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首页> 外文期刊>Fuel Processing Technology >Catalytic hydrodeoxygenation of crude bio-oil over an unsupported bimetallic dispersed catalyst in supercritical ethanol
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Catalytic hydrodeoxygenation of crude bio-oil over an unsupported bimetallic dispersed catalyst in supercritical ethanol

机译:在超临界乙醇中的无载体双金属分散催化剂上粗生物油的催化加氢脱氧

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Catalytic hydrodeoxygenation of the crude bio-oil derived from hydrothermal liquefaction of cornstalk using bimetallic ammonium nickel molybdate as a dispersed catalyst precursor at different temperatures (280-370 degrees C) was conducted under supercritical ethanol with initial 4 MPa H-2, 60 min reaction time. Results showed that the yield of upgraded bio-oil was decreased from 26.7 to 163 wt% with an increase in temperature. The water content and viscosity of upgraded bio-oil were decreased from 25.6 wt.% and 37.3 mm(2)/s to 1.6 wt.% and 8.8 mm(2)/s, respectively, and the heating value was increased from 32.1 to 38.3 MJ/kg. Compared with crude bio-oil, the upgraded bio-oil at 370 degrees C has minimum molar ratio of O/C (0.05) and the highest degree of deoxygenation (74.24%). FT-IR and GC-MS analysis found that the acids were almost removed via esterification; the phenols and esters decreased gradually, whereas hydrocarbons significantly increased and the functional groups and compositions were retuned. In addition, the esters produced at lower temperature were cracked into intermediates for further reactions to obtain the valuable hydrocarbons at higher temperature, for obtaining a potential transportation fuel after further refining. (C) 2016 Published by Elsevier B.V.
机译:在初始温度为4 MPa H-2的条件下,在超临界乙醇中,采用双金属钼酸镍镍作为分散催化剂前体,在不同温度(280-370摄氏度)下对玉米秸秆的水热液化衍生的粗制生物油进行催化加氢脱氧。时间。结果表明,随着温度的升高,提质生物油的产率从26.7%降至163 wt%。升级后的生物油的水含量和粘度分别从25.6 wt。%和37.3 mm(2)/ s降低到1.6 wt。%和8.8 mm(2)/ s,热值从32.1提高到38.3 MJ /千克。与原始生物油相比,在370摄氏度下提质的生物油具有最小的O / C摩尔比(0.05)和最高的脱氧度(74.24%)。 FT-IR和GC-MS分析发现,酸几乎是通过酯化作用去除的。酚类和酯类逐渐减少,而烃类显着增加,官能团和组成得到重新调节。另外,将在较低温度下产生的酯裂化为中间体以进一步反应,从而在较高温度下获得有价值的烃,从而在进一步精制后获得潜在的运输燃料。 (C)2016由Elsevier B.V.发布

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