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Title: Hydrogenation of aromatic hydrocarbons over supported Pt catalysts

Journal Article · · Journal of Catalysis; (United States)
;  [1]
  1. Pennsylvania State Univ., University Park, PA (United States)

Vapor-phase benzene hydrogenation was studied over Pt dispersed on SiO[sub 2], [eta]-Al[sub 2]O[sub 3], SiO[sub 2][center dot]Al[sub 2]O[sub 3], and TiO[sub 2], as well as Pt powder. Activation energies and reaction orders were independant of the support as all E[sub act] values fell between 10 and 13 kcal/mol and partial pressure dependencies were 0.6 [+-] 0.1 on H[sub 2] and 0.1 [+-] 0.1 on benzene between 317 and 356 K. However, higher specific activities were obtained with acidic supports; for example, at 333 K under 50 torr benzene and 685 torr H[sub 2], turnover frequencies increased from 0.015 s[sup [minus]1] on 0.78% Pt/[eta]-Al[sub 2]O[sub 3] and 0.033 s[sup [minus]1] on 0.96% Pt/SiO[sub 2] to 0.072 on 0.24% Pt/SiO[sub 2] [center dot] Al[sub 2]O[sub 3] and 0.078 on 0.95% Pt/TiO[sub 2]. An even larger increase occurred under 35 Torr benzene. This rate enhancement, which is similar to that found with Pd on these same supports, is associated with an additional contribution from benzene adsorbing on acidic sites on the support and reacting with spilled-over hydrogen. Significant inhibition and deactivation occurred under certain reaction conditions which altered steady-state activities. This is attributed to the concurrent formation of hydrogen-deficient surface species during benzene hydrogenation. 115 refs., 7 figs., 4 tabs.

DOE Contract Number:
FG02-84ER13276
OSTI ID:
5183476
Journal Information:
Journal of Catalysis; (United States), Vol. 143:2; ISSN 0021-9517
Country of Publication:
United States
Language:
English