Limitation in Fabricating PSf/ZIF-8 Hollow Fiber Membrane for CO2/CH4 Separation

Q1 Earth and Planetary Sciences Indonesian Journal of Science and Technology Pub Date : 2018-08-30 DOI:10.17509/IJOST.V3I2.12757
N. Nordin, A. Ismail, Surya Murali Racha, N. B. Cheer, M. Bilad, Z. Putra, M. D. H. Wirzal
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引用次数: 3

Abstract

Hollow fiber membrane configuration is way forward in membrane development since it possesses higher packing density and effective surface area per unit module compared to other configuration. Since majority of mixed matrix membrane (MMM) for gas separation reported focuses on flat sheet membrane development, this report aims to address the challenges faced in fabricating hollow fiber MMM. In this study, hollow fiber formulation is fabricated and their MMM using different types of fillers (virgin and modified ZIF-8) are prepared and used as a dispersed phase. The neat hollow fiber membrane shows good results with CO2 permeance of 104.39 GPU and CO2/CH4 selectivity of 29.28, in comparison with reported literature. Upon filler incorporation, the resulted MMMs appear to be diminished in both CO2 permeance and CO2/CH4 selectivity. While using modified ZIF-8, lesser deterioration was shown compared to pure ZIF-8, this phenomenon is likely to occur due to the changes in solution stability which causes notable changes in membrane morphology and performances.
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制备用于CO2/CH4分离的PSf/ZIF-8中空纤维膜的局限性
中空纤维膜结构是膜发展的方向,因为与其他结构相比,它具有更高的填料密度和单位模块的有效表面积。由于大多数用于气体分离的混合基质膜(MMM)都集中在平板膜的发展上,本报告旨在解决制造中空纤维MMM所面临的挑战。在本研究中,制备了中空纤维配方,并使用不同类型的填料(原生和改性ZIF-8)制备了它们的MMM,并作为分散相使用。与文献报道的结果相比,整齐中空纤维膜的CO2透过率为104.39 GPU, CO2/CH4选择性为29.28。在填料掺入后,所得到的MMMs在CO2渗透率和CO2/CH4选择性方面都有所降低。当使用改性ZIF-8时,与纯ZIF-8相比,劣化程度较小,这种现象可能是由于溶液稳定性的变化导致膜的形态和性能发生显著变化。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Indonesian Journal of Science and Technology
Indonesian Journal of Science and Technology Engineering-Engineering (all)
CiteScore
11.20
自引率
0.00%
发文量
10
审稿时长
16 weeks
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