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Thermochemical conversion of guaiacol with supercritical CO2 : Experimental insights
被引:2
作者:
Wei, Yimeng
[1
]
Zhuang, Zitong
[1
]
Shi, Jinwen
[1
]
Jin, Hui
[1
]
机构:
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn SKLMF, 28 Xianning West Rd, Xian 710049, Shaanxi, Peoples R China
来源:
关键词:
Supercritical CO2;
Thermochemical conversion;
Biomass;
Synthesis gases;
Catalyst;
HYDROGEN-PRODUCTION;
COAL-GASIFICATION;
BIOMASS;
PYROLYSIS;
WATER;
OIL;
MECHANISM;
STEAM;
D O I:
10.1016/j.energy.2024.131534
中图分类号:
O414.1 [热力学];
学科分类号:
摘要:
The excessive CO2 in the environment resulting from the combustion of fossil fuels has posed a significant challenge in terms of its conversion and utilization. In this work, the thermochemical conversion of guaiacol under supercritical CO2 (scCO(2)) was proposed, which not only enabled the consumption of CO2 but also facilitated the conversion of biomass into valuable products. It was concluded that the carbon gasification efficiency (CE) and hydrogen gasification efficiency (HE) were 37.10 % and 51.77 %, respectively, when the CO reached the maximum of 8.72 +/- 0.28 mol/kg at 700 degrees C for 20 min. The addition of catalyst promoted the production of H-2 and increased CE, the H-2 yield of guaiacol gasification under different catalysts was ordered as Al2O3 > KOH > without catalyst > KCl. As the reaction temperature increased, the unreacted guaiacol and phenol decreased and were gradually converted to liquid products such as pyrene and benzo[c]phenanthrene. With the increase in reaction temperature, the more fully guaiacol was reacted, the easier it was to carbonize and form more carbon microspheres. In addition, reaction pathways for free radicals were proposed, including cleavage of free radicals, isomerization of free radicals, secondary cleavage of free radicals and recombination of free radicals. In short, degrading guaiacol using scCO(2) is a feasible approach, which provides a new direction for the disposal and energy recovery of biomass in the future.
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页数:10
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