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Blending ZIF-67 into PDMS Membranes to Promote the Separation Performance of Propylene/nitrogen Mixed Gas

Journal of physics. Conference series(2022)

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Abstract
The membrane-based gas separation is well-suited for the recovery of hydrocarbons from nitrogen-rich exhaust gases. However, the separation performance of the existing polymeric membranes was insufficient. In this study, zeolitic imidazolate framework-67 (ZIF-67) was synthesized and then incorporated into polydimethylsiloxane (PDMS) to prepare ZIF-67/PDMS mixed matrix membranes via the spin-coating method. The resultant ZIF-67 and membranes were characterized by Fourier transform infrared spectroscopy, X-ray diffraction, and scanning electron microscope. The C3H6/N2 (20:80 vol) mixed gas separation tests indicated that the ZIF-67/PDMS membranes achieved the higher C3H6/N2 separation factor but the lower C3H6 permeance in contrast with pure PDMS membrane. At the ZIF-67 loading of 5 wt%, the membrane displayed the optimal separation factor of 16.5 with comparable C3H6 permeance of 86.9 GPU. Besides, the relatively low operating temperature and pressure were advantageous to gaining good gas separation performance.
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要点】:本研究通过将ZIF-67融入PDMS膜,提高了丙烷/氮气混合气体的分离性能,其创新点在于通过制备ZIF-67/PDMS混合基质膜,提升了现有聚合物膜的分离效率。

方法】:采用旋涂法制备ZIF-67/PDMS混合基质膜,并通过傅里叶变换红外光谱、X射线衍射和扫描电子显微镜对ZIF-67和膜进行表征。

实验】:使用C3H6/N2(20:80体积比)混合气体分离实验测试,结果显示与纯PDMS膜相比,ZIF-67/PDMS膜实现了更高的C3H6/N2分离因子,但C3H6的渗透率较低。当ZIF-67负载量为5 wt%时,膜展现出最优的分离因子16.5和相似的C3H6渗透率86.9 GPU。此外,相对较低的操作温度和压力有利于获得良好的气体分离性能。