The hydrogenolysis of glycerol was performed in an autoclave at temperatures between 190 and 225 °C and at a H₂ pressure of 5 MPa over a CuO/ZnO catalyst prepared by an oxalate gel (OG) method. Compared to a CuO/ZnO catalyst prepared by coprecipitation, much higher conversions of glycerol and space–time yields up to 9.8 gpropylene glycol g(Cu)⁻¹ h⁻¹ are achieved with CuO/ZnO-OG, whereas both catalysts produced propylene glycol with selectivities of about 90%. Additionally, the influence of the temperature and the solvent was examined. Compared to a conversion of glycerol of only 5% in an aqueous glycerol solution, the use of 1,2-butanediol as a solvent leads to a high conversion of 55%. Moreover, experiments were carried out in pure glycero...
he hydrogenolysis of glycerol was performed both in liquid and in vapour phase by the use of differe...
he hydrogenolysis of glycerol was performed both in liquid and in vapour phase by the use of differe...
In this study, the catalytic activity of Cu-derived oxide catalysts in glycerol hydrogenolysis was i...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
The hydrogenolysis of glycerol is considered a sustainable process to produce 1,2-propanediol (1,2-P...
The hydrogenolysis of glycerol is considered a sustainable process to produce 1,2-propanediol (1,2-P...
Cu-ZnO catalysts were prepared by homogeneous coprecipitation with varying Cu/Zn atomic ratios (0.4-...
The hydrogenolysis of glycerol is considered a sustainable process to produce 1,2-propanediol (1,2-P...
The kinetics of glycerol hydrodeoxygenation to 1,2-propanediol via the selective cleavage of the pri...
The glycerol hydrogenolysis reaction was performed in a continuous flow trickle bed reactor using a ...
A series of transition metal oxides (e.g., Ni, Cu, Zn, and Zr) were supported on H-beta with loading...
A series of Cu–ZrO2 catalysts with different copper contents have been prepared by the coprecipitati...
he hydrogenolysis of glycerol was performed both in liquid and in vapour phase by the use of differe...
he hydrogenolysis of glycerol was performed both in liquid and in vapour phase by the use of differe...
In this study, the catalytic activity of Cu-derived oxide catalysts in glycerol hydrogenolysis was i...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
Copper/zinc oxide catalysts prepared by coprecipitation were proved to be highly active and selectiv...
The hydrogenolysis of glycerol is considered a sustainable process to produce 1,2-propanediol (1,2-P...
The hydrogenolysis of glycerol is considered a sustainable process to produce 1,2-propanediol (1,2-P...
Cu-ZnO catalysts were prepared by homogeneous coprecipitation with varying Cu/Zn atomic ratios (0.4-...
The hydrogenolysis of glycerol is considered a sustainable process to produce 1,2-propanediol (1,2-P...
The kinetics of glycerol hydrodeoxygenation to 1,2-propanediol via the selective cleavage of the pri...
The glycerol hydrogenolysis reaction was performed in a continuous flow trickle bed reactor using a ...
A series of transition metal oxides (e.g., Ni, Cu, Zn, and Zr) were supported on H-beta with loading...
A series of Cu–ZrO2 catalysts with different copper contents have been prepared by the coprecipitati...
he hydrogenolysis of glycerol was performed both in liquid and in vapour phase by the use of differe...
he hydrogenolysis of glycerol was performed both in liquid and in vapour phase by the use of differe...
In this study, the catalytic activity of Cu-derived oxide catalysts in glycerol hydrogenolysis was i...