4.7 Article

Controllable synthesis of ZIF-8 interlocked membranes for propylene/propane separation

Journal

SEPARATION AND PURIFICATION TECHNOLOGY
Volume 300, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.seppur.2022.121811

Keywords

ZIF-8 membrane; Interlocked architecture; Ligand activation; Long-term durability; C3H6/C3H8 separation

Funding

  1. National Key R&D Program of China [2021YFB3802204]
  2. Natural Science Foundation of China [21921006, 22022807]
  3. Natural Science Foundation of Jiangsu Province [BK20200033]
  4. Priority Academic Program Development of Jiangsu Higher Education Institutions (PAPD)
  5. Six Talent Peaks Project
  6. Qing-Lan Engincering Project of Jiangsu Province

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ZIF-8 membrane has received extensive attention for propylene/propane separation. However, its durability and scalability are limited by poor adhesion with the support. This study successfully prepared interlocked ZIF-8 membranes with improved durability and efficient separation. The findings are significant for practical industrial gas separation.
ZIF-8 membrane has received extensive attention recently for propylene/propane (C3H6/C3H8) separation. However, the weak long-term durability and scalability/reproducibility of ZIF-8 membranes are limited by the poor adhesion between the membrane and the curved support. A successful preparation of high adhesion ZIF-8 membranes on the curved support remains a challenge. The ZIF-8 membrane with interlocked architecture was expected to exhibit more reliable durability due to the strengthened crystal boundaries. Herein, we synthesized uniform ZnO nanoparticles in the inner upper layer of the ceramic tube support by combining slip-casting and vacuum drying methods. The dense ZIF-8 interlocked membranes were further prepared by the ligand activation processing for efficient C C3H6/C3H8 separation. The interlocked ZIF-8 membrane exhibited reliable long-term durability over 54 h under different operation conditions. Furthermore, the C3H6 permeance and separation factor of the membrane reached 8 x 10(-9) mol h(-2) S-1Pa-1 and 130 at 25 degrees C and feed pressure of 1 bar, respectively, comparable to that of previously reported other supported ZIF-8 membranes. Therefore, the ZIF-8 interlocked membranes are promising for practical industrial gas separation.

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