Hydrogen production by the catalytic steam reforming of methanol: Part 3: Kinetics of methanol decomposition using C18HC catalyst

1988 ◽  
Vol 66 (6) ◽  
pp. 950-956 ◽  
Author(s):  
J. C. Amphlett ◽  
R. F. Mann ◽  
R. D. Weir
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Methanol Decomposition ◽  
Steam Reforming Of Methanol ◽  
Catalytic Steam Reforming ◽  
Kinetics Of

Hydrogen production by the catalytic steam reforming of methanol part 1: The thermodynamics

1981 ◽  
Vol 59 (6) ◽  
pp. 720-727 ◽  
Author(s):  
J. C. Amphlett ◽  
M. J. Evans ◽  
R. A. Jones ◽  
R. F. Mann ◽  
R. D. Weir
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Steam Reforming Of Methanol ◽  
Catalytic Steam Reforming

Synthesis of CuO/ZnO/Al2O3/ZrO2/CeO2 nanocatalysts via homogeneous precipitation and combustion methods used in methanol steam reforming for fuel cell grade hydrogen production

RSC Advances ◽  
2016 ◽  
Vol 6 (62) ◽  
pp. 57199-57209 ◽  
Author(s):  
Saeed Khajeh Talkhoncheh ◽  
Mohammad Haghighi ◽  
Shahab Minaei ◽  
Hossein Ajamein ◽  
Mozaffar Abdollahifar
Keyword(s):  
Fuel Cell ◽  
Hydrogen Production ◽  
Steam Reforming ◽  
Synthesis Method ◽  
Methanol Steam Reforming ◽  
Homogeneous Precipitation ◽  
Steam Reforming Of Methanol

In this research the effects of synthesis method and CeO2 and ZrO2 promoters were studied in the steam reforming of methanol over a CuO/ZnO/Al2O3 nanocatalyst. Addition of ZrO2 and CeO2 reduces CO selectivity, while CeO2 is more effective.

Catalytic steam reforming of simulated bio-oil for green hydrogen production using highly active LaNixCo1-xO3 perovskite catalyst

2022 ◽  
Author(s):  
Piyush Pratap Singh ◽  
Neelkanth Nirmalkar ◽  
Tarak Mondal
Keyword(s):  
Hydrogen Production ◽  
Waste Management ◽  
Steam Reforming ◽  
Energy Production ◽  
Sustainable Energy ◽  
Agricultural Waste ◽  
Perovskite Catalyst ◽  
Highly Active ◽  
Bio Oil ◽  
Catalytic Steam Reforming

Catalytic steam reforming (SR) of agricultural waste derived bio-oil for hydrogen production is a unique technology, offering twin benefits of waste management as well as sustainable energy production. In the...

Hydrogen production from oxidative steam reforming of methanol: Effect of the Cu and Ni impregnation on ZrO2 and their molecular simulation studies

2012 ◽  
Vol 37 (11) ◽  
pp. 9018-9027 ◽  
Author(s):  
P. López ◽  
G. Mondragón-Galicia ◽  
M.E. Espinosa-Pesqueira ◽  
D. Mendoza-Anaya ◽  
Ma.E. Fernández ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Molecular Simulation ◽  
Steam Reforming ◽  
Simulation Studies ◽  
Steam Reforming Of Methanol

Hydrogen production from catalytic steam reforming of glycerol over various supported nickel catalysts

2017 ◽  
Vol 42 (14) ◽  
pp. 9087-9098 ◽  
Author(s):  
Nurul Huda Zamzuri ◽  
Ramli Mat ◽  
Nor Aishah Saidina Amin ◽  
Amin Talebian-Kiakalaieh
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Supported Nickel Catalysts ◽  
Catalytic Steam Reforming

scholarly journals Catalytic Steam Reforming of Glycerol Over Cerium and Palladium-Based Catalysts for Hydrogen Production

2013 ◽  
Vol 10 (2) ◽  
Author(s):  
Ali Ebshish ◽  
Zahira Yaakob ◽  
Y. H. Taufiq-Yap ◽  
Ahmed Bshish ◽  
Abdulmajid Shaibani
Keyword(s):  
Electron Microscopy ◽  
Hydrogen Production ◽  
Steam Reforming ◽  
Catalytic Reactions ◽  
Fixed Bed Reactor ◽  
Hydrogen Yield ◽  
Water Mixture ◽  
Impregnation Method ◽  
Catalytic Steam Reforming ◽  
Total Average

In this work, catalytic steam reforming of glycerol for hydrogen production was performed over Ce/Al2O3 and Pd/Al2O3 catalysts prepared via the impregnation method. The catalysts were characterized by scanning electron microscopy (SEM-EDX), transmission electron microscopy (TEM), BET surface area, and X-ray diffraction (XRD). Two sets of catalytic reactions were conducted, one comparing 1% Pd/Al2O3 to 1% Ce/Al2O3 and the second comparing 1% Ce/Al2O3 loading to 10% Ce/Al2O3 loading. All catalytic reactions were performed using a fixed-bed reactor operated at 600 °C and atmospheric pressure. Aglycerol–water mixture at a molar ratio of 1:6 was fed to the reactor at 0.05 ml/min. In the first set of experiments, Pd/Al2O3 exhibited higher hydrogen productivity than Ce/Al2O3. A maximum hydrogen yield of 56% and a maximum selectivity of 78.7% were achieved over the Pd/Al2O3 catalyst. For the second set of experiments, the results show that the reaction conversion increased as the cerium loading increased from 1% to 10%. A total average hydrogen yield of 28.0% and a selectivity of 45.5% were obtained over 1% Ce/Al2O3, while the total average hydrogen yield and selectivity were 42.2% and 52.7%, respectively, for 10% Ce/Al2O3.

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