4.7 Article

Multi-ionic electrolytes and E.coli removal from wastewater using chitosan-based in-situ mediated thin film composite nanofiltration membrane

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JOURNAL OF ENVIRONMENTAL MANAGEMENT
卷 294, 期 -, 页码 -

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ACADEMIC PRESS LTD- ELSEVIER SCIENCE LTD
DOI: 10.1016/j.jenvman.2021.112996

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Nanofiltration membrane; Electrolytes; E; coli; Interfacial polymerization; Crossflow membrane

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This study investigated the experimental application of a flat sheet composite nanofiltration membrane synthesized with chitosan nanoparticles and interfacial polymerization of piperazine with polyethersulfone/sulfonated polysulfone substrates in wastewater treatment. The rejection rates for various ions and E. coli were measured under different operating conditions, showing promising results for water flux and species rejection in the permeate.
This work presents the experimental investigation of flat sheet composite nanofiltration membrane synthesized with chitosan nanoparticles through interfacial polymerization of piperazine with trimesoyl chloride on polyethersulfone/sulfonated polysulfone substrates. The synthesized membrane was tested in wastewater treatment containing inorganic salts and E.Coli. Single binary electrolyte solution of KCl, MgCl2, MgSO4, and Na2SO4, ternary electrolyte solution, containing a combination of MgCl2 and MgSO4, KCl and MgCl2 and quaternary electrolyte solution of KCl, MgCl2, and MgSO4 as feed were treated in crossflow membrane cell for the water flux and species rejection in the permeate under operating pressure up to 0.5 MPa. The rejection of Na1+, K1+, Mg2+, Cl1xe213;, and SO42xe213; was observed to be 81, 28, 87, 96, and 98%, respectively with an average water flux up to 214 +/- 10 L m-2.hr-1 in the permeate for the binary electrolyte solution. Similarly, the rejection for K1+, Mg2+, Cl1xe213; and SO42xe213; was noted to be 33, 94, 97, and 99%, respectively, for ternary electrolyte solution with an average water flux up to 211 +/- 10 L mxe213; 2.hrxe213; 1. The quaternary ion system in the feed resulted in an average water flux up to 198 +/- 12 L m-2.hr-1 with the rejection of K+, Mg+2, Clxe213; and SO4xe213; 2 as 35, 87, 96, and 99%, respectively. The model feed solution of E. coli after passing through the membrane achieved an E. coli rejection (99%) with water flux up to 220 L mxe213; 2.hrxe213; 1.

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