单胞菌ATCC49451增强苯酚和4-氯苯酚(4-cp)的代谢代谢。在分批和连续操作模式下研究,比较和分析了生物反应器的性能。纺丝溶液包含聚砜(PS),N-甲基-2-吡咯烷酮和各种重量比的颗粒活性炭(GAC)(GAC:PS为0、1:4和1:2)。用1:2 GAC混合中空纤维膜制造的生物反应器在分批操作和连续操作下均表现出去除苯酚和4-cp的最佳性能。在分批操作下,在23小时内,生物反应器中500 mg L-1苯酚和4-cp被完全去除,而1:4 GAC和无GAC的生物反应器分别在26和30 h内被去除。吸附,生物转化,解吸和生物再生被确定为批处理操作中去除底物的四个步骤。 1:2 GAC中空纤维膜生物反应器在连续操作的启动和进料冲击负荷后的过渡阶段中也表现出优于其他两个反应器的优势。在1:2 GAC混合中空纤维膜生物反应器中,300 mg L-1苯酚和4-cp被完全去除,而在另外两个生物反应器中,进料速率为30 mL h?1,4-cp未被完全去除。从实验结果可以推断,在稳态下,通过生物反应器内建立的吸附,解吸和生物转化速率之间的动态平衡实现了生物转化。

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