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在填充无机载体的生物过滤器中同时生物降解甲烷和苯乙烯:实验和宏观动力学研究。

Simultaneous biodegradation of methane and styrene in biofilters packed with inorganic supports: Experimental and macrokinetic study.

机构信息

Department of Chemical Engineering and Biotechnological Engineering, Faculty of Engineering, 2500 boulevard de l'Université, Université de Sherbrooke, Sherbrooke, J1K 2R1, Quebec, Canada.

Department of Chemical Engineering and Biotechnological Engineering, Faculty of Engineering, 2500 boulevard de l'Université, Université de Sherbrooke, Sherbrooke, J1K 2R1, Quebec, Canada.

出版信息

Chemosphere. 2020 Aug;252:126492. doi: 10.1016/j.chemosphere.2020.126492. Epub 2020 Mar 17.

Abstract

Four upflow 0.018 m biofilters (3 beds), B-ME, B-200, B-500 and B-700, all packed with inorganic materials, were operated at a constant air flow rate of 0.18 m h to eliminate methane (CH), a harmful greenhouse gas (GHG), and styrene (CH), a carcinogenic volatile organic compound (VOC). The biofilters were irrigated with 0.001 m of recycled nutrient solution (NS) every day (flow rate of 60 × 10 m h). Styrene inlet load (IL) was kept constant in each biofilter. Different CH-ILs varying in the range of 7-60 gCH m h were examined in B-ME (IL of 0 gCH m h), B-200 (IL of 9 gCH m h), B-500 (IL of 22 gCH m h) and B-700 (IL of 32 gCH m h). Finally, the effect of CH on the macrokinetic parameters of CH biofiltration was studied based on the Michaelis-Menten model. Average CH removal efficiencies (RE) varying between 64 and 100% were obtained at CH-ILs increasing from 7 to 60 gCH m h and for CH-ILs range of 0-32 gCH m h. More than 90% of CH was removed in the bottom and middle beds of the biofilters. By increasing CH-IL from 0 to 32 gCH m h, maximal EC in Michaelis-Menten model and macrokinetic saturation constant declined from 311 to 39 g m h and from 19 to 2.3 g m, respectively, which confirmed that an uncompetitive inhibition occurred during CH biofiltration in the presence of CH.

摘要

四个上流式 0.018 米生物过滤器(3 个床层),B-ME、B-200、B-500 和 B-700,均采用无机材料填充,以 0.18 米/小时的恒定空气流速运行,以消除甲烷(CH)这种有害的温室气体(GHG)和苯乙烯(CH)这种致癌挥发性有机化合物(VOC)。生物过滤器每天用 0.001 米的再循环营养液(NS)灌溉(流量为 60×10 米/小时)。每个生物过滤器中的苯乙烯入口负荷(IL)保持不变。在 B-ME(IL 为 0 gCH m h)、B-200(IL 为 9 gCH m h)、B-500(IL 为 22 gCH m h)和 B-700(IL 为 32 gCH m h)中检查了范围在 7-60 gCH m h 之间的不同 CH-IL。最后,根据米氏-门捷列夫模型研究了 CH 对 CH 生物过滤宏观动力学参数的影响。在 CH-IL 从 7 增加到 60 gCH m h 以及 CH-IL 范围为 0-32 gCH m h 时,获得了在 64%到 100%之间变化的平均 CH 去除效率(RE)。在生物过滤器的底部和中部床层中去除了超过 90%的 CH。通过将 CH-IL 从 0 增加到 32 gCH m h,米氏-门捷列夫模型中的最大 EC 和宏观动力学饱和常数分别从 311 降至 39 g m h 和从 19 降至 2.3 g m,这证实了在存在 CH 的情况下,CH 生物过滤过程中发生了非竞争性抑制。

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