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Promotional Effect of Copper on Activity and Selectivity to Hydrocarbons and Oxygenates for Fischer-Tropsch Synthesis over Potassium-Promoted Iron Catalysts Supported on Activated Carbon

机译:铜对活性炭负载的钾促进铁催化剂上费托合成的活性及对烃和氧的选择性的促进作用

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摘要

The effect of 0—2 wt % copper on the activity and selectivity to hydrocarbons and oxygenates was studied over activated-carbon (AC)-supported 15.7 wt % Fe and 0.9 wt % K catalysts for the Fischer-Tropsch synthesis (FTS). The catalysts were examined in a fixed-bed reactor at 300 psig, 3 nL (g of catalyst)~(-1) h~(-1), and a syngas with a H_2/CO molar feed ratio of 0.9 in a temperature range of 260—290 ℃. The addition of up Co 2.0 wt % Cu promoter enhances iron reduction significantly. However, the improved iron reduction does not benefit the catalyst activity. Instead, both FTS and water—gas shift (WGS) activities of the Fe—K/ AC catalyst are lowered. This may be due to high Cu loadings, suppressing iron carbonization and increasing the deposition of carbon on the catalyst surface during the initial iron carbonization and/or the formation of some Fe—Cu clusters during reduction. The addition of Cu on the Fe—K/AC catalysts changes selectivities to methane and other hydrocarbons only slightly; however, it increases the internal olefin content and decreases the olefin content. This could be attributed to Cu-promoting hydrogen adsorption and enhanced hydrogenation/isomerization. Cu increases oxygenate selectivity of the Fe—K/AC catalysts, implying that Cu enhances molecular CO adsorption, but inhibits CO dissociation on the Fe—K/AC catalyst. The addition of Cu also changes the alcohol distribution of the Fe- K/AC catalysts. The ethanol formation decreases slightly, but the formation of methanol and C_3-C_5 alcohols increases. The highest Cu loading (2 wt %) reduces this trend somewhat. Furthermore, from the kinetic point of view, the addition of 0.8—2.0 wt % Cu decreases both the apparent activation energies and the apparent pre-exponential factors of the FTS and WGS reactions over the catalysts. The decrease in the pre-exponential factor is related to the lower activities of the Cu-containing Fe-K/AC catalysts.
机译:在费托合成(FTS)的活性炭(AC)负载的15.7 wt%的Fe和0.9 wt%的K催化剂上,研究了0-2 wt%的铜对活性和对烃类和含氧化合物的选择性的影响。在固定床反应器中于300 psig,3 nL(g催化剂)〜(-1)h〜(-1)和温度范围内H_2 / CO摩尔进料比为0.9的合成气中检查催化剂260-290℃。添加向上的Co 2.0 wt%Cu促进剂可显着提高铁还原率。但是,改进的铁还原没有助益催化剂活性。相反,Fe-K / AC催化剂的FTS和水煤气变换(WGS)活性均降低。这可能是由于高的Cu含量,抑制了铁的碳化以及在初始铁的碳化过程中和/或在还原过程中某些Fe-Cu簇的形成过程中增加了碳在催化剂表面的沉积。在Fe-K / AC催化剂上添加Cu只会稍微改变对甲烷和其他碳氢化合物的选择性。然而,它增加了内部烯烃的含量并降低了烯烃的含量。这可以归因于促进铜的氢吸附和增强的氢化/异构化。 Cu增加了Fe-K / AC催化剂的氧化选择性,这意味着Cu增强了分子对CO的吸附,但抑制了Fe-K / AC催化剂上的CO离解。 Cu的添加还改变了Fe-K / AC催化剂的醇分布。乙醇的形成略有减少,但甲醇和C_3-C_5醇的形成增加。最高的铜含量(2 wt%)在某种程度上降低了这种趋势。此外,从动力学的观点来看,添加0.8-2.0wt%的Cu降低了催化剂上FTS和WGS反应的表观活化能和表观指数前因子。预指数因子的降低与含铜Fe-K / AC催化剂活性降低有关。

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  • 来源
    《Energy & fuels》 |2011年第mayajuna期|p.1931-1936|共6页
  • 作者单位

    Department of Chemical Engineering, West Virginia University, Morgantown, West Virginia 26S06, United States;

    Department of Chemical Engineering, West Virginia University, Morgantown, West Virginia 26S06, United States;

    Department of Chemical Engineering, West Virginia University, Morgantown, West Virginia 26S06, United States;

  • 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 00:41:37

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