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Suppression of Addition Reactions during Thermal Cracking Using Hydrogen and Sulfided Iron Catalyst

机译:氢气和硫化铁催化剂抑制热裂解过程中的加成反应

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摘要

Due to the complexity of the vacuum residue fraction of petroleum and bitumen, a model compound was used to probe cracking and addition reactions in the liquid phase. Hydrogenation reactions were conducted in a batch microreactor at 430 ℃, 13.9 MPa H_2 for 30 min using a solution of 1,3A8-tetraherylpyrene (THP) in tetralin. Sulfided iron was prepared on a-alumina, γ-alumina, and glass beads as support materials. The hypothesis of this study was that addition reactions can be suppressed under hydrogenation conditions by using iron sulfide as a low-activity catalyst in the presence of hydrogen gas and a hydrogen donor solvent, by saturating olefin intermediates. The products were analyzed by high performance liquid chromatography, gas chromatography, matrix-assisted laser desorption ionization mass spectrometry, and proton nuclear magnetic resonance spectroscopy to investigate conversion and product distribution for different catalysts and without added catalyst The results show that sulfided iron can give significant suppression of addition reactions, decreasing from 63 mol % for the noncatalytic reaction to 13 mol % under catalytic conditions, and shirting the selectivity toward cracking, without competitive hydrogenation of the aromatics. The catalysts were characterized by measuring bulk and surface composition, and by scanning electron microscopy before and after the reaction. The data show that catalyst does not have an impact on conversion; therefore, the data do not support the claim that free radicals are efficiently hydrogenated. The results confirm the presence of iron sulfide on the catalyst surface and a change in its crystalline structure from pyrite to pyrrhotite during reaction. This study shows the value of using a low-cost iron catalyst, as compared to the commercial nickel-based catalysts, as an additive to reduce the amount of coke formation in thermal cracking processes conducted in the presence of hydrogen.
机译:由于石油和沥青的真空残渣馏分的复杂性,模型化合物被用于探测液相中的裂解和加成反应。氢化反应在分批式微反应器中,使用1,3A8-四亚乙基py(THP)在四氢化萘中的溶液在430℃,13.9 MPa H_2下进行30分钟。在α-氧化铝,γ-氧化铝和玻璃珠上作为载体材料制备了硫化铁。该研究的假设是,在氢气和氢供体溶剂存在下,通过使用硫化铁作为低活度催化剂,通过饱和烯烃中间体,可以在氢化条件下抑制加成反应。通过高效液相色谱,气相色谱,基质辅助激光解吸电离质谱和质子核磁共振波谱对产物进行了分析,研究了不加催化剂的情况下不同催化剂的转化率和产物分布。抑制加成反应,从非催化反应的63 mol%降低到催化条件下的13 mol%,并提高了裂解的选择性,而没有芳香族化合物的竞争性加氢作用。通过测量体积和表面组成以及在反应之前和之后通过扫描电子显微镜来表征催化剂。数据表明催化剂对转化率没有影响。因此,数据不支持自由基被有效氢化的说法。该结果证实了催化剂表面上存在硫化铁,并且在反应过程中其晶体结构从黄铁矿变为黄铁矿。这项研究表明,与商业化的镍基催化剂相比,使用低成本的铁催化剂作为添加剂可减少在氢气存在下进行的热裂化过程中焦炭形成量的价值。

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  • 来源
    《Energy & fuels 》 |2013年第novaadeca期| 6637-6645| 共9页
  • 作者单位

    Department of Chemical and Materials Engineering, University of Alberta, Edmonton, Alberta T6G 2V4, Canada;

    Department of Chemistry, University of Alberta, Edmonton, Alberta T6G 2G2, Canada;

    Department of Chemistry, University of Alberta, Edmonton, Alberta T6G 2G2, Canada;

    Department of Chemical and Materials Engineering, University of Alberta, Edmonton, Alberta T6G 2V4, Canada;

    Department of Chemical and Materials Engineering, University of Alberta, Edmonton, Alberta T6G 2V4, Canada;

  • 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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