Propane hydrogenolysis over supported nickel catalysts: Structural and support effects
Kinetic data for propane hydrogenolysis were determined for Ni catalysts supported on SiO 2, Nb 2O 5, Nb 2O 5SiO 2, and TiO 2. Over a metal particle size range of 2.5–6.0 nm, the activities for three Ni SiO 2 catalysts varied by no more than a factor of 5. The lowest activity was found for a sample...
Saved in:
Published in | Journal of catalysis Vol. 116; no. 1; pp. 230 - 239 |
---|---|
Main Authors | , |
Format | Journal Article |
Language | English |
Published |
Amsterdam
Elsevier Inc
01.03.1989
Elsevier |
Subjects | |
Online Access | Get full text |
Cover
Loading…
Summary: | Kinetic data for propane hydrogenolysis were determined for Ni catalysts supported on SiO
2, Nb
2O
5, Nb
2O
5SiO
2, and TiO
2. Over a metal particle size range of 2.5–6.0 nm, the activities for three
Ni
SiO
2
catalysts varied by no more than a factor of 5. The lowest activity was found for a sample which had been reduced under the most severe conditions and believed to have a large proportion of (111) planes. The sample with the smallest particle size showed a higher selectivity. Activities for Ni supported on the other three oxides were lower, indicative of support effects. For samples reduced at 773 K, the suppression in activity varied in the order Nb
2O
5 > TiO
2 ~ Nb
2O
5 SiO
2. The metal-support interactions were reversible by oxidizing the samples and rereducing at a lower temperature. An oxygen treatment at 473 K was sufficient to recover the activity of
Ni
TiO
2
but not for
Ni
Nb
2O
5
, which required an oxygen treatment at 673 K. A model which considers the overall energetics of the regeneration process is presented to explain this difference. |
---|---|
ISSN: | 0021-9517 1090-2694 |
DOI: | 10.1016/0021-9517(89)90088-2 |