The antagonist effect of pressure on the thermodynamic equilibrium and the H2 permeation rate has been studied in a small-scale membrane reactor (MR) with no sweep gas. The influence of some design parameters as membrane surface area (Am), catalyst volume (Vcat), methane load in feed (Ls) and gas hourly space velocity (GHSV) on theMRperformance has also been evaluated.

Pd/Ag based Membrane Reactors on small scale: assessment on the high pressure importance and design parameters

Chiappetta G;Barbieri G;Drioli E
2010

Abstract

The antagonist effect of pressure on the thermodynamic equilibrium and the H2 permeation rate has been studied in a small-scale membrane reactor (MR) with no sweep gas. The influence of some design parameters as membrane surface area (Am), catalyst volume (Vcat), methane load in feed (Ls) and gas hourly space velocity (GHSV) on theMRperformance has also been evaluated.
2010
Istituto per la Tecnologia delle Membrane - ITM
Membrane reactor
Methane steam reforming
Pd-based membrane
Hydrogen production
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/28925
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