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Treatment of industrial wastewater produced by desulfurization process in a coal-fired power plant via FO-MD hybrid process

Authors
Lee, SongbokKim, YoungjinHong, Seungkwan
Issue Date
Nov-2018
Publisher
PERGAMON-ELSEVIER SCIENCE LTD
Keywords
Forward osmosis (FO); Flue gas desulfurization (FGD) wastewater; Membrane distillation (MD); Membrane fouling control; Industrial wastewater treatment
Citation
CHEMOSPHERE, v.210, pp.44 - 51
Indexed
SCIE
SCOPUS
Journal Title
CHEMOSPHERE
Volume
210
Start Page
44
End Page
51
URI
https://scholar.korea.ac.kr/handle/2021.sw.korea/71992
DOI
10.1016/j.chemosphere.2018.06.180
ISSN
0045-6535
Abstract
In this study, the feasibility of forward osmosis (FO) hybridized with membrane distillation (MD) was systematically investigated for treating flue gas desulfurization (FGD) wastewater. FO experiments were conducted using raw FGD wastewater obtained from a coal-fired power plant in Korea. Severe membrane fouling in FO was observed since FGD wastewater contained various components (i.e., particles, colloids, organics, and ions). The combined fouling layer by particulates and scales was identified via scanning electron microscope (SEM), energy dispersive X-ray (EDX) and X-ray diffraction (XRD). Therefore, fouling control strategies were suggested and evaluated. Microfiltration (MF) pre-treatment was effective in removing particulates and mitigating the initial fouling. Antiscalant-blended draw solution (DS) could inhibit the formation of membrane scaling. With such fouling control schemes, FO achieved the highest recovery rate compared to other desalting processes (i.e., RO and MD), suggesting that FO is suitable for treating wastewater with high fouling potential and high TDS. Finally, the diluted DS was recovered by MD. MD could re-concentrate the diluted DS up to 50% recovery rate with no significant flux decline. Rapid flux decline was then observed due to membrane scaling. Thus, appropriate antiscalants in DS should be considered to inhibit scaling formation in FO and MD simultaneously. (C) 2018 Elsevier Ltd. All rights reserved.
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