4.4 Article

Preparation of a thin-film nanocomposite forward osmosis membrane for the removal of organic micro-pollutants from aqueous solutions

Journal

ENVIRONMENTAL TECHNOLOGY
Volume 42, Issue 19, Pages 3011-3024

Publisher

TAYLOR & FRANCIS LTD
DOI: 10.1080/09593330.2020.1720307

Keywords

Thin-film nanocomposite; forward osmosis; benzene; phenol; toluene

Funding

  1. Department of Environmental Health Engineering, School of Public Health, Iran University of Medical Sciences
  2. Iran University of Medical Sciences [97-01-27-33503]

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In this study, a thin-film nanocomposite forward osmosis (TFN FO) membrane was synthesized and evaluated for removing organic micro-pollutants from wastewater. The TFN membrane showed higher hydrophilicity, porosity, water permeability, water flux, and salt rejection compared to traditional thin-film composite (TFC) membranes. The results suggest that TFN-FO membranes have the potential to improve water flux and wastewater treatment.
In this study, a thin-film nanocomposite forward osmosis (TFN FO) membrane was synthesized. The properties and structures of membranes were evaluated for the removal of three organic micro-pollutants from synthetic and real industrial wastewater samples. Laboratory scale fabrication thin-film nanocomposite forward osmosis (FO) membranes composed of a support layer and an active layer. The former was constructed by adding different weight ratios of polyethylene glycol 400 (PEG-400) (0-8 wt.%), polysulfone (PSf), and 1-methyl, 2-pyrrolidone via the phase inversion process, while the latter was synthesized by the incorporation of different weight ratios of graphene oxide (GO) (0-0.012 wt.%), M-phenylenediamine, and 1, 3, 5-benzene trichloride into polyamide layer through the interfacial polymerization reaction. In comparison with thin-film composite (TFC) membranes, the TFN membranes revealed higher hydrophilicity, porosity, water permeability, water flux and salt rejection and lower internal concentration polarization (ICP), reverse salt flux and specific reverse salt flux. The TFN membrane containing 0.008% GO in the active layer and 4% PEG 400 in the support layer exhibited maximum water flux (34.3 LMH) and rejection rate of benzene, phenol and toluene (97%, 84%, and 91%, respectively). The results revealed that the TFN-FO membranes possess a promising potential to improve the water flux and wastewater treatment.

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