DIMERIZATION AND TRIMERIZATION OF ACETYLENE OVER A MODEL SN PT CATALYST/

Citation
J. Szanyi et Mt. Paffett, DIMERIZATION AND TRIMERIZATION OF ACETYLENE OVER A MODEL SN PT CATALYST/, Journal of the American Chemical Society, 117(3), 1995, pp. 1034-1042
Citations number
46
Categorie Soggetti
Chemistry
ISSN journal
00027863
Volume
117
Issue
3
Year of publication
1995
Pages
1034 - 1042
Database
ISI
SICI code
0002-7863(1995)117:3<1034:DATOAO>2.0.ZU;2-A
Abstract
The di- and trimerization reactions of acetylene were studied over Pt( 111) and (root 3x root 3)R30 degrees-Sn/Pt(111) model catalysts at mod erate pressures (20-100 Torr, hydrogen-hydrocarbon ratio of 10). The c atalyst surfaces were prepared and characterized in a UHV surface anal ysis system and moderate pressure catalytic reactions were 1/3 conduct ed with an attached batch reactor. The overall catalytic activity of t he (root 3x root 3)R30 degrees-Sn/Pt(111) surface alloy was similar to -4-5 times higher than that of Pt(lll). Both surfaces produced only C- 4 and C-6 hydrocarbons as di- and trimerization products with C-4 prod uction rates being about an order of magnitude higher than that for C- 6 hydrocarbons. Besides the di- and trimerization reaction, hydrogenat ion of acetylene into ethylene was also observed. Among the C-4 produc ts, butadiene, l-butene, and n-butane were the major components. Both linear and cyclic C-6 hydrocarbons were produced. Among the linear C-6 products paraffinic (n-hexane), olefinic (l-hexene), and diolefinic ( hexadiene) hydrocarbons were observed. The main components of the cycl ic C-6 products were cyclohexane, cyclohexene, 1,3-cyclohexadiene, and benzene. For both product groups the degree of unsaturation of the hy drocarbon molecules depended upon the experimental conditions applied (P-H2/P-C2H2; T). The formation of carbonaceous surface residues was s een under all experimental conditions. The di- and trimerization of ac etylene was not eliminated by the presence of surface carbonaceous dep osits and even at a high level of carbon buildup the catalysts exhibit ed significant activities. The very good correlation found between the formation rates of butadiene and cyclic C-6 hydrocarbons suggests tha t the formation of ring C-6 products proceeds through a metallocyclope ntadiene intermediate. This species can either be hydrogenated off fro m the catalyst surfaces to produce butadiene or be reacted with a thir d acetylene molecule to form ring C-6 hydrocarbons.