Hydrogen production from the steam reforming of bio-butanol over novel supported Co-based bimetallic catalysts

2012 ◽  
Vol 107 ◽  
pp. 482-486 ◽  
Author(s):  
Weijie Cai ◽  
Pilar Ramirez de la Piscina ◽  
Narcis Homs
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Bimetallic Catalysts

Ni-Cu bimetallic catalysts on Yttria-stabilized zirconia for hydrogen production from ethanol steam reforming

Fuel ◽  
2020 ◽  
Vol 280 ◽  
pp. 118612
Author(s):  
Fangyuan Chen ◽  
Yongwen Tao ◽  
Huajuan Ling ◽  
Cuifeng Zhou ◽  
Zongwen Liu ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Bimetallic Catalysts ◽  
Yttria Stabilized Zirconia ◽  
Ethanol Steam Reforming ◽  
Stabilized Zirconia ◽  
Ethanol Steam

Steam Reforming of Bio-Oil for Hydrogen Production: Effect of Ni-Co Bimetallic Catalysts

2011 ◽  
Vol 35 (2) ◽  
pp. 302-308 ◽  
Author(s):  
Y. Zhang ◽  
W. Li ◽  
S. Zhang ◽  
Q. Xu ◽  
Y. Yan
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Bimetallic Catalysts ◽  
Production Effect ◽  
Bio Oil

scholarly journals Hydrogen production from steam reforming of acetic acid over Pt–Ni bimetallic catalysts supported on ZrO2

2022 ◽  
Vol 156 ◽  
pp. 106317
Author(s):  
Isabella C.A. Souza ◽  
Robinson L. Manfro ◽  
Mariana M.V.M. Souza
Keyword(s):  
Acetic Acid ◽  
Hydrogen Production ◽  
Steam Reforming ◽  
Bimetallic Catalysts

Hydrogen Production from Acetic Acid Steam Reforming over Bimetallic Ni-Co on La2O3 Catalyst-Effect of the Catalyst Dilution

2014 ◽  
Vol 493 ◽  
pp. 39-44 ◽  
Author(s):  
Tuan Amran Tuan Abdullah ◽  
Walid Nabgan ◽  
Mohd Johari Kamaruddin ◽  
Ramli Mat ◽  
Anwar Johari ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Hydrogen Production ◽  
Steam Reforming ◽  
Atmospheric Pressure ◽  
Bimetallic Catalysts ◽  
Fixed Bed ◽  
Fixed Bed Reactor ◽  
Product Gas ◽  
Catalyst Effect ◽  
Catalytic Steam Reforming

Catalytic steam reforming of acetic acid using bimetallic catalysts of 5 wt.% nickel and 5 wt.% cobalt supported on Lanthanum (III) oxide (La2O3) for hydrogen production was investigated in a micro fixed bed reactor. The reactor was of quartz tube with a 10 mm inside diameter. The effect of catalyst dilution on the reaction was studied. Silicon carbide was used as the dilution material. The experiments were conducted at atmospheric pressure and temperatures ranging from 500 to 700°C. The complete conversion of acetic acid to product gases has been observed at 550°C and 700°C for diluted and non-diluted catalysts respectively. It shows that catalyst dilution had a profound effect on the conversion of acetic acid at low temperature (550°C) whilst high temperature of 700°C was required for the non-diluted catalyst. The product gas distributions are similar when using both diluted and non-diluted catalysts.

Pure Hydrogen Production from Steam Reforming of Bio-Sources

2015 ◽  
Vol 2 (2) ◽  
pp. 48-56 ◽  
Author(s):  
A. Iulianelli ◽  
◽  
G. Bagnato ◽  
A. Iulianelli ◽  
A. Vita Vita ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Pure Hydrogen

Hydrogen production for fuel cells via steam reforming of dimethyl ether over commercial Cu/ZnO/Al2O3 and zeolite

2012 ◽  
Vol 187 ◽  
pp. 299-305 ◽  
Author(s):  
Jing Li ◽  
Qi-Jian Zhang ◽  
Xu Long ◽  
Ping Qi ◽  
Zhao-Tie Liu ◽  
...  
Keyword(s):  
Fuel Cells ◽  
Hydrogen Production ◽  
Dimethyl Ether ◽  
Steam Reforming

Hydrogen production by steam reforming of ethanol over Ni/Al 2 O 3 -La 2 O 3 xerogel catalysts

2017 ◽  
Vol 434 ◽  
pp. 123-133 ◽  
Author(s):  
Ji Hwan Song ◽  
Sangbeom Yoo ◽  
Jaekyeong Yoo ◽  
Seungwon Park ◽  
Min Yeong Gim ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Steam Reforming Of Ethanol
Sign in / Sign up

Export Citation Format

Share Document