Carbon-supported transition metal sulfide (TMS) catalysts were prepared by impregnation of an activated carbon support with aqueous solutions of first-, second-, and third-row (group V-VIII) transition metal salts followed by drying and in situ sulfidation. Their activity for the hydrodenitrogenation of decahydroquinoline (5.2–5.5 MPa, 623–653 K), cyclohexylamine (4.8-5.5 MPa, 543–653 K), and o-propylaniline (5.1–5.5 MPa, 593–653 K) was tested in microautoclaves. When plotted versus the position of the transition metal in the Periodic System, the conversions of all three N-containing reactants to hydrocarbons over the first-row transition metal sulfides formed U-shaped curves with a minimum at Mn, while V had the highest conversion. The dec...
For zeolite Y-supported nickel sulfide catalysts the influence of the metal sulfide dispersion on th...
Carbon- and alumina-supported Fe, Mo, Fe-Mo, and Co-Mo sulfide catalysts were compared for their abi...
Catalysis plays a fundamental role in petroleum refining and basic petrochemical industries creating...
Carbon-supported transition metal sulfide (TMS) catalysts were prepared by impregnation of an activa...
Transition metal sulfide (TMS) catalysts were prepared by impregnation of an activated carbon suppor...
The catalytic properties of the first, second and third row transition metal sulfides supported on a...
International audienceLiterature data published mainly during the two last decades and dealing with ...
The catalytic vapor-phase isomerization, hydrogenolysis, and/or disproportionation of trimethylbenze...
The hydrocracking properties of various CaY-supported metal (Fe, Co, Ni, Mo, Ru, Rh, Pd, W, Re, Ir, ...
Supported MoS2/γ-Al2O3 and Ni-MoS2/γ-Al2O3 as well as unsupported Ni-MoS2 were investigated in the h...
Thesis (Sc. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1983.MICROFIC...
Transition metal sulfides (TMSs) are typically used in the traditional petroleum refining industry f...
The activities of sulfided Mo/C, W/C, Co/C, Ni/C, Co-Mo/C, and Ni-W/C catalysts for thiophene hydrod...
This document is the Accepted Manuscript version of a Published Work that appeared in final form in ...
For zeolite Y-supported nickel sulfide catalysts the influence of the metal sulfide dispersion on th...
Carbon- and alumina-supported Fe, Mo, Fe-Mo, and Co-Mo sulfide catalysts were compared for their abi...
Catalysis plays a fundamental role in petroleum refining and basic petrochemical industries creating...
Carbon-supported transition metal sulfide (TMS) catalysts were prepared by impregnation of an activa...
Transition metal sulfide (TMS) catalysts were prepared by impregnation of an activated carbon suppor...
The catalytic properties of the first, second and third row transition metal sulfides supported on a...
International audienceLiterature data published mainly during the two last decades and dealing with ...
The catalytic vapor-phase isomerization, hydrogenolysis, and/or disproportionation of trimethylbenze...
The hydrocracking properties of various CaY-supported metal (Fe, Co, Ni, Mo, Ru, Rh, Pd, W, Re, Ir, ...
Supported MoS2/γ-Al2O3 and Ni-MoS2/γ-Al2O3 as well as unsupported Ni-MoS2 were investigated in the h...
Thesis (Sc. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1983.MICROFIC...
Transition metal sulfides (TMSs) are typically used in the traditional petroleum refining industry f...
The activities of sulfided Mo/C, W/C, Co/C, Ni/C, Co-Mo/C, and Ni-W/C catalysts for thiophene hydrod...
This document is the Accepted Manuscript version of a Published Work that appeared in final form in ...
For zeolite Y-supported nickel sulfide catalysts the influence of the metal sulfide dispersion on th...
Carbon- and alumina-supported Fe, Mo, Fe-Mo, and Co-Mo sulfide catalysts were compared for their abi...
Catalysis plays a fundamental role in petroleum refining and basic petrochemical industries creating...