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公开(公告)号:US10214482B2
公开(公告)日:2019-02-26
申请号:US15506472
申请日:2015-08-20
Applicant: BASF SE
Inventor: Thomas Ingram , Marion Da Silva , Georg Sieder
IPC: B01D53/14 , B01D53/52 , B01D53/62 , B01D53/78 , B01D53/96 , C07C217/42 , B01J31/24 , C07C217/08 , C10L3/10
Abstract: A compound of the general formula (I) in which R1, R2 and R3 are independently selected from C1-4-alkyl and C1-4-hydroxyalkyl; each R4 is independently selected from hydrogen, C1-4-alkyl and C1-4-hydroxyalkyl; each R5 is independently selected from hydrogen, C1-4-alkyl and C1-4-hydroxyalkyl; m is 2, 3, 4 or 5; n is 2, 3, 4 or 5; and o is an integer from 0 to 10. A preferred compound of the formula (I) is 2-(2-tert-butylaminoethoxy)ethylamine. Absorbents comprising a compound of the formula (I) have rapid absorption of carbon dioxide from fluid streams and are also suitable for processes for the simultaneous removal of H2S and CO2, where given H2S limits have to be observed but complete removal of CO2 is not required.
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公开(公告)号:US10207217B2
公开(公告)日:2019-02-19
申请号:US15506635
申请日:2015-08-20
Applicant: BASF SE
Inventor: Thomas Ingram , Ralf Notz , Gerald Vorberg , Georg Sieder
IPC: B01D53/14 , B01D53/52 , B01D53/78 , B01D53/96 , C07C217/08 , C07C217/28 , C07C217/42
Abstract: A process for removing hydrogen sulfide and carbon dioxide from a fluid stream comprises a) an absorption step in which the fluid stream is contacted with an absorbent comprising an aqueous solution (i) of an amine of the general formula (I) in which R1, R2 and R3 are each independently selected from C1-4-alkyl and C1-4-hydroxyalkyl; each R4 is independently selected from hydrogen, C1-4-alkyl and C1-4-hydroxyalkyl; each R5 is independently selected from hydrogen, C1-4-alkyl and C1-4-hydroxyalkyl; X is OH or NH(CR1R2R3); m is 2, 3, 4 or 5; n is 2, 3, 4 or 5; and o is 0 or 1; and optionally (ii) at least one tertiary amine, where the molar ratio of (i) to (ii) is greater than 0.05; wherein at least 90% of the hydrogen sulfide is removed from the fluid stream and selectivity for hydrogen sulfide over carbon dioxide is not greater than 8, wherein a CO2- and H2S-laden absorbent is obtained; b) a regeneration step in which at least a substream of the CO2- and H2S-laden absorbent is regenerated and a regenerated absorbent is obtained; and c) a recycling step in which at least a substream of the regenerated absorbent is recycled into the absorption step a). The process allows a high level of hydrogen sulfide removal with a simultaneously high coabsorption of carbon dioxide.
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公开(公告)号:US09931594B2
公开(公告)日:2018-04-03
申请号:US13780377
申请日:2013-02-28
Applicant: BASF SE
Inventor: Torsten Katz , Christian Riemann , Georg Sieder
CPC classification number: B01D53/1456 , B01D53/1425 , B01D53/1475 , B01D53/1493 , B01D53/263 , B01D53/265 , B01D2252/202 , B01D2252/2053 , B01D2252/40 , B01D2252/504 , B01D2256/24 , B01D2257/302 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/408 , B01D2257/504 , B01D2257/80 , B01D2258/0283 , B01D2258/05
Abstract: A process for removing acid gases from a water vapor-containing fluid stream comprises a) providing an absorption liquid which is incompletely miscible with water; b) treating the fluid stream in an absorption zone with the absorption liquid to obtain an acid gas-depleted treated fluid stream and an acid gas-loaded absorption liquid; c) directing the treated fluid stream to a rehydration zone and treating the fluid stream with an aqueous liquid to volatilize at least part of the aqueous liquid; d) regenerating the loaded absorption liquid to expel the acid gases at least in part and obtain a regenerated absorption liquid, and directing the regenerated absorption liquid to step b); and e) separating, from the absorption liquid, an aqueous liquid that has condensed in the absorption zone, and directing the aqueous liquid to step c). The process allows for an efficient removal of water accumulated in the absorption liquid system.
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14.
