曝气
过滤(数学)
生物反应器
膜生物反应器
膜污染
化学
制浆造纸工业
胞外聚合物
废水
结垢
化学需氧量
污染物
膜
硝化作用
色谱法
化学工程
废物管理
环境工程
环境科学
氮气
有机化学
遗传学
生物化学
生物膜
工程类
细菌
数学
统计
生物
作者
Conghui He,Kaijun Wang,Qianqian Wang,Juan Luo,Kuo Fang
标识
DOI:10.1016/j.seppur.2022.122853
摘要
A-stage technology is acknowledged as a promising process for organic recovery. Due to its superior separation performance, the high-loaded membrane bioreactor (HLMBR) is a competitive variant of the A-stage. In this study, a pilot-scale chemically enhanced HLMBR (CE-HLMBR) was established to enhance the practical feasibility of the process. Polyaluminium chloride (PAC) and activated carbon (AC) were added to address membrane fouling, dependence on intensive aeration, and inadequate concentration factors. Eight conditions were designed to investigate the role of chemicals and aeration in filtration, pollutant removal, and organic recovery. Stable filtration (8–10 LMH) was achieved at SS concentrations of 15–20 g/L, benefiting from the dynamic formation and shedding of the protective cake layer, as well as the reduction of extracellular polymer substances (EPS). Over 75 % soluble organics and 80 % soluble phosphorous were removed by CE-HLMBR, mainly subject to the chemicals. Simultaneous nitrification–denitrification occurred due to uneven oxygen distribution. The influent organics were concentrated by factors ranging from 27 to 80 and the loss rate was less than 15 %. Meanwhile, methane production may not be an efficient method of resource extraction. The practical feasibility of the proposed CE-HLMBR was confirmed based on an additional three-month stable operation. This study will open new possibilities for the application of HLMBR systems.
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