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Antifouling zwitterion embedded forward osmosis thin film composite membrane for highly concentrated oily wastewater treatment

机译:防污倍动嵌入式前渗透渗透薄膜复合膜,用于高浓度油性废水处理

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The raising oil consumption in oil and gas industries has exacerbated the disposal of oil waste into various water streams. This phenomenon has called for treatments to prevent threats to the human and environment. With some great advantages such as lower membrane fouling rate, lower energy requirement and higher water recovery rate compared to the conventional pressure-driven membrane processes, forward osmosis (FO) has been recognized as a potential candidate for oily wastewater treatment In this study, a poly[3-(N-2-methacry-loylxyethyl-N,N-dimethyl)-anunonatopropanesulfonate] (PMAPS) incorporated thin film composite (TFC) membrane with excellent anti-fouling properties was fabricated for oily wastewater through forward osmosis process. PMAPS was blended with polyethersulfone (PES) dope solution and cast into PES support layer. Interfacial polymerization (IP) technique was applied to form a thin polyamide (PA) layer atop of the PES support layer. The PMAPS incorporated TFC membranes were characterized for their morphology and surface hydrophilicity. The resultant 1% PMAPS-TFC membrane exhibited high water flux of 15.79 +/- 0.3 L/m(2).h and oil flux of 12.54 +/- 0.8 L/m(2).h when tested in FO mode for oil removal from oily wastewater using 1000 ppm emulsified oily solution as feed solution and 2 M NaCl as draw solution. The oil rejection up to 99% was also obtained. Most significantly, PMAPS incorporated TFC membrane outperformed neat TFC membrane with lower fouling propensity for oily waste treatment. When treating 10000 ppm oil emulsion, PMAPS-TFC was able to achieve average flux recovery rate of 97% while neat TFC only able to achieve 70.8% of average flux recovery rate.
机译:石油和天然气行业的石油消耗加剧了石油废物处理到各种水流中。这种现象呼吁治疗以防止对人类和环境的威胁。与常规的压力驱动膜过程相比,诸如较低的膜污垢速率,较低的能量需求和更高的水回收率等优点,正常渗透(FO)被认为是本研究中油性废水处理的潜在候选者,a聚[3-(N-2-甲基 - 氯约甲酰基-N,N-二甲基) - 丁替替丙烷磺酸盐](PMAPS)掺入具有优异的抗结垢性能的薄膜复合物(TFC)膜通过前渗透过程制造油性废水。 PMAP与聚醚砜(PES)掺杂溶液混合并浇铸成PES支撑层。施用界面聚合(IP)技术以形成PES支撑层的薄聚酰胺(PA)层。掺入TFC膜的PMAPS掺入其形态和表面亲水性。所得1%的PMAPS-TFC膜表现出15.79 +/- 0.3L / m(2).h和12.54 +/- 0.8L / m / m(2).h的高水量的水通量为12.54 +/- 0.8L / m(2).h使用1000ppm乳化油性溶液作为进料溶液和2m NaCl作为抽取溶液从油性废水中除去。还获得了高达99%的排油。最显着的是,PMAPS掺入TFC膜优于整齐的TFC膜,具有较低的油性废物处理倾向。当治疗10000ppm油乳液时,PMAPS-TFC能够达到平均通量回收率97%,而整洁的TFC只能达到平均通量回收率的70.8%。

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