| 丁醛加氢制丁醇反应器的数学模拟 |
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| 引用本文： | 张海涛,张欣荣,房鼎业. 丁醛加氢制丁醇反应器的数学模拟[J]. 华东理工大学学报(自然科学版), 2005, 31(1): 5-8 |
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| 作者姓名： | 张海涛 张欣荣 房鼎业 |
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| 作者单位： | 华东理工大学化学工程系,上海,200237;华东理工大学化学工程系,上海,200237;华东理工大学化学工程系,上海,200237 |
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| 摘 要： | 在对混合丁醛加氢制丁醇的反应体系进行热力学与动力学分析的基础上。采用一维拟均相数学模型对丁醛加氢制丁醇管壳式固定床反应器进行数学模拟设计。预测了反应温度、冷却介质温度、反应压力和反应空速对加氢反应结果的影响。结果表明：丁醛加氢制丁醇的数学模拟结果与生产数据吻合良好。
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| 关 键 词： | 丁醛 丁醇 加氢 反应器 数学模型 |
| 文章编号： | 1006-3080(2005)01-0005-04 |
| 修稿时间： | 2004-01-15 |
Mathematical Modeling of the Reactor Synthesizing Butanol from Butyraldehyde by Hydrogenation |
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| ZHANG Hai-tao,ZHANG Xin-rong,FANG Ding-ye. Mathematical Modeling of the Reactor Synthesizing Butanol from Butyraldehyde by Hydrogenation[J]. Journal of East China University of Science and Technology, 2005, 31(1): 5-8 |
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| Authors: | ZHANG Hai-tao ZHANG Xin-rong FANG Ding-ye |
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| Affiliation: | ZHANG Hai-tao,ZHANG Xin-rong,FANG Ding-ye~* |
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| Abstract: | On the basis of the analysis of thermodynamics and kinetics of hydrogenation system synthesizing butanol from (butyraldehyde), the tubular reactor synthesizing butanol from butyraldehyde was mathematically simulated through one-dimensional mathematical model. The results are close to the industrial data. The influence of reaction temperature, coolant temperature, reaction pressure and reactor air speed was predicted. From the calculated results, the simulation data of the reactor synthesizing butanol from butyraldehyde are identical with the industrial data. |
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| Keywords: | butyraldehyde butanol hydrogenation reactor mathematical modeling |
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