Optimizing hierarchical membrane/catalyst systems for oxidative coupling of methane using additive manufacturing

The advantage of a membrane/catalyst system in the oxidative coupling of methane compared with conventional reactive systems is that by introducing oxygen into the catalytic sites through a membrane, the parasitic gas-phase reactions of O 2 (g)—responsible for lowering product selectivity—can be avoided. The design and fabrication of membrane/catalyst systems has, however, been hampered by low volumetric chemical conversion rates, high capital cost and difficulties in co-designing membrane and catalyst properties to optimize the performance. Here we solve these issues by developing a dual-layer additive manufacturing process, based on phase inversion, to design, fabricate and optimize a hollow-fibre membrane/catalyst system for the oxidative coupling of methane. We demonstrate the approach through a case study using BaCe 0.8 Gd 0.2 O 3– δ as the basis of both catalyst and separation layers. We show that by using the manufacturing approach, we can co-design the membrane thickness and catalyst surface area so that the flux of oxygen transport through the membrane and methane activation rates in the catalyst layer match each other. We demonstrate that this ‘rate matching’ is critical for maximizing the performance, with the membrane/catalyst system substantially overperforming conventional reactor designs under identical conditions. Membrane/catalyst systems in the oxidative coupling of methane are promising for their high product selectivity but suffer from low volumetric chemical conversion rates, high capital cost and optimizing performance. A dual-layer additive manufacturing process, based on phase inversion, is now proposed to optimize a hollow-fibre membrane/catalyst system.