渗透
分子筛
微型多孔材料
膜
介孔材料
沸石
化学工程
选择性
材料科学
ZSM-5型
化学
吸附
有机化学
催化作用
复合材料
工程类
生物化学
作者
Sungwon Hong,Yanghwan Jeong,Hionsuck Baik,Nakwon Choi,Alex C.K. Yip,Jungkyu Choi
标识
DOI:10.1002/anie.202010957
摘要
Abstract MFI type zeolites with 10‐membered‐ring pores (ca. 0.55 nm) have the ability to separate p‐xylene (ca. 0.58 nm) from its bulkier isomers. Here, we introduced non‐zeolitic micropores (ca. 0.6–1.5 nm) and mesopores (ca. 2–7 nm) to a conventional microporous MFI type zeolite membrane, yielding an unprecedented hierarchical membrane structure. The uniform, embedded non‐zeolitic pores decreased defect formation considerably and facilitated molecular transport, resulting in high p‐xylene perm‐selectivity and molar flux. Specifically, compared to a conventional, crack network‐containing MFI membranes of similar thickness (ca. 1 μm), the mesoporous MFI membranes showed almost double p‐xylene permeance (ca. 1.6±0.4×10 −7 mol m −2 s −1 Pa −1 ) and a high p‐/o‐xylene separation factor (ca. 53.8±7.3 vs. 3.5±0.5 in the conventional MFI membrane) at 225 °C. The embedded non‐zeolitic pores allowed for decreasing the separation performance degradation, which was apparently related to coke formation.
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