Catalytic dehydrogenation of 2-propanol over Cu-SiO2 catalyst was investigated. The undesired side reaction of dehydration can be controlled by a selective catalyst and choice of proper operating conditions. The kinetics of the heterogeneous catalytic reaction can be adequately expressed by a forward first-order and reverse second-order mechanism. The rate-controlling step with chemically pure 2-propanol is single-site surface reaction, while for the technical grade alcohol the adsorption of alcohol is rate-controlling. The static bed data are compared with the fluidized bed da
Acceptorless dehydrogenation into carbonyls and molecular hydrogen is an attractive strategy to valo...
The catalytic decomposition of 2-propanol has been investigated in a flow system from 200-300°C on ...
Chemistry Department, Indian Institute of Technology, Kharagpur-721 302 Manuscript received 27 Marc...
Catalytic dehydrogenation of 2-propanol over Cu-SiO2 catalyst was investigated. The undesired side r...
Catalytic and photocatalytic tests for 2-propanol dehydration to propene were successfully carried o...
The vapor-phase dehydrogenation of 1 -butanol to butyraldehyde was studied in a fixed bed of catalys...
The vapor-phase dehydrogenation of 1-butanol to butyraldehyde was studied in a fixed bed of catalyst...
A kinetic study of the ethanol dehydrogenation to ethyl acetate on a copper/copper-chromite catalyst...
The kinetics of the selective oxidative dehydrogenation of ethanol to ethanal over a platinum on gra...
Catalytic and photocatalytic tests for 2-propanol dehydration to propene were successfully carried o...
Mesoporous silica with strongly acid sulfonic sites were synthesized and used as catalytic supports ...
1,2-propanediol (PDO) and 1,2-butanediol (BDO) are preferentially dehydrated over the H-Beta zeolite...
An economically viable approach for the synthesis of different alpha, 8-unsaturated aldehydes throug...
CuO/ZnO/Al2O3 samples (1 and 4 Cu atoms and 1, 5, 15, and 30 Zn atoms per 100 Al atoms, respectively...
Gas-phase hydrogenation of dimethyl oxalate (DMO) on a copper-based catalyst is one of the crucial t...
Acceptorless dehydrogenation into carbonyls and molecular hydrogen is an attractive strategy to valo...
The catalytic decomposition of 2-propanol has been investigated in a flow system from 200-300°C on ...
Chemistry Department, Indian Institute of Technology, Kharagpur-721 302 Manuscript received 27 Marc...
Catalytic dehydrogenation of 2-propanol over Cu-SiO2 catalyst was investigated. The undesired side r...
Catalytic and photocatalytic tests for 2-propanol dehydration to propene were successfully carried o...
The vapor-phase dehydrogenation of 1 -butanol to butyraldehyde was studied in a fixed bed of catalys...
The vapor-phase dehydrogenation of 1-butanol to butyraldehyde was studied in a fixed bed of catalyst...
A kinetic study of the ethanol dehydrogenation to ethyl acetate on a copper/copper-chromite catalyst...
The kinetics of the selective oxidative dehydrogenation of ethanol to ethanal over a platinum on gra...
Catalytic and photocatalytic tests for 2-propanol dehydration to propene were successfully carried o...
Mesoporous silica with strongly acid sulfonic sites were synthesized and used as catalytic supports ...
1,2-propanediol (PDO) and 1,2-butanediol (BDO) are preferentially dehydrated over the H-Beta zeolite...
An economically viable approach for the synthesis of different alpha, 8-unsaturated aldehydes throug...
CuO/ZnO/Al2O3 samples (1 and 4 Cu atoms and 1, 5, 15, and 30 Zn atoms per 100 Al atoms, respectively...
Gas-phase hydrogenation of dimethyl oxalate (DMO) on a copper-based catalyst is one of the crucial t...
Acceptorless dehydrogenation into carbonyls and molecular hydrogen is an attractive strategy to valo...
The catalytic decomposition of 2-propanol has been investigated in a flow system from 200-300°C on ...
Chemistry Department, Indian Institute of Technology, Kharagpur-721 302 Manuscript received 27 Marc...