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    • 2. 发明申请
    • CARBON DIOXIDE RECOVERY
    • 二氧化碳回收
    • WO2015047838A1
    • 2015-04-02
    • PCT/US2014/056181
    • 2014-09-18
    • INNOSEPRA LLCJAIN, Ravi
    • JAIN, Ravi
    • B01D53/047B01D53/46C01B31/20B01D53/14
    • B01D53/0462B01D53/04B01D53/047B01D53/14B01D53/261B01D53/268B01D2257/30B01D2257/404B01D2257/504B01D2257/602B01D2257/80Y02C10/06Y02C10/08Y02C10/10
    • For separating carbon dioxide (C0 2 ) from a gas stream, a substantially moisture free gas stream is produced using a first temperature swing adsorption (TSA), a first pressure swing adsorption (PSA), a first vacuum swing adsorption (VSA), membrane separation, a first absorption, or any combination thereof. C0 2 is captured from the substantially moisture free gas stream and substantially dry C0 2 depleted stream is produced using a second TSA, a second PSA, a second VSA, or a second absorption with a non-aqueous solvent with or without a chemical reaction. Adsorbents and/or absorbents used during moisture removal are regenerated using the substantially dry C0 2 depleted stream. Purifying a gas stream containing C0 2 and impurities includes producing a stream substantially depleted of moisture and impurities using a physical or reactive adsorbent, thermally regenerating the adsorbent to produce a stream substantially enriched in impurities, and removing impurities from the stream substantially enriched in impurities.
    • 为了从气流中分离二氧化碳(CO 2),使用第一变温吸附(TSA),第一变压吸附(PSA),第一真空变压吸附(VSA),膜分离 ,第一吸收或其任何组合。 从基本上无水分的气流中捕获CO 2,并且使用第二TSA,第二PSA,第二VSA或具有或不具有化学反应的非水溶剂的第二吸收来产生基本上干的CO 2贫化流。 除湿期间使用的吸附剂和/或吸收剂使用基本上干的CO 2贫化物流再生。 净化含有CO 2和杂质的气流包括使用物理或反应性吸附剂产生基本上不含水分和杂质的物流,热再生吸附剂以产生基本上富集杂质的流,以及从基本上富集杂质的物流中除去杂质。