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Performance study of ZrO2 ceramic micro-filtration membranes used in pretreatment of DMF wastewater

机译:ZrO2陶瓷微滤膜在DMF废水预处理中的性能研究

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Three kinds of 19-channel ZrO2 micro-filtration membranes with different pore size were used for pretreatment of dimethylformamide (DMF) wastewater from the polyurethane (PU) synthetic leather factories, which would enter the distillation column for further purification. The effects of membrane pore size, cross flow velocity (CFV) and transmembrane pressure (TMP) on ceramic membrane filtration performances were investigated. Experimental results indicated that the optimum membrane pore size, CFV and TMP were 0.2 um, 3 m s~(-1) and 0.2 MPa, respectively, with the corresponding liquid turbidity removal rate of 99.62% and suspended solid content retention rate of 99.99%. The membrane fouling mechanism was analyzed by resistance in series model. The main resistance derived from the particle adsorption and sedimentation on the membrane surface. The ratio of particle adsorption and sedimentation resistance to total resistance was above 70% for the 0.2 um membrane. The backflushing technology was applied and the effect of backflushing on the permeate flux was studied. The permeate flux eventually increased by 50% with the optimum backflushing pressure of 0.6 MPa, backflushing time of 5 s and backflushing interval of 20 min. A combination cleaning method was used to regenerate the ZrO2 micro-filtration membrane. The pure water flux recovered to 608.2 L m~(-2) h~(-1) and flux recovery rate was 96.8% which indicated that the combination cleaning method was effective.
机译:三种不同孔径的19通道ZrO2微滤膜用于预处理聚氨酯(PU)合成革工厂的二甲基甲酰胺(DMF)废水,该废水将进入蒸馏塔进行进一步纯化。研究了膜孔径,错流速度(CFV)和跨膜压力(TMP)对陶瓷膜过滤性能的影响。实验结果表明,最佳膜孔径,CFV和TMP分别为0.2 um,3 m s〜(-1)和0.2 MPa,相应的浊度去除率为99.62%,悬浮物保留率为99.99%。通过阻力串联模型分析了膜的结垢机理。主要阻力来自颗粒在膜表面的吸附和沉淀。对于0.2um的膜,颗粒吸附和沉降阻力与总阻力的比率高于70%。应用了反吹技术,研究了反吹对渗透通量的影响。最终,渗透流量增加了50%,最佳反冲洗压力为0.6 MPa,反冲洗时间为5 s,反冲洗间隔为20分钟。使用组合清洁方法再生ZrO2微滤膜。纯净水通量恢复到608.2 L m〜(-2)h〜(-1),通量回收率为96.8%,表明组合清洗方法是有效的。

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