▎ 摘　　要

Hydrogen (H-2) is a clean energy carrier and its cost-effective separation is important for future H-2 energy deployment. Currently, H-2 is mainly produced from high temperature methane steam reforming reactions and thus the availability of membrane separation technology that can work at elevated temperatures can reduce the production cost. In this work, a cross-linked polybenzimidazole (PBI)-triglycidylisocyanurate (TGIC) and sulfonated graphene (SG) composite membrane was developed using a mixed proton-electron conducting concept. In such a membrane, protons diffuse by hopping along the cross-linking sites between the sulfonic groups of SG and the pyrrole rings of PBI, while electrons are transported via highly electron conductive SG. Following the addition of SG, the membrane became more compact, given the reduced interlayer spacing and swelling ratio. The thermal stability and oxidative resistance are comparable to those of other PBI-based membranes. For H-2/CO2 separation, H-2 can permeate through a 132 mu m-thick membrane with 99.99% selectivity and a high flux of up to 0.22 mL min(-1) cm(-2) at 300 degrees C. The stable operation at 280 degrees C for 160 hours proves the membrane robustness at such an elevated temperature. Compared to the previously reported mixed conducting ceramic membranes exhibiting equivalent H-2 fluxes requiring operation temperatures above 800 degrees C, the polymer and graphene composite membrane presented herein can reduce the operation temperature by 500 degrees C. This is an important requirement to ensure a more practical integration of membrane technology into industrial processes.