TY - JOUR
T1 - Combination of a Two-Zone Fluidized Bed Reactor with a Pd hollow fibre membrane for catalytic alkane dehydrogenation
AU - Gimeno, M. P.
AU - Wu, Z. T.
AU - Soler, J.
AU - Herguido, J.
AU - Li, K.
AU - Menéndez, M.
PY - 2009/12/1
Y1 - 2009/12/1
N2 - The combination of a Pd hollow fibre membrane with a Two-Zone Fluidized Bed Reactor (TZFBR) is described for catalytic dehydrogenation of propane. This configuration aims to combine the in situ catalyst regeneration provided by the TZFBR with the increased conversion that can be achieved with a Pd membrane, which removes hydrogen from the reactor, thus enhancing the reaction rate and in theory allowing even higher than equilibrium conversion. The experiments show that the Pd hollow fibre membrane acts effectively removing hydrogen from the reaction media and that with a Pt-Sn/Al2O3 catalyst the TZFBR can achieve steady state operation in spite of the increased coking of the catalyst. However, with this catalyst the quicker coke formation caused by the removal of hydrogen outweighs the beneficial effect of hydrogen removal and the yield achievable for a given feed is lower in the presence of the membrane. A conclusion from these results is that a catalyst with lower coke tendency is needed to apply this combination of Pd membrane and TZFBR.
AB - The combination of a Pd hollow fibre membrane with a Two-Zone Fluidized Bed Reactor (TZFBR) is described for catalytic dehydrogenation of propane. This configuration aims to combine the in situ catalyst regeneration provided by the TZFBR with the increased conversion that can be achieved with a Pd membrane, which removes hydrogen from the reactor, thus enhancing the reaction rate and in theory allowing even higher than equilibrium conversion. The experiments show that the Pd hollow fibre membrane acts effectively removing hydrogen from the reaction media and that with a Pt-Sn/Al2O3 catalyst the TZFBR can achieve steady state operation in spite of the increased coking of the catalyst. However, with this catalyst the quicker coke formation caused by the removal of hydrogen outweighs the beneficial effect of hydrogen removal and the yield achievable for a given feed is lower in the presence of the membrane. A conclusion from these results is that a catalyst with lower coke tendency is needed to apply this combination of Pd membrane and TZFBR.
KW - Membrane reactor
KW - Pd hollow fibre membrane
KW - Propane dehydrogenation
KW - Two-Zone Fluidized Bed Reactor
UR - http://www.scopus.com/inward/record.url?scp=71549126241&partnerID=8YFLogxK
UR - https://www.sciencedirect.com/science/article/pii/S1385894709004835?via%3Dihub
U2 - 10.1016/j.cej.2009.06.037
DO - 10.1016/j.cej.2009.06.037
M3 - Article
AN - SCOPUS:71549126241
SN - 1385-8947
VL - 155
SP - 298
EP - 303
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
IS - 1-2
ER -