XPS and catalytic properties of the bifunctional supported MoO2(Hx)ac on TiO2 for the hydroisomerization reactions of hexanes and 1-hexene

[1]  U. B. Demirci,et al.  Kinetic study of n-heptane conversion on sulfated zirconia-supported platinum catalyst: the metal–proton adduct is the active site , 2002 .

[2]  A. Jablonski,et al.  Surface studies and catalytic properties of the bifunctional bulk MoO2 system , 2002 .

[3]  A. Wootsch,et al.  Reactions of n-hexane on Pt catalysts: Reaction mechanism as revealed by hydrogen pressure and compensation effect , 2002 .

[4]  A. Katrib,et al.  Molybdenum and tungsten dioxides, XO2 (X=Mo,W), as reforming catalysts for hydrocarbon compounds , 2001 .

[5]  R. Snurr,et al.  Evidence of different reaction mechanisms during the cracking of n-hexane on H-USY zeolite , 2000 .

[6]  S. Canavese,et al.  Influence of Pt concentration on tungsten oxide-promoted zirconia during n-hexane isomerization , 2000 .

[7]  J. Bokhoven,et al.  Influence of the Generation of Mesopores on the Hydroisomerization Activity and Selectivity of n-Hexane over Pt/Mordenite , 2000 .

[8]  T. Matsuda,et al.  Effect of H2 reduction on the catalytic properties of molybdenum oxides for the conversions of heptane and 2-propanol , 2000 .

[9]  A. Katrib,et al.  The reforming catalytic properties of bulk and supported molybdenum and tungsten dioxides XO2 (X=Mo, W) , 2000 .

[10]  D. Guillaume,et al.  Isomerization of n-hexane over sulfated zirconia : Influence of hydrogen and platinum , 2001 .

[11]  A. Sinha,et al.  Hydroisomerization of n-hexane over Pt-SAPO-11 and Pt-SAPO-31 molecular sieves , 1999 .

[12]  S. Canavese,et al.  Effect of operational conditions during η‐hexane isomerization over platinum on tungsten‐oxide‐promoted zirconia , 1998 .

[13]  S. Vaudagna,et al.  Hydroisomerization of n-hexane on Pt/SO42™™ZrO2: effect of total and hydrogen partial pressure , 1997 .

[14]  P. Wehrer,et al.  Surface electronic structure and isomerization reactions of alkanes on some transition metal oxides , 1997 .

[15]  C. Pham‐Huu,et al.  Effect of the reaction temperature and hydrocarbon partial pressure on the activity of carbon-modified MoO3 for n-hexane isomerization , 1997 .

[16]  T. Yashima,et al.  Isomerization of n-hexane over Platinum loaded zeolite catalysts , 1996 .

[17]  A. Katrib,et al.  Molybdenum based catalysts. I. MoO2 as the active species in the reforming of hydrocarbons , 1996 .

[18]  A. Gulino,et al.  Influence of metal–metal bonds on electron spectra of MoO2 and WO2 , 1996 .

[19]  S. Tougaard,et al.  Quantitative analysis by XPS using the multiline approach , 1994 .

[20]  F. Hemming,et al.  Surface characterization and catalytic properties of supported tungsten and platinum-tungsten carbide and oxycarbide , 1994 .

[21]  F. Ribeiro.  Reactions of neopentane, methylcyclohexane, and 3,3-dimethylpentane on tungsten carbides: The effect of surface oxygen on reaction pathways , 1991 .

[22]  C. Clayton,et al.  Electrochemical and XPS evidence of the aqueous formation of Mo2O5 , 1989 .

[23]  F. G. Gault.  Mechanisms of Skeletal Isomerization of Hydrocarbons on Metals , 1982 .

[24]  M. Boudart,et al.  Platinum-Like Behavior of Tungsten Carbide in Surface Catalysis , 1973, Science.

[25]  R. C. Olberg,et al.  Studies in the Terpene Series. VIII.1 Effect of Catalyst, Solvent and Temperature on the Dehydrogenation of Pinane and p-Menthane2 , 1948 .