| 氨合成反应器的模拟计算和设计优化 |
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| 引用本文： | 叶启亮,应卫勇,房鼎业. 氨合成反应器的模拟计算和设计优化[J]. 中国化学工程学报, 2001, 9(4): 441-446 |
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| 作者姓名： | 叶启亮 应卫勇 房鼎业 |
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| 作者单位： | DepartmentofChemicalEngineering,EastChinaUniversityofScienceandTechnology,Shanghai200237,China |
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| 基金项目： | China Petrochemical Corporation (No. 297034). |
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| 摘 要： | One-dimensional pseudo-homogeneous model of an axial flow converter and one-dimensional heteroge-neous model of a horizontal converter have been presented, which describe the distribution of gaseous composition,temperature and pressure along the height in the two converters, respectively. Design optimization methods of the two converters have been proposed, by which the minimum catalyst volume can be obtained to satisfy the productive capacity of 1000 tons per day, when the operating pressure is 15.0, 10.0 and 7.5 MPa, respectively.
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| 关 键 词： | 合成氨 反应器 模拟计算 优化设计 轴向流转换器 水平转换器 |
| 修稿时间： | |
Simulation and Design Optimization of Ammonia Synthesis Converter |
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| YE Qiliang,YING Weiyong,FANG Dingye. Simulation and Design Optimization of Ammonia Synthesis Converter[J]. Chinese Journal of Chemical Engineering, 2001, 9(4): 441-446 |
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| Authors: | YE Qiliang YING Weiyong FANG Dingye |
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| Affiliation: | Department of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China |
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| Abstract: | One-dimensional pseudo-homogeneous model of an axial flow converter and one-dimensional heterogeneous model of a horizontal converter have been presented, which describe the distribution of gaseous composition, temperature and pressure along the height in the two converters, respectively. Design optimization methods of the two converters have been proposed, by which the minimum catalyst volume can be obtained to satisfy the productive capacity of 1000 tons per day, when the operating pressure is 15.0, 10.0 and 7.5MPa, respectively. |
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| Keywords: | ammonia synthesis axial flow converter horizontal converter mathematical model design optimiza-tion |
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