公开(公告)号:US12138583B2
公开(公告)日:2024-11-12
申请号:US17431872
申请日:2020-02-14
Applicant: BASF SE
Inventor: Martin Ernst , Thomas Ingram , Gerald Vorberg , Georg Sieder
IPC: B01D53/14 , C07D295/13 , C10L3/10
Abstract: A process for removal of acid gases from fluid stream, wherein the fluid stream is brought into contact with an absorbent to obtain a treated fluid stream and a laden absorbent, the absorbent comprising a diluent and a compound of the general formula (I) wherein R1 is selected from C1-C8-alkyl and C2-C8-hydroxyalkyl; R2 is selected from hydrogen and C1-C8-alkyl; R3 is selected from hydrogen and C1-C8-alkyl; R4 is selected from hydrogen and C1-C8-alkyl; R5 is C1-C8-alkyl; with the proviso that at least one of the following conditions (i) and (ii) is met: (i) R5 is C3-C8-alkyl bound to the nitrogen atom via a secondary or tertiary carbon atom; (ii) when R4 is hydrogen, R3 is C1-C8-alkyl; or when R4 is C1-C8-alkyl, at least one of R2 and R3 is C1-C8-alkyl; and n is an integer from 0 to 6. Further provided is an absorbent for the absorption of acid gases from a fluid stream, comprising a diluent and a compound of the general formula (I) as defined above, as well as the use of a compound of the general formula (I) as defined above for removal of acid gases from a fluid stream. The absorbents are useful for the selective removal of hydrogen sulfide from fluid streams and have high acid gas loading capacity, high stability, and low volatility.
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公开(公告)号:US11278841B2
公开(公告)日:2022-03-22
申请号:US16238069
申请日:2019-01-02
Applicant: BASF SE
Inventor: Thomas Ingram , Ralf Notz , Gerald Vorberg , Georg Sieder
IPC: B01D53/14 , B01D53/52 , B01D53/78 , B01D53/96 , C07C217/08 , C07C217/28 , C07C217/42
Abstract: A process for removing hydrogen sulfide and carbon dioxide from a fluid stream comprises a) an absorption step in which the fluid stream is contacted with an absorbent comprising an aqueous solution (i) of an amine of the general formula (I) in which R1, R2 and R3 are each independently selected from C1-4-alkyl and C1-4-hydroxyalkyl; each R4 is independently selected from hydrogen, C1-4-alkyl and C1-4-hydroxyalkyl; each R5 is independently selected from hydrogen, C1-4-alkyl and C1-4-hydroxyalkyl; X is OH or NH(CR1R2R3); m is 2, 3, 4 or 5; n is 2, 3, 4 or 5; and o is 0 or 1; and optionally (ii) at least one tertiary amine, where the molar ratio of (i) to (ii) is greater than 0.05; wherein at least 90% of the hydrogen sulfide is removed from the fluid stream and selectivity for hydrogen sulfide over carbon dioxide is not greater than 8, wherein a CO2— and H2S-laden absorbent is obtained; b) a regeneration step in which at least a substream of the CO2— and H2S-laden absorbent is regenerated and a regenerated absorbent is obtained; and c) a recycling step in which at least a substream of the regenerated absorbent is recycled into the absorption step a). The process allows a high level of hydrogen sulfide removal with a simultaneously high coabsorption of carbon dioxide.
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公开(公告)号:US11173446B2
公开(公告)日:2021-11-16
申请号:US16484860
申请日:2018-02-09
Applicant: BASF SE , ExxonMobil Research and Engineering Company
Inventor: Thomas Ingram , Martin Ernst , Gerald Vorberg , Alexander Panchenko , Sophia Ebert , Thomas Wesley Holcombe , Michael Siskin , Carla Pereira , Georg Sieder
Abstract: In a process for removal of acid gases from a fluid stream the fluid stream is contacted with an absorbent to obtain a treated fluid stream and a laden absorbent. The absorbent comprises a diluent and a compound of the general formula (I) wherein R1 is C1-C3-alkyl; R2 is C1-C3-alkyl; R3 is selected from hydrogen and C1-C3-alkyl; and R4 is selected from hydrogen and C1-C3-alkyl.
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公开(公告)号:US10464013B2
公开(公告)日:2019-11-05
申请号:US15506451
申请日:2015-08-20
Applicant: BASF SE
Inventor: Gerald Vorberg , Ralf Notz , Thomas Ingram , Georg Sieder , Torsten Katz
IPC: B01D53/14 , B01D53/78 , B01D53/96 , C07C217/08 , C07C217/28 , C07C217/42 , C10L3/10
Abstract: An absorbent for selective removal of hydrogen sulfide from a fluid stream comprises an aqueous solution of a) a tertiary amine, b) a sterically hindered secondary amine of the general formula (I) in which R1 and R2 are each independently selected from C1-4-alkyl and C1-4-hydroxyalkyl; R3, R4, R5 and R6 are each independently selected from hydrogen, C1-4-alkyl and C1-4-hydroxyalkyl, with the proviso that at least one R4 and/or R5 radical on the carbon atom bonded directly to the nitrogen atom is C1-4-alkyl or C1-4-hydroxyalkyl when R3 is hydrogen; x and y are integers from 2 to 4 and z is an integer from 1 to 4; where the molar ratio of b) to a) is in the range from 0.05 to 1.0, and c) an acid in an amount, calculated as neutralization equivalent relative to the protonatable nitrogen atoms in a) and b), of 0.05 to 15.0%. One preferred amine of the formula I is 2-(2-tert-butylaminoethoxy)ethanol. The absorbent allows a defined H2S selectivity to be set at pressures of the kind typical in natural gas processing.
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