HMSand Al-HMSmaterials were synthesized by neutral templating pathway and Mo, CoMo, NiMo catalysts were prepared using them as the support. On Al-HMS material (Si/Al = 35) as the support, Mo concentration varied from 2 to 14 wt.%. The promotional effects were studied on 10 wt.% Mo/Al-HMS using 1–5 wt.% Co and Ni. All these catalysts were characterized by surface area, X-ray diffraction (XRD), temperature programmed reduction (TPR) and oxygen chemisorption methods. The catalytic activities for HDS, HYD and HDO were evaluated on sulfided catalysts. The oxygen chemisorption and catalytic activities as a function of Mo loading indicated that a correlation exists between these two parameters for all these reactions. A comparison with -Al2O3 sup...
The influence of Mo content on thiophene hydrodesulfurization for alumina- and carbon-supported (Co)...
A series of molybdenum catalysts supported on Al2O3–ZrO2 mixed oxide containing 50% ZrO2 and 50% Al2...
362-365A series of catalysts have been prepared by varying the molybdenum metal content from 4 to 1...
HMS and Al-HMS materials were synthesized by neutral templating pathway and Mo, CoMo, NiMo catalysts...
Al-HMS mesoporous materials with varying Si/Al ratios were synthesized and characterized using XRD a...
High surface area, ordered mesoporous SBA-15 and Al-SBA-15 were synthesized using published procedur...
Catalysts containing 2-12 wt % Mo and 1-5 wt % Co or Ni were prepared using commercial H-â-zeolite a...
326-330A series of molybdenum catalysts supported on MgO/Al2O3 (1:1) mixed oxide were prepared and ...
A series of titania supported molybdenum catalysts were prepared by incipient wetness impregnation m...
KIT-6 silica with well-ordered 3-D mesoporosity was developed as support for Mo, CoMo and NiMo catal...
FSM-16 (Folded Sheet Silica) supported catalysts could accommodate 12 wt% Mo (18% MoO3) as a monolay...
Traditional hydrotreating catalysts are constituted by molybdenum deposited on Al2O3 promoted by nic...
This project focuses on the modification of silica and alumina surfaces by titania and hydrous titan...
Supported Mo-sulfide catalysts were structurally characterized by means of transmission electron mic...
Two series of Mo-containing catalysts supported on alumina and silica, respectively, modified with d...
The influence of Mo content on thiophene hydrodesulfurization for alumina- and carbon-supported (Co)...
A series of molybdenum catalysts supported on Al2O3–ZrO2 mixed oxide containing 50% ZrO2 and 50% Al2...
362-365A series of catalysts have been prepared by varying the molybdenum metal content from 4 to 1...
HMS and Al-HMS materials were synthesized by neutral templating pathway and Mo, CoMo, NiMo catalysts...
Al-HMS mesoporous materials with varying Si/Al ratios were synthesized and characterized using XRD a...
High surface area, ordered mesoporous SBA-15 and Al-SBA-15 were synthesized using published procedur...
Catalysts containing 2-12 wt % Mo and 1-5 wt % Co or Ni were prepared using commercial H-â-zeolite a...
326-330A series of molybdenum catalysts supported on MgO/Al2O3 (1:1) mixed oxide were prepared and ...
A series of titania supported molybdenum catalysts were prepared by incipient wetness impregnation m...
KIT-6 silica with well-ordered 3-D mesoporosity was developed as support for Mo, CoMo and NiMo catal...
FSM-16 (Folded Sheet Silica) supported catalysts could accommodate 12 wt% Mo (18% MoO3) as a monolay...
Traditional hydrotreating catalysts are constituted by molybdenum deposited on Al2O3 promoted by nic...
This project focuses on the modification of silica and alumina surfaces by titania and hydrous titan...
Supported Mo-sulfide catalysts were structurally characterized by means of transmission electron mic...
Two series of Mo-containing catalysts supported on alumina and silica, respectively, modified with d...
The influence of Mo content on thiophene hydrodesulfurization for alumina- and carbon-supported (Co)...
A series of molybdenum catalysts supported on Al2O3–ZrO2 mixed oxide containing 50% ZrO2 and 50% Al2...
362-365A series of catalysts have been prepared by varying the molybdenum metal content from 4 to 1...