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Influence of Support Acidity and Ir Content on the Selective Ring Opening of Decalin over Ir/SiO2-Al2O3

机译:载体酸度和Ir含量对Ir / SiO2-Al2O3上萘烷选择性开环的影响

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摘要

The influence of the addition of HCl and Ir (1 wt %) to different SiO2-Al2O3 supports of varying silica content was studied in the reaction of selective ring opening of decalin. The addition of HCl to silica alumina supports containing 70 and 80 wt % SiO2 was found to have little influence in the distribution of reaction products compared to the calcined supports. The incorporation of Ir to the silica alumina catalysts has a beneficial effect, increasing the decalin conversion, being this effect more noticeable in the low acidity supports, i.e., those containing 30-40 wt % SiO2. The iridium-containing materials display the highest yield of cracking products, ring opening products, and ring contraction products. Increasing the reaction temperature promotes cracking and dehydrogenation but markedly decreases the selectivity to ring contraction products. At 350 degrees C a slight decrease in selectivity to ring opening products occurs, though the overall increase in conversion results in an increased yield of these products. An optimum ratio between the acid sites and metal activity that favors the formation of ring opening products was found. At lower acid sites/metal activity ratios the isomerization reaction which leads to C-5 cycle isomers is low, and ring opening by hydrogenolysis is limited as a consequence. On the other hand, at high acid sites/metal activity ratios the cracking reactions are favored, decreasing the yield of RO products.
机译:在萘烷的选择性开环反应中研究了向不同二氧化硅含量的不同SiO2-Al2O3载体中添加HCl和Ir(1 wt%)的影响。与煅烧的载体相比,发现向包含70和80重量%的SiO 2的二氧化硅氧化铝载体中添加HCl对反应产物的分布几乎没有影响。将Ir掺入二氧化硅氧化铝催化剂中具有有益的作用,增加了十氢化萘转化率,因为这种作用在低酸度的载体,即含有30-40wt%SiO 2的那些中更明显。含铱材料显示出最高的裂解产物,开环产物和开环收缩产物的产率。提高反应温度促进裂化和脱氢,但显着降低了对环收缩产物的选择性。在350℃下,对开环产物的选择性略有降低,尽管转化率的总体提高导致这些产物的产率提高。发现了有利于开环产物形成的酸位和金属活性之间的最佳比例。在较低的酸位/金属活度比下,导致C-5循环异构体的异构化反应低,因此限制了通过氢解作用的开环。另一方面,在高酸位/金属活性比的情况下,裂解反应是有利的,从而降低了RO产物的产率。

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  • 来源
    《Energy & fuels》 |2017年第5期|5461-5471|共11页
  • 作者单位

    FIQ UNL, CONICET, Inst Invest Catalisis & Petroquim INCAPE, Colectora Ruta Nac 168, RA-3000 Paraje El Pozo, Santa Fe, Argentina;

    FIQ UNL, CONICET, Inst Invest Catalisis & Petroquim INCAPE, Colectora Ruta Nac 168, RA-3000 Paraje El Pozo, Santa Fe, Argentina;

    FIQ UNL, CONICET, Inst Invest Catalisis & Petroquim INCAPE, Colectora Ruta Nac 168, RA-3000 Paraje El Pozo, Santa Fe, Argentina;

  • 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
  • 中图分类
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  • 入库时间 2022-08-18 00:39:32

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