Abstract
The membrane-based separation of propylene/propane represents a promising breakthrough, with the potential to reshape this energy-intensive chemical process. Zeolitic imidazolate framework-8 (ZIF-8) membranes stand out among the various material candidates due to their superior performance. However, advancing ZIF-8 membranes from laboratory-scale demonstrations to industrial deployment requires breakthroughs in scalable, defect-free preparation, challenges that conventional methods have yet to overcome. Here we present a micro-space transformation process (MSTP) that enables controlled nucleation and crystallization by decoupling the direct collision between zinc ions and ligands. This approach allows the sealed inner cavities of tubular supports to serve as reaction spaces to scalably fabricate heterostructured ZIF-8 membranes with an industrially relevant area of 200 cm2. We demonstrate the batch preparation of 234 membranes (totaling >4.6 m2), which were assembled into membrane modules with attractive performance and long-term stability toward industrial feed gases. We also take a critical step toward industrial implementation by developing a side-stream separation unit and demonstrating membrane integration applications, thereby establishing an energy-efficient pathway for practical membrane-based olefin purification.

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Acknowledgements
This work was supported by the National Natural Science Foundation of China (U22A20414 to W.X., 22408158 to H.L.), the National Key Research and Development Program of China (2021YFB3802200 to Y.P.) and the Natural Science Foundation of Jiangsu Province (BK20240558 to H.L.), the State Key Laboratory of Materials-Oriented Chemical Engineering (SKL-MCE-24A07 to Y.P.) and the Jiangsu Provincial High-Level Talent Training Program (‘333 Project’ to Y.P.).
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Y.P. and H.L. conceived the idea. H.L., J.H. and Q.W. designed the experiments, analyzed the data and wrote the paper. Q.W. and E.S. synthesized and characterized the membranes. H.L. and Y.G. conducted the density functional theory simulations and computational fluid dynamics simulations. H.L. conducted and analyzed the economic evaluation of membrane and distillation coupling process. H.L., J.H., Q.W., E.S., Y.G., Y.P. and W.X. discussed the results and commented on the paper.
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Nature Chemical Engineering thanks Hae-Kwon Jeong, Jerry Y.S. Lin and the other, anonymous, reviewer(s) for their contribution to the peer review of this work.
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Extended data
Extended Data Fig. 1 Synthesis schematic of HZIF-8 membrane.
Schematic of a HZIF-8 membrane fabricated by the micro-space transformation process (MSTP).
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Supplementary materials and methods, Figs. 1–54, Tables 1–17 and references.
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Atomic coordinates of the optimized computational models.
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Statistical source data.
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Experimental datasets supporting proposed synthesis mechanism, including CFD simulations, intermediate layer characterization, and reaction parameter records.
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Raw separation performance data, including permeance and selectivity measurements, pressure, temperature, and flow rate records for propylene/propane separation tests.
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Experimental datasets demonstrating scalability, including batch fabrication, uniformity assessments, and module performance records.
Source Data Fig. 5 (download XLSX )
Raw operational data from industrial side-stream separation tests, including feed composition, permeate and retentate composition, flow rates, pressure, temperature, and long-term stability measurements.
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Lian, H., Hua, J., Wang, Q. et al. Scalable large-area ZIF-8 membranes for industrial propylene/propane separations. Nat Chem Eng (2026). https://doi.org/10.1038/s44286-026-00373-4
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DOI: https://doi.org/10.1038/s44286-026-00373-4


