TY - JOUR
T1 - N2, He and CO2 diffusion mechanism through nanoporous YSZ/γ-Al2O3 layers and their use in a pore-filled membrane for hydrogen membrane reactors
AU - Arratibel, Alba
AU - Astobieta, Uxue
AU - Pacheco Tanaka, David Alfredo
AU - Van Sint Annaland, Martin
AU - Gallucci, Fausto
N1 - Publisher Copyright:
© 2015 Hydrogen Energy Publications LLC.
PY - 2016/6/1
Y1 - 2016/6/1
N2 - Nanoporous ceramic supports for pore filled membranes were prepared on ceramic supports (α-Al2O3) with pore size of 100 nm by adding additional layers with different proportions of YSZ/γ-Al2O3 (ranging from 50% to 90% of YSZ) by dip-coating and the effect of different parameters in the preparation method have been investigated. The diffusion mechanisms of N2, He and CO2 through the supported nanoporous layers have been studied in detail with permeation measurements at a temperature range of 50-400°C and pressure difference of 30-100 kPa. It was observed that as the amount of γ-Al2O3 in the nanoporous layers increases, the adsorption of CO2 is favored at low temperatures and pressures. Finally, a pore-filled Pd/YSZ/γ-Al2O3 (60 wt%YSZ-40 wt. γ-Al2O3) membrane was successfully prepared and its permeation performance was tested over 900 h at 500 and 550 C, showing relatively low ideal H2/N2 perm-selectivity of about 50 due to low hydrogen flux.
AB - Nanoporous ceramic supports for pore filled membranes were prepared on ceramic supports (α-Al2O3) with pore size of 100 nm by adding additional layers with different proportions of YSZ/γ-Al2O3 (ranging from 50% to 90% of YSZ) by dip-coating and the effect of different parameters in the preparation method have been investigated. The diffusion mechanisms of N2, He and CO2 through the supported nanoporous layers have been studied in detail with permeation measurements at a temperature range of 50-400°C and pressure difference of 30-100 kPa. It was observed that as the amount of γ-Al2O3 in the nanoporous layers increases, the adsorption of CO2 is favored at low temperatures and pressures. Finally, a pore-filled Pd/YSZ/γ-Al2O3 (60 wt%YSZ-40 wt. γ-Al2O3) membrane was successfully prepared and its permeation performance was tested over 900 h at 500 and 550 C, showing relatively low ideal H2/N2 perm-selectivity of about 50 due to low hydrogen flux.
KW - Hydrogen separation
KW - Membrane preparation
KW - Pore-filled membranes
KW - Porous supports
UR - http://www.scopus.com/inward/record.url?scp=84951964257&partnerID=8YFLogxK
U2 - 10.1016/j.ijhydene.2015.11.152
DO - 10.1016/j.ijhydene.2015.11.152
M3 - Article
AN - SCOPUS:84951964257
SN - 0360-3199
VL - 41
SP - 8732
EP - 8744
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
IS - 20
ER -