Structural engineering on 6FDA-Durene based polyimide membranes for highly selective gas separation

Abstract

In this work, four diamine monomers, selected based-on steric hindrance and affinity with gas to be separated, were separately introduced into 6FDA-Durene to prepare co-polyimides. The influences of incorporating diamine monomer geometry on free volume elements (FFV, FAV, cavity size distribution, surface area and cavity connectivity) and gas transport properties (solubility and diffusion) of synthesized co-polyimide membranes were systematically investigated. The introduction of second amino monomer can increase gas selectivity, however leaded to lower gas permeability. Gas solubility and solubility selectivity of membrane remained almost stable with introduction of different amino monomer. While the gas diffusion changed remarkably, and the diffusion selectivity increased by about 170%. The FDDA membrane with crown ether structure displayed the highest gas selectivity (increased by 122%, 121%, 158%, 115% and 115% for H2/N2, H2/CH4, O2/N2, CO2/N2 and CO2/CH4, respectively, compared to 6FDA-Durene membrane), whose selectivity was relatively high among the PI-based membranes. This can be explained that the crown ether group granted the membrane with largest FAV ratio of specific gas pair, as well as the smallest pore size that would cause stronger size sieving effect. These results indicated that gas separation property of polyimide membranes can be effectively adjusted via tuning monomer structure, which is easily synthesized or has been commercialized, to realize the industrial application of membrane-based gas separation.