首页> 外文学位 >Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity, providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds.
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Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity, providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds.

机译:振动床微反应器的冷模型能够在固定重量的时空速度下改变Peclet数,为模拟大型催化流化床中反应动力学场景的重要特征提供了一种工具。

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摘要

A cold-flow model of a vibrated-bed microreactor has been designed and tested with capability for varying the level of gas dispersion (characterized by axial Peclet number) at a fixed weight hourly space velocity (WHSV). A tool has thus been provided whereby an important feature (viz., gas dispersion) of the reaction kinetic scene in large catalytic fluid beds can be simulated on a microscale, using approximately 5 grams of catalyst.;The new microreactor exploits the coherent-expanded (C-E) vibrated-bed state, and is perhaps the first technical use of this state. The C-E state is achieved by subjecting a shallow layer of a fine powder to vertical sinusoidal vibration. The microreactor is charged with a powder, such as fluid catalytic cracking (FCC) catalyst, at a compacted depth of 1 mm, and is vibrated at ;An important object of the present research is to measure horizontal (axial) gas dispersion in a cold model (i.e., an unheated microreactor) by observing the residence time distribution of a tracer gas admitted as a pulse at microreactor inlet. Three mechanisms are responsible for axial gas dispersion. There is a diffusional exchange of gas between the interior and exterior of these packets of particles, and this exchange plays a greater role if the gas molecular diffusivity is large.;We have discovered a general correlation for axial gas dispersion, which incorporates these three mechanisms. The first mechanism displays a finite value at zero gas velocity, and increases in linear fashion with velocity. The second and third mechanisms, together, contribute 1.1 times the gas molecular diffusivity.;Discovery of this general correlation has led to design of a variable-length microreactor in which different levels of fluid-bed gas dispersion (i.e., different Peclet numbers) may be obtained at fixed WHSV simply by varying the length of the duct. (Abstract shortened by UMI.).
机译:设计并测试了振动床微反应器的冷流模型,该模型具有以固定的时空速(WHSV)改变气体扩散水平(以轴向Peclet数为特征)的能力。因此,提供了一种工具,通过该工具可以使用约5克催化剂在微观规模上模拟大型催化流化床中反应动力学场景的重要特征(即气体分散)。新的微反应器利用了相干扩展(CE)振动床状态,也许是该状态的第一个技术用途。 C-E状态是通过使细粉的浅层受到垂直正弦振动来实现的。微型反应器中装有粉末,例如流化催化裂化(FCC)催化剂,压实深度为1 mm,并在50毫米下振动;本研究的重要目标是测量冷态下的水平(轴向)气体弥散通过观察示踪气体在微反应器入口处被视为脉冲的停留时间分布来建立模型(即未加热的微反应器)。轴向气体扩散由三种机制引起。在这些小包的内部和外部之间存在气体的扩散交换,如果气体分子的扩散率大,则这种交换起着更大的作用。;我们发现了轴向气体扩散的一般相关性,其中包含了这三种机理。第一种机制在零气体速度下显示一个有限值,并随速度线性增加。第二种和第三种机理加在一起,是气体分子扩散性的1.1倍。发现这种一般相关性导致设计了可变长度微反应器,其中不同水平的流化床气体扩散(即,不同的Peclet数)可能只需通过改变风管的长度即可在固定的WHSV下获得。 (摘要由UMI缩短。)。

著录项

  • 作者

    Benge, G. Gregory.;

  • 作者单位

    Virginia Polytechnic Institute and State University.;

  • 授予单位 Virginia Polytechnic Institute and State University.;
  • 学科 Chemical engineering.;Petroleum engineering.;Chemistry.
  • 学位 Ph.D.
  • 年度 1992
  • 页码 476 p.
  • 总页数 476
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

  • 入库时间 2022-08-17 11:50:12
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