Membrane performance: the key issues for dehydrogenation reactions in a catalytic membrane reactor

Citation
H. Weyten et al., Membrane performance: the key issues for dehydrogenation reactions in a catalytic membrane reactor, CATAL TODAY, 56(1-3), 2000, pp. 3-11
Citations number
21
Categorie Soggetti
Physical Chemistry/Chemical Physics
Journal title
CATALYSIS TODAY
ISSN journal
09205861 → ACNP
Volume
56
Issue
1-3
Year of publication
2000
Pages
3 - 11
Database
ISI
SICI code
0920-5861(20000225)56:1-3<3:MPTKIF>2.0.ZU;2-S
Abstract
In a high-temperature membrane reactor, one of the reaction products is sel ectively removed from the reaction mixture, thus preventing the mixture fro m reaching equilibrium. In a previous study [I], a CVI-silica membrane was used for the direct dehydrogenation of propane in a high-temperature cataly tic membrane reactor This H-2 selective membrane had only a moderate permea tion (similar to 140 x 10(-9) mol/m(2)Pa s) and a limited H-2/C3H8 permsele ctivity (alpha(0) approximate to 70-90 at 500 degrees C). These experiments proved that (at 500 degrees C) the propane conversion could be improved fr om the equilibrium value (similar to 18%) to a value which is about twice a s high. The increase was however only significant for relatively small valu es of the propane feed stream less than or equal to 16.5 mu mol/s. This is because at high propane feed, the hydrogen cannot be removed fast enough th rough the membrane and conversion is again limited by the thermodynamic equ ilibrium. In this study, the comparison is made between the performance of the CVI-silica membrane and a Pd/Ag membrane when used as the H-2 selective membrane. The performance of the Pd/Ag membrane is far superior to the per formance of the SiO2 membrane. H-2 fluxes of more than 0.1 mol/m(2)s were m easured and the H-2/Ar permselectivity exceeds 4500. When it is run under c omparable conditions, the performance of the Pd/Ag membrane reactor is much better. The increase in propane conversion persists at values of the propa ne feed stream that are about six times higher (105 mu mol/s). Since the: H-2 is selectively removed from the reaction mixture, it is not available for any competitive side reactions. The production of methane, wh ich limits the propene selectivity of the reaction in a conventional plug-f low reactor, is much less in a catalytic membrane reactor. This means that the selectivity in the membrane reactor is higher than in the plug-flow rea ctor when they are fun under similar conditions. (C) 2000 Elsevier Science B.V. All rights reserved.