| 1.6MPa甲醇合成系统设计运行总结 |
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| 引用本文： | 汤海琦.1.6MPa甲醇合成系统设计运行总结[J].煤化工,2004,32(3):48-49,52. |
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| 作者姓名： | 汤海琦 |
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| 作者单位： | 山西原平化学工业集团有限责任公司,原平,034100 |
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| 摘 要： | 对国内首家1.6MPa单醇合成系统的设计运行进行了总结。该装置利用了拆迁的旧联醇设备进行优化设计。简述了工艺流程,介绍了甲醇合成工段主要设备由来,分析了系统存在的问题并提出对策。生产中实现了合成尾气的回收利用。
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| 关 键 词： | 1.6MPa甲醇合成 设计运行 问题探讨 |
| 文章编号： | 1005-9598(2004)-03-0048-02 |
Summary on the Design and Operation of the 1.6MPa Methanol Synthesis System |
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| Shanxi Yuanping Chemical Industry Group Co.,Ltd.,Yuanping.Summary on the Design and Operation of the 1.6MPa Methanol Synthesis System[J].Coal Chemical Industry,2004,32(3):48-49,52. |
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| Authors: | Shanxi Yuanping Chemical Industry Group Co Ltd Yuanping |
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| Affiliation: | Shanxi Yuanping Chemical Industry Group Co.,Ltd.,Yuanping 034100) |
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| Abstract: | The design and operation of 1.6 MPa methanol synthesis system in China is summarized. The used apparatus is relocated and optimized in the new design. During start up, the charge of catalyst and the temperature programmed reduction are strictly based on 《Plan of temperature programmed reduction of C301 catalyst for methanol synthesis》 suggested by Nanjing Institute of Chemical Engineering. The project turns out to be a success at the first trial of the start up operation and the recycle of the flue gas is realized. |
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| Keywords: | MPa methanol synthesis design and operation problem discussionOOL-? |
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