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Open AccessDOI: 10.1007/s40843-026-4306-5Original Research

Scale-up fabrication of MOF membranes toward olefin/paraffin separation

State Key Laboratory of Bioinspired Interfacial Materials Science, College of Chemistry, Chemical Engineering and Materials Science, Soochow University, Suzhou, 215123, P. R. China

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Scale-up fabrication of MOF membranes toward olefin/paraffin separation
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Published In
SCIENCE CHINA Materials
Published:January 15, 2026Edition:Vol. 32, Issue 1 • pp. 100-112Citation:Yang Liu et al. (2026), SCIENCE CHINA Materials
Impact Factor3.5 (Q2 Scopus)
Source Journal中国科学: 材料

Key Takeaways & Executive Findings

  • • • The MSTP enables fabrication of HZIF-8 membranes with a single-tube area of ~200 cm² and a total area exceeding 4.6 m², marking a >20-fold increase over typical lab-scale membranes (<10 cm²) and approaching industrially relevant dimensions. • • Extended stability tests show the HZIF-8 membranes maintain separation performance for 30 days under harsh conditions of 17 bar and 55 °C with a feed flow of 20 Nm³ d⁻¹, demonstrating operational robustness for continuous industrial use. • • The use of tubular ceramic supports with sealed inner lumens as confined reaction spaces allows precise control over membrane formation, addressing defect control and structural uniformity issues that plague scale-up. • • The heterostructured design of ZIF-8 membranes likely enhances mechanical stability and separation performance, as evidenced by successful operation at elevated pressures and temperatures, which is critical for petrochemical process integration.

Abstract

Olefin-paraffin separation is a critical and energy-intensive process in the petrochemical industry, with ethylene and propylene purification alone consuming 0.3% of global energy. Current distillation methods are energy-inefficient, and polymer membranes exhibit inadequate separation performance. Metal-organic frameworks (MOFs), particularly ZIF-8, offer precise molecular sieving due to their uniform pore aperture (~3.4 Å), which lies between the kinetic diameters of propylene and propane. Despite excellent lab-scale performance, ZIF-8 membranes face scalability challenges, with effective areas typically below 10 cm², far from the tens of thousands to millions of square meters required industrially. This paper reviews a recent breakthrough by Weihong Xing, Yichang Pan, and colleagues, who developed a micro-space transformation process (MSTP) for scalable fabrication of heterostructured ZIF-8 (HZIF-8) membranes. Using sealed inner lumens of tubular ceramic supports as confined reaction spaces, they achieved single-tube areas of ~200 cm² and total fabricated areas exceeding 4.6 m². The membranes demonstrated stable separation performance over 30 days at 17 bar and 55 °C with a feed flow of 20 Nm³ d⁻¹. This work represents a significant step toward industrial application, addressing critical bottlenecks in membrane area expansion, defect control, and mechanical stability.

1. Introduction

Olefin/paraffin separation, particularly propylene/propane, is a cornerstone of petrochemical processing, yet current distillation methods are energy-intensive, consuming 0.3% of global energy. Polymer membranes, while commercially available, suffer from insufficient selectivity and permeability, failing to meet industrial demands. Metal-organic frameworks (MOFs), especially ZIF-8, offer a promising alternative due to their uniform pore aperture (~3.4 Å) that precisely sieves propylene from propane. However, translating lab-scale successes to industrial reality has been stymied by the inability to fabricate large-area, defect-free membranes. Typical lab-scale ZIF-8 membranes have areas below 10 cm², whereas industrial applications require areas spanning tens of thousands to millions of square meters. Maintaining structural uniformity, controlling defects, and ensuring mechanical stability during scale-up remain formidable challenges.

The recent work by Xing, Pan, and colleagues introduces a micro-space transformation process (MSTP) that leverages the sealed inner lumen of tubular ceramic supports as confined reaction spaces. This innovative approach enables the fabrication of heterostructured ZIF-8 (HZIF-8) membranes with a single-tube area of ~200 cm² and a total area exceeding 4.6 m². More importantly, these membranes exhibit stable separation performance over 30 days at 17 bar and 55 °C, demonstrating their operational robustness. This breakthrough directly addresses the scalability bottleneck by providing a method that can be extended to industrial production, marking a pivotal transition from laboratory curiosity to practical application.

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Cite This Research Paper
Yang Liu, Zhenggong Wang, Jian Jin (2026). Scale-up fabrication of MOF membranes toward olefin/paraffin separation. SCIENCE CHINA Materials. https://doi.org/10.1007/s40843-026-4306-5
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Frequently Asked Questions

What are the key failure mechanisms that could compromise the long-term stability of HZIF-8 membranes under industrial operating conditions, and how does the MSTP mitigate them?

The extended stability test (30 days at 17 bar and 55 °C) indicates robust performance, but potential failure mechanisms include support-membrane delamination due to thermal expansion mismatch, defect formation from pressure cycling, and degradation of the ZIF-8 framework under humid or contaminant-laden feeds. The MSTP's confined reaction space promotes uniform nucleation and growth, reducing defects and enhancing adhesion to the tubular support. The heterostructured design may also provide mechanical reinforcement, as evidenced by stable operation at elevated pressures.

How does the separation performance of the HZIF-8 membranes compare to state-of-the-art polymer membranes in terms of selectivity and permeability, and what is the energy-saving potential?

While the text does not provide specific selectivity/permeability values, ZIF-8 membranes typically exhibit propylene/propane selectivity in the range of 30-100 with propylene permeance of 1-10 GPU, far surpassing polymer membranes (selectivity <10). The energy savings are substantial: membrane separation could reduce energy consumption by up to 80% compared to distillation. The MSTP's ability to produce large-area membranes with consistent performance is critical for realizing these savings at industrial scale.

What are the cost implications of scaling up the MSTP compared to conventional membrane fabrication methods, and what is the projected cost per square meter?

The MSTP uses tubular ceramic supports and mild synthesis conditions, which are cost-effective. While exact cost figures are not provided, the use of low-cost raw materials (zinc salts, 2-methylimidazole) and scalable tube-to-tube processing suggests a competitive cost trajectory. Compared to polymer membranes, MOF membranes are typically more expensive, but the enhanced performance and durability may justify the higher upfront cost. A detailed techno-economic analysis is needed to project cost per square meter, but the reported total area of 4.6 m² indicates feasibility for pilot-scale production.

How does the heterostructured design of the HZIF-8 membrane contribute to its mechanical stability and separation performance, and can this be generalized to other MOF systems?

The heterostructure likely involves a gradient or composite structure that enhances interfacial adhesion and reduces stress concentrations. This design may also create a more tortuous path for propane, improving selectivity. The MSTP's confined space allows precise control over the heterostructure formation. The principles can be extended to other MOFs with similar pore characteristics, but each system requires optimization of synthesis parameters. The success of HZIF-8 suggests that heterostructuring is a viable strategy for improving membrane robustness.

What are the next steps required to transition from the reported 4.6 m² total area to industrial-scale modules (e.g., >100 m²), and what challenges are anticipated?

Scaling to industrial modules requires further optimization of the tube-to-tube process to ensure uniformity across larger batches, development of module designs that accommodate multiple tubes, and validation under real-world feed conditions (e.g., presence of impurities). Challenges include maintaining defect-free membranes over larger areas, ensuring consistent performance across modules, and reducing fabrication time. The MSTP's demonstrated scalability to 4.6 m² provides a foundation, but engineering efforts are needed to integrate these membranes into commercial membrane modules.

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