ZIF-8 membrane-based cryo-stripping of trace impurities towards electronic grade C<sub>3</sub>H<sub>6</sub> production.

Yu, Kunpeng; Dong, Yachao; Ji, Taotao; Liu, Jiaxu; Gu, Shiya; Yin, Jianzhong; He, Xinyu; Zheng, Bin et al. · Nat Commun · 2026

basic_science · Level V

Where this comes from

Abstract

Electronic-grade (EG) C<sub>3</sub>H<sub>6</sub> represents an essential feedstock for semiconductor manufacturing, yet its purification remains energy-intensive due to the difficulty in removing trace C<sub>3</sub>H<sub>8</sub> impurities via conventional cryogenic distillation, which requires high pressure and low temperature operation conditions. In this study, we demonstrate efficient C<sub>3</sub>H<sub>6</sub>/C<sub>3</sub>H<sub>8</sub> separation under practical operation conditions using a ZIF-8 membrane prepared at near-freezing temperature. Gas permeation results show that the C<sub>3</sub>H<sub>6</sub>/C<sub>3</sub>H<sub>8</sub> separation factor (SF) increases as temperature decreases, reaching 607 at -40 °C and remaining independent of operating pressure. Under industry-relevant conditions (-20 °C, 3 bar), the membrane achieved a SF of 362 with C<sub>3</sub>H<sub>6</sub> flux of 135.3× 10<sup>-5 </sup>mol m<sup>-2</sup> s<sup>-1</sup>, enabling one-step reduction of C<sub>3</sub>H<sub>8</sub> from 2998 ppm to 8 ppm and complete removal of C<sub>4</sub>H<sub>10</sub> from polymer-grade C<sub>3</sub>H<sub>6</sub> feed. Adsorption-diffusion analysis reveals that enhanced separation at subfreezing temperature originates from increased diffusion selectivity caused by contraction and rigidification of ZIF-8 window. Process analysis further shows that integrating the membrane with distillation column can upgrade 99.5% C<sub>3</sub>H<sub>6</sub> to ~5 N purity while reducing operating cost by 56.57% (1.34 US$ kg<sup>-1</sup> EG C<sub>3</sub>H<sub>6</sub>).