(378h) Ethylene Production Using Oxidative Dehydrogenation with an M1 Catalyst: Effects of Membrane Separation & NOVEL Distillation Technologies | AIChE

Other Sites & Tools

Technical Groups

(378h) Ethylene Production Using Oxidative Dehydrogenation with an M1 Catalyst: Effects of Membrane Separation & NOVEL Distillation Technologies

Authors 

Roberts, K. - Presenter, University of South Carolina, 301 Main St Rm 2C02
Gaffney, A., Idaho National Laboratory
Hoorfar, M., University of British Columbia
Murnen, H., Compact Membrane Systems
Majumdar, S., Compact Membrane Systems
Alcheikhhamdona, Y., University of British Columbia
Chen, B., SINOPEC Dalian Research Institute of Petroleum and Petrochemicals
Aleman, A.
Cook, K. M., University of South Carolina
Daniel, A. B., University of South Carolina
Dodson, R. D. Jr., University of South Carolina
Donnelly, G. O., University of South Carolina
Previous work from this group has utilized a HYSYS simulator to predict the performance of an ethylene oxidative dehydrogenation (ODH) production facility using alternative diluents and separation technology not currently used in the standard industrial process. This work has investigated the development of membrane-based separation technology for the production of ethylene for the oxidative dehydrogenation (ODH) reaction of ethane using a HYSYS simulator with MEMCAL extension software in concert with kinetic reaction data for the M1 catalyst, flammability safety determinations and economic analysis. The application of polymer-membrane separation and non-cryogenic distillation alternatives, such as bottom-flash, heat-pump assisted and low-temperature distillation, were simulated and evaluated individually and in-tandem with membrane separation. The effects of ODH reaction kinetics, alternative diluents, process flammability issues, and economic analysis results will be discussed.

Topics 

Catalysis
Reactors
Separations

More Conference Links