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Methane steam reforming in a Pd-Ag membrane reformer: an experimental study on the reaction pressure influence at middle temperature (Articolo in rivista)
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- Label
- Methane steam reforming in a Pd-Ag membrane reformer: an experimental study on the reaction pressure influence at middle temperature (Articolo in rivista) (literal)
- Anno
- 2011-01-01T00:00:00+01:00 (literal)
- Alternative label
A. Basile1, S. Campanari2, G. Manzolini2, A. Iulianelli1, T. Longo1, S. Liguori1,3, M. De Falco4, V. Piemonte5 (2011)
Methane steam reforming in a Pd-Ag membrane reformer: an experimental study on the reaction pressure influence at middle temperature
in International journal of hydrogen energy
(literal)
- Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#autori
- A. Basile1, S. Campanari2, G. Manzolini2, A. Iulianelli1, T. Longo1, S. Liguori1,3, M. De Falco4, V. Piemonte5 (literal)
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- ISI Web of Science (WOS) (literal)
- Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#affiliazioni
- 1. Institute on Membrane Technology of Italian National Research Council (ITM-CNR), Via P. Bucci, c/o University of Calabria Cubo 17/C, 87036 Rende (CS), Italy
2. Politecnico di Milano, Department of Energy, via Lambruschini 4, Milano (MI) 20156, Italy
3. University of Calabria, Department of Engineering Modeling, University of Calabria, via Pietro Bucci, Cubo 39/C, 87030 Rende (CS), Italy
4. University Campus Bio-Medico of Rome, Faculty of Engineering, via Alvaro del Portillo 21, 00128 Rome, Italy
5. University of Rome La Sapienza, Department of Chemical Eng. Materials & Environment, via Eudossiana 18, 00184 Rome, Italy
(literal)
- Titolo
- Methane steam reforming in a Pd-Ag membrane reformer: an experimental study on the reaction pressure influence at middle temperature (literal)
- Abstract
- In this experimental work, methane steam reforming (MSR) reaction is performed in
a dense Pd-Ag membrane reactor and the influence of pressure on methane conversion,
COx-free hydrogen recovery and COx-free hydrogen production is investigated. The reaction is conducted at 450 _C by supplying nitrogen as a sweep gas in co-current flow
configuration with respect to the reactants. Three experimental campaigns are realized in
the MR packed with Ni-ZrO catalyst, which showed better performances than Ni-Al2O3
used in a previous paper dealing with the same MR system. The first one is directed to keep
constant the total pressure in both retentate and permeate sides of the membrane reactor.
In the second case study, the total retentate pressure is kept constant at 9.0 bar, while the
total permeate pressure is varied between 5.0 and 9.0 bar. As the best result of this work, at
450 _C and 4.0 bar of total pressure difference between retentate and permeate sides,
around 65% methane conversion and 1.2 l/h of COx-free hydrogen are reached, further
recovering 80% COx-free hydrogen over the total hydrogen produced during the reaction.
Moreover, a study on the influence of hydrogen-rich gas mixtures on the hydrogen
permeation through the Pd-Ag membrane is also performed and discussed. (literal)
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