Acetic acid hydrogenation over supported platinum catalysts

Citation
W. Rachmady et Ma. Vannice, Acetic acid hydrogenation over supported platinum catalysts, J CATALYSIS, 192(2), 2000, pp. 322-334
Citations number
29
Categorie Soggetti
Physical Chemistry/Chemical Physics","Chemical Engineering
Journal title
JOURNAL OF CATALYSIS
ISSN journal
00219517 → ACNP
Volume
192
Issue
2
Year of publication
2000
Pages
322 - 334
Database
ISI
SICI code
0021-9517(20000610)192:2<322:AAHOSP>2.0.ZU;2-K
Abstract
Acetic acid was chosen to probe the kinetic behavior of carboxylic acid hyd rogenation over platinum supported on TiO2, SiO2, eta-Al2O3, and Fe2O3. The reaction was studied in the vapor phase under conditions of 423-573 K, 100 -700 Torr hydrogen, and 7-50 Torr acetic acid in a differential, fixed-bed reactor. Product selectivity was strongly dependent on the oxide supports. Carbon-containing products during hydrogenation at low conversions consiste d of about: 50% CO and 50% CH4 over Pt/SiO2; 8% ethanol, 4% ethyl acetate, 10% ethane, 40% CH4, 33% CO, and 5% CO2 over Pt/eta-Al2O3; 50% ethanol, 30% ethyl acetate, and 20% ethane over Pt/TiO2 reduced at either 473 or 773 K; and about 80% acetaldehyde and 20% ethanol over Pt/Fe2O3. The TiO2-support ed Pt catalysts were the most active, and both their activities and their t urnover frequencies were up to two orders of magnitude larger than those fo r Pt dispersed on SiO2 eta-Al2O3, or Fe2O3. The activity dependence on the partial pressures of hydrogen, P-H2, and acetic acid, P-A, was determined f or Pt/TiO2 catalysts at three operating temperatures-422, 445, and 465 K-af ter reduction at either 473 or 773 K. The apparent reaction order with resp ect to Hz was found to vary between 0.4 and 0.6, while that with respect to acetic acid was between 0.2 and 0.4. One reaction model that correlated th ese data well involves a Langmuir-Hinshelwood-type catalytic sequence that incorporates dissociative hydrogen and acetic acid adsorption on one type o f site existing on the Pt surface, but only molecular acetic acid adsorptio n at another type of site on the oxide surface. Only the latter species on the titania surface was considered catalytically significant in the formati on of desired products, i.e., acetaldehyde, ethanol, and ethane. The result ing rate expression in terms of acetic acid disappearance has the form r(HOAc) = k(1)P(A)P(H2)(1/2)/[(K2PH21/2 + K3PA/P-H2(1/2)) (1 + K4PA)]. Values of enthalpy and entropy of adsorption obtained from the optimized ra te for hydrogen on platinum and acetic acid on titania were reasonable and thermodynamically consistent. (C) 2000 Academic Press.