Catalyst Deactivation Simulation Through Carbon Deposition in Carbon Dioxide Reforming over Ni/CaO-Al2O3 Catalyst

Main Authors: Istadi, I., Anggoro, D. D., Amin, N.A.S., Ling, D.H.W
Format: Article PeerReviewed application/pdf
Terbitan: Dept. of Chemical Engineering, Diponegoro University , 2011
Subjects:
Online Access: http://eprints.undip.ac.id/30974/1/bcrecv6n2year2011p129-136.pdf
http://ejournal.undip.ac.id/index.php/bcrec/article/view/1213
http://eprints.undip.ac.id/30974/
Daftar Isi:
  • Major problem in CO2 reforming of methane (CORM) process is coke formation which is a carbonaceous residue that can physically cover active sites of a catalyst surface and leads to catalyst deactivation. A key to develop a more coke-resistant catalyst lies in a better understanding of the methane reforming mechanism at a molecular level. Therefore, this paper is aimed to simulate a micro-kinetic approach in order to calculate coking rate in CORM reaction. Rates of encapsulating and filamentous carbon formation are also included. The simulation results show that the studied catalyst has a high activity, and the rate of carbon formation is relatively low. This micro-kinetic modeling approach can be used as a tool to better understand the catalyst deactivation phenomena in reaction via carbon deposition. Copyright © 2011 BCREC UNDIP. All rights reserved. [How to Cite: I. Istadi, D.D. Anggoro, N.A.S. Amin, and D.H.W. Ling. (2011). Catalyst Deactivation Simulation Through Carbon Deposition in Carbon Dioxide Reforming over Ni/CaO-Al2O3 Catalyst. Bulletin of Chemical Reaction Engineering & Catalysis, 6 (2): 129-136]