| 采用平衡模型对变换气提氢PSA工艺的模拟 |
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| 引用本文： | 朱大方.采用平衡模型对变换气提氢PSA工艺的模拟[J].天然气化工,1998,23(1):36-39. |
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| 作者姓名： | 朱大方 |
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| 作者单位： | 西南化工研究院变压吸附分离技术研究所 |
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| 摘 要： | 对早期建立的多组份主体分离的平衡模型进行了改进和完善，并应用于变换气提氢变压吸附工业装置的模拟，模拟结果符合于工业装置的运行性能，这表明理论研究在与工业应用的结合上取得了重大进展。
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| 关 键 词： | 变压吸附（PSA） 平衡模型 氢提纯 |
Simulation of a PSA process for purifying hydrogen from reforming gas by using an equilibrium model |
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| Abstract: | The previously established equilibrium model is improved and perfected for bulk separation of multiple components, and then used to simulate the purification of hydrogen from reforming gas in a commercial PSA plant. The simulation result is well fitted to the operation performance of the plant, showing an important progress in combination of theoretical research with industrial application. |
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| Keywords: | pressure swing adsorption (PSA) equilibrium model hydrogen purification |
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