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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2024, Vol. 18 Issue (1) : 3    https://doi.org/10.1007/s11783-024-1763-z
RESEARCH ARTICLE
Conductive and stable polyphenylene/CNT composite membrane for electrically enhanced membrane fouling mitigation
Huijuan Xie, Haiguang Zhang, Xu Wang, Gaoliang Wei, Shuo Chen, Xie Quan()
Key Laboratory of Industrial Ecology and Environmental Engineering (Ministry of Education), School of Environmental Science and Technology, Dalian University of Technology, Dalian 116024, China
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Abstract

● A conductive and stable polyphenylene/CNT membrane was fabricated.

● The conductivity of the membrane was 3.4 times higher than that of the CNT membrane.

● Structural stability of the membrane is superior to that of the CNT membrane.

● Electro-assistance can effectively enhance membrane fouling mitigation.

Nanocarbon-based conductive membranes, especially carbon nanotube (CNT)-based membranes, have tremendous potential for wastewater treatment and water purification because of their excellent water permeability and selectivity, as well as their electrochemically enhanced performance (e.g., improved antifouling ability). However, it remains challenging to prepare CNT membranes with high structural stability and high electrical conductivity. In this study, a highly electroconductive and structurally stable polyphenylene/CNT (PP/CNT) composite membrane was prepared by electropolymerizing biphenyl on a CNT hollow fiber membrane. The PP/CNT membrane showed 3.4 and 5.0 times higher electrical conductivity than pure CNT and poly(vinyl alcohol)/CNT (PVA/CNT) membranes, respectively. The structural stability of the membrane was superior to that of the pure CNT membrane and comparable to that of the PVA/CNT membrane. The membrane fouling was significantly alleviated under an electrical assistance of −2.0 V, with a flux loss of only 11.7% after 5 h filtration of humic acid, which is significantly lower than those of PP/CNT membranes without electro-assistance (56.8%) and commercial polyvinylidene fluoride (PVDF) membranes (64.1%). Additionally, the rejection of negatively charged pollutants (humic acid and sodium alginate) was improved by the enhanced electrostatic repulsion. After four consecutive filtration-cleaning cycle tests, the flux recovery rate after backwashing reached 97.2%, which was much higher than those of electricity-free PP/CNT membranes (67.0%) and commercial PVDF membranes (61.1%). This study offers insights into the preparation of stable conductive membranes for membrane fouling control in potential water treatment applications.

Keywords Polyphenylene      CNTs      Membrane      Electro-assistance      Membrane fouling mitigation     
Corresponding Author(s): Xie Quan   
Issue Date: 09 August 2023
 Cite this article:   
Huijuan Xie,Haiguang Zhang,Xu Wang, et al. Conductive and stable polyphenylene/CNT composite membrane for electrically enhanced membrane fouling mitigation[J]. Front. Environ. Sci. Eng., 2024, 18(1): 3.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-024-1763-z
https://academic.hep.com.cn/fese/EN/Y2024/V18/I1/3
Fig.1  Scheme for the fabrication of PP/CNT membrane.
Fig.2  SEM images of the uncrosslinked CNT membrane of (a) surface, (b) magnified surface, and (c) cross section (inset: the low-magnification SEM image). SEM images of the crosslinked CNT membrane of (d) surface, (e) magnified surface, and (f) cross section (inset: the low-magnification SEM image).
Fig.3  FTIR spectrum (a) and XPS spectrum (b) of PP. XPS spectra (c) and Raman spectra (d) of the CNT and PP/CNT membranes.
Fig.4  Photographs of (a) before and (b) after ultrasound of 10 min (40 kHz, 120 W) of the CNT and PP/CNT membranes. Nano-scratch results of (c) the CNT and (d) the PP/CNT membranes. Both (c) and (d) have insets showing the SEM images of nano-scratch results. (e) Conductivities of the CNT, PPx/CNT and PVA/CNT membranes. (f) Water contact angles of the CNT and PPx/CNT membranes.
Fig.5  Average pore sizes (a) and pure water fluxes under operation pressure of 0.5 bar (b) of the CNT and PPx/CNT membranes. Average pore sizes (c) and pure water fluxes under operation pressure of 0.5 bar (d) of the PP/CNT membrane, three commercial membranes and PVA/CNT membrane.
Fig.6  Normalized fluxes (a) and HA removal efficiency (b) of the PP/CNT membranes at different cell voltages (operation pressure of 0.2 bar). Normalized fluxes (c) and SA removal efficiency (d) of the PP/CNT membranes at different cell voltages (operation pressure of 0.2 bar). (e) Schematic diagram of the antifouling mechanism of the PP/CNT conductive membrane under electro-assistance.
Fig.7  SEM images of membrane fouling of the PP/CNT membranes after HA filtration at the voltages of (a) −2.0 V, (b) −1.0 V, (c) 0 V, (d) +1.0 V, and (e) +2.0 V.
Fig.8  (a) Flux variations of the PP/CNT membrane, PP/CNT membrane with −2.0 V, and CM2 membrane when filtrating HA solution (operation pressure of 0.2 bar). (b) Flux recovery rates (FRR) of PP/CNT membrane, PP/CNT membrane with −2.0 V, and CM2 membrane after hydraulic cleaning.
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