TY - JOUR
T1 - Study on CO2 reforming of methane to syngas over Al 2O3-ZrO2 supported Ni catalysts prepared via a direct sol-gel process
AU - Li, Hansheng
AU - Wang, Jinfu
PY - 2004/11
Y1 - 2004/11
N2 - Ni-based catalysts supported on Al2O3-ZrO2 (Ni/Al2O3-ZrO2) were prepared by a direct sol-gel process with citric acid as the gelling agent. The evaluation of the catalyst prepared for methane reforming with CO2 was carried out with thermal gravimetric analysis (TGA), infrared spectroscopy (IR), X-ray diffraction (XRD), microscopy analyses (SEM and TEM), temperature-programmed reduction (TPR) and in a micro-reactor system. The catalytic performance for CO2 reforming of methane to synthesis gas in a continuous-flow micro-reactor under atmospheric pressure was investigated. TGA, IR, XRD and microscopy analyses show that the Ni particles have a nanostructure of around 5nm and are uniformly dispersed on the Al2O3-ZrO 2 support, which exists as an amorphous phase. Catalytic tests using CO2 reforming of methane to synthesis gas show that the catalytic activity increases with increasing metal loading, and the 20Ni/Al 2O3-ZrO2 (0.2 Ni/Al molar ratio) catalyst has excellent activity and stability, compared with that of the Al2O 3 supported Ni catalyst, with 91.9% conversion of CO2 and 82.9% conversion of CH4 over 50 h at 1073 K, atmospheric pressure, hourly space velocity of 11, 200 ml gcat-1 h-1 and CH 4:CO2:N2 of 2:2:1. The excellent catalytic activity and stability is attributed to the very highly and uniformly dispersed small metallic Ni particles, the reducibility of the Ni oxides and an interaction between metallic Ni particles and the support Al2O 3-ZrO2.
AB - Ni-based catalysts supported on Al2O3-ZrO2 (Ni/Al2O3-ZrO2) were prepared by a direct sol-gel process with citric acid as the gelling agent. The evaluation of the catalyst prepared for methane reforming with CO2 was carried out with thermal gravimetric analysis (TGA), infrared spectroscopy (IR), X-ray diffraction (XRD), microscopy analyses (SEM and TEM), temperature-programmed reduction (TPR) and in a micro-reactor system. The catalytic performance for CO2 reforming of methane to synthesis gas in a continuous-flow micro-reactor under atmospheric pressure was investigated. TGA, IR, XRD and microscopy analyses show that the Ni particles have a nanostructure of around 5nm and are uniformly dispersed on the Al2O3-ZrO 2 support, which exists as an amorphous phase. Catalytic tests using CO2 reforming of methane to synthesis gas show that the catalytic activity increases with increasing metal loading, and the 20Ni/Al 2O3-ZrO2 (0.2 Ni/Al molar ratio) catalyst has excellent activity and stability, compared with that of the Al2O 3 supported Ni catalyst, with 91.9% conversion of CO2 and 82.9% conversion of CH4 over 50 h at 1073 K, atmospheric pressure, hourly space velocity of 11, 200 ml gcat-1 h-1 and CH 4:CO2:N2 of 2:2:1. The excellent catalytic activity and stability is attributed to the very highly and uniformly dispersed small metallic Ni particles, the reducibility of the Ni oxides and an interaction between metallic Ni particles and the support Al2O 3-ZrO2.
KW - CO reforming of methane
KW - Catalysis
KW - Nanostructure
KW - Reaction engineering
KW - Sol-gel processing
KW - Stability
UR - http://www.scopus.com/inward/record.url?scp=9944234550&partnerID=8YFLogxK
U2 - 10.1016/j.ces.2004.07.076
DO - 10.1016/j.ces.2004.07.076
M3 - Article
AN - SCOPUS:9944234550
SN - 0009-2509
VL - 59
SP - 4861
EP - 4867
JO - Chemical Engineering Science
JF - Chemical Engineering Science
IS - 22-23
ER -