发明名称 RTSA method using adsorbent structure for CO2 capture from low pressure and low concentration sources
摘要 A Temperature Swing Adsorption method for separating a first component, comprising a more adsorbable component, from a feed stream comprising more than 50 mol % of a second component, comprising a less adsorbable component, is provided. The method includes providing an adsorbent structure suitable for adsorbing the first component, the structure being of the parallel passage contactor type, and cyclically implementing the following steps. Passing the feed stream through the adsorbent structure thus adsorbing the first component and producing a stream depleted in the first component and enriched in the second component. Heating the adsorbent structure to desorb the adsorbed first component by means of circulating a heating stream enriched in the first component at a temperature suitable for regeneration. And cooling the structure by means of passing through it more than 50% of the stream enriched in the second component produced in the step a).
申请公布号 US9314731(B2) 申请公布日期 2016.04.19
申请号 US201314084945 申请日期 2013.11.20
申请人 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude 发明人 Chen Yudong;Monereau Christian;Sanders, Jr. Edgar S.;Tessier Pascal
分类号 B01D53/04;B01J20/08;B01D53/06 主分类号 B01D53/04
代理机构 代理人 Haynes Elwood L.
主权项 1. A Temperature Swing Adsorption method for separating a first component, comprising a more adsorbable component, from a feed stream comprising more than 50 mol % of a second component, comprising a less adsorbable component, the method comprising: providing an adsorbent structure suitable for adsorbing the first component, the structure being of the parallel passage contactor type, and cyclically implementing the steps consisting of: a) passing the feed stream through the adsorbent structure thus adsorbing the first component and producing a stream depleted in the first component and enriched in the second component, b) heating the adsorbent structure to desorb the adsorbed first component by means of circulating a heating stream enriched in the first component at a temperature suitable for regeneration, c) cooling the structure by means of passing through it more than 50% of the stream enriched in the second component produced in the step a).
地址 Paris FR