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Anaerobic membrane bioreactor for treatment of synthetic municipal wastewater at ambient temperature

机译:厌氧膜生物反应器在环境温度下处理合成市政废水

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摘要

Non-woven fabric filter and poly-tetrafluoroethylene (PTFE) composite membrane were investigated to determine their applicability to treat low strength wastewater in an anaerobic membrane bioreactor (AMBR). Sludge cake resistance of the membrane was quantified using pure water flux of anaerobic sludge cake accumulated on the glass fiber filter of similar pore size. It is hypothesized that the formation of thin cake layer on the porous medium, e.g. non-woven and PTFE acts as a dynamic membrane. Thus, the capture of thin sludge cake inside the non-woven fabric matrix and accumulation on the PTFE membrane surface forms a membrane system equivalent to a commercial membrane system. The permeate quality was found to improve as the cake became more dense with filtration time. The PTFE composite membrane coated with thin PTFE film on the non-woven fabric filter enhanced the filtration performance by improving flux and minimizing the propensity of bio-fouling. The membrane flux was restored by back-flushing with permeate. The AMBR coupled with PTFE laminated membrane was operated continuously during the experiment at a cross flow velocity (CFV) of 0.1–0.2 m/sec and a transmembrane pressure (TMP) of 0.5–3 psi. Although about a month of acclimation was required to reach steady state, the effluent chemical oxygen demand (COD), volatile fatty acids (VFAs) as acetic acid, and suspended solids (SS) concentrations were below 30, 20 and 10 mg/L, respectively, during 90 days of operation with intermittent back washing. The lower operation TMP and CFV were subjected to less shear stress on the microbial community during continuous AMBR operation. In addition, thin sludge film accumulated on the membrane surface also acted as a biofilm bioreactor to remove additional COD in this study.
机译:研究了无纺布过滤器和聚四氟乙烯(PTFE)复合膜,以确定它们在厌氧膜生物反应器(AMBR)中处理低强度废水的适用性。使用堆积在具有类似孔径的玻璃纤维过滤器上的厌氧污泥饼的纯净水通量来量化膜的抗污饼饼性。假设在多孔介质上形成薄的滤饼层,例如多孔的。无纺布和PTFE充当动态膜。因此,薄的污泥饼在无纺布基质内的捕获和在PTFE膜表面上的积累形成了与商业膜系统等效的膜系统。随着滤饼时间的增加,滤饼变得更致密,渗透物质量得到改善。在无纺布过滤器上涂有PTFE薄膜的PTFE复合膜通过改善通量并最大程度降低生物结垢的倾向来增强过滤性能。通过用渗透液反冲洗来恢复膜通量。在实验过程中,AMBR与PTFE层压膜的连接以0.1–0.2 m / sec的错流速度(CFV)和0.5–3 psi的跨膜压力(TMP)连续运行。尽管需要大约一个月的时间才能达到稳定状态,但污水中的化学需氧量(COD),作为乙酸的挥发性脂肪酸(VFA)和悬浮固体(SS)的浓度分别低于30、20和10 mg / L,分别在操作90天期间进行间歇性反冲洗。在连续AMBR操作期间,较低操作的TMP和CFV在微生物群落上受到的剪切应力较小。此外,在这项研究中,积聚在膜表面的污泥薄膜还充当生物膜生物反应器,以去除额外的COD。

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