Separation of hydrogen sulfide from natural gas
US-2015027055-A1 · Jan 29, 2015 · US
US11458433B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11458433-B2 |
| Application number | US-201816643665-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 30, 2018 |
| Priority date | Sep 4, 2017 |
| Publication date | Oct 4, 2022 |
| Grant date | Oct 4, 2022 |
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An absorbent for the selective removal of hydrogen sulfide over carbon dioxide from a fluid stream, wherein the absorbent contains an aqueous solution, comprising an amine of formula (I) and/or an amine of formula (II) wherein U—V—W is CH—O—CHR5, N—CO—CHR5 or N—CO—NR5; U′—V′—W is C—O—CR5; R1 is independently C1-C5-alkyl; R2 is selected from hydrogen and C1-C5-alkyl; R3 is independently selected from hydrogen and C1-C5-alkyl; R4 is independently selected from hydrogen and C1-C5-alkyl; R5 is selected from hydrogen, C1-C5-alkyl, (C1-C5-alkoxy)-C1-C5-alkyl, and hydroxy-C1-C5-alkyl; and x is an integer from 1 to 10. The absorbent has a reduced tendency for phase separation at temperatures falling within the usual range of regeneration temperatures for the aqueous amine mixtures and a low volatility in aqueous solvents.
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The invention claimed is: 1. A process for the selective removal of hydrogen sulfide over carbon dioxide from a fluid stream, comprising contacting the fluid stream with an absorbent containing an aqueous solution, comprising an amine of formula (I) wherein U—V—W is N—CO—CHR 5 ; R 1 is independently C 1 -C 5 -alkyl; R 2 is selected from hydrogen and C 1 -C 5 -alkyl; R 3 is independently selected from hydrogen and C 1 -C 5 -alkyl; R 4 is independently selected from hydrogen and C 1 -C 5 -alkyl; R 5 is selected from hydrogen, C 1 -C 5 -alkyl, (C 1 -C 5 -alkoxy)-C 1 -C 5 -alkyl, and hydroxy-C 1 -C 5 -alkyl; and x is an integer from 1 to 10, wherein the absorbent comprises a total amount of 15% to 70% by weight of amine of formula (I), based on the total weight of the absorbent, and obtaining a laden absorbent and a treated fluid stream. 2. The process according to claim 1 , wherein the amine is selected from 1[2-(tert-butylamino)ethyl]pyrrolidin-2-one, 1-[2-(tert-butylamino)propyl]pyrrolidin-2-one, 1-[2-(isopropylamino)ethyl]pyrrolidin-2-one, and 1-[2-(isopropylamino)propyl]pyrrolidin-2-one. 3. The process according to claim 2 , wherein the amine is selected from 1-[2-(tert-butylamino)ethyl]pyrrolidin-2-one, and 1-[2-(isopropylamino)ethyl]pyrrolidin-2-one. 4. The absorbent according to claim 3 , wherein the amine is 1-[2-(tert-butylamino)-ethyl]pyrrolidin-2-one. 5. The process according to claim 1 , wherein the absorbent additionally comprises an acid. 6. The process according to claim 1 , wherein the absorbent additionally comprises a tertiary amine and/or severely sterically hindered amine other than the compounds of the general formula (I), wherein severe steric hindrance is understood to mean a tertiary carbon atom directly adjacent to a primary or secondary nitrogen atom. 7. The process according to claim 1 , wherein the absorbent comprises a non-aqueous organic solvent. 8. The process according to claim 7 , wherein the non-aqueous organic solvent is selected from C 4-10 alcohols, ketones, esters, lactones, amides, lactams, sulfones, sulfoxides, glycols, polyalkylene glycols, di- or mono(C 1 -C 4 -alkyl ether) glycols, di- or mono(C 1 -C 4 -alkyl ether) polyalkylene glycols, cyclic ureas, thioalkanols and mixtures thereof. 9. The process according to claim 1 , further comprising regenerating the laden absorbent by heating, decompressing or stripping with an inert fluid.
Removing hydrogen sulfide · CPC title
Secondary amines · CPC title
Methane · CPC title
containing a pyrrolidone-ring · CPC title
Selection of liquid materials for use as absorbents · CPC title
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