Catalyst Deactivation and Reactor Fouling during Hydrogenation of Conjugated Cyclic Olefins over a Commercial Ni–Mo–S/γ-Al2O3 Catalyst

Author:

Alzaid Ali1,Wiens Jason2,Adjaye John2,Smith Kevin J.1ORCID

Affiliation:

1. Department of Chemical and Biological Engineering, University of British Columbia, 2360 East Mall, Vancouver, British Columbia V6T 1Z3, Canada

2. Edmonton Research Centre, Syncrude Canada, Limited, 9421 17th Avenue, Edmonton, Alberta T6N 1H4, Canada

Funder

Saudi Aramco

Natural Sciences and Engineering Research Council of Canada

Syncrude Canada Ltd.

Publisher

American Chemical Society (ACS)

Subject

Energy Engineering and Power Technology,Fuel Technology,General Chemical Engineering

Reference28 articles.

1. U.S. Energy Information Administration (EIA). Energy Information Administration Trend 1980–2010. International Energy Statistics: Energy Intensity | Country: Oman | Indicator: Energy Intensity—Total Primary Energy Consumption per Dollar of GDP (Btu per Year 2005 U.S. Dollar, 1980–2010. Data-Planet Statistical Ready Reference by Conquest Systems, Inc. Data Set-ID: 004-014-0412015; EIA: Washington, D.C., 2017.

2. Impact of molecular structure on the hydrogenation and oligomerization of diolefins over a Ni-Mo-S/γ-Al2O3 catalyst

3. Competitive hydrogenation in alkene–alkyne–diene systems with palladium and platinum catalysts1This work is a part of the Selective Catalytic Hydrogenation and Transfer Hydrogenation project GA CR 104/96/1445.1

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