The glycerol hydrogenolysis reaction was performed in a continuous flow trickle bed reactor using a water glycerol feed and both copper chromite and Cu/Al2O3 catalysts. The commercial copper chromite had a higher activity than the laboratory prepared Cu/Al2O3 and was used for most of the tests. Propylene glycol was the main product with both catalysts, acetol being the main by-product. It was found that temperature is the main variable influencing the conversion of glycerol. When the state of the glycerol-water reactant mixture was completely liquid, at temperatures lower than 190 °C, conversion was low and deactivation was observed. At reaction temperatures of 210-230 °C the conversion of glycerol was complete and the selectivity to propyl...
Glycerol conversion to value-added product, acetol was studied through dehydration reaction of glyce...
The development of catalytic materials, hydrothermally stable and selective to the desired products,...
High activity of copper based catalysts for C-O bond hydro-dehydrogenation and their poor activity f...
BACKGROUND: Hydrogenolysis of glycerol to glycols in continuous flow three phase reactors is of prac...
Abstract only availableHydrogenolysis of glycerin to propylene glycol using a copper-chromite cataly...
The purpose of this research was to achieved selective hydrogenolysis of glycerol to 1,2-PDO (1,2-pr...
The hydrogenolysis of glycerol was performed in an autoclave at temperatures between 190 and 225 °C ...
A Cu-ZnO-Al2O3 catalyst has been observed in laboratory scale tests to effectively produce propylene...
In this paper, we report that the hydrogenolysis of glycerol can be carried out at atmospheric press...
A Cu-ZnO-Al2O3 catalyst has been observed in laboratory scale tests to effectively produce propylene...
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...
Abstract. The conversion of 30 % glycerol mixture in ethanol over Cu/Al2O3 catalyst at 493 K/0.1MPa ...
The present study is dedicated to the experimental verification of a concept for the hydrogenolysis ...
World demand for energy, chemicals and products is increasing every year. Current production systems...
Glycerol conversion to value-added product, acetol was studied through dehydration reaction of glyce...
The development of catalytic materials, hydrothermally stable and selective to the desired products,...
High activity of copper based catalysts for C-O bond hydro-dehydrogenation and their poor activity f...
BACKGROUND: Hydrogenolysis of glycerol to glycols in continuous flow three phase reactors is of prac...
Abstract only availableHydrogenolysis of glycerin to propylene glycol using a copper-chromite cataly...
The purpose of this research was to achieved selective hydrogenolysis of glycerol to 1,2-PDO (1,2-pr...
The hydrogenolysis of glycerol was performed in an autoclave at temperatures between 190 and 225 °C ...
A Cu-ZnO-Al2O3 catalyst has been observed in laboratory scale tests to effectively produce propylene...
In this paper, we report that the hydrogenolysis of glycerol can be carried out at atmospheric press...
A Cu-ZnO-Al2O3 catalyst has been observed in laboratory scale tests to effectively produce propylene...
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...
Abstract. The conversion of 30 % glycerol mixture in ethanol over Cu/Al2O3 catalyst at 493 K/0.1MPa ...
The present study is dedicated to the experimental verification of a concept for the hydrogenolysis ...
World demand for energy, chemicals and products is increasing every year. Current production systems...
Glycerol conversion to value-added product, acetol was studied through dehydration reaction of glyce...
The development of catalytic materials, hydrothermally stable and selective to the desired products,...
High activity of copper based catalysts for C-O bond hydro-dehydrogenation and their poor activity f...