首页> 外国专利> METHOD FOR THE SEPARATION OF A GAS MIXTURE FLOW USING TEMPERATURE CHANGE ADSORPTION AND TEMPERATURE CHANGE ADSORPTION INSTALLATION

METHOD FOR THE SEPARATION OF A GAS MIXTURE FLOW USING TEMPERATURE CHANGE ADSORPTION AND TEMPERATURE CHANGE ADSORPTION INSTALLATION

机译:利用温度变化吸附和温度变化吸附安装分离气体混合物的方法

摘要

The invention relates to a method for separating a gas mixture flow, in which a temperature swing adsorption system (100) is used which has a number of adsorption units (A1, A2, A3), which are each operated in a first mode and a second mode, the first Operating mode comprises guiding the gas mixture flow (G) at least partially through an adsorption space of the respective adsorption unit (A1, A2, A3) and subjecting it to an adsorptive mass transfer with at least one adsorbent in its adsorption space, and the second operating mode comprises a first heat transfer fluid flow (W1 ) at a first temperature level through a heat exchange arrangement of the respective adsorption unit (A1, A2, A3) and to transfer heat from the first heat transfer fluid flow (W1) indirectly to the at least one adsorbent in its adsorption space. It is provided that the first mode of operation includes conducting a second heat transfer fluid flow (W2) at a second temperature level through the heat exchange arrangement of the respective adsorption unit (A1, A2, A3) and transferring heat from the at least one adsorbent in its adsorber space indirectly to the second heat transfer fluid flow (W1) to be transferred, and the adsorption units (A1, A2, A3) are each operated in a third operating mode, which includes a third heat transfer fluid flow (W3) at a third temperature level through the heat exchange arrangement of the respective adsorption unit (A1, A2, A3) and to transfer heat from the at least one adsorbent in its adsorption space to the third heat transfer fluid stream (W3). A corresponding temperature swing adsorption system (100) is also the subject of the invention.
机译:本发明涉及一种用于分离气体混合物流的方法,其中使用变温吸附系统(100),该系统具有多个吸附单元(A1,A2,A3),它们分别以第一模式和在第二模式中,第一操作模式包括引导气体混合物流(G)至少部分地通过相应的吸附单元(A1,A2,A3)的吸附空间,并使其在其至少一种吸附剂的作用下进行吸附传质。吸附空间,并且第二操作模式包括处于第一温度水平的第一传热流体流(W1),该第一传热流体流通过相应的吸附单元(A1,A2,A3)的换热装置,并从第一传热流体传热在至少一个吸附剂的吸附空间中间接地流动(W1)。规定,第一运行模式包括通过相应的吸附单元(A1,A2,A3)的热交换装置在第二温度水平下传导第二传热流体流(W2),并从至少一个传热流体传热。吸附剂在其吸附器空间中间接与要传递的第二传热流体流(W1)接触,并且吸附单元(A1,A2,A3)分别在第三操作模式下运行,该模式包括第三传热流体流(W3)通过各自的吸附单元(A1,A2,A3)的热交换装置在第三温度水平下)将热量从至少一种吸附剂在其吸附空间中传递到第三传热流体流(W3)。相应的变温吸附系统(100)也是本发明的主题。

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