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    • 1. 发明申请
    • METHOD AND SYSTEM FOR PRODUCING AN H2 PRODUCT FLOW AND A CO PRODUCT FLOW
    • 方法和系统,用于生成H2产物流和CO流产品
    • WO2014012629A2
    • 2014-01-23
    • PCT/EP2013001972
    • 2013-07-04
    • LINDE AG
    • TROTT THOMAS
    • C01B3/50
    • C01B3/506C01B3/56C01B2203/043C01B2203/046C01B2203/047C01B2203/147F25J3/0223F25J3/0252F25J3/0261F25J2205/04F25J2205/30F25J2205/40F25J2205/60F25J2205/66F25J2210/02F25J2210/04F25J2210/42F25J2220/02F25J2230/32F25J2245/02F25J2270/04F25J2270/24F25J2280/02
    • The invention relates to a method for producing an H2product flow (P) and a CO product flow (Rho') from a supply flow (E"), comprising the steps of: feeding a supply flow (E") having H2 and CO into a separating device (20), which is arranged more particularly in a cold box, separating the supply flow (E") in said separating device (20) into an H2-rich, CO-containing gas fraction (G) and a CO-rich, H2-containing condensate, wherein the condensate is separated into an H2-rich flash gas (F) and the CO product flow (Rho'), wherein when a H2/CO ratio of the supply flow (E") is above that or equal to a pre-definable threshold value, the gas fraction (G) for separating CO and other components (e. g. CH4, C02, H20 and inert gases) is directed through at least one adsorber of an alternating pressure adsorption device (30), and therefore these components are adsorbed onto the at least one adsorber, wherein the adsorber for cleaning the adsorber is purged with a partial current of the H2 product flow (P), which is drawn as a purge gas (S) from the alternating pressure adsorption device (3), wherein said purge gas (S) and the flash gas (F) upstream of the separating device (2) are returned to the supply flow (E"), and wherein at a H2/CO ratio is below said threshold value, the gas fraction (G), the flash gas (F) and, where required, at least part of the CO product flow (Rho') upstream of the separating device (20) is returned to the supply flow (E"). The invention further relates to a system for producing an H2 product flow (P) and a CO product flow (Rho').
    • 本发明涉及一种方法,用于生产H 2产物物流(P)和从进料流(E‘)一个CO产物流(RHO“),包括以下步骤:进料的进料流(E’),其包括H 2和CO(在分离 20),其被布置在特别是在冷箱,在富H 2分离在所述分隔装置(进料流(E“)20),气体成分(G)和富含CO的,含H 2冷凝含CO, 富H 2闪蒸气体中的(F)的冷凝物和CO的产物流(RHO“)被断开,从而高于或在进料流(E“)的H 2 / CO比例等于一个预先给定的阈值时,气体馏分(G),用于 CO和其他部件(例如。B. CH4,CO 2,H 2 O和惰性气体)的分离通过至少一个吸附器的压力回转吸附系统(30)被传递,使得这些部件被吸附在所述至少一个吸附器,该吸附器的吸附器的清洁 用 EM H2产品流(P)的部分流被用作从抽出的变压吸附系统(30)的吹扫气体(S)冲洗,由此该吹扫气体(S),和闪蒸气体(F)的分离装置(20)到进料流的上游(E 是“)则返回,并且其中,在H 2 / CO比率小于所述阈值时,气体部分(G),闪蒸气体(F)和至少(在CO产物流的一部分的上游,如果必要的Rho”分离装置的) (20)的进料流(E“)中被返回。 此外,本发明涉及一种植物用于生产H2产物流(P)和CO的产物流(RHO“)。