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    • 4. 发明申请
    • REMOVAL OF HYDROGEN SULPHIDE AND CARBON DIOXIDE FROM A STREAM OF FLUID
    • 二氧化碳和氢气从流体流动去除
    • WO2016030272A3
    • 2016-05-12
    • PCT/EP2015069154
    • 2015-08-20
    • BASF SE
    • INGRAM THOMASNOTZ RALFVORBERG GERALDSIEDER GEORG
    • B01D53/14
    • B01D53/1462B01D53/1493B01D2252/2026B01D2252/20405B01D2252/2041B01D2252/20426B01D2252/20431B01D2252/20484B01D2252/502B01D2252/504C07C217/08
    • The invention relates to a method for removing hydrogen sulphide and carbon dioxide from a stream of fluid, the method comprising: a) an absorption step, in which the stream of fluid is brought into contact with an absorption agent comprising an aqueous solution (i) of an amine of general formula (I), where R1, R2 and R3 are selected independently of one another from among C1-4 alkyl and C1-4 hydroxyalkyl; R4 in each case is independently selected from among hydrogen, C1-4 alkyl and C1-4 hydroxyalkyl; R5 in each case is selected from among hydrogen, C1-4 alkyl and C1-4 hydroxyalkyl; X represents OH or NH(CR1 R2R3); m represents 2, 3, 4 or 5; n represents 2, 3, 4 or 5; and o represents 0 or 1; and optionally (ii) at least one tertiary amine, the molar ratio of (i) to (ii) is greater than 0.05; wherein at least 90% of the hydrogen sulphide is removed from the stream of fluid, the selectivity for hydrogen sulphide in relation to carbon dioxide is no greater than 8 and a CO2- and H2S-loaded absorbent agent is thus obtained; b) a regeneration step, in which at least one sub-stream of the CO2- and H2S-loaded absorption agent is regenerated and a regenerated absorption agent is thus obtained; and c) a recirculation step, in which at least one sub-stream of the regenerated absorption agent is recirculated to the absorption step a). The method permits a high degree of separation of the hydrogen sulphide with a simultaneously high coabsorption of carbon dioxide.
    • 一种用于从流体流中除去硫化氢和二氧化碳的方法,包括:a)在接触的吸收剂,水溶液(ⅰ)通式(I)的胺使流体流的吸收步骤,其中R1,R2和R3 独立地选自C 1-4烷基和C1-4Hydroxyalkyl选择; R4独立地选自氢,C 1-4烷基和C 1-4羟基烷基; R5独立地选自氢,C 1-4烷基和C 1-4羟基烷基; X为OH或NH(CR1 R2R3)基团; m为2,3,4或5; n为2,3,4或5; 并且o是0或1; 和任选地(ii)至少一种叔胺,其中的(i)至的摩尔比(ii)的大于0.05; 其中,所述硫化氢的至少90%以从流体流和用于硫化氢超过二氧化碳的选择性除去不大于8,以获得CO 2和H 2 S的负载的吸收剂; b)一种再生步骤,其中至少再生CO 2和H 2 S的负载的吸收剂并获得再生的吸收液的部分流; 和c),其中的再循环步骤是在吸收步骤a)至少循环再生的吸收剂的部分流。 该过程允许在二氧化碳的同时具有高共吸收高度硫化氢的分离。