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鲁奇副产蒸汽管壳型和I.C.I.四段冷激式甲醇合成塔的数学模拟和比较 Ⅰ.鲁奇副产蒸汽管壳型甲醇合成塔的数学模拟

Mathematical Modeling and Comparison of Lurgi Tube-Shell Type Methanol Synthesis Reactor with by-Product Steam and I. C.I. Four Stage Quench Type Methanol Synthesis Reactor Ⅰ.Mathematical Modeling of Lurgi Tube-Shell Type Methanol Shyntesis React

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【作者】 朱炳辰房鼎业姚佩芳

【Author】 Zhu Bingchen Fang Dingye Yao Peifang(East China University of Chemical Technology)

【机构】 华东化工学院华东化工学院

【摘要】 本文建立了鲁奇副产蒸汽管壳型甲醇合成塔催化床的双速率二维模型,求得反应管内轴向及径向的浓度及温度分布的数值解。由于管间副产40kg/cm~2的蒸汽,其温度与管内催化床的温度接近,反应管内外的温度差小,反应管内径向温度差小。模拟计算结果表明,由于径向温度分布均匀,工业装置的计算可采用一维模型。

【Abstract】 In this paper, the two-dimensional model of Lurgi tube-shell type methanol synthesis catalyst beds has been established.The numerical solutions of concentration and temperature profiles in the radial and axial direction of the reaction tubes have been obtained. As the temperature of the by-product 40 kg/cm~2 steam between tubes approaches the temperature of the catalyst bed,the difference of the temperatures within and outside the reaction tubes is very small, hence the temperature differcnce in the radial direction within the tubes is also very small. The result of modeling calculation shows that under the above condition one dimensional model may be used in the calculation of commercial device.

  • 【文献出处】 化学反应工程与工艺 ,Chemical Reaction Engineering and Technology , 编辑部邮箱 ,1985年Z1期
  • 【被引频次】3
  • 【下载频次】149
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