Affiliations 

  • 1 Department of Chemical Technology and Environment, University of Technology and Education, The University of Da Nang, Da Nang City, Viet Nam; Department of Chemical Engineering/Graduate School of Biochemical Engineering, Ming Chi University of Technology, New Taipei City 243303, Taiwan; Department of Chemical Engineering, National Taiwan University of Science and Technology, Taipei City, 106335, Taiwan
  • 2 Department of Applied Chemistry, Chaoyang University of Technology, Taichung 413310, Taiwan
  • 3 Department of Chemical and Environmental Engineering, Faculty of Engineering, University of Nottingham Malaysia Campus, Jalan Broga, Semenyih 43500, Selangor, Malaysia
  • 4 Department of Chemical Engineering, National Taiwan University of Science and Technology, Taipei City, 106335, Taiwan. Electronic address: stsai@mail.ntust.edu.tw
  • 5 Department of Chemical Engineering/Graduate School of Biochemical Engineering, Ming Chi University of Technology, New Taipei City 243303, Taiwan. Electronic address: ykchang@mail.mcut.edu.tw
Int J Biol Macromol, 2020 Dec 15;165(Pt A):1410-1421.
PMID: 33045299 DOI: 10.1016/j.ijbiomac.2020.10.034

Abstract

Electrospinning technology was applied for the preparation of polyacrylonitrile (PAN) nanofiber membrane in this work. After hot pressing, alkaline hydrolysis and neutralization treatment, a weak acid cation exchange membrane (P-COOH) was prepared. By the covalent coupling reaction between the acidic membrane and aminomethane sulfonic acid (AMSA), a strong acidic nanofiber membrane (P-SO3H) was obtained. The surface morphology, chemical structure, and thermal stability of the prepared ion exchange membranes were analyzed via SEM, FTIR and TGA. Analytical results showed that the membranes were prepared successfully and thermally stable. The ion exchange membrane (IEX) was conducted with the newly designed membrane reactor, and different operating conditions affecting the adsorption efficiency of Toluidine Blue dye (TBO) were investigated by dynamic flow process. The results showed that dynamic binding capacity (DBC) of weak and strong IEX membranes for TBO dye was ~170 mg/g in a dynamic flow process. Simultaneously, the ion exchange membranes were also used for purifying lysozyme from chicken egg white (CEW). Results illustrated that the recovery yield and purification factor of lysozyme were 93.43% and 29.23 times (P-COOH); 90.72% and 36.22 times (P-SO3H), respectively. It was revealed that two type ion exchange membranes were very suitable as an adsorber for use in dye waste treatment and lysozyme purification process. P-SO3H strong ion-exchange membrane was more effective either removal of TBO dye or purification of lysozyme. The ion exchange membranes not only effectively purified lysozyme from CEW solution, but also effectively removed dye from wastewater.

* Title and MeSH Headings from MEDLINE®/PubMed®, a database of the U.S. National Library of Medicine.