TY - JOUR
T1 - Ni/SBA-15 Catalysts for combined steam methane reforming and water gas shift - Prepared for use in catalytic membrane reactors
AU - Gouveia Gil, Ana
AU - Wu, Zhentao
AU - Chadwick, David
AU - Li, K.
PY - 2015/10/5
Y1 - 2015/10/5
N2 - This study focuses on the preparation, characterization and catalytic performance evaluation of Ni/SBA-15 catalysts for the combined steam methane reforming (SMR) and water gas shift (WGS) reaction. Specific efforts have been directed towards the impact of the SBA-15 preparation methods on further incorporating the resultant catalysts into the micro-structured ceramic hollow fibres for the development of more advanced membrane reactors. The effect of Ni loading (5-25 wt.%) on the catalytic performance was investigated using the SBA-15 prepared via a sol-gel method. Furthermore, the effect of SBA-15 preparation methods (sol-gel and hydrothermal methods) on the catalyst properties and performance were also systematically investigated in a packed-bed reactor, using a fixed Ni loading of 25 wt.%. For the purpose of comparison, a commercially available SBA-15 powder was also employed. Apart from the different distribution and particle size of Ni, the interaction between Ni and SBA-15 is considered as the major reason for the difference in catalytic performance.
AB - This study focuses on the preparation, characterization and catalytic performance evaluation of Ni/SBA-15 catalysts for the combined steam methane reforming (SMR) and water gas shift (WGS) reaction. Specific efforts have been directed towards the impact of the SBA-15 preparation methods on further incorporating the resultant catalysts into the micro-structured ceramic hollow fibres for the development of more advanced membrane reactors. The effect of Ni loading (5-25 wt.%) on the catalytic performance was investigated using the SBA-15 prepared via a sol-gel method. Furthermore, the effect of SBA-15 preparation methods (sol-gel and hydrothermal methods) on the catalyst properties and performance were also systematically investigated in a packed-bed reactor, using a fixed Ni loading of 25 wt.%. For the purpose of comparison, a commercially available SBA-15 powder was also employed. Apart from the different distribution and particle size of Ni, the interaction between Ni and SBA-15 is considered as the major reason for the difference in catalytic performance.
KW - Micro-structured ceramic hollow fibre
KW - Ni/SBA-15 catalyst
KW - Steam methane reforming
KW - Water-gas shift
UR - http://www.scopus.com/inward/record.url?scp=84941991950&partnerID=8YFLogxK
UR - https://www.sciencedirect.com/science/article/pii/S0926860X15301423?via%3Dihub
U2 - 10.1016/j.apcata.2015.09.009
DO - 10.1016/j.apcata.2015.09.009
M3 - Article
AN - SCOPUS:84941991950
SN - 0926-860X
VL - 506
SP - 188
EP - 196
JO - Applied Catalysis A: General
JF - Applied Catalysis A: General
ER -