Single bed pressure swing adsorption process to generate high purity nitrogen

A.I. LaCava, N.O. Lemcoff
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引用次数: 6

Abstract

The separation of air for the production of nitrogen by pressure swing adsorption over a carbon molecular sieve is kinetically based. The basic steps involved in a cycle are typically pressurization, high pressure adsorption, countercurrent blowdown and vent. Simulations studies with DAPS (Dynamic Adsorption Process Simulator) were performed to analyze the effect of the pressurization rate and bed length on the performance of a single bed nitrogen pressure swing adsorption unit in the high purity region. Both specific product and yield improve with the bed length due to the reduction in the axial dispersion effect. A comparison between the predictions of the theoretical model and experimental results was carried out.

单床变压吸附工艺制备高纯氮气
通过变压吸附在碳分子筛上分离氮气是基于动力学的。一个循环的基本步骤通常是加压、高压吸附、逆流排污和排气。利用动态吸附过程模拟器(DAPS)进行了模拟研究,分析了加压速率和床长对高纯区单床氮气变压吸附装置性能的影响。随着床层长度的增加,由于轴向分散效应的减弱,比产物和产率都有所提高。对理论模型的预测结果与实验结果进行了比较。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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