Abstract
Numerical and experimental study is performed to evaluate the reactant by-pass flow in a catalytic plate reactor with a coated wire mesh catalyst for steam reforming of methane for hydrogen generation. By-pass of unconverted methane is evaluated under different wire mesh catalyst width to reactor duct width ratios, the results show that altering this ratio from 0.98 to 0.96 results in an increase in by-pass mass flow of 22%. Effect of catalytic wire mesh flow resistance on by-pass flow has also been investigated and results show increased by-pass flow as catalytic wire mesh flow resistance increases. The numerical results are in good agreement with experimental data. The study improves the understanding of the underlying transport phenomena in these reactors and shows that the flow maldistribution in a catalytic plate reactor using a coated wire mesh has to be considered.
Originalsprog | Engelsk |
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Titel | Proceedings of ASME 2011 5th International Conference on Energy Sustainability & 9th Fuel Cell Science, Engineering and Technology Conference : ESFuelCell2011 |
Antal sider | 9 |
Forlag | American Society of Mechanical Engineers |
Publikationsdato | 7 aug. 2011 |
ISBN (Trykt) | 978-0-7918-5469-3 |
Status | Udgivet - 7 aug. 2011 |
Begivenhed | ASME 2011 9th Fuel Cell Science, Engineering and Technology Conference - Washington, DC, USA Varighed: 7 aug. 2011 → 10 aug. 2011 |
Konference
Konference | ASME 2011 9th Fuel Cell Science, Engineering and Technology Conference |
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Land/Område | USA |
By | Washington, DC |
Periode | 07/08/2011 → 10/08/2011 |