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首页> 外文期刊>Theoretical foundations of chemical engineering >Gases High Purification from Unreadily Permeating Impurities in One-Compressor Multistage Membrane Apparatuses
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Gases High Purification from Unreadily Permeating Impurities in One-Compressor Multistage Membrane Apparatuses

机译:从一台压缩机多级膜设备中未渗透的杂质中纯化出高纯度气体

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摘要

The present work is focused on gases high purification from unreadily permeating impurities by one-compressor multistage membrane apparatus (OMMA). It looks like a simple one way membrane cascade, consisting from several membrane modules with only one compressing point. In this operating regime the pressure of high pressure cavity is decreasing from one to another while the concentration of high penetrating component is increasing. The equation of purification degree calculation was obtained. It shows how the impurity concentration of permeate reduces in comparison with initial concentration of flow (feed flow), incoming to the membrane module or apparatus. The equation for purification degree calculation was obtained. For the case of low impurity concentration there was leaded the comparison of calculated and experimental (from patent) data. The dependence of purification degree on the number of membrane modules composed apparatus which has an extremum was shown.rnThe description of one-compressor multistage membrane apparatus was determined. The equation of purification degree calculation was obtained. It shows how the impurity concentration of permeate reduces in comparison with initial concentration of flow (feed flow), incoming to the membrane module or apparatus. The equation for purification degree calculation was obtained. For the case of low impurity concentration there was leaded the comparison of calculated and experimental (from patent) data. The dependence of purification degree on the number of membrane modules composed apparatus was shown.
机译:目前的工作集中在通过一台压缩机多级膜装置(OMMA)从未渗透的杂质中高度净化气体。它看起来像一个简单的单向膜级联,由几个只有一个压缩点的膜模块组成。在这种工作状态下,高压腔的压力从一个压力降到另一个压力,而高渗透组分的浓度却在增加。得到纯化度计算方程。它显示了与进入膜组件或设备的初始流量(进料流量)浓度相比,渗透液的杂质浓度如何降低。获得用于纯化度计算的方程。对于低杂质浓度的情况,需要对计算和实验数据(来自专利)进行比较。显示了纯化程度对具有极值的膜组件组成设备数量的依赖性。确定了单压缩机多级膜设备的描述。得到纯化度计算方程。它显示了与进入膜组件或设备的初始流量(进料流量)浓度相比,渗透液的杂质浓度如何降低。获得用于纯化度计算的方程。对于低杂质浓度的情况,需要对计算和实验数据(来自专利)进行比较。显示了纯化程度对组成膜组件的装置数量的依赖性。

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