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Hydrodeoxygenation of phenols, acids, and ketones as model bio-oil for hydrocarbon fuel over Ni-based catalysts modified by Al, La and Ga

机译:在Al,La和Ga改性的Ni基催化剂上,酚类,酸类和酮类作为烃类燃料的模型生物油进行加氢脱氧

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The large-scale application of bio-oil has been restricted due to its high O content, strong acidity and low heat value. Therefore, the hydrodeoxygenation (HDO) of phenols, acids, and ketones as bio-oil model compounds for hydrocarbon fuel via Ni-based catalysts modified by metal oxides (Al, La and Ga) was investigated. The results showed that the hydrocarbon content was over 70.65% when the mixed supported catalysts Ni/HZSM-5-gamma-Al2O3, Ni/HBeta-La2O3 and Ni/HBeta-Ga2O3 were used for the HDO of guaiacol (GUA). Cyclic hydrocarbons and aromatic hydrocarbons were the main products. Among these catalysts, Ni/HZSM-5-gamma-Al2O3 was the most effective in the HDO of acetic acid. The conversion and hydrocarbon content were 100.00% and 88.62%, respectively. Long-chain alkanes were the main components of the upgraded liquid. Ni/HZSM-5-gamma-Al2O3 was beneficial for the HDO of hydroxyacetone with 100.00% conversion, 80.30% hydrocarbon content and 48.67% yield. The HDO pathways of GUA, acetic acid and hydroxyacetone were as follows: 1) GUA was mainly converted into benzene and its derivatives by transmethylation, isomerization and hydrogenation (HYD). 2) Acetic acid was converted to long-chain alkanes by HYD, self-condensation, saturated HYD and isomerization. 3) Hydroxyacetone was converted into long-chain alkanes by HYD, self-condensation, demethylation, aldol condensation and saturated HYD. This work provides basic data for obtaining renewable hydrocarbon fuel from biomass via HDO with a low-cost catalyst. (C) 2019 Published by Elsevier Ltd.
机译:由于其高的O含量,强的酸度和低的热值,生物油的大规模应用受到了限制。因此,研究了通过金属氧化物(Al,La和Ga)改性的Ni基催化剂对作为烃燃料生物油模型化合物的酚,酸和酮进行加氢脱氧(HDO)。结果表明,当混合载体催化剂Ni /HZSM-5-γ-Al2O3,Ni / HBeta-La2O3和Ni / HBeta-Ga2O3用作愈创木酚的HDO时,烃含量超过70.65%。环状烃和芳烃是主要产物。在这些催化剂中,Ni /HZSM-5-γ-Al2O3在乙酸的HDO中最有效。转化率和烃含量分别为100.00%和88.62%。长链烷烃是提纯液体的主要成分。 Ni /HZSM-5-γ-Al2O3有利于羟丙酮的HDO,转化率为100.00%,烃含量为80.30%,产率为48.67%。 GUA,乙酸和羟基丙酮的HDO途径如下:1)GUA主要通过甲基化,异构化和氢化(HYD)转化为苯及其衍生物。 2)通过HYD,自缩合,饱和HYD和异构化将乙酸转化为长链烷烃。 3)羟丙酮通过水合,自缩合,脱甲基,羟醛缩合和饱和水合转化为长链烷烃。这项工作为利用低成本催化剂通过HDO从生物质获得可再生碳氢燃料提供了基础数据。 (C)2019由Elsevier Ltd.发布

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