The hydrogenolysis of sorbitol (15% aqueous solution) was carried out at 60 bar pressure at 220 °C in a stirred batch reactor using Ni-NaY (2, 4, 6 wt.% Ni) with and without added Pt(1 wt.%). 1,2-Propanediol was the major product over Ni-NaY and glycerol was the main product over Pt(1 wt.%)-NaY. The addition of 1 wt.% Pt to the Ni-catalysts had only a marginal effect on conversion and selectivity of the catalysts. Addition of Ca(OH)2 as the promoter to both Ni and Pt catalysts increased the conversion significantly without any significant effect on selectivity
The aqueous hydrogenolysis of glycerol was performed over Ni-Ce/AC catalyst. The addition of cerium ...
Hydrogenation of aqueous glucose solution was performed in batch and continuous reactors using suppo...
International audienceThe effect of the metal/acid balance of Pt/SiO2-Al2O3 catalysts on the catalyt...
The hydrogenolysis of sorbitol (15% aqueous solution) was carried out at 60 bar pressure at 220 °C i...
226-231Hydrogenolysis of sorbitol (15% aqueous solution) has been carried out in a batch reactor ove...
A series of Ni based catalysts with different supports and basic additives were prepared by sequenti...
A series of Ni based catalysts with different supports and basic additives were prepared by sequenti...
Ni/La2O3/ZrO2 catalysts were prepared by a step-by-step impregnation method through regulation of th...
Ni/La2O3/ZrO2 catalysts were prepared by a step-by-step impregnation method through regulation of th...
Hydrogenolysis of sorbitol (15% aqueous solution) has been carried out in a batch reactor over Ni (6...
Sorbitol is one of the key platform chemicals that can be applied to several industrial applications...
Most of the sorbitol processing at industrial scale is performed by hydrogenation of d-glucose using...
Using hydrogen generated in situ from aqueous phase reforming provides an efficient and economic rou...
Hydrogen was produced by Aqueous Phase Reforming (APR) of 10% (w/w) sorbitol using mono- and bi-meta...
Hydrogenation of aqueous glucose solution was performed in batch and continuous reactors using suppo...
The aqueous hydrogenolysis of glycerol was performed over Ni-Ce/AC catalyst. The addition of cerium ...
Hydrogenation of aqueous glucose solution was performed in batch and continuous reactors using suppo...
International audienceThe effect of the metal/acid balance of Pt/SiO2-Al2O3 catalysts on the catalyt...
The hydrogenolysis of sorbitol (15% aqueous solution) was carried out at 60 bar pressure at 220 °C i...
226-231Hydrogenolysis of sorbitol (15% aqueous solution) has been carried out in a batch reactor ove...
A series of Ni based catalysts with different supports and basic additives were prepared by sequenti...
A series of Ni based catalysts with different supports and basic additives were prepared by sequenti...
Ni/La2O3/ZrO2 catalysts were prepared by a step-by-step impregnation method through regulation of th...
Ni/La2O3/ZrO2 catalysts were prepared by a step-by-step impregnation method through regulation of th...
Hydrogenolysis of sorbitol (15% aqueous solution) has been carried out in a batch reactor over Ni (6...
Sorbitol is one of the key platform chemicals that can be applied to several industrial applications...
Most of the sorbitol processing at industrial scale is performed by hydrogenation of d-glucose using...
Using hydrogen generated in situ from aqueous phase reforming provides an efficient and economic rou...
Hydrogen was produced by Aqueous Phase Reforming (APR) of 10% (w/w) sorbitol using mono- and bi-meta...
Hydrogenation of aqueous glucose solution was performed in batch and continuous reactors using suppo...
The aqueous hydrogenolysis of glycerol was performed over Ni-Ce/AC catalyst. The addition of cerium ...
Hydrogenation of aqueous glucose solution was performed in batch and continuous reactors using suppo...
International audienceThe effect of the metal/acid balance of Pt/SiO2-Al2O3 catalysts on the catalyt...