4.7 Article

Process development for textile wastewater treatment towards zero liquid discharge: Integrating membrane separation process and advanced oxidation techniques

Journal

PROCESS SAFETY AND ENVIRONMENTAL PROTECTION
Volume 157, Issue -, Pages 537-546

Publisher

ELSEVIER
DOI: 10.1016/j.psep.2021.10.037

Keywords

Integrated treatment process; Dye recovery; Membrane technology; Advanced oxidation processes; Water reclamation

Funding

  1. Coordination for the Improvement of Higher Education Personnel (CAPES)
  2. National Council for Scientific and Technological Development (CNPq)
  3. Foundation for Research Support of the State of Minas Gerais (FAPEMIG)
  4. Federal University of Minas Gerais, Brazil (UFMG)
  5. Tear Textil Ind. e Com. Ltda.

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The study proposed a treatment process for textile wastewater based on microfiltration and nanofiltration, which efficiently removed pollutants through a series of chemical treatment processes, achieving reuse and reducing environmental impacts. The treated wastewater had high removal rates of COD and color, and had a competitive advantage in terms of economic cost.
A treatment process based on microfiltration followed by nanofiltration (MF-NF) is proposed for textile wastewater treatment. The NF concentrate is further treated by UV/H2O2, Fenton, and photo-Fenton processes. Results showed that the dye was efficiently retained by the MF membrane (>99.1%), which allowed its reuse. The MF-NF was able to reject 92% of the chemical oxygen demand (COD) and >98.5% of color. When the NF concentrate was treated by UV/H2O2, it was achieved a maximum COD removal of 63% in the condition C:H2O2 1:3 (molar ratio of COD and hydrogen peroxide) and pH 3. The Fenton process, optimized through response surface methodology, achieved 84.7% of COD removal, which increased when combined with UV irradiation (92.2%). An analysis of the NF permeate physicochemical quality and its treated concentrate suggested that it can be reused in the textile industry for different purposes as yarn washing-off and equipment's washdown. The operating cost for MF-NF corresponded to 0.240 US$/m(3) and, including the cost of NF concentrate treatment by photo-Fenton, 0.517 US$/m(3), lower than currently practiced by the water distribution company. The system proposed for water reuse and NF concentrate treatment was able to increase the water recovery and decrease the environmental impacts that could be caused by the NF concentrate disposal. (C) 2021 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.

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