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Activated carbon supported cobalt based catalyst for direct conversion of synthesis gas to diesel fuels

机译:活性炭负载的钴基催化剂,用于将合成气直接转化为柴油燃料

摘要

Diesel fuels or blending stocks having high cetane number are produced from non-shifting Fischer-Tropsch processes, which directly convert carbon monoxide and hydrogen to diesel distillates over activated carbon supported cobalt based Fischer-Tropsch catalysts. The activated carbon supported cobalt based catalysts comprise a substantially high dispersion of at least one of a zirconium component, an cerium component, a ruthenium component or a potassium component in porous carbon and elemental cobalt either deposited thereon or substantially uniformly dispersed therein, wherein the concentration of activated carbon in the catalyst is from about 20 to about 90 percent by weight, based on the weight of the catalyst, the concentration of elemental cobalt in the catalyst is from about 4 to about 50 percent by weight, based on the weight of the catalyst, the total concentration of the zirconium component, the cerium component, or a combination thereof in the catalyst is from about 0.01 to about 20 percent by weight, based on the weight of the catalyst and calculated as the elemental metal or metals, and the total concentration of the ruthenium component, the potassium component, or a combination thereof in the catalyst is from about 0.01 to about 5.0 percent by weight, based on the weight of the catalyst and calculated as the elemental metal or metals. Activated carbon carrier has a surface area in the range of about 200-2000 m2/g, preferably 800-1500 m2/g, and a pore volume of 0.3 to 2.0 ml/g, preferably 0.35 to 0.75 ml/g, a distribution of pore diameter of 4 to 1000 Å, preferably 5 to 500 Å.
机译:十六烷值高的柴油燃料或混合原料是由非移位费托工艺生产的,该工艺通过活性炭负载的钴基费托催化剂将一氧化碳和氢气直接转化为柴油馏出物。活性炭负载的钴基催化剂包括沉积在其上或基本上均匀地分散在其中的多孔碳和元素钴中的锆组分,铈组分,钌组分或钾组分中的至少一种的高分散度。基于催化剂的重量,催化剂中活性炭的含量为约20-约90重量%,基于催化剂的重量,元素钴的浓度为约4-约50重量%。催化剂中,锆组分,铈组分或其组合的总浓度为催化剂重量的约0.01%至约20%(以催化剂的重量为基准,并以一种或多种元素金属计),并且催化剂中钌组分,钾组分或其组合的总浓度为约0.01至约5 0.00重量%,基于催化剂的重量并以一种或多种元素金属计算。活性炭载体的表面积为约200-2000m 2 / g,优选为800-1500m 2 / g,且孔体积为0.3-1.5m2。 2.0ml / g,优选0.35-0.75ml / g,孔径分布为4-1000&,优选5-500 500。

著录项

  • 公开/公告号US2003121826A1

    专利类型

  • 公开/公告日2003-07-03

    原文格式PDF

  • 申请/专利权人 DING YUNJIE;MA WENPING;LIN LIWU;

    申请/专利号US20020034206

  • 发明设计人 WENPING MA;YUNJIE DING;LIWU LIN;

    申请日2002-01-03

  • 分类号C07C27/06;C10G11/04;B01J21/18;

  • 国家 US

  • 入库时间 2022-08-22 00:10:29

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