Membrane achieves 330 separation factor using alcohol-selective permeation in azeotropic mixtures, highlighting energy efficiency.
The energy-efficient separation of azeotropic organic mixtures remains a critical challenge in chemical manufacturing. Conventional thermal-driven processes like distillation and pervaporation face fundamental thermodynamic constraints, requiring energy-intensive phase transitions. We present a pressure-driven membrane solution using a spirocyclic poly(vinylene ether ketone) membrane with enhanced microporosity that achieves alcohol-selective permeation from alcohol-hydrocarbon azeotropes. The membrane demonstrates separation factors of 330 for ethanol/cyclohexane and 74 for ethanol/heptane systems, while reducing energy consumption by 2-3 orders of magnitude compared to conventional methods. Through multiscale characterization and molecular dynamics simulations, we elucidate the dual mechanism governing separation performance: differential surface adsorption affinity and restricted hydrocarbon diffusion within micropores of membrane. Here, we show a molecular sieving strategy bypasses traditional volatility-based separation paradigms, offering an approach for azeotrope fractionation with transformative potential for sustainable chemical processing.
No takes yet. Share an insight, caveat, or question.
Li et al. (2025) studied this question.
Synapse has enriched 5 closely related papers on similar clinical questions. Consider them for comparative context: