scholarly journals Selective CO Methanation on Highly Active Ru/TiO2 Catalysts: Identifying the Physical Origin of the Observed Activation/Deactivation and Loss in Selectivity

ACS Catalysis ◽  
2018 ◽  
Vol 8 (6) ◽  
pp. 5399-5414 ◽  
Author(s):  
Ali M. Abdel-Mageed ◽  
Daniel Widmann ◽  
Sine E. Olesen ◽  
Ib Chorkendorff ◽  
R. Jürgen Behm
2019 ◽  
Vol 58 (31) ◽  
pp. 10732-10736 ◽  
Author(s):  
Shilong Chen ◽  
Ali M. Abdel‐Mageed ◽  
Dan Li ◽  
Joachim Bansmann ◽  
Sebastian Cisneros ◽  
...  

2018 ◽  
Vol 148 (11) ◽  
pp. 3502-3513 ◽  
Author(s):  
David O. Kumi ◽  
Mbongiseni W. Dlamini ◽  
Tumelo N. Phaahlamohlaka ◽  
Sabelo D. Mhlanga ◽  
Neil J. Coville ◽  
...  

2018 ◽  
Vol 232 ◽  
pp. 492-500 ◽  
Author(s):  
David O. Kumi ◽  
Tumelo N. Phaahlamohlaka ◽  
Mbongiseni W. Dlamini ◽  
Ian T. Mangezvo ◽  
Sabelo D. Mhlanga ◽  
...  

Energies ◽  
2020 ◽  
Vol 13 (11) ◽  
pp. 2844 ◽  
Author(s):  
Panagiota Garbis ◽  
Andreas Jess

Polymer electrolyte membrane fuel cells (PEMFCs) are often used for household applications, utilizing hydrogen produced from natural gas from the gas grid. The hydrogen is thereby produced by steam reforming of natural gas followed by a water gas shift (WGS) unit. The H2-rich gas contains besides CO2 small amounts of CO, which deactivates the catalyst used in the PEMFCs. Preferential oxidation has so far been a reliable process to reduce this concentration but valuable H2 is also partly converted. Selective CO methanation considered as an attractive alternative. However, CO2 methanation consuming the valuable H2 has to be minimized. The modelling of selective CO methanation in a household fuel cell system is presented. The simulation was conducted for single and two-stage adiabatic fixed bed reactors (in the latter case with intermediate cooling), and the best operating conditions to achieve the required residual CO content (100 ppm) were calculated. This was done by varying the gas inlet temperature as well as the mass of the catalyst. The feed gas represented a reformate gas downstream of a typical WGS reaction unit (0.5%–1% CO, 10%–25% CO2, and 5%–20% H2O (rest H2)).


2013 ◽  
Vol 452 ◽  
pp. 174-178 ◽  
Author(s):  
Kohei Urasaki ◽  
Yuta Tanpo ◽  
Yuta Nagashima ◽  
Ryuji Kikuchi ◽  
Shigeo Satokawa

2017 ◽  
Vol 147 (5) ◽  
pp. 1172-1180 ◽  
Author(s):  
Lin Zhang ◽  
Dong-Xue Gu ◽  
Yi liu ◽  
Yi Zhang

2011 ◽  
Vol 404 (1-2) ◽  
pp. 149-154 ◽  
Author(s):  
Shohei Tada ◽  
Ryuji Kikuchi ◽  
Kohei Urasaki ◽  
Shigeo Satokawa

ACS Catalysis ◽  
2015 ◽  
Vol 5 (11) ◽  
pp. 6753-6763 ◽  
Author(s):  
Ali M. Abdel-Mageed ◽  
D. Widmann ◽  
S. E. Olesen ◽  
I. Chorkendorff ◽  
J. Biskupek ◽  
...  

2015 ◽  
Vol 251 ◽  
pp. 81-87 ◽  
Author(s):  
Toshihiro Miyao ◽  
Junya Tanaka ◽  
Weihua Shen ◽  
Katsuhiko Hayashi ◽  
Kazutoshi Higashiyama ◽  
...  

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