制备用于 CO2/CH4 分离的自支撑沸石玻璃复合膜

Dudu Li, Mao Ye, Chao Ma, Ning Li, Zhenjie Gu, Z. Qiao
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引用次数: 0

摘要

由于金属有机框架玻璃的孔隙率较低,因此很难制备出具有高渗透性的膜。为了解决这个问题,我们利用沸石丰富的孔隙结构,制备了一系列不同 4A 沸石负载量的自支撑沸石玻璃复合膜。沸石玻璃复合膜中嵌入的 4A 沸石保留了配位键和化学结构。自支撑沸石玻璃复合膜表现出良好的界面相容性。更重要的是,4A 沸石的加入显著提高了纯 agZIF-62 膜的二氧化碳吸附能力。此外,气体分离性能测量结果表明,(agZIF-62)0.7(4A)0.3 膜对纯 CO2 的渗透率为 13,329 巴,对 CO2/CH4 的理想选择性为 31.7,超过了罗伯逊的上限。在变压试验和 48 小时长期连续试验中,(agZIF-62)0.7(4A)0.3 膜表现出良好的操作稳定性。这项研究为制备沸石玻璃复合膜提供了一种方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Preparation of a self‐supported zeolite glass composite membrane for CO2/CH4 separation

Preparation of a self‐supported zeolite glass composite membrane for CO2/CH4 separation
The low porosity of metal‐organic framework glass makes it difficult to prepare membranes with high permeability. To solve this problem, we fabricated a series of self‐supported zeolite glass composite membranes with different 4A zeolite loadings using the abundant pore structure of the zeolite. The 4A zeolite embedded in the zeolite glass composite membrane preserved the ligand bonds and chemical structure. The self‐supported zeolite glass composite membranes exhibited good interfacial compatibility. More importantly, the incorporation of the 4A zeolite significantly improved the CO2 adsorption capacity of the pure agZIF‐62 membranes. In addition, gas separation performance measurements showed that the (agZIF‐62)0.7(4A)0.3 membrane had a permeability of 13,329 Barrer for pure CO2 and an ideal selectivity of 31.7 for CO2/CH4, which exceeded Robeson's upper bound. The (agZIF‐62)0.7(4A)0.3 membrane exhibited good operational stability in the variable pressure test and 48 h long‐term continuous test. This study provides a method for preparing zeolite glass composite membranes.
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