Khan Muhammad Imran, Shanableh Abdallah, Khraisheh Majeda, AlMomani Fares
Research Institute of Sciences and Engineering (RISE), University of Sharjah, Sharjah 27272, United Arab Emirates.
Department of Chemical Engineering, College of Engineering, Qatar University, Doha P.O. Box 2713, Qatar.
Membranes (Basel). 2022 Jan 16;12(1):95. doi: 10.3390/membranes12010095.
Diffusion dialysis (DD) is an anion exchange membrane-based functional separation process used for acid recovery. TMA (trimethylamine) and BPPO (brominated poly(2,6-dimethyl-1,4-phenylene oxide) were utilized in this manuscript to formulate AEMs (anion exchange membranes) for DD (diffusion dialysis) using the phase-inversion technique. FTIR (Fourier transfer infrared) analysis, proton NMR spectroscopy, morphology, IEC (ion exchange capacity), (linear expansion ratio), (fixed group concentration), (water uptake/adsorption), water contact angle, chemical, and thermal stability, were all used to evaluate the prepared membranes. The effect of TMA content within the membrane matrix on acid recovery was also briefly discussed. It was reported that porous AEMs have a of 149.6% to 233.8%, IEC (ion exchange capacity) of 0.71 to 1.43 mmol/g, (fixed group concentration) that ranged from 0.0046 mol/L to 0.0056 mol/L, of 3.88% to 9.23%, and a water contact angle of 33.10° to 78.58°. The (acid dialysis coefficients) for designed porous membranes were found to be 0.0043 to 0.012 m/h, with separation factors () ranging from 13.14 to 32.87 at the temperature of 25 °C. These observations are comparable to those found in the DF-120B commercial membrane with of 0.004 m/h and S of 24.3 m/h at the same temperature (25 °C). This porous membranes proposed in this paper are excellent choices for acid recovery through the diffusion dialysis process.
扩散渗析(DD)是一种基于阴离子交换膜的功能分离过程,用于回收酸。本文采用三甲胺(TMA)和溴化聚(2,6-二甲基-1,4-苯撑醚)(BPPO),通过相转化技术制备用于扩散渗析的阴离子交换膜(AEMs)。利用傅里叶变换红外光谱(FTIR)分析、质子核磁共振光谱、形态学、离子交换容量(IEC)、线性膨胀率、固定基团浓度、吸水率/吸附率、水接触角、化学稳定性和热稳定性对制备的膜进行评估。还简要讨论了膜基质中TMA含量对酸回收的影响。据报道,多孔AEMs的线性膨胀率为149.6%至233.8%,离子交换容量为0.71至1.43 mmol/g,固定基团浓度范围为0.0046 mol/L至0.0056 mol/L,线性膨胀率为3.88%至9.23%,水接触角为33.10°至78.58°。在25℃温度下,设计的多孔膜的酸透析系数为0.0043至0.012 m/h,分离因子范围为13.14至32.87。这些观察结果与在相同温度(25℃)下DF-120B商业膜的观察结果相当,其酸透析系数为0.004 m/h,分离因子为24.3。本文提出的这种多孔膜是通过扩散渗析过程回收酸的极佳选择。