H2 production by low pressure methane steam reforming in a Pd–Ag membrane reactor over a Ni-based catalyst: Experimental and modeling

2010 ◽  
Vol 35 (20) ◽  
pp. 11514-11524 ◽  
Author(s):  
A. Iulianelli ◽  
G. Manzolini ◽  
M. De Falco ◽  
S. Campanari ◽  
T. Longo ◽  
...  
Keyword(s):  
Steam Reforming ◽  
Membrane Reactor ◽  
Low Pressure ◽  
H2 Production ◽  
Methane Steam Reforming ◽  
Methane Steam

Methane steam reforming in a Pd-Ru membrane reactor

2000 ◽  
Vol 17 (3) ◽  
pp. 288-291 ◽  
Author(s):  
Suk Woo Nam ◽  
Sung Pil Yoon ◽  
Heung Yong Ha ◽  
Seong-Ahn Hong ◽  
Anatoly P. Maganyuk
Keyword(s):  
Steam Reforming ◽  
Membrane Reactor ◽  
Methane Steam Reforming ◽  
Methane Steam

Methane Steam Reforming in a Zirconia Membrane Reactor

2006 ◽  
Vol 39 (4) ◽  
pp. 444-447 ◽  
Author(s):  
Katsuki Kusakabe ◽  
Hitomi Mizoguchi
Keyword(s):  
Steam Reforming ◽  
Membrane Reactor ◽  
Methane Steam Reforming ◽  
Methane Steam ◽  
Zirconia Membrane

Effect of Catalytic Distribution on the Performance of Microreactor for Hydrogen Production through Methane Steam Reforming

2010 ◽  
Vol 156-157 ◽  
pp. 873-876 ◽  
Author(s):  
Feng Wang ◽  
Zi Long An ◽  
Bo Qi ◽  
Jing Zhou
Keyword(s):  
Steam Reforming ◽  
Active Sites ◽  
Flow Direction ◽  
Space Velocity ◽  
H2 Production ◽  
Methane Steam Reforming ◽  
Reactor Performance ◽  
Methane Steam ◽  
Site Density ◽  
Availability Ratio

The effect of catalyst coating distributing on the reactor performance for methane steam reforming(MSR) was numerically investigated. In calculation, the amount catalyst loaded on the microreactor wall was fixed but the catalyst active site density was distributed according to arithmetic progression along the flow direction. Results show that it is possible to get the higher conversion of CH4 and output of H2 due to the higher availability ratio of catalyst surface active sites at this distribution. And this distribution effect is more remarkable at higher space velocity or lower reaction temperature, however, there exists an optimal distribution which can reach the highest CH4 conversion and H2 production at 900K.

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