TY - JOUR
T1 - Biofuel production using Pd/Zn synergistically catalyzed hydrodeoxygenation applied at bio oil extracted in biomass pyrolysis process
AU - Huang, Yinbin
AU - Wei, Lin
AU - Zhao, Xianhui
AU - Julson, James
AU - Qiu, Changling
AU - Dharmarajan, Shanmugapriya
AU - Kiratu, John
AU - Raynie, Douglas
AU - Dubey, Ashish
AU - Qiao, Qiquan
N1 - Publisher Copyright:
Copyright © 2016 John Wiley & Sons, Ltd.
Copyright:
Copyright 2017 Elsevier B.V., All rights reserved.
PY - 2016/10/10
Y1 - 2016/10/10
N2 - Raw bio oil includes multicomponents. In order to avoid the interference between complex reactions, the model compounds, instead of the real bio oil, have been widely used for the study of raw bio-oil upgrade. In this work, the hydrodeoxygenation (HDO) of raw pine pyrolysis bio oil was investigated at 200 °C using Pd/Zn synergistic catalysis under hydrogen pressures of 200, 300, and 400 psi, separately. The resulting product included gas, liquid, and coke. The gas was characterized using a gas chromatography. The liquid was characterized using a gas chromatography–mass spectrometry. The results showed that the HDO performance achieved promotion to some extent by the Pd/Zn synergistic catalysis compared with use of Pd/C or Zn2+, independently. The HDO also gave rise to improvements on physicochemical properties of bio oils. Notably, the highest water content (13.16 wt%) revealed that deoxygenation reaction could be promoted by Pd/Zn synergistic catalysis compared with use of Pd/C or Zn2+, independently. More importantly, the highest hydrocarbon yield (19.15% on the base of liquid part) could be obtained by the treatment of 300 psi pressure and 200 °C temperature over Zn/Pd/C synergistic catalysis.
AB - Raw bio oil includes multicomponents. In order to avoid the interference between complex reactions, the model compounds, instead of the real bio oil, have been widely used for the study of raw bio-oil upgrade. In this work, the hydrodeoxygenation (HDO) of raw pine pyrolysis bio oil was investigated at 200 °C using Pd/Zn synergistic catalysis under hydrogen pressures of 200, 300, and 400 psi, separately. The resulting product included gas, liquid, and coke. The gas was characterized using a gas chromatography. The liquid was characterized using a gas chromatography–mass spectrometry. The results showed that the HDO performance achieved promotion to some extent by the Pd/Zn synergistic catalysis compared with use of Pd/C or Zn2+, independently. The HDO also gave rise to improvements on physicochemical properties of bio oils. Notably, the highest water content (13.16 wt%) revealed that deoxygenation reaction could be promoted by Pd/Zn synergistic catalysis compared with use of Pd/C or Zn2+, independently. More importantly, the highest hydrocarbon yield (19.15% on the base of liquid part) could be obtained by the treatment of 300 psi pressure and 200 °C temperature over Zn/Pd/C synergistic catalysis.
KW - bio-oil upgrading
KW - hydrodeoxygenation
KW - Pd/C
KW - Zn
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U2 - 10.1002/er.3547
DO - 10.1002/er.3547
M3 - Article
AN - SCOPUS:84968586423
SN - 0363-907X
VL - 40
SP - 1724
EP - 1730
JO - International Journal of Energy Research
JF - International Journal of Energy Research
IS - 12
ER -