(654a) Investigating Solid Oxide Membrane Reactors for Direct Methane Conversion to Ethylene and Ethane By Oxidative Coupling | AIChE

(654a) Investigating Solid Oxide Membrane Reactors for Direct Methane Conversion to Ethylene and Ethane By Oxidative Coupling

Authors 

Igenegbai, V. O. - Presenter, University of Michigan
Meyer, R., Exxonmobil
Linic, S., University of Michigan-Ann Arbor
There is significant interest in developing direct natural gas upgrading routes as alternatives to current energy-intensive multi-step industrial methods of upgrading natural gas into value-added chemicals. These direct routes can potentially be applied in the upgrading of natural gas from small-scale sources; thereby mitigating their underutilization and flaring. The oxidative coupling of methane (OCM) is a promising route for direct upgrading of methane; the major component in natural gas. In OCM, methane reacts with oxygen at high temperatures, typically in the presence of a catalyst, to produce ethane and ethylene (C2), which are key feedstocks for the chemical industry. However, the yield of C2 products from OCM have remained below the techno-economic target due to formation of undesired CO and CO2, particularly in conventional packed bed reactors (PBRs). Studies have shown that by applying O2− conducting solid oxide membrane reactors that distribute the oxygen feed, the selectivity to C2 products can be significantly increased compared to a PBR.1 A rational design for these membrane reactors would include an O2- conducting OCM catalyst integrated with an O2- conducting membrane. In this study, we identify O2- conducting perovskite oxide materials that are active and selective for OCM.2,3 We test these materials for OCM in dense (non-porous) solid oxide membrane reactors modified with a porous O2- conducting layer to facilitate methane activation. From our reactor tests, we identify the most promising membrane system in terms of OCM performance and stability. We also present results from our efforts to optimize the membrane reactor performance by modifying the membrane features.

(1) Farrell, B. L.; Igenegbai, V. O.; Linic, S. ACS Catal. 2016, 6 (7), 4340–4346.

(2) Farrell, B. L.; Linic, S. Catal. Sci. Technol. 2016, 6, 4370–4376.

(3) Igenegbai, V. O.; Meyer, R. J.; Linic, S. Appl. Catal. B Environ. 2018, 230, 29–35.