TY - JOUR
T1 - Comparison of Ni Based and Rh Based Catalyst Performance in the Oxidative Steam Reforming of Raw Bio-Oil
AU - Remiro, A.
AU - Arandia, A.
AU - Bilbao, J.
AU - Gayubo, A.G.
PY - 2017
Y1 - 2017
N2 - The effect of O
2 content in the oxidative steam reforming (OSR) of raw bio-oil has been studied, and the kinetic behavior, particularly deactivation, has been compared between two catalysts (Ni/La
2O
3-αAl
2O
3 and Rh/CeO
2-ZrO
2). The experiments have been carried out in an apparatus with two steps in series: (1) thermal treatment (at 500°C, for the controlled deposition of pyrolytic lignin) and (2) catalytic in-line reforming in a fluidized bed. The reaction conditions have been as follows: oxygen/carbon ratio (O/C), 0, 0.17, 0.34, and 0.67; 700°C; steam/carbon ratio (S/C), 6; space time, 0.3 g
catalysth/g
bio-oil (for Ni/La
2O
3-αAl
2O
3) and 0.15 g
catalysth/g
bio-oil (for Rh/CeO
2-ZrO
2); time on stream, 4 h. The content and morphology of the coke deposited on the catalysts has been determined by temperature-programmed oxidation (TPO), and the deterioration of the metallic properties of the catalysts by temperature-programmed reduction (TPR) and X-ray diffraction (XRD). The results (bio-oil conversion, product yield and their evolution with time on stream) show that for Rh/CeO
2-ZrO
2 catalyst the decrease in coke deposition as O/C ratio is increased involves attenuation of catalyst deactivation. Consequently, this catalyst is stable after 24 h operation for high O/C ratios, thus keeping constant the activity for reforming reactions and the WGS reaction, with a high yield of H
2 and low yields of CO, CH
4, and hydrocarbons. However, for the Ni/La
2O
3-αAl
2O
3 catalyst of lower activity than the Rh/CeO
2-ZrO
2, the decrease in coke content as O/C ratio is increased does not involve a noticeable attenuation in catalyst deactivation, which is due to Ni sintering.
AB - The effect of O
2 content in the oxidative steam reforming (OSR) of raw bio-oil has been studied, and the kinetic behavior, particularly deactivation, has been compared between two catalysts (Ni/La
2O
3-αAl
2O
3 and Rh/CeO
2-ZrO
2). The experiments have been carried out in an apparatus with two steps in series: (1) thermal treatment (at 500°C, for the controlled deposition of pyrolytic lignin) and (2) catalytic in-line reforming in a fluidized bed. The reaction conditions have been as follows: oxygen/carbon ratio (O/C), 0, 0.17, 0.34, and 0.67; 700°C; steam/carbon ratio (S/C), 6; space time, 0.3 g
catalysth/g
bio-oil (for Ni/La
2O
3-αAl
2O
3) and 0.15 g
catalysth/g
bio-oil (for Rh/CeO
2-ZrO
2); time on stream, 4 h. The content and morphology of the coke deposited on the catalysts has been determined by temperature-programmed oxidation (TPO), and the deterioration of the metallic properties of the catalysts by temperature-programmed reduction (TPR) and X-ray diffraction (XRD). The results (bio-oil conversion, product yield and their evolution with time on stream) show that for Rh/CeO
2-ZrO
2 catalyst the decrease in coke deposition as O/C ratio is increased involves attenuation of catalyst deactivation. Consequently, this catalyst is stable after 24 h operation for high O/C ratios, thus keeping constant the activity for reforming reactions and the WGS reaction, with a high yield of H
2 and low yields of CO, CH
4, and hydrocarbons. However, for the Ni/La
2O
3-αAl
2O
3 catalyst of lower activity than the Rh/CeO
2-ZrO
2, the decrease in coke content as O/C ratio is increased does not involve a noticeable attenuation in catalyst deactivation, which is due to Ni sintering.
UR - http://www.scopus.com/inward/record.url?scp=85025117554&partnerID=8YFLogxK
U2 - 10.1021/acs.energyfuels.7b00735
DO - 10.1021/acs.energyfuels.7b00735
M3 - Article
SN - 0887-0624
VL - 31
SP - 7147
EP - 7156
JO - Energy & Fuels
JF - Energy & Fuels
IS - 7
ER -