C214 AN ANALYTICAL AND EXPERIMENTAL STUDY OF ETHANOL STEAM REFORMING WITH Cu/ZnO/Al_2O_3 CATALYST(Hydrogen and Reforming-1)
Yuki Okuhigashi, Toshio Shinoki, Yuichi Sono, Jiro FUNAKI, Katsuya HIRATA
Abstract
Open-access reader
Yuki Okuhigashi, Toshio Shinoki, Yuichi Sono, Jiro FUNAKI, Katsuya HIRATA
Abstract
Open-access reader
In the present study, we reveal the dominant chemical reactions and the optimum conditions, supposing the design of ethanol steam-reforming reactors. Experiments are conducted for Cu/ZnO/Al_2O_3 catalyst. Using a household-use-scale reactor with well-controlled temperature distributions, we compare experimental results with chemical-equilibrium theories. As a result, the Cu/ZnO/Al_2O_3 catalyst shows rather high performance at low values of reaction temperature T. This suggests that the Cu/ZnO/Al_2O_3 catalyst promotes the ethanol-steam-reforming and water-gas-shift reactions, but does not promote the methanation reaction. Furthermore, we specify the effect of steam-carbon molar ratio S/C upon concentrations such as C_ , C_ , C_ and C_ , together with the effect of T upon C_ , C_ , C_ and C_ . In addition, we have researched the influence of liquid-hourly space velocity LHSV upon the ethanol conversion X_ at in the range of LHSV from 0.05 to 1.40h^<-1>, at S/C = 3.0 and T= 420K, 470K and 520K.
A significance statement is not available in the OpenAlex record.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
In the present study, we reveal the dominant chemical reactions and the optimum conditions, supposing the design of ethanol steam-reforming reactors. Experiments are conducted for Cu/ZnO/Al_2O_3 catalyst. Using a household-use-scale reactor with well-controlled temperature distributions, we compare experimental results with chemical-equilibrium theories. As a result, the Cu/ZnO/Al_2O_3 catalyst shows rather high performance at low values of reaction temperature T. This suggests that the Cu/ZnO/Al_2O_3 catalyst promotes the ethanol-steam-reforming and water-gas-shift reactions, but does not promote the methanation reaction. Furthermore, we specify the effect of steam-carbon molar ratio S/C upon concentrations such as C_ , C_ , C_ and C_ , together with the effect of T upon C_ , C_ , C_ and C_ . In addition, we have researched the influence of liquid-hourly space velocity LHSV upon the ethanol conversion X_ at in the range of LHSV from 0.05 to 1.40h^<-1>, at S/C = 3.0 and T= 420K, 470K and 520K.
Key concepts: Steam reforming, Space velocity, Catalysis, Methanation, Hydrogen, Ethanol, Water-gas shift reaction, Molar ratio