TY - JOUR
T1 - A multifunctional Pd/alumina hollow fibre membrane reactor for propane dehydrogenation
AU - Gbenedio, Ejiro
AU - Wu, Zhentao
AU - Hatim, Irfan
AU - Kingsbury, Benjamin F.K.
AU - Li, K.
PY - 2010/10/31
Y1 - 2010/10/31
N2 - Following a successful development of a hollow fibre membrane reactor (HFMR-I) [1], a highly compact multifunctional Pd/alumina hollow fibre membrane reactor (HFMR-II) was further developed and applied to the catalytic dehydrogenation of propane to propene. The developed HFMR-II consists of a thin and defect-free Pd membrane coated directly onto the outer surface of an alumina hollow fibre substrate with a unique asymmetric pore structure, i.e. a sponge-like outer layer and a finger-like inner layer where Pt (1 wt.%)/SBA-15 catalyst is deposited. Benefiting from this novel design, the functionalized alumina hollow fibre substrates with a surface area/volume value of up to 1918.4 m2/m3 possess a catalyst surface area of 31.8 m 2/g, which is significantly higher than that of the HFMR-I in which Pt (0.5 wt.%)/γ-Al2O3 catalyst is deposited. In contrast with a conventional fixed bed reactor (FBR), greater propene selectivity and a one order of magnitude higher space-time yield (STY) have been achieved by using the HFMR-II for propane dehydrogenation. Although the process controlling step in the HFMR-II is believed to be the catalytic reaction, as a consequence of catalyst deactivation due to coke-formation, the advantages of HFMR-II, such as easy catalyst deposition and high catalytic surface area for catalytic reactions, are promising for other catalytic reactions with less coking problems, such as the water-gas-shift (WGS) reaction and steam reforming (SR) etc.
AB - Following a successful development of a hollow fibre membrane reactor (HFMR-I) [1], a highly compact multifunctional Pd/alumina hollow fibre membrane reactor (HFMR-II) was further developed and applied to the catalytic dehydrogenation of propane to propene. The developed HFMR-II consists of a thin and defect-free Pd membrane coated directly onto the outer surface of an alumina hollow fibre substrate with a unique asymmetric pore structure, i.e. a sponge-like outer layer and a finger-like inner layer where Pt (1 wt.%)/SBA-15 catalyst is deposited. Benefiting from this novel design, the functionalized alumina hollow fibre substrates with a surface area/volume value of up to 1918.4 m2/m3 possess a catalyst surface area of 31.8 m 2/g, which is significantly higher than that of the HFMR-I in which Pt (0.5 wt.%)/γ-Al2O3 catalyst is deposited. In contrast with a conventional fixed bed reactor (FBR), greater propene selectivity and a one order of magnitude higher space-time yield (STY) have been achieved by using the HFMR-II for propane dehydrogenation. Although the process controlling step in the HFMR-II is believed to be the catalytic reaction, as a consequence of catalyst deactivation due to coke-formation, the advantages of HFMR-II, such as easy catalyst deposition and high catalytic surface area for catalytic reactions, are promising for other catalytic reactions with less coking problems, such as the water-gas-shift (WGS) reaction and steam reforming (SR) etc.
KW - Alumina hollow fibre
KW - Asymmetric structure
KW - Dehydrogenation of propane
KW - Membrane reactor
KW - Pd membrane
KW - SBA-15
UR - http://www.scopus.com/inward/record.url?scp=77958089833&partnerID=8YFLogxK
UR - https://www.sciencedirect.com/science/article/pii/S0920586110003469?via%3Dihub
U2 - 10.1016/j.cattod.2010.04.044
DO - 10.1016/j.cattod.2010.04.044
M3 - Article
AN - SCOPUS:77958089833
SN - 0920-5861
VL - 156
SP - 93
EP - 99
JO - Catalysis Today
JF - Catalysis Today
IS - 3-4
ER -