4.7 Article

Industrial wastewater treatment using PES UF membranes containing hydrophilic additives: Experimental and modeling of fouling mechanism

Journal

ENVIRONMENTAL TECHNOLOGY & INNOVATION
Volume 23, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.eti.2021.101701

Keywords

Industrial wastewater treatment; Ultrafiltration (UF); Polyethersulfone (PES); Hydrophilic additives; Hermia's model

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The effects of different hydrophilic additives and coagulation bath temperature on the morphology and performance of PES ultrafiltration membranes were studied. PES/PVP membranes exhibited denser structure, while increasing CBT led to higher porosity and water permeability. Membranes containing 5% TEG showed the best separation performance for treating wastewater.
In order to acquire preferred structure and performance, the effects of different hydrophilic additives, including triethylene glycol (TEG), polyethylene glycol (PEG), polyvinylpyrrolidone (PVP) at various concentrations, and coagulation bath temperature (CBT) on the morphology and performance of polyethersulfone (PES) ultrafiltration (UF) membranes were studied. The PES membranes were fabricated via non-solvent induced phase separation (NIPS) technique, and their performances were measured in terms of pure water flux (PWF), the flux of synthetic oil/water (O/W) emulsion, and industrial oily and textile wastewater, and oil rejection. Additionally, the morphology and hydrophilicity of the membranes were characterized by the SEM and water contact angle (CA) tests, respectively. The results revealed that the morphology and structure of the PES membranes depend on the type and concentration of the additive in the casting solution, as PES/PVP membranes had a denser structure than the PES/TEG and PES/PEG membranes. Besides, increasing CBT from 25 degrees C to 45 degrees C leads to the formation of a membrane with higher porosity, larger pores, higher water permeability, and lower oil rejection. The membrane containing 5%wt of TEG showed the best separation performance for treating synthetic and industrial wastewaters. Moreover, modeling of the flux decline using Hermia's model and second kind standard blocking indicated the gel layer formation is the dominant fouling mechanism of the UF process of the oily wastewaters. (C) 2021 Elsevier B.V. All rights reserved.

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