加氢脱氧
木质纤维素生物量
镍
生物量(生态学)
催化作用
沸石
化学工程
化学
生产(经济)
材料科学
制浆造纸工业
有机化学
木质素
选择性
农学
宏观经济学
经济
生物
工程类
作者
Odiri K. Siakpebru,Anoop Uchagawkar,Lakshmiprasad Gurrala,Jared Bartlett,P. S. Adamson,Nicholas Gorschak,Adam Hassiba,Prashant S. Niphadkar,Vijay V. Bokade,Ana Rita C. Morais
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2024-07-02
卷期号:38 (14): 13029-13038
被引量:6
标识
DOI:10.1021/acs.energyfuels.4c00659
摘要
The synthesis of liquid hydrocarbons from lignocellulosic biomass has been achieved with notable success. However, these technologies often require multistep approaches and are energy intensive. Thus, there is a considerable economic and environmental benefit of process intensification by the synthesis of liquid hydrocarbons in a one-pot process. For the first time, we report direct conversion of raw poplar into liquid alkanes and aromatics (carbon yield of 15.6 ± 0.6 wt %) with high selectivity toward C 7 –C 15 cycloalkanes (7.8 ± 0.1 wt %) and low level of oxygenated compounds (<2.0 wt %) at 270 °C and 3 MPa initial H 2 pressure for 6 h using 10% Ni/H-β zeolite as a catalyst and cyclohexane as a solvent. The effect of temperature (250–270 °C), Ni loading (0–10%), and type of zeolite support (H-β, ZSM-5, and USY) on process performance was also investigated. In addition, the 10% Ni/H-β catalyst showed recyclability over two reactions, with a 17.6% decrease in liquid hydrocarbon yield after the first reaction. This approach has the potential to simplify the synthesis of liquid fuels from lignocellulosic biomass.
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