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    • 5. 发明公开
    • VERFAHREN UND ANLAGE ZUR SAUERGASANREICHERUNG
    • EP3386608A1
    • 2018-10-17
    • EP16809359.9
    • 2016-12-07
    • BASF SE
    • INGRAM, ThomasVORBERG, GeraldSIEDER, Georg
    • B01D53/14B01D53/86C01B17/04C10L3/10
    • The invention relates to a method for treating an H2S and CO2-containing fluid flow, wherein a) the fluid flow is treated with a first sub-flow (3.01) of a regenerated H2S-selective absorbent in a first absorber (A1) at a pressure of 10 to 150 bar, and a treated fluid flow (3.03) and an H2S-loaded absorbent (3.04) are obtained; b) the H2S-loaded absorbent is heated by means of an indirect heat exchange (3.07) with a regenerated H2S-selective absorbent (3.08); c) the heated H2S-loaded absorbent (3.09) is expanded to a pressure of 1.2 to 10 bar in a low-pressure expansion container (LPF), and a first CO2-enriched exhaust gas and a partially regenerated absorbent (3.11) are obtained; d) the partially regenerated absorbent (3.11) is regenerated in a desorption column (D), and an H2S-enriched exhaust gas (3.23) and a regenerated absorbent (3.08) are obtained; e) the H2S-enriched exhaust gas (3.23) is supplied to a Claus unit (CL), the exhaust gas of the Claus unit is supplied to a hydrogenation unit (HY), and a hydrogenated Claus final gas is obtained; f) the hydrogenated Claus final gas and the first CO2-enriched exhaust gas are treated with a second sub-flow (3.18) of the regenerated H2S-selective absorbent (3.17) in a second absorber (TGA) at a pressure of 1 to 4 bar, and a second CO2-enriched exhaust gas (3.25) and a second H2S-loaded absorbent (3.02) are obtained; and g) the second H2S-loaded absorbent is conducted into the first absorber (A1). The invention further relates to a system which is suitable for carrying out the method. The invention is characterized by a low energy requirement.
    • 8. 发明公开
    • ENTFERNUNG VON SCHWEFELWASSERSTOFF UND KOHLENDIOXID AUS EINEM FLUIDSTROM
    • EP3185989A2
    • 2017-07-05
    • EP15753046.0
    • 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 R
      1 , R
      2 and R
      3 are selected independently of one another from among C
      1-4 alkyl and C
      1-4 hydroxyalkyl; R
      4 in each case is independently selected from among hydrogen, C
      1-4 alkyl and C
      1-4 hydroxyalkyl; R
      5 in each case is selected from among hydrogen, C
      1-4 alkyl and C
      1-4 hydroxyalkyl; X represents OH or NH(CR
      1 R
      2 R
      3 ); 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 CO
      2 - and H
      2 S-loaded absorbent agent is thus obtained; b) a regeneration step, in which at least one sub-stream of the CO
      2 - and H
      2 S-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.
    • 本发明涉及从流体流中除去硫化氢和二氧化碳的方法,该方法包括:a)吸收步骤,其中使流体流与包含水溶液(i)的吸收剂接触, 的通式(I)的胺,其中R 1,R 2和R 3彼此独立地选自C 1-4烷基和C 1-4羟烷基; R4在每种情况下独立地选自氢,C1-4烷基和C1-4羟烷基; R5各自选自氢,C1-4烷基和C1-4羟烷基; X代表OH或NH(CR 1 R 2 R 3); m代表2,3,4或5; n代表2,3,4或5; o代表0或1; 和任选地(ii)至少一种叔胺,(i)与(ii)的摩尔比大于0.05; 其中至少90%的硫化氢从流体流中除去,硫化氢相对于二氧化碳的选择性不大于8,因此获得负载CO 2和H 2 S的吸收剂; b)再生步骤,其中负载CO 2和H 2 S的吸收剂的至少一个子流被再生并由此获得再生的吸收剂; 和c)再循环步骤,其中再生的吸收剂的至少一个子流再循环至吸收步骤a)。 该方法允许高度分离硫化氢同时高度共同吸收二氧化碳。