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
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.