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Upgrading Process of 4-Methylanisole as a Lignin-Derived Bio-Oil Catalyzed by Pt/gamma-Al2O3: Kinetic Investigation and Reaction Network Development

机译:Pt /γ-Al2O3催化4-甲基苯甲醚作为木质素衍生生物油的升级工艺:动力学研究和反应网络的发展

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摘要

This study investigated the catalytic upgrading of 4-methylanisole using Pt/gamma-Al2O3 in the presence of hydrogen with a fixed-bed tubular flow reactor at 573-673 K, 8-20 bar, and space velocities in the range of 3-120 (g of 4-methylanisole)/(g of catalyst X h). Selectivity-conversion data were used to determine an approximate reaction network. It is observed that the scission of the C-methyl-O bond is faster that the scission of the C-aromatic-O bond. So 4-methylphenol forms as a primary intermediate product via scission of the C-methyl-O bond, and then hydrogenolysis of the C-aromatic-O occurs giving toluene. Also another possible deoxygenation route involves a direct C-aromatic-O bond-breaking reaction, leading to toluene. Multiple transalkylation reactions including intramolecular and bimolecular rearrangement account for methylphenols with multiple methyl substituents. The major products were 4-methylphenol, 2,4-dimethylphenol, and 2,4,6-trimethylphenol. So we inferred that transalkylation involving methyl in methoxy groups is one of the kinetically significant reaction classes catalyzed by the acidic support. A pseudo-first-order kinetic model was found to describe well the observed product distribution and to estimate kinetic parameters such as kinetic constants and activation energy of reactions. Kinetic studies revealed that the overall conversion improves with increasing temperature, pressure, and inverse space velocity. The formation of 4-methylphenol by the hydrogenolysis reaction was about two times faster than the formation of toluene by hydrodeoxygenation. The apparent activation energy for the formation of 4-methylphenol as the main product was approximately 15.5 kJ/mol.
机译:这项研究研究了在固定存在的管式流动反应器中,在氢气存在下,在氢气存在下,使用Pt /γ-Al2O3在573-673 K,8-20 bar的空间速度在3-120范围内对4-甲基苯甲醚的催化改性作用。 (g 4-甲基茴香醚)/(g催化剂X h)。选择性转化数据用于确定近似反应网络。观察到C-甲基-O键的断裂比C-芳族-O键的断裂更快。因此,通过裂开C-甲基-O键,形成4-甲基苯酚作为主要的中间产物,然后发生C-芳族-O的氢解,得到甲苯。另一种可能的脱氧途径涉及直接的C-芳族-O键断裂反应,从而导致甲苯。包括分子内和双分子重排在内的多次烷基转移反应说明了具有多个甲基取代基的甲基苯酚。主要产物是4-甲基苯酚,2,4-二甲基苯酚和2,4,6-三甲基苯酚。因此,我们推断甲氧基中涉及甲基的烷基转移反应是酸性载体催化的动力学上重要的反应类别之一。发现伪一级动力学模型很好地描述了观察到的产物分布并估计了动力学参数,例如动力学常数和反应的活化能。动力学研究表明,总转化率随温度,压力和空速的增加而提高。通过氢解反应形成4-甲基苯酚比通过加氢脱氧形成甲苯的速度快约两倍。形成4-甲基苯酚作为主要产物的表观活化能约为15.5 kJ / mol。

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  • 来源
    《Energy & fuels》 |2015年第mayajuna期|3335-3344|共10页
  • 作者单位

    Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Iran;

    Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Iran|Univ Calif Davis, Dept Chem Engn & Mat Sci, Davis, CA 95616 USA;

    Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Iran;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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  • 入库时间 2022-08-18 00:40:19

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