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Autopsy of high-pressure membranes to compare effectiveness of MF and UF pretreatment in water reclamation

机译:高压膜尸检以比较MF和UF预处理在水回收中的有效性

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A pilot-plant study was designed to compare the effectiveness of microfiltration (MF) and ultrafiltration (UF) as pretreatment for high-pressure membranes in reclamation of biologically treated wastewater effluent. Granular media, filtered secondary effluent from a full-scale wastewater treatment plant, was fed to MF and UF units that operated in parallel. Each of these filtrates served as the feedwater to two reverse osmosis (RO) units and one nanofiltration (NF) unit that operated in parallel. The decline in specific flux was substantially lower for high-pressure membranes receiving UF than MF pretreatment over the course of each of four pilot plant runs that lasted from 1 to 7 weeks. The removal of organic matter as measured by dissolved organic carbon (DOC) was somewhat higher by UF than MF pretreatment (about 15% by UF compared with 11% by MF). Addition of ferric chloride ahead of the UF unit, but not ahead of the MF unit, may account for this additional removal of organic matter. However, the additional DOC removal appeared insufficient to explain the differential in foulant accumulation between high-pressure membranes receiving UF and MF pretreatment. Extensive autopsy analyses of these high-pressure membranes showed from 35% to 56% less organic carbon on those receiving UF rather than MF pretreatment. A more specific indicator of a differential in organic fouling was the accumulation of polysaccharides and this showed from 27% to 38% less on UF- than on MF-pretreated membranes. Yet another possible source of foulants is inorganic material given that the inorganic and organic weight percentages were nearly equal (56% vs. 44%) on the membrane surface. One specific source was aluminum added for phosphorus removal. Less fouling of high-pressure membranes pretreated by UF than MF could be due to the following: (1) a small, but very important, colloidal fouling fraction may have passed through MF but was rejected by UF pretreatment; (2) organic fouling was not related to organics in either the MF or UF filtrates but rather to organics that are generated in situ by microbial activity on the membrane surface; and/or (3) less passage of colloidal Al-P that carried over from secondary wastewater treatment.
机译:设计了一项中试工厂研究,以比较微滤(MF)和超滤(UF)作为高压膜在生物处理废水的回收中的预处理的有效性。颗粒介质,是来自大型废水处理厂的经过滤的二次废水,被送入并行运行的MF和UF装置。这些滤液中的每一种均作为并行运行的两个反渗透(RO)单元和一个纳滤(NF)单元的给水。在持续1到7周的四个试验工厂运行过程中,接受超滤的高压膜的比通量的下降明显低于MF预处理。 UF测得的溶解有机碳(DOC)去除有机物的量比MF预处理要高一些(UF约为15%,MF则为11%)。在超滤装置之前而不是在MF装置之前添加氯化铁可能是有机物去除的原因。但是,额外的DOC去除似乎不足以解释接受UF和MF预处理的高压膜之间积垢的差异。对这些高压膜的广泛尸检分析表明,与使用超滤而不是MF预处理相比,这些有机膜的有机碳减少了35%至56%。有机污垢差异的更具体指标是多糖的积累,与用MF预处理的膜相比,UF-的多糖减少了27%至38%。考虑到膜表面的无机重量百分比和有机重量百分比几乎相等(56%比44%),还有可能的污染源是无机材料。一种特定的来源是添加铝以去除磷。 UF预处理后的高压膜结垢少于MF,可能是由于以下原因:(1)很小但很重要的胶体结垢部分可能已通过MF,但被UF预处理拒绝了; (2)有机污垢与MF或UF滤液中的有机物无关,而与膜表面微生物活性就地产生的有机物有关;和/或(3)二次废水处理中残留的胶体Al-P通道较少。

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