Zhan Xia, Gao Kaixiang, Jia Yucheng, Deng Wen, Liu Ning, Guo Xuebin, Li Hehe, Li Jiding
China Food Flavor and Nutrition Health Innovation Center, Beijing Technology and Business University, Beijing 100048, China.
Key Laboratory of Cleaner Production and Integrated Resource Utilization of China National Light Industry, Beijing Technology and Business University, Beijing 100048, China.
Membranes (Basel). 2023 May 15;13(5):515. doi: 10.3390/membranes13050515.
Constructing efficient and continuous transport pathways in membranes is a promising and challenging way to achieve the desired performance in the pervaporation process. The incorporation of various metal-organic frameworks (MOFs) into polymer membranes provided selective and fast transport channels and enhanced the separation performance of polymeric membranes. Particle size and surface properties are strongly related to the random distribution and possible agglomeration of MOFs particles, which may lead to poor connectivity between adjacent MOFs-based nanoparticles and result in low-efficiency molecular transport in the membrane. In this work, ZIF-8 particles with different particle sizes were physically filled into PEG to fabricate mixed matrix membranes (MMMs) for desulfurization via pervaporation. The micro-structures and physi-/chemical properties of different ZIF-8 particles, along with their corresponding MMMs, were systematically characterized by SEM, FT-IR, XRD, BET, etc. It was found that ZIF-8 with different particle sizes showed similar crystalline structures and surface areas, while larger ZIF-8 particles possessed more micro-pores and fewer meso-/macro-pores than did the smaller particles. ZIF-8 showed preferential adsorption for thiophene rather than n-heptane molecules, and the diffusion coefficient of thiophene was larger than that of thiophene in ZIF-8, based on molecular simulation. PEG MMMs with larger ZIF-8 particles showed a higher sulfur enrichment factor, but a lower permeation flux than that found with smaller particles. This might be ascribed to the fact that larger ZIF-8 particles provided more and longer selective transport channels in one single particle. Moreover, the number of ZIF-8-L particles in MMMs was smaller than the number of smaller ones with the same particle loading, which might weaken the connectivity between adjacent ZIF-8-L nanoparticles and result in low-efficiency molecular transport in the membrane. Moreover, the surface area available for mass transport was smaller for MMMs with ZIF-8-L particles due to the smaller specific surface area of the ZIF-8-L particles, which might also result in lower permeability in ZIF-8-L/PEG MMMs. The ZIF-8-L/PEG MMMs exhibited enhanced pervaporation performance, with a sulfur enrichment factor of 22.5 and a permeation flux of 183.2 g/(m·h), increasing by 57% and 389% compared with the results for pure PEG membrane, respectively. The effects of ZIF-8 loading, feed temperature, and concentration on desulfurization performance were also studied. This work might provide some new insights into the effect of particle size on desulfurization performance and the transport mechanism in MMMs.
在膜中构建高效且连续的传输通道是在渗透汽化过程中实现理想性能的一种有前景且具有挑战性的方法。将各种金属有机框架(MOF)掺入聚合物膜中可提供选择性且快速的传输通道,并增强聚合物膜的分离性能。粒径和表面性质与MOF颗粒的随机分布及可能的团聚密切相关,这可能导致相邻的基于MOF的纳米颗粒之间连通性差,进而导致膜中分子传输效率低下。在本工作中,将不同粒径的ZIF-8颗粒物理填充到聚乙二醇(PEG)中,以制备用于渗透汽化脱硫的混合基质膜(MMM)。通过扫描电子显微镜(SEM)、傅里叶变换红外光谱(FT-IR)、X射线衍射(XRD)、比表面积分析仪(BET)等系统地表征了不同ZIF-8颗粒及其相应MMM的微观结构和物理/化学性质。结果发现,不同粒径的ZIF-8具有相似的晶体结构和表面积,而较大粒径的ZIF-8颗粒比较小粒径的颗粒具有更多的微孔和更少的介孔/大孔。基于分子模拟,ZIF-8对噻吩而非正庚烷分子表现出优先吸附,且噻吩在ZIF-8中的扩散系数大于在PEG中的扩散系数。含有较大粒径ZIF-8颗粒的PEG MMM表现出更高的硫富集因子,但渗透通量低于含有较小粒径颗粒的MMM。这可能归因于较大粒径的ZIF-8颗粒在单个颗粒中提供了更多且更长的选择性传输通道。此外,MMM中较大粒径ZIF-8颗粒(ZIF-8-L)的数量少于相同颗粒负载量下较小粒径颗粒的数量,这可能会削弱相邻ZIF-8-L纳米颗粒之间的连通性,导致膜中分子传输效率低下。此外,由于ZIF-8-L颗粒的比表面积较小,含有ZIF-8-L颗粒的MMM中可用于传质的表面积较小,这也可能导致ZIF-8-L/PEG MMM的渗透率较低。ZIF-8-L/PEG MMM表现出增强的渗透汽化性能,硫富集因子为22.5,渗透通量为183.2 g/(m²·h),分别比纯PEG膜的结果提高了57%和389%。还研究了ZIF-8负载量、进料温度和浓度对脱硫性能的影响。这项工作可能为粒径对脱硫性能的影响以及MMM中的传输机制提供一些新的见解。