首页> 外文OA文献 >I. Synthesis, characterization, and base catalysis of novel zeolite supported super-basic materials. II. Oxidative dehydrogenation of ethane over reduced heteropolyanion catalysts
【2h】

I. Synthesis, characterization, and base catalysis of novel zeolite supported super-basic materials. II. Oxidative dehydrogenation of ethane over reduced heteropolyanion catalysts

机译:I.新型沸石负载的超基础材料的合成,表征和碱催化。 II。乙烷在还原的杂多阴离子催化剂上的氧化脱氢

摘要

This thesis is composed of two separate and unrelated projects. The first part of this thesis outlines an investigation into the synthesis and characterization of a novel zeolite supported super-base capable of carbon-carbon olefin addition to alkyl aromatics. A zeolite supported basic material capable of such reactions would benefit many fine chemical syntheses, as well as vastly improve the economics associated with production of the high performance thermoplastic polyester polyethylene naphthalate.The thermal decomposition of alkali—metal azides impregnated in zeolite X is investigated as a novel route to the synthesis of a zeolite supported super-base. Impregnation of the alkali—metal azide precursor is shown to result in azide species occluded within the pores of the zeolite support by using high speed, solid-state 23Na MAS and 2D MQMAS NMR, FTIR, and TGA characterization methods. Addition of alkali—metal azides to the zeolite results in redistribution of the extra-lattice cations in the zeolite framework. Thermal decomposition of impregnated azide species produces further cation redistribution, but no neutral metallic clusters are detected by high speed, solid-state 23Na MAS NMR following thermal activation of the materials. Instead, it is possible that inactive ionic clusters are formed. The thermally activated materials do not promote base catalysis for the isomerization of 1-butene, the ethylation of toluene and o-xylene, and the alkenylation of o-xylene with 1,3-butadiene to produce 5-ortho-tolyl-pent-2-ene (5-OTP). The lack of catalytic activity in the materials is attributed to failure of the materials to form neutral metallic clusters during thermal treatment, possibly due to preferential formation of NMR silent ionic clusters. The formation of neutral metallic clusters is found to be insensitive to synthesis technique and activation procedure. It is concluded that the impregnation of alkali—metal azides in zeolite X does not provide a reliable precursor for the formation of zeolite supported super-basic materials.The second part of this thesis describes the oxidative dehydrogenation of ethane over partially reduced heteropolyanions. Niobium and pyridine exchanged salts of phosphomolybdic (NbPMo12Pyr) and phosphovanadomolybdic (NbPMo11VPyr) acids are investigated as catalyst precursors to prepare materials for catalyzing the oxidative dehydrogenation of ethane to ethylene and acetic acid at atmospheric pressure. The effects of feed composition, steam flow, temperature, and precursor composition on catalytic activity and selectivity are presented for both ethane and ethylene oxidation. Production of ethylene and acetic acid from ethane using the catalytic materials exceeds that reported in the literature for Mo-V-Nb-Ox systems under atmospheric or elevated pressure. Production of acetic acid from ethylene is also greater than that observed for Mo-V-Nb-Ox systems. Addition of vanadium reduces catalytic activity and selectivity to both ethylene and acetic acid while niobium is essential for the formation of acetic acid from ethane. Other metals such as antimony, iron, and gallium do not provide the same beneficial effect as niobium. Molybdenum in close proximity to niobium is the active site for ethane activation while niobium is directly involved in the transformation of ethylene to acetic acid. A balance of niobium and protonated pyridine is required to produce an active catalyst. Water is found to aid in desorption of acetic acid, thereby limiting deep oxidation to carbon oxides. A reaction scheme is proposed for the production of acetic acid from ethane over the catalytic materials.
机译:本文由两个独立且无关的项目组成。本论文的第一部分概述了对新型的能够将碳-碳烯烃加成至烷基芳族化合物的沸石负载的超碱的合成和表征的研究。能够进行这种反应的沸石担载的基础材料将有益于许多精细的化学合成,并且极大地提高了与生产高性能热塑性聚酯聚萘二甲酸乙二醇酯有关的经济性。研究了浸渍在沸石X中的碱金属叠氮化物的热分解过程。合成沸石负载的超碱的新途径。通过使用高速,固态23Na MAS和2D MQMAS NMR,FTIR和TGA表征方法,碱金属叠氮化物前体的浸渍显示会导致叠氮化物物种滞留在沸石载体的孔中。将碱金属叠氮化物添加到沸石中会导致格外阳离子在沸石骨架中的重新分布。浸渍的叠氮化物物质的热分解会进一步产生阳离子再分布,但是在材料热活化后,高速固态23Na MAS NMR并未检测到中性金属簇。相反,有可能形成无活性的离子簇。热活化材料不促进1-丁烯的异构化,甲苯和邻二甲苯的乙基化以及邻二甲苯与1,3-丁二烯的烯基化以产生5-邻甲苯基-2的碱催化。 -ene(5-OTP)。材料中缺乏催化活性是由于材料在热处理过程中未能形成中性金属簇,这可能是由于NMR沉默离子簇的优先形成所致。发现中性金属簇的形成对合成技术和活化过程不敏感。结论是,在沸石X中浸渍碱金属叠氮化物不能为形成沸石负载的超碱性材料提供可靠的前体。本论文的第二部分描述了乙烷在部分还原的杂多阴离子上的氧化脱氢。研究了磷钼酸(NbPMo12Pyr)和磷钒钼酸(NbPMo11VPyr)的铌和吡啶交换盐作为催化剂前体,以制备在大气压下催化乙烷氧化脱氢为乙烯和乙酸的材料。给出了乙烷和乙烯氧化反应中进料组成,蒸汽流量,温度和前体组成对催化活性和选择性的影响。使用催化材料由乙烷生产乙烯和乙酸超过了在大气压或高压下Mo-V-Nb-Ox系统的文献报道。从乙烯生产乙酸的产量也高于Mo-V-Nb-Ox体系的产量。钒的添加降低了对乙烯和乙酸的催化活性和选择性,而铌对于由乙烷形成乙酸是必不可少的。锑,铁和镓等其他金属不能提供与铌相同的有益效果。紧邻铌的钼是乙烷活化的活性中心,而铌直接参与乙烯向乙酸的转化。生产活性催化剂需要平衡的铌和质子化吡啶。发现水有助于乙酸的解吸,从而将深度氧化限制为碳氧化物。提出了一种用于在催化材料上由乙烷生产乙酸的反应方案。

著录项

  • 作者

    Galownia Jonathan Michael;

  • 作者单位
  • 年度 2005
  • 总页数
  • 原文格式 PDF
  • 正文语种
  • 中图分类

相似文献

  • 外文文献
  • 中文文献
  • 专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号