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Equilibrium shift in reactors with a permselective wall

机译:具有选择性渗透壁的反应堆的平衡位​​移

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摘要

The objective of this study is to obtain a fundamental understanding of the behavior of reactors with a permselective wall (membrane reactors) in terms of design parameters (reactor length, membrane thickness) operating variables (pressure ratio, feed flow rate, feed temperature), physical properties (rate constant, permeability of fast gas, permselectivity, equilibrium constant, heat of reaction), and flow patterns (recycle, cocurrent, countercurrent). Pure feed reacts on the high pressure side of the membrane, and the product(s) formed are continuously removed to the low pressure side so that thermodynamic equilibrium is never reached.;It is shown by simulation that equilibrium shift can be enhanced by: recycling unconverted reactant; shifting feed location in plug flow membrane reactors to separate products; and maintaining high permeation rates to reduce backreaction. It is shown that the choice between cocurrent flow and countercurrent flow depends on the system parameters. It is also shown that diffusional resistance will degrade performance at high permeation fluxes and/or high aspect ratios (diameter/length).
机译:这项研究的目的是从设计参数(反应器长度,膜厚度),运行变量(压力比,进料流速,进料温度),设计参数(反应器长度,膜厚度),对具有选择性渗透壁的反应器(膜反应器)的行为获得基本了解,物理性质(速率常数,快速气体的渗透性,渗透选择性,平衡常数,反应热)和流动方式(循环,并流,逆流)。纯进料在膜的高压侧发生反应,并且将形成的产物连续移至低压侧,因此从未达到热力学平衡。;通过仿真表明,平衡位移可通过以下方法增强:未转化的反应物;改变活塞流膜反应器中的进料位置以分离产物;并保持较高的渗透率,以减少逆反应。结果表明,顺流和逆流之间的选择取决于系统参数。还显示出,在高渗透通量和/或高纵横比(直径/长度)下,扩散阻力会降低性能。

著录项

  • 作者

    Mohan, Krishna.;

  • 作者单位

    University of Cincinnati.;

  • 授予单位 University of Cincinnati.;
  • 学科 Chemical engineering.
  • 学位 Ph.D.
  • 年度 1988
  • 页码 148 p.
  • 总页数 148
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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