Citation:
XIE Deng-yin, ZHANG Su-ping, CHEN Zhi-yuan, CHEN Zhen-qi, XU Qing-li. Co and Cu modified Ni/Al2O3 steam reforming catalysts for hydrogen production from model bio-oil[J]. Journal of Fuel Chemistry and Technology,
;2015, 43(3): 302-308.
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Ni/Al2O3 catalyst was selected as the reference catalyst for steam reforming of model bio-oil to produce hydrogen. Ni-Cu/Al2O3, Ni-Co/Al2O3 and Ni-Co-Cu/Al2O3 were prepared to investigate the influence of Co and Ni on steam reforming of bio-oil. The results show that Co can enhance the water gas shift (WGS) reaction rate, and Cu can prevent the formation of coke. The reaction conditions for the steam reforming of bio-oil with the Ni-Co-Cu/Al2O3 catalyst were optimized as the follows: temperature of 900 ℃, water-oil ratio (the mass ratio of steam to oil) of 6 g/g and weight hourly space velocity (WHSV) of 1 h-1. The carbon selectivity of 87.5%, hydrogen yield of 84.2% and potential hydrogen yield of 92.4% can be obtained at the optimum conditions.
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Keywords:
- bio-oil,
- catalytic reforming,
- hydrogen
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