变压吸附层状柱的动态特性

M. Chlendi, D. Tondeur
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引用次数: 43

摘要

在某些吸附过程中,可以使用几种不同的吸附剂,每种吸附剂或多或少专门用于选择性地吸收某些成分的特定任务。不同的吸附剂可以装在不同的柱中,或者,作为叠加层,装在同一柱中。在后一种情况下,它们在吞吐量、压力和温度方面必然经历相同的条件。这种吸附床的动态特性,以及因此的最佳设计和操作,不同于单一吸附床。浓度波从一层到另一层的传递和流动反转会引起特殊的折射、色散和干涉现象。我们提出了一种分析和表示这些现象的方法,基于伪特征,定义为传播特定浓度的恒定值的线。除了在某些理想情况下(无色散、无压力和速度变化的准平衡),这些伪特征通常与平衡模型框架内的特征方法生成的经典线不一致。这些线可以通过使用非理想复杂模型的计算机模拟生成,并提供一种方便和紧凑的方法来分析启动和收敛到循环状态,在任何时候都代表浓度曲线的基本特征,调整操作时间和优化层厚度。这个分析是用氢净化的例子说明,从一个四组分混合物使用两床两吸附六步PSA过程。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Dynamic behaviour of layered columns in pressure swing adsorption

In certain adsorption processes, several different adsorbents may be used, each more or less specialized for a particular task of selectively taking up certain components. The different adsorbents may be packed in different columns, or, alternatively, in the same column as superposed layers. In the latter case, they necessarily experience the same conditions in terms of throughput, pressure and temperature. The dynamic behaviour, and therefore the optimal design and operation of such beds, is different from that of single adsorbent beds. The passage of concentration waves from one layer to the other and the flow reversal induce particular refraction, dispersion and interference phenomena. We propose a method of analysis and representation of these phenomena, based on pseudo-characteristics defined as lines propagating constant values of particular concentrations. The pseudo-characteristics do not in general coincide with the classical lines generated by the method of characteristics within the framework of equilibrium models, except in some ideal situations (quasi-equilibrium without dispersion and without pressure and velocity changes). These lines can be generated by computer simulations using non-ideal complex models, and offer a convenient and compact way to analyse the start-up and convergence towards the cyclic regime, to represent the essential features of the concentration profiles at all times, to adjust the operating times and to optimize the layer thickness. This analysis is illustrated using the example of hydrogen purification from a four-component mixture using a two-bed two-adsorbent six-step PSA process.

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