An explorative screening study with Pt/CeZrO2, Ni/ZrO2. Ni/CaO-6Al(2)O(3), NiCu/CeZrO2, and a CuZn alloy was carried out to investigate the influence of different catalysts on the carbon-to-gas efficiency and gas composition in the reforming of glycerol in supercritical water. Experiments were conducted at 255-270 bar in a continuous set-up, with temperatures ranging from 375 to 700 degrees C. a feed concentration of 10 wt%, and a residence time of 8-87 s. The catalysts promoted the decomposition of glycerol significantly. At 674 degrees C the conversion of glycerol without catalyst was approximately 40%, while in the presence of catalysts (almost) complete conversion was obtained. All catalysts promoted the water-gas shift reaction, while ...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2. Ni/CaO-6Al(2)O(3), NiCu/CeZrO2, and a CuZn a...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2. Ni/CaO-6Al(2)O(3), NiCu/CeZrO2, and a CuZn a...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2. Ni/CaO-6Al(2)O(3), NiCu/CeZrO2, and a CuZn a...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2, Ni/CaO–6Al2O3, NiCu/CeZrO2, and a CuZn alloy...
Catalytic reforming of pure glycerol for the production of hydrogen at low temperature and short res...
Catalytic reforming of pure glycerol for the production of hydrogen at low temperature and short res...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
The conversion of glycerol in supercritical water (SCW) was studied at 510-550 °C and a pressure of ...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na2CO3) in sup...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2. Ni/CaO-6Al(2)O(3), NiCu/CeZrO2, and a CuZn a...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2. Ni/CaO-6Al(2)O(3), NiCu/CeZrO2, and a CuZn a...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2. Ni/CaO-6Al(2)O(3), NiCu/CeZrO2, and a CuZn a...
An explorative screening study with Pt/CeZrO2, Ni/ZrO2, Ni/CaO–6Al2O3, NiCu/CeZrO2, and a CuZn alloy...
Catalytic reforming of pure glycerol for the production of hydrogen at low temperature and short res...
Catalytic reforming of pure glycerol for the production of hydrogen at low temperature and short res...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na(2)CO(3)) in...
The conversion of glycerol in supercritical water (SCW) was studied at 510-550 °C and a pressure of ...
Reforming of pure glycerol, crude glycerin, and methanol (pure and in the presence of Na2CO3) in sup...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...
Due to the rise in global biodiesel production, the amount of crude glycerol, the main byproduct, ha...