TY - JOUR
T1 - Quaternized poly(2,6-dimethyl-1,4-phenylene oxide)s with zwitterion groups as diffusion dialysis membranes for acid recovery
AU - Zhang, Xiaojuan
AU - Zhang, Fan
AU - Liu, Minghui
AU - Wang, Yiguang
AU - Xu, Zhaozan
AU - Li, Nanwen
N1 - Publisher Copyright:
© 2020 Elsevier B.V.
PY - 2020/11/1
Y1 - 2020/11/1
N2 - For the purpose of simultaneously improving H+ dialysis coefficient and selectivity between proton and metal ions in acid diffusion dialysis (DD), a series of quaternized poly(2,6-dimethyl-1,4-phenylene oxide)s (PPO) anion exchange membranes (AEMs) containing zwitterion groups were designed and synthesized via Cu(I)-catalyzed “click chemistry”. The ion exchange capacity (IEC) and degree of functional zwitterion groups were controlled readily by adjusting the amount of the reagent due to the quantitative click reaction. The electrostatic effects of zwitterionic groups provided AEMs with proper water uptake (<65 wt%), dimensional stabilities (<19%) even under elevated temperatures (60 °C) as well as robust mechanical properties. Taking the simulated iron polishing waste solution (HCl, 1.0 mol/L; FeCl2, 0.2 mol/L) for research, the diffusion dialysis performance of membranes was investigated. As expected, the zwitterionic functionalization of the membrane enhanced the H+ dialysis coefficient and selectivity simultaneously. The zwitterion groups-based membranes with a thickness of 30–40 μm showed high acid dialysis coefficient up to 0.037 m/h and selectivity up to 32.7 at 30 °C. Therefore, the introduction of zwitterionic groups into anion exchange membrane is an effective approach for the simultaneous H+ dialysis coefficient and selectivity improvement of the membrane in DD for acid recovery.
AB - For the purpose of simultaneously improving H+ dialysis coefficient and selectivity between proton and metal ions in acid diffusion dialysis (DD), a series of quaternized poly(2,6-dimethyl-1,4-phenylene oxide)s (PPO) anion exchange membranes (AEMs) containing zwitterion groups were designed and synthesized via Cu(I)-catalyzed “click chemistry”. The ion exchange capacity (IEC) and degree of functional zwitterion groups were controlled readily by adjusting the amount of the reagent due to the quantitative click reaction. The electrostatic effects of zwitterionic groups provided AEMs with proper water uptake (<65 wt%), dimensional stabilities (<19%) even under elevated temperatures (60 °C) as well as robust mechanical properties. Taking the simulated iron polishing waste solution (HCl, 1.0 mol/L; FeCl2, 0.2 mol/L) for research, the diffusion dialysis performance of membranes was investigated. As expected, the zwitterionic functionalization of the membrane enhanced the H+ dialysis coefficient and selectivity simultaneously. The zwitterion groups-based membranes with a thickness of 30–40 μm showed high acid dialysis coefficient up to 0.037 m/h and selectivity up to 32.7 at 30 °C. Therefore, the introduction of zwitterionic groups into anion exchange membrane is an effective approach for the simultaneous H+ dialysis coefficient and selectivity improvement of the membrane in DD for acid recovery.
KW - Anion exchange membrane
KW - Click chemistry
KW - Diffusion dialysis
KW - Electrostatic interaction
KW - Zwitterion group
UR - http://www.scopus.com/inward/record.url?scp=85087044743&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2020.117267
DO - 10.1016/j.seppur.2020.117267
M3 - Article
AN - SCOPUS:85087044743
SN - 1383-5866
VL - 250
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 117267
ER -