Pd-Ag membrane reactor for steam reforming reactions: a comparison between different fuels

F. Gallucci; A. Basile

doi:10.1016/j.ijhydene.2008.01.010

Pd-Ag membrane reactor for steam reforming reactions: a comparison between different fuels

F. Gallucci, A. Basile

Research output: Contribution to journal › Article › Academic › peer-review

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Abstract

The simulation of a dense Pd-based membrane reactor for carrying out the methane, the methanol and the ethanol steam reforming (SR) reactions for pure hydrogen production is performed. The same simulation is also performed in a traditional reactor. This modelling work shows that the use of membrane reactor is effective for carrying out the methane SR reaction, giving in the best conditions a conversion increase of 800% with respect to a traditional system, and can be really useful for carrying out the methanol SR reaction (25% conversion increase). Vice versa, the use of the membrane reactor in the ethanol SR reaction is still affected by the low catalytic activity. However, also for the ethanol SR reaction system, the use of the membrane reactor gives an increase of the ethanol conversion (30%) and a relatively high increase of the hydrogen yield. & 2008 International Association for Hydrogen Energy

Original language	Undefined
Pages (from-to)	1671-1687
Number of pages	16
Journal	International journal of hydrogen energy
Volume	33
Issue number	6
DOIs	https://doi.org/10.1016/j.ijhydene.2008.01.010
Publication status	Published - 2008

Keywords

IR-67399
METIS-254272

Access to Document

10.1016/j.ijhydene.2008.01.010

Cite this

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title = "Pd-Ag membrane reactor for steam reforming reactions: a comparison between different fuels",

abstract = "The simulation of a dense Pd-based membrane reactor for carrying out the methane, the methanol and the ethanol steam reforming (SR) reactions for pure hydrogen production is performed. The same simulation is also performed in a traditional reactor. This modelling work shows that the use of membrane reactor is effective for carrying out the methane SR reaction, giving in the best conditions a conversion increase of 800{\%} with respect to a traditional system, and can be really useful for carrying out the methanol SR reaction (25{\%} conversion increase). Vice versa, the use of the membrane reactor in the ethanol SR reaction is still affected by the low catalytic activity. However, also for the ethanol SR reaction system, the use of the membrane reactor gives an increase of the ethanol conversion (30{\%}) and a relatively high increase of the hydrogen yield. & 2008 International Association for Hydrogen Energy",

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AU - Basile, A.

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AB - The simulation of a dense Pd-based membrane reactor for carrying out the methane, the methanol and the ethanol steam reforming (SR) reactions for pure hydrogen production is performed. The same simulation is also performed in a traditional reactor. This modelling work shows that the use of membrane reactor is effective for carrying out the methane SR reaction, giving in the best conditions a conversion increase of 800% with respect to a traditional system, and can be really useful for carrying out the methanol SR reaction (25% conversion increase). Vice versa, the use of the membrane reactor in the ethanol SR reaction is still affected by the low catalytic activity. However, also for the ethanol SR reaction system, the use of the membrane reactor gives an increase of the ethanol conversion (30%) and a relatively high increase of the hydrogen yield. & 2008 International Association for Hydrogen Energy

KW - IR-67399

KW - METIS-254272

U2 - 10.1016/j.ijhydene.2008.01.010

DO - 10.1016/j.ijhydene.2008.01.010

M3 - Article

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EP - 1687

JO - International journal of hydrogen energy

JF - International journal of hydrogen energy

SN - 0360-3199

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