Fabrication of PSf/P84-blended membranes with low P84 content: Characteristics and gas separation performance

Victor Kayadoe , Nurul Widiastuti , Triyanda Gunawan , Wan Norhayati Wan Salleh , Hamzah Fansuri , Taufik Qodar Romadiansyah , Agus Wedi Pratama
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Abstract

The demand for efficient and sustainable gas separation technologies is ever-increasing in various industries, including petrochemicals, natural gas processing, and carbon capture. Polymer-based membranes offer a promising solution due to their potential for high selectivity and energy efficiency. However, achieving optimal gas separation performance often requires overcoming the limitations of individual polymers through modifications such as polymer blending. In this study, PSf/P84 blended membranes with low P84 content were fabricated using the phase separation technique with a mixture of N-methyl-2-pyrrolidone and tetrahydrofuran as solvents. The effect of varying the mass ratio of PSf to P84 on membrane characteristics and gas separation performance was investigated. Characterization techniques included FTIR, XRD, SEM, TGA, Water Contact Angle (WCA) measurement, and mechanical property testing. Gas permeation tests were conducted with single gases at room temperature and 1 bar pressure. The results revealed that the addition of P84 increased membrane thickness, Young's modulus, and thermal stability, while decreasing d-spacing, dense layer thickness, hydrophilicity, tensile strength, and elongation. The Findex values, indicating the competence of the blended membranes compared to the ideal quality, demonstrated the positive impact of P84 addition on gas separation performance compared to pure PSf membranes. The optimal gas separation selectivity was achieved with the PSf/P84 1:0.025 blended membrane for H2/CH4 (11.28, 58 % increase), H2/CO2 (6.25, 193 % increase), and H2/N2 (5.25, 35 % increase). The highest N2/CH4 selectivity (6.29, 253 % increase) was observed with the 1:0.10 composition. Regarding commercially relevant separations based on the 2008 Robeson curve, the PSf/P84 1:0.20 blend showed promise for H2/CO2 separation, while the 1:0.05 and 1:0.10 blends were suitable for N2/CH4 separation.

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制造低 P84 含量的 PSf/P84 混合膜:特性和气体分离性能
石油化工、天然气处理和碳捕集等各行各业对高效和可持续气体分离技术的需求与日俱增。聚合物基膜具有高选择性和高能效的潜力,因此是一种很有前景的解决方案。然而,要达到最佳的气体分离性能,往往需要通过聚合物混合等改性措施来克服单个聚合物的局限性。在本研究中,使用相分离技术,以 N-甲基-2-吡咯烷酮和四氢呋喃的混合物为溶剂,制造出了 P84 含量较低的 PSf/P84 混合膜。研究了改变 PSf 与 P84 的质量比对膜特性和气体分离性能的影响。表征技术包括傅立叶变换红外光谱(FTIR)、X 射线衍射(XRD)、扫描电镜(SEM)、热重分析(TGA)、水接触角(WCA)测量和机械性能测试。在室温和 1 巴压力下对单一气体进行了气体渗透测试。结果表明,添加 P84 增加了膜厚度、杨氏模量和热稳定性,同时降低了 d 间距、致密层厚度、亲水性、拉伸强度和伸长率。Findex 值表明混合膜与理想质量相比的能力,与纯 PSf 膜相比,添加 P84 对气体分离性能有积极影响。PSf/P84 1:0.025 混合膜对 H2/CH4(11.28,增加 58%)、H2/CO2(6.25,增加 193%)和 H2/N2(5.25,增加 35%)的气体分离选择性达到最佳。1:0.10 成分的 N2/CH4 选择性最高(6.29,增加 253%)。关于基于 2008 年罗伯逊曲线的商业相关分离,PSf/P84 1:0.20 混合物有望实现 H2/CO2 分离,而 1:0.05 和 1:0.10 混合物则适合实现 N2/CH4 分离。
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来源期刊
Case Studies in Chemical and Environmental Engineering
Case Studies in Chemical and Environmental Engineering Engineering-Engineering (miscellaneous)
CiteScore
9.20
自引率
0.00%
发文量
103
审稿时长
40 days
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