| 工业变换炉最佳催化剂粒度 |
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| 引用本文： | 丁百全,郭幸子,朱炳辰.工业变换炉最佳催化剂粒度[J].化肥设计,1994(1). |
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| 作者姓名： | 丁百全 郭幸子 朱炳辰 |
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| 作者单位： | 华东理工大学，武汉葛化集团公司化工研究所 |
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| 摘 要： | 本文在建立数学模型的基础上，用计算机模拟变换炉的操作工况，考察改变催化剂粒度对经济效益的影响，从而得到工业变换炉催化剂颗粒最佳尺寸，开发了以经济效益为考察依据，工业反应器中催化剂颗粒最佳尺寸的计算方法。
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| 关 键 词： | 变换反应器，催化剂粒度，计算机模拟，最优化 |
Optimum catalyst size of industrial shift peactor |
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| Ding Baiquan, Guo Xingzi, Zhu Bingchen.Optimum catalyst size of industrial shift peactor[J].Chemical Fertilizer Design,1994(1). |
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| Authors: | Ding Baiquan Guo Xingzi Zhu Bingchen |
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| Affiliation: | Ding Baiquan; Guo Xingzi; Zhu Bingchen |
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| Abstract: | in this paper, based on the establishment of mathematical model, we use computer to simulatethe operating condition of shift reactor. The effect of changing catalyst size on economy was investigated and theoptimum catalyst size of industrial shift reactor was found. The calculating strategy of optimum catalyst size inthe industrial reactor on the basis of economic benefit was developed. |
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| Keywords: | Shift reactor Catalyst size Computer simulation Optimization |
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