The influence of Mo content on thiophene hydrodesulfurization for alumina- and carbon-supported (Co)Mo catalysts is investigated by TPR, XPS and H-2-D-2 equilibration. Activity trends for alumina-supported catalysts are explained by a gradual change of the type I MoS2 active phase from a large to a small number of Mo-O-Al anchors. A pure type II phase without such anchors and a high HDS activity is only obtained employing chelating ligands or a carbon support. At low Mo loading a separate oxysulfidic Mo species in strong interaction with alumina exhibits an unexpectedly high HDS activity, which, however, is difficult to promote by C
The identification of the phase responsible for hydrodesulfurization (HDS) activity has been the sub...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
The identification of the phase responsible for hydrodesulfurization (HDS) activity has been the sub...
The thiophene hydrodesulfurization activity was measured under continuous flow conditions at 400 °C ...
The thiophene hydrodesulfurization activity was measured under continuous flow conditions at 400 °C ...
Several MO and CoMo catalysts on different supports, previously evaluated for thiophene hydro-desulf...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo-sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Hydrodesulfurization (HDS) converts organic sulfur compounds to H2S and desulfurized organic compoun...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
The identification of the phase responsible for hydrodesulfurization (HDS) activity has been the sub...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
The identification of the phase responsible for hydrodesulfurization (HDS) activity has been the sub...
The thiophene hydrodesulfurization activity was measured under continuous flow conditions at 400 °C ...
The thiophene hydrodesulfurization activity was measured under continuous flow conditions at 400 °C ...
Several MO and CoMo catalysts on different supports, previously evaluated for thiophene hydro-desulf...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo-sulfide catalysts were structurally characterized by means of transmission electron mic...
Supported Mo–sulfide catalysts were structurally characterized by means of transmission electron mic...
Hydrodesulfurization (HDS) converts organic sulfur compounds to H2S and desulfurized organic compoun...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
The identification of the phase responsible for hydrodesulfurization (HDS) activity has been the sub...
Model catalysts, consisting of a conducting substrate with a thin SiO2 layer on top of which the act...
The identification of the phase responsible for hydrodesulfurization (HDS) activity has been the sub...