Mixed matrix membranes by incorporating methyl-functionalized covalent organic framework into PDMS for high flux ethanol/water separation

Zhibin Ma , Peitong Lian , Jie Li , Yanxiong Ren , Yonghui Shi , Hanze Ma , Yuhang Guo , Qianfeng Pan , Sheng Yuan , Yutong Wang , Heyang Liu , Lixuan Liu , Yuao Dong , Yanlei Su , Jing Zhao , Quanfu An , Guangwei He , Zhongyi Jiang
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Abstract

Polydimethylsiloxane (PDMS) membranes are commonly utilized for ethanol-water separation. However, the separation performance is insufficient owing to the inherent trade-off between permeability and selectivity. In this study, we reported the incorporation of methyl-functionalized covalent organic framework (COF, TpBD-CH3) into PDMS membranes to prepare mixed matrix membranes (MMMs), greatly increasing ethanol flux by 2.7 times. Under testing conditions of 60 ​°C with a feed solution containing 5 ​wt% ethanol in water, the permeation flux of the membrane incorporating 0.1 ​wt% TpBD-CH3 significantly increased from 1738 ​g/(m2·h) to 4648 ​g/(m2·h) compared to the original PDMS membrane, while the separation factor improved from 7.32 to 8.40. The improved separation performance is attributed to that the incorporation of the COF enhances the hydrophobicity as well as the free volume cavities of the membranes as evidenced by the significantly increased gas permeability (CO2 permeability reaches 26,720 Barrer). This study indicates the potential of COF in the development of PDMS-based MMMs for the separation of organic aqueous solutions or gas components.
在PDMS中加入甲基功能化共价有机骨架的混合基质膜用于高通量乙醇/水分离
聚二甲基硅氧烷(PDMS)膜通常用于乙醇-水分离。然而,由于渗透性和选择性之间的内在权衡,分离性能不足。在本研究中,我们报道了将甲基功能化的共价有机骨架(COF, TpBD-CH3)掺入PDMS膜中制备混合基质膜(MMMs),使乙醇通量大大提高了2.7倍。在60°C、5 wt%乙醇水溶液条件下,与原PDMS膜相比,添加0.1 wt% TpBD-CH3的膜的渗透通量从1738 g/(m2·h)显著提高到4648 g/(m2·h),分离系数从7.32提高到8.40。分离性能的提高是由于COF的掺入增强了膜的疏水性和自由腔体,其气体渗透性显著提高(CO2渗透性达到26,720 Barrer)。这项研究表明,COF在开发基于pdms的有机水溶液或气体组分分离的MMMs方面具有潜力。
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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CiteScore
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