4.8 Article

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

期刊

WATER RESEARCH
卷 135, 期 -, 页码 31-43

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.watres.2018.02.011

关键词

Membrane contactor; PDMS; Electrospun membrane; Phenol separation; Mass transfer

资金

  1. National Natural Science Foundation of China [21577089]
  2. Major Science and Technology Program for Water Pollution Control and Treatment [2014ZX07206001]
  3. National Research Foundation Singapore under its Campus for Research Excellence and Technological Enterprise (CREATE)

向作者/读者索取更多资源

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(2) effective area to separate phenol from saline wastewater. Phenol and water contact angles of 0 degrees and 162 degrees 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 IA 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 phenol, 10.0 g/L NaCl) under room temperature (20 degrees 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-ov) was 6.7 x 10(-7) m s(-1). 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. (C) 2018 Elsevier Ltd. All rights reserved.

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