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Mesoporous supports for the catalysis of Friedel-Crafts alkylation and cyclialkylation reactions with sulfur-containing aromatics.

机译:介孔载体,用于催化含硫芳烃的弗瑞德-克拉夫茨烷基化和环烷基化反应。

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The thesis describes the synthesis of a variety of porous aluminosilicate supports which have been impregnated with zinc chloride and then used as heterogeneous Friedel-Crafts catalysts for the alkylation and cycli-alkylation of sulfur containing aromatics. The liquid phase benzylation of thiophene was adopted as a test reaction for the investigation into the effectiveness of each of the catalysts with the product analysis performed using both quantitative GC and GC-MS. Cyclisation of phenylthio-acetaldehyde diethylacetals to substituted benzolbrack{lcub}it b/{rcub}rbrack thiophenes using a clayzic catalyst was performed in the vapor phase and illustrates a particular application of zinc chloride impregnated acid-treated clays in the synthesis of fine chemicals.; An industrially modified montmorillonite clay, K{dollar}sb{lcub}10{rcub},{dollar} was loaded with ZnCl{dollar}sb2{dollar} and examined under a multitude of experimental conditions in the benzylation of thiophene. The selectivity towards mono-benzylthiophene products was optimised by performing the reaction in nitrobenzene at {dollar}60spcirc{dollar}C. The K{dollar}sb{lcub}10{rcub}{dollar} support, loaded with 2.0 to 2.2 mmol ZnCl{dollar}sb2{dollar} per gram catalyst and activated at {dollar}275spcirc{dollar}C for one hour in air, resulted in a 77% yield of mono-benzylthiophene, 4% di-benzylthiophene and 8 to 11% tar in under 10 min. A degree of regioselectivity towards the formation of 2-benzylthiophene isomer was observed when the reaction time was reduced and further benzylation of the mono-benzyl products was prevented. The heightened ratio of 2- to 3-benzylthiophene isomers was found to depend more on the rate of benzylation of the two mono-benzylthiophene isomers and their subsequent loss through polymerisation and conversion to tar. Isomerisation was observed to occur relatively slowly at higher reaction temperatures, suggesting an equilibrium to a thermodynamically more stable 3-benzylthiophene isomer.; Modification of montmorillonite clay by mineral acid-treatment and loading with ZnCl{dollar}sb2{dollar} provided a series of catalysts with varying pore diameters (0 to 100 A) which could also effectively catalyse the benzylation of thiophene. Use of these micro-/mesoporous catalyst supports resulted in improved yields of mono-benzylthiophene through the suppression of polyalkylation and polymerisation of the thiophene nucleus.; Friedel-Crafts cycli-alkylation reactions of substituted phenylthio-acetaldehyde diethylacetals to their corresponding benzolbrack{lcub}it b/{rcub}rbrack thiophene products was also tested using this same ``clayzic'' catalyst. Under a variety of reaction conditions in the liquid phase, only poor yields were obtained. Suppression of the bimolecular pathways, which generally lead to the production of unwanted by-products including diphenyldisulfide, was possible by carrying out the reaction in the vapor phase over a heated clay catalyst. Excellent yields were thus obtained.; The major drawback of the above clay catalysts was the poor control of pore size. By modification of a montmorillonite clay such that its natural ``cation-exchange-capacity'' was reduced, a series of aluminum-pillared ``charge-reduced'' clays were prepared in an attempt to increase the average spacing between neighbouring pillars and increase the microporosity of the clay. Loading with a Lewis acidic zinc chloride salt produced an active Friedel-Crafts catalyst for the benzylation of thiophene. Lower yields of polyalkylated thiophene and tar were observed.; Incorporation of permanent zinc chloride Lewis acid sites, within the clay structure, was possible by pillaring the clay with mixed zinc and aluminum pillars. The resulting structures would benefit from the catalytic activity of the pillars and the combined micro-/mesopore structure of the pillared clay structure.; A series of synthetic aluminosilicate MCM-41 supports, with cylindrical mesopore s
机译:本文描述了多种多孔铝硅酸盐载体的合成方法,这些载体已用氯化锌浸渍,然后用作含硫芳烃的烷基化和环烷基化的非均相弗瑞德-克来福特催化剂。噻吩的液相苄基化被用作测试反应,用于研究每种催化剂的有效性,同时使用定量GC和GC-MS进行产物分析。在气相中使用粘土催化剂将苯硫基-乙醛二乙基缩醛环化成取代的苯并布雷基噻吩,从而说明了氯化锌浸渍酸处理过的粘土在精细化学品合成中的特殊应用。 ;将工业改性的蒙脱石粘土K {dollar} sb {lcub} 10 {rcub} {dollar}加载ZnCl {dollar} sb2 {dollar},并在多种实验条件下检查噻吩的苄基化。通过在{60}环{C}下于硝基苯中进行反应来优化对单苄基噻吩产物的选择性。每克催化剂载有2.0至2.2 mmol的ZnCl {dolb} sb2 {dollar}的K {dollar} sb {lcub} 10 {rcub} {dollar}载体,并在275spcirc {dollar} C下于1℃活化1小时。空气,在10分钟内产生77%的单苄基噻吩,4%二苄基噻吩和8至11%的焦油。当减少反应时间并防止单苄基产物进一步苄基化时,观察到了对形成2-苄基噻吩异构体的区域选择性的程度。发现2-与3-苄基噻吩异构体的增加的比例更多地取决于两种单苄基噻吩异构体的苄基化速率以及它们随后通过聚合和转化为焦油的损失。在较高的反应温度下观察到异构化发生得相对较慢,表明与热力学上更稳定的3-苄基噻吩异构体达到平衡。通过无机酸处理和负载ZnCl {sb2 {dollar}来改性蒙脱土,提供了一系列具有不同孔径(0至100 A)的催化剂,这些催化剂也可以有效催化噻吩的苄基化反应。这些微/介孔催化剂载体的使用通过抑制多烷基化和噻吩核的聚合而提高了单苄基噻吩的产率。还使用相同的``粘土''催化剂测试了取代的苯硫基-乙醛二乙基缩醛与它们相应的苯并布雷基噻吩的Friedel-Crafts环烷基化反应。在液相中多种反应条件下,仅获得不良的收率。通过在加热的粘土催化剂上在气相中进行反应,可以抑制通常导致产生不希望的副产物包括二苯基二硫化物的双分子途径。因此获得了优异的产量。上述粘土催化剂的主要缺点是对孔径的控制差。通过改性蒙脱土,使其天然的``阳离子交换容量''减少,制备了一系列铝立柱的``减电荷''粘土,以期增加相邻立柱之间的平均间距。增加粘土的微孔率。用路易斯酸酸性氯化锌盐加载产生了用于噻吩苄基化的活性弗瑞德-克来福特催化剂。观察到聚烷基化噻吩和焦油的产率较低。通过在粘土中掺入锌和铝的混合支柱,可以在粘土结构中引入永久的氯化锌路易斯酸位。所得结构将受益于柱的催化活性和柱状粘土结构的组合的微孔/中孔结构。一系列合成铝硅酸盐MCM-41载体,带有圆柱形中孔

著录项

  • 作者

    Kirk, Andrew.;

  • 作者单位

    University of Calgary (Canada).;

  • 授予单位 University of Calgary (Canada).;
  • 学科 Chemistry Organic.
  • 学位 Ph.D.
  • 年度 1998
  • 页码 268 p.
  • 总页数 268
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 有机化学;
  • 关键词

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