This study concerns palladium membrane reactors for methane steam reforming by means of mathematical modeling. In terms of similarity in reaction rate profiles, a whole reactor can be divided into three zones: I common to conventional and membrane reactors; II common to the co-current and counter-current membrane reactors; III characteristic of the counter-current membrane reactors. Although reaction rate decreased from the inlet in zones I and II, it increased in zone III. Furthermore, a part with apparently slow reaction and permeation was found in the profile for counter-current long reactor. The part is the end of zone II, which is normally seen in a co-current MR. It locates at the end of reactor in a co-current, however, in the middle of the reactor in a counter-current.

Reaction rate profiles in long palladium membrane reactors for methane steam reforming

Barbieri G;Drioli E
2008

Abstract

This study concerns palladium membrane reactors for methane steam reforming by means of mathematical modeling. In terms of similarity in reaction rate profiles, a whole reactor can be divided into three zones: I common to conventional and membrane reactors; II common to the co-current and counter-current membrane reactors; III characteristic of the counter-current membrane reactors. Although reaction rate decreased from the inlet in zones I and II, it increased in zone III. Furthermore, a part with apparently slow reaction and permeation was found in the profile for counter-current long reactor. The part is the end of zone II, which is normally seen in a co-current MR. It locates at the end of reactor in a co-current, however, in the middle of the reactor in a counter-current.
2008
Istituto per la Tecnologia delle Membrane - ITM
Membrane reactor
Methane steam reforming
Palladiummembrane
Counter-current mode
Reaction rate
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/35032
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