Effect of the Co/Mo Ratio on the Morphology and Activity of the CoMo Catalyst Supported on MgO Nanosheets in Dibenzothiophene Hydrodesulfurization

2020 ◽  
Vol 59 (27) ◽  
pp. 12338-12351
Author(s):  
Lei Zhang ◽  
Zhongmiao Chen ◽  
Shifu Zheng ◽  
Guoren Cai ◽  
Wenqian Fu ◽  
...  
Keyword(s):  
Como Catalyst

Hydrodesulphurization of thiophene over zirconia and alumina supported Co-Mo catalysts

1989 ◽  
Vol 54 (8) ◽  
pp. 2064-2068 ◽  
Author(s):  
Jiří Sedláček ◽  
Zdeněk Vít
Keyword(s):  
Total Pressure ◽  
Supported Catalysts ◽  
Atomic Concentration ◽  
Commercial Sample ◽  
Sulphur Oxidation ◽  
Como Catalysts ◽  
Zirconia Support ◽  
Como Catalyst ◽  
Concentration Ratios

The zirconia supported CoMo catalysts and the commercial sample CoMo/Al2O3 were characterized by XPS measurements and by testing of activity in the HDS of thiophene at 280 °C and 1 MPa of total pressure. The XPS measurements revealed the better reducibility of molybdenum, higher sulphidability of cobalt and the absence of surface sulphur oxidation in the presence of zirconia support. The surface atomic concentration ratios S/Mo were 1.2 and 2.2 for zirconia and alumina supported catalysts, respectively. The activity of the zirconia supported CoMo catalyst normalized to the overal amounts of active metals was lower than that of the commercial CoMo/Al2O3 catalyst.

Hydrocracking of waste lubricant into gasoline fraction over CoMo catalyst supported on mesoporous carbon from bovine bone gelatin

2017 ◽  
Vol 34 (10) ◽  
pp. 2591-2596 ◽  
Author(s):  
Marthinus Pongsendana ◽  
Wega Trisunaryanti ◽  
Farin Windy Artanti ◽  
Iip Izul Falah ◽  
Sutarno
Keyword(s):  
Mesoporous Carbon ◽  
Gasoline Fraction ◽  
Bovine Bone ◽  
Como Catalyst

scholarly journals Deactivation of a CoMo Catalyst during Catalytic Hydropyrolysis of Biomass. Part 1. Product Distribution and Composition

2019 ◽  
Vol 33 (12) ◽  
pp. 12374-12386 ◽  
Author(s):  
M. Z. Stummann ◽  
M. Høj ◽  
A. B. Hansen ◽  
P. Beato ◽  
P. Wiwel ◽  
...  
Keyword(s):  
Product Distribution ◽  
Como Catalyst ◽  
Catalytic Hydropyrolysis

scholarly journals Deactivation of a CoMo Catalyst during Catalytic Hydropyrolysis of Biomass. Part 2. Characterization of the Spent Catalysts and Char

2019 ◽  
Vol 33 (12) ◽  
pp. 12387-12402 ◽  
Author(s):  
M. Z. Stummann ◽  
M. Høj ◽  
B. Davidsen ◽  
L. P. Hansen ◽  
P. Beato ◽  
...  
Keyword(s):  
Spent Catalysts ◽  
Como Catalyst ◽  
Catalytic Hydropyrolysis

Influence of arsenic on light cycle oil hydrodesulfurization over a CoMo catalyst

2020 ◽  
Vol 131 (1) ◽  
pp. 199-211
Author(s):  
Mildred Rodriguez ◽  
Susana Pinto-Castilla ◽  
Myloa Morgado-Vargas ◽  
Paulino Betancourt
Keyword(s):  
Light Cycle ◽  
Light Cycle Oil ◽  
Como Catalyst ◽  
Cycle Oil

Investigation on the active phase of CoMo catalyst for selective HDS by low temperature in situ FT-IR

2011 ◽  
Vol 22 (3) ◽  
pp. 366-369 ◽  
Author(s):  
Qiherima ◽  
Hui Yuan ◽  
Hui Feng Li ◽  
Yun Hong Zhang ◽  
Guang Tong Xu
Keyword(s):  
Low Temperature ◽  
Active Phase ◽  
Ft Ir ◽  
Como Catalyst

CoMo catalyst on zeolite TS-1 nanorod assemblies with high activity in the hydrodesulfurization of 4,6-dimethyldibenzothiophene

2018 ◽  
Vol 359 ◽  
pp. 130-142 ◽  
Author(s):  
Lei Zhang ◽  
Quan Dai ◽  
Wenqian Fu ◽  
Tiandi Tang ◽  
Pengxiang Dong ◽  
...  
Keyword(s):  
High Activity ◽  
Como Catalyst

High pressure Water Gas Shift performance over a commercial non-sulfide CoMo catalyst using industrial coal-derived syngas

Fuel ◽  
2012 ◽  
Vol 97 ◽  
pp. 428-434 ◽  
Author(s):  
A.R. de la Osa ◽  
A. De Lucas ◽  
A. Romero ◽  
P. Casero ◽  
J.L. Valverde ◽  
...  
Keyword(s):  
High Pressure ◽  
Water Gas Shift ◽  
Shift Performance ◽  
Pressure Water ◽  
Como Catalyst ◽  
Water Gas
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