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Paving the way towards green catalytic materials for green fuels: impact of chemical species on Mo-based catalysts for hydrodeoxygenation

机译:为绿色燃料铺平绿色催化材料:化学物质对水冰氧基催化剂的影响

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摘要

A series of Mo-based catalysts were synthesized by tuning the sulfidation temperature to produce mixtures of MoO3 and MoS2 as active phases for the hydrodeoxygenation (HDO) of palmitic acid. Differences in the oxidation states of Mo, and the chemical species present in the catalytic materials were determined by spectroscopic techniques. Palmitic acid was used as a fatty-acid model compound to test the performance of these catalysts. The catalytic performance was related to different chemical species formed within the materials. Sulfidation of these otherwise inactive catalysts significantly increased their performance. The catalytic activity remains optimal between the sulfidation temperatures of 100 degrees C and 200 degrees C, whereas the most active catalyst was obtained at 200 degrees C. The catalytic performance decreased significantly at 400 degrees C due to a higher proportion of sulfides formed in the materials. Furthermore, the relative proportion of MoO3 to MoS2 is essential to form highly active materials to produce O-free hydrocarbons from biomass feedstock. The transition from MoS2 to MoO3 reveals the importance of Mo-S and Mo-O catalytically active species needed for the HDO process and hence for biomass transformation. We conclude that transitioning from MoS2 to MoO3 catalysts is a step in the right direction to produce green fuels.
机译:通过调节硫化温度来合成一系列基于MO的催化剂,以产生MOO3和MOS2的混合物作为棕榈酸的加氢脱氧(HDO)的活性阶段。通过光谱技术测定催化材料中氧化态的氧化状态和催化材料中的化学物质。使用棕榈酸作为脂肪酸模型化合物以测试这些催化剂的性能。催化性能与材料中形成的不同化学物质有关。这些否则灭活催化剂的硫化显着提高了它们的性能。催化活性在100℃和200℃的硫化温度之间保持最佳,而最具活性催化剂在200℃下获得。由于在材料中形成的硫化物比例较多,催化性能在400℃下显着降低。此外,MOO3至MOS2的相对比例对于形成来自生物量原料的无活性材料以形成高活性材料是必不可少的。从MOS2到MOO3的转变揭示了HDO过程所需的MO-S和MO-O催化活性物种的重要性,从而才能实现生物质转化。我们得出结论,从MOS2转换到MOO3催化剂是朝向正确方向的步骤,以产生绿色燃料。

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  • 来源
    《RSC Advances》 |2019年第32期|共10页
  • 作者单位

    Inst Mexicano Petr Direcc Invest Transformac Hidrocarburos Eje Cent Lazaro Cardenas 152 Mexico City 07730 DF Mexico;

    Inst Mexicano Petr Direcc Invest Transformac Hidrocarburos Eje Cent Lazaro Cardenas 152 Mexico City 07730 DF Mexico;

    Inst Mexicano Petr Direcc Invest Transformac Hidrocarburos Eje Cent Lazaro Cardenas 152 Mexico City 07730 DF Mexico;

    Univ Saskatchewan Dept Phys &

    Engn Phys 116 Sci Pl Saskatoon SK S7N 5E2 Canada;

    Univ Saskatchewan Dept Phys &

    Engn Phys 116 Sci Pl Saskatoon SK S7N 5E2 Canada;

    Inst Mexicano Petr Direcc Invest Transformac Hidrocarburos Eje Cent Lazaro Cardenas 152 Mexico City 07730 DF Mexico;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 化学;
  • 关键词

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