TY - JOUR
T1 - Light olefin synthesis from CO2 hydrogenation over K-promoted Fe-Co bimetallic catalysts
AU - Satthawong, Ratchprapa
AU - Koizumi, Naoto
AU - Song, Chunshan
AU - Prasassarakich, Pattarapan
N1 - Funding Information:
This research was supported in part by the Pennsylvania State University through Penn State Institutes of Energy and the Environment. The authors also wish to thank the Thailand Research Fund and Graduate School of Chulalongkorn University through the Royal Golden Jubilee Ph.D. Program Scholarship to RS at PSU.
Publisher Copyright:
© 2015 Elsevier B.V. All rights reserved.
Copyright:
Copyright 2016 Elsevier B.V., All rights reserved.
PY - 2015/8/1
Y1 - 2015/8/1
N2 - This work investigates the effects of potassium addition on light olefin production from CO2 hydrogenation over the Al2O3-supported Fe-Co bimetallic catalysts. The addition of small amount of K on the Fe-Co catalyst significantly enhanced C2-C4 olefin formation. The C2-C4 olefins predominated among C2+ hydrocarbons at K/Fe atomic ratio of 1. Temperature-programmed desorption experiments demonstrated that K addition diminished the weakly adsorbed hydrogen but enhanced CO2 adsorption on the catalyst surface, which led to significantly enhanced production of light olefins. For C2-C4 olefin synthesis at 573 K and 1.0 MPa, the K-promoted Fe-Co/Al2O3 catalyst also showed better performance than the K-promoted Fe-Mn/Al2O3 catalyst which is known as a good catalyst for olefin production, under the present conditions employed. The pathway of olefin formation from CO2 hydrogenation was analyzed. Light olefins were formed via two-step reactions over K-promoted Fe-Co catalysts with the formation of CO or CO-like intermediate as the first step. Some of these olefins could be further hydrogenated to paraffins, depending on the type and concentration of chemisorbed hydrogen on the catalyst surface.
AB - This work investigates the effects of potassium addition on light olefin production from CO2 hydrogenation over the Al2O3-supported Fe-Co bimetallic catalysts. The addition of small amount of K on the Fe-Co catalyst significantly enhanced C2-C4 olefin formation. The C2-C4 olefins predominated among C2+ hydrocarbons at K/Fe atomic ratio of 1. Temperature-programmed desorption experiments demonstrated that K addition diminished the weakly adsorbed hydrogen but enhanced CO2 adsorption on the catalyst surface, which led to significantly enhanced production of light olefins. For C2-C4 olefin synthesis at 573 K and 1.0 MPa, the K-promoted Fe-Co/Al2O3 catalyst also showed better performance than the K-promoted Fe-Mn/Al2O3 catalyst which is known as a good catalyst for olefin production, under the present conditions employed. The pathway of olefin formation from CO2 hydrogenation was analyzed. Light olefins were formed via two-step reactions over K-promoted Fe-Co catalysts with the formation of CO or CO-like intermediate as the first step. Some of these olefins could be further hydrogenated to paraffins, depending on the type and concentration of chemisorbed hydrogen on the catalyst surface.
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U2 - 10.1016/j.cattod.2015.01.011
DO - 10.1016/j.cattod.2015.01.011
M3 - Article
AN - SCOPUS:84929893451
SN - 0920-5861
VL - 251
SP - 34
EP - 40
JO - Catalysis Today
JF - Catalysis Today
ER -