Abstract

To reduce the environmental impact of acids present in various industrial wastes, improved and robust anion exchange membranes (AEMs) are highly desired. Moreover, they should exhibit high retention of salts, fast acid permeation and they should be able to operate with low energy input. In this work, AEMs are prepared using a facile solution-casting from brominated poly-(2,6-dimethyl-1,4-phenylene oxide) (BPPO) and increasing amounts of 2-phenylimidazole (PI). Neither quaternary ammonium salts, nor ionic liquids and silica-containing compounds are involved in the synthesis. The prepared membranes showed an ion exchange capacity of 1.1–1.8 mmol/g, a water uptake of 22%–47%, a linear expansion ratio of 1%–6% and a tensile strength of 0.83–10.20 MPa. These membranes have potential for recovering waste acid via diffusion dialysis, as the acid dialysis coefficient (UH) at room temperature for HCl is in the range of 0.006–0.018 m/h while the separation factor (S) is in the range of 16–28, which are higher than commercial DF-120B membranes (UH = 0.004 m/h, S = 24).

Highlights

  • Ion exchange membranes can be suitable for diffusion dialysis (DD) processes [1,2,3]

  • The successful synthesis of BPPO-based anion exchange membranes (AEMs) was confirmed by Fourier Transform Infrared Spectrometry (FTIR) (Figure 2)

  • 1450 cm successful synthesis of BPPO-based AEMs was confirmed by FTIR (Figure 2)

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Summary

Introduction

Ion exchange membranes can be suitable for diffusion dialysis (DD) processes [1,2,3]. A series of AEMs are synthesized from commercial BPPO by increasing the amounts of phenylimidazole (PI, pKa = 6.5) These membranes show higher acid stability due to the non-aromatic character of PI, which may be beneficial for electrochemical applications. The prepared membranes were evaluated using FTIR (Fourier Transform Infrared) spectroscopy, thermal stability (TGA), ion exchange capacity (IEC), water uptake (WU), the linear expansion ratio (LER), morphology (SEM), and chemical and mechanical stability. They were tested for acid recovery via DD in a feed mixture containing HCl and FeCl2

Materials
Membrane Preparation
Functional Groups and Thermal Stability
Morphology
Chemical and Mechanical Stability
Functional Groups
Functional
Thermal
Figure
TGA of BPPO-based
Chemical and Mechanical
The TS values of the fabricated
Dialysis coefficient
Conclusions

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