Effect of Hydrogen Ratio and Tin Addition on the Coke Formation of Platinum Catalyst for Propane Dehydrogenation Reaction 


Vol. 22,  No. 2, pp. 82-88, Jun.  2016
10.7464/ksct.2016.22.2.082


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  Abstract

The loss of activity by coke is an important cause of catalyst deactivation during industrial operation. In this study, hydrogen ratio of reaction condition, which has influenced on coke formation over Pt-Sn catalyst, and regeneration of catalysts activity by coke burning, Pt sintering of coke burning as coke contents, effects of coke formation and deactivation with different Sn contents were confirmed. Pt-Sn-K catalyst supported on θ-alumina and γ-alumina was prepared progressively. Activity of regenerated catalyst for propane dehydrogenation was compared with fresh catalyst by coke burning, after propane dehydrogenation was carried out with different hydrogen ratio at 620 ℃ on fresh catalyst. Regenerated catalyst’s physical characterization such as BET, coke analysis and XRD was investigated. Through catalytic activity test and characterization, Sn contents of catalyst and hydrogen ratio in feed stream could affect coke formation on catalyst surface. Excessive coke makes loss of activity and Pt sintering during air regeneration process.

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  Cite this article

[IEEE Style]

K. SY, K. GH, K. HL, "Effect of Hydrogen Ratio and Tin Addition on the Coke Formation of Platinum Catalyst for Propane Dehydrogenation Reaction," Clean Technology, vol. 22, no. 2, pp. 82-88, 2016. DOI: 10.7464/ksct.2016.22.2.082.

[ACM Style]

Kim SY, Kim GH, and Koh HL. 2016. Effect of Hydrogen Ratio and Tin Addition on the Coke Formation of Platinum Catalyst for Propane Dehydrogenation Reaction. Clean Technology, 22, 2, (2016), 82-88. DOI: 10.7464/ksct.2016.22.2.082.

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pISSN : 1598 - 9712
eISSN : 2288 - 0690

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