(200d) Techno-Economic Analysis (TEA) of CO2 Electrolysis Systems for Ethylene Production
AIChE Annual Meeting
2019
2019 AIChE Annual Meeting
Sustainable Engineering Forum
Design, Analysis, and Optimization of Sustainable Energy Systems and Supply Chains III
Monday, November 11, 2019 - 4:45pm to 5:10pm
In this study, we evaluated the capital, operating cost and minimum ethylene product selling prices (MPSP) of a large-scale CO2 electrolysis and upgrading system to produce ethylene at 100 metric tonnes per day. Current economic analysis indicates that electricity is a major contributor to the ethylene break-even selling price, while the electrolyzer reactor requires a high capital investment. We also did uncertainty analysis to understand uncertainty impacts of the major performance metrics on the MPSP of ethylene. The preliminary analysis shows that faradaic efficiency, electrolyzer cost, electricity price and current density have significant impacts on the ethylene MPSP. We envision to provide targets for reactor performance metrics and important economic inputs in order to produce economic competitive ethylene from this CO2 electrochemical reduction system.
References:
[1] Eskew, B. US Petrochemicals: The growing importance of export markets EIA. (2018).
[2] Dinh, C., Burdyny, T., Kibria, G., Seifitokaldani, A., Gabardo, C. M., Arquer, F. P. G. de, Kiani, A., Edwards, J. P., Luna, P. De, Bushuyev, O. S., Zou, C., Quintero-Bermudez, R., Pang, Y., Sinton, D. & Sargent, E. H. CO 2 electroreduction to ethylene via hydroxide-mediated catalysis at an abrupt reaction interface. Science 360, 783â787 (2018). DOI:10.1126/science.aas9100