Carbon dioxide absorbent comprising triamine
US-2017246587-A1 · Aug 31, 2017 · US
US12290779B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12290779-B2 |
| Application number | US-202318353338-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 17, 2023 |
| Priority date | Mar 25, 2019 |
| Publication date | May 6, 2025 |
| Grant date | May 6, 2025 |
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Disclosed herein is a method and system for CO 2 removal from a gas stream using a diamine solvent having a Formula I R 1 (R 2 )N-L 1 -NH—R 3 Formula I. With respect to Formula I, each of R 1 and R 2 independently is aliphatic, cycloaliphatic, or R 1 and R 2 together with the nitrogen to which they are attached, form a heterocyclyl ring; L 1 is aliphatic, cycloaliphatic, or L 1 and R 1 together with the nitrogen to which they are attached form a heterocyclyl ring; and R 3 is aliphatic, cycloaliphatic, cycloalkylalkyl, or alkoxyalkyl. And/or the compound may have a viscosity of less than 75 cP at a CO 2 -loading of 40 mol % and at a temperature of 40° C.
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We claim: 1. A method, comprising: contacting a gas stream comprising a first amount of CO 2 with a CO 2 -lean solvent stream comprising a compound according to Formula I, to form a treated gas stream comprising a second amount of CO 2 that is less than the first amount, and to form a CO 2 -rich solvent stream; and heating the CO 2 -rich solvent stream to form a CO 2 stream and regenerate the CO 2 -lean solvent; wherein the compound according to Formula I has a structure R 1 (R 2 )N-L 1 -NH—R 3 Formula I each of R 1 and R 2 independently is aliphatic, cycloaliphatic, or R 1 and R 2 together with the nitrogen to which they are attached, form a heterocyclyl ring; L 1 is aliphatic, cycloaliphatic, or L 1 and R 1 together with the nitrogen to which they are attached form a heterocyclyl ring; and R 3 is aliphatic, cycloaliphatic, cycloalkylalkyl, or alkoxyalkyl; and wherein the CO 2 -lean solvent stream consists essentially of the compound of Formula I; and the compound according to Formula I is not 2. The method of claim 1 , wherein the CO 2 -rich solvent comprises less than 10 wt % water. 3. The method of claim 1 , wherein at least one of R 1 and R 2 is branched alkyl or cycloalkyl. 4. The method of claim 1 , wherein R 1 forms a heterocyclyl with L 1 . 5. The method of claim 1 , wherein R 1 and R 2 together with the nitrogen to which they are attached, forms a heterocyclyl ring. 6. The method of claim 1 , wherein at least one of R 1 and R 2 is not linear alkyl. 7. The method of claim 1 , wherein R 3 is alkoxyalkyl. 8. The method of claim 1 , wherein each of R 1 and R 2 independently is C 1-6 alkyl. 9. The method of claim 1 , wherein R 1 and R 2 together with the nitrogen to which they are attached form a 5- or 6-membered heterocyclyl ring. 10. The method of claim 1 , wherein L 1 is C 2-4 alkyl. 11. The method of claim 1 , wherein L 1 and R 1 together with the nitrogen to which they are attached form a 5- or 6-membered heterocyclyl ring. 12. The method of claim 1 , wherein R 3 is branched C 3-6 alkyl, or alkoxyalkyl. 13. The method of claim 1 , wherein the compound is selected from 14. The method of claim 1 , wherein: the solvent has a vapor pressure of less than 1 Torr at 40° C. and a residual water content of less than 0.1 wt %; the solvent has a viscosity of less than 75 cP at a CO 2 -loading of 40 mol % and at a temperature of 40° C.; or a combination thereof. 15. The method of claim 1 , wherein contacting the gas stream with the CO 2 -lean solvent comprises contacting the gas stream at a first temperature of from 30° C. to 80° C. 16. The method of claim 1 , wherein heating the CO 2 -rich solvent comprises heating the CO 2 -rich solvent to a second temperature of 80° C. to 160° C. 17. The method of claim 1 , further comprising cooling the regenerated CO 2 -lean solvent to a temperature of from 30° C. to 60° C.
Regeneration of liquid absorbents · CPC title
Secondary amines · CPC title
Tertiary amines · CPC title
Diamines · CPC title
containing a morpholine-ring · CPC title
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