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采用超疏水/亲有机物电纺 PDMS/PMMA 膜的膜芳烃回收系统样膜接触器从含酚盐废水中分离苯酚。

Phenol separation from phenol-laden saline wastewater by membrane aromatic recovery system-like membrane contactor using superhydrophobic/organophilic electrospun PDMS/PMMA membrane.

机构信息

School of Environmental Science and Engineering, Shanghai Jiao Tong University, No. 800 Dongchuan Road, Shanghai 200240, Shanghai, PR China.

School of Environmental Science and Engineering, Shanghai Jiao Tong University, No. 800 Dongchuan Road, Shanghai 200240, Shanghai, PR China.

出版信息

Water Res. 2018 May 15;135:31-43. doi: 10.1016/j.watres.2018.02.011. Epub 2018 Feb 10.

DOI:10.1016/j.watres.2018.02.011
PMID:29454239
Abstract

Phenol recovery from phenol-laden saline wastewater plays an important role in the waste reclamation and pollution control. A membrane aromatic recovery system-like membrane contactor (MARS-like membrane contactor) was set up in this study using electrospun polydimethylsiloxane/polymethyl methacrylate (PDMS/PMMA) membrane with 0.0048 m effective area to separate phenol from saline wastewater. Phenol and water contact angles of 0° and 162° were achieved on this membrane surface simultaneously, indicating its potential in the separation of phenol and water-soluble salt. Feed solution (500 mL) of 0.90 L/h and receiving solution (500 mL) of 1.26 L/h were investigated to be the optimum conditions for phenol separation, which corresponds to the employed Reynolds number of 14.6 and 20.5. During 108-h continuous separation for feed solution (2.0 g/L phenol, 10.0 g/L NaCl) under room temperature (20 °C), 42.6% of phenol was recycled in receiving solution with a salt rejection of 99.95%. Meanwhile, the mean phenol mass transfer coefficient (K) was 6.7 × 10 m s. As a membrane-based process, though the permeated phenol increased with the increase of phenol concentration in feed solution, the phenol recovery ratio was determined by the membrane properties rather than the pollutant concentrations. Phenol was found to permeate this membrane via adsorption, diffusion and desorption, and therefore, the membrane fouling generated from pore blockage in other membrane separation processes was totally avoided.

摘要

从含酚盐废水中回收苯酚对于废物回收和污染控制具有重要作用。本研究采用静电纺丝制备的聚二甲基硅氧烷/聚甲基丙烯酸甲酯(PDMS/PMMA)膜构建了一种膜芳香族回收系统样膜接触器(MARS 样膜接触器),用于从含盐废水中分离苯酚。该膜表面同时实现了苯酚和水的接触角为 0°和 162°,表明其在分离苯酚和水溶性盐方面具有潜力。进料溶液(500mL)流速为 0.90L/h,接收溶液(500mL)流速为 1.26L/h 被认为是苯酚分离的最佳条件,对应的雷诺数分别为 14.6 和 20.5。在 20°C 室温下连续分离 108 小时后,接收溶液中回收了 42.6%的苯酚,盐截留率为 99.95%。同时,平均苯酚传质系数(K)为 6.7×10-5m/s。作为一种基于膜的工艺,尽管透过的苯酚随进料溶液中苯酚浓度的增加而增加,但苯酚的回收率取决于膜的性质而不是污染物的浓度。研究发现,苯酚通过吸附、扩散和解吸透过该膜,因此完全避免了其他膜分离过程中由于孔堵塞而产生的膜污染。

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