| 天然气水蒸气转化制氢中变换气热量回收过程的模拟 |
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| 引用本文： | 刘连国,徐显明,王斯晗,张宝军.天然气水蒸气转化制氢中变换气热量回收过程的模拟[J].化工科技市场,2008,31(6). |
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| 作者姓名： | 刘连国 徐显明 王斯晗 张宝军 |
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| 作者单位： | 1. 大庆石化公司塑料厂,大庆,163714
2. 中国石油大庆化工研究中心 |
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| 摘 要： | 应用ASPEN PLUS软件对天然气、水蒸气转化制氢中温变换气热量回收系统进行模拟,考察了压力对热量回收利用率的影响,结果表明,提高压力对提高变换气的热量回收有利.
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| 关 键 词： | 模拟 制氢 变换气 热量回收 |
Heat recovery process simulation of shift gas in hydrogen production from natural gas steam reforming |
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| Liu Lianguo,Xu Xianming,Wang Sihan,Zhang Baojun.Heat recovery process simulation of shift gas in hydrogen production from natural gas steam reforming[J].Chemical Technology Market,2008,31(6). |
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| Authors: | Liu Lianguo Xu Xianming Wang Sihan Zhang Baojun |
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| Institution: | Liu Lianguo~1 Xu Xianming~2 Wang Sihan~2 Zhang Baojun~21.Daqing Petroleum Chemical Company Plastics Plant,Daqing 163714,China,2.Research Institute of Daqing Petrochemical Co. |
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| Abstract: | Applied ASPEN PLUS software,simulated heat recovery system of medium temperature shift gas in hydrogen production from natural gas steam reforming.And the impact of pressure on the heat recovery utilization ratio was studied. Results showed that improving pressure is beneficial to the heat recovery of shift gas. |
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| Keywords: | ASPEN PLUS |
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