催化作用
纤维素
木质素
超临界流体
化学
吸附
水溶液
制氢
氢
程序升温还原
核化学
无机化学
化学工程
有机化学
工程类
作者
Changqing Cao,Yupeng Xie,Linhu Li,Wenwen Wei,Hui Jin,Sheng Wang,Wenhao Li
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2021-03-15
卷期号:35 (7): 6030-6039
被引量:30
标识
DOI:10.1021/acs.energyfuels.1c00242
摘要
Lignin and cellulose were gasified at 500 and 600 °C in supercritical water over co-precipitated CeO2–ZrO2 catalyst. The addition of CeO2–ZrO2 improved the gasification efficiency and hydrogen production, and the catalytic effect was more significant at lower temperatures. The H2 yield from cellulose gasification at 500 °C increased by over 2.5 times to 8.50 mol/kg with the presence of CeO2–ZrO2. The gas chromatography-mass spectrometry (GC-MS) analysis showed that the catalyst reduced the content of cyclopentenone and furan derivatives in the aqueous product but increased the content of refractory phenols. We characterized the fresh and the used catalysts with H2-temperature-programmed reduction (H2-TPR), X-ray diffraction (XRD), and scanning electron microscopy-energy-dispersive X-ray spectroscopy (SEM-EDS) analysis, showing that CeO2 was the main active component, which catalyzed gasification through redox reactions. ZrO2 enhanced the catalytic activity of CeO2 by lowering the reduction temperature in hydrogen, increasing the dispersion of CeO2, and facilitating H2 adsorption on the catalyst surface.
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