Carbon dioxide capture and liquefaction
View Patent ↗An energy-efficient method of recovering carbon dioxide (CO 2 ) in a high-pressure liquid state from a high-pressure gas stream. The method includes cooling, condensing, and/or separating CO 2 from a high-pressure gas stream in two or more separation zones and further purifying the resulting sub-critical pressure liquid CO 2 streams in a third purification zone to thereby provide purified CO 2 . The purified liquid CO 2 may be pumped to above the critical pressure for further utilization and/or sequestration for industrial or environmental purposes.
1. A method of recovering carbon dioxide (CO 2 ) in a liquid state from a high-pressure gas stream, said method comprising:
(a) cooling and partially condensing a high-pressure feed gas stream to thereby provide a condensed CO 2 -rich fraction and an uncondensed CO 2 -lean fraction;
(b) recovering a CO 2 -rich liquid stream from at least a portion of said uncondensed CO 2 -lean fraction wherein said recovering comprises one or more of the following steps—
(i) absorbing CO 2 from said uncondensed CO 2 -lean fraction, and/or
(ii) adsorbing CO 2 from said uncondensed CO 2 -lean fraction, and/or
(iii) freezing CO 2 from said uncondensed CO 2 -lean fraction;
(c) combining at least a portion of said CO 2 -rich liquid stream recovered in step (b) with at least a portion of said condensed CO 2 -rich fraction to thereby provide a combined CO 2 -rich stream; and
(d) fractionating at least a portion of said combined CO 2 -rich stream to separate non-CO 2 components therefrom and thereby provide a purified CO 2 -rich liquid stream,
wherein said high-pressure feed gas stream has a pressure of at least 60.4 psia, wherein said condensed CO 2 -rich fraction and said combined CO 2 -rich stream are liquid streams, wherein said purified CO 2 -rich liquid stream has a pressure of at least 100 psia.
2. The process of claim 1 , wherein said condensed CO 2 -rich fraction has a pressure of at least 650 psia and said combined CO 2 -rich stream has a pressure of at least 500 psia.
3. The process of claim 1 , further comprising injecting said purified CO 2 -rich liquid stream into a geological formation at a pressure greater than the average formation pressure of said geological formation.
4. The process of claim 1 , wherein said high-pressure feed gas stream comprises a natural gas stream or a synthesis gas stream.
5. The process of claim 1 , wherein said high-pressure feed gas stream has a pressure of at least 350 psia and comprises at least 20 mole percent CO 2 prior to said cooling of step (a).
6. The process of claim 1 , wherein said high-pressure feed gas stream comprises water in an amount not more than 50 ppm by volume and less than 1 mole percent of one or more sulfur-containing compounds.
7. The process of claim 1 , wherein said condensed CO 2 -rich fraction comprises at least 10 percent of the total CO 2 originally present in said high-pressure feed gas stream and said uncondensed CO 2 -lean fraction comprises at least about 50 percent of the total non-CO 2 components originally present in said high-pressure feed gas stream.
8. The process of claim 1 , wherein the pressure of said uncondensed CO 2 -lean fraction is within 200 pounds per square inch, (psi) of the pressure of said high-pressure feed gas stream prior to said cooling of step (a).
9. The process of claim 1 , wherein at least a portion of said cooling of step (a) is provided by a cascade refrigeration system, a mixed refrigeration system, an acoustic refrigeration system, and/or an absorption refrigeration system.
10. The process of claim 1 , wherein said recovering of step (b) comprises adsorbing and/or absorbing CO 2 from said uncondensed CO 2 -lean fraction to thereby produce a CO 2 -rich gaseous stream, wherein said recovering of step (b) includes compressing and/or cooling said CO 2 -rich gaseous stream to form said CO 2 -rich liquid stream having a pressure of at least 100 psig.
11. The process of claim 1 , wherein said recovering of step (b) comprises adsorbing CO 2 from said uncondensed CO 2 -lean fraction using a solid adsorbent material, wherein said adsorbing produces a CO 2 -rich tail gas stream, wherein said recovering of step (b) comprises compressing and/or cooling at least a portion of said CO 2 -rich tail gas stream to thereby provide said CO 2 -rich liquid stream.
12. The process of claim 1 , wherein said recovering of step (b) comprises absorbing CO 2 from said uncondensed CO 2 -lean fraction using a circulating liquid solvent, wherein said absorbing produces a CO 2 -rich off-gas stream, wherein said recovering of step (b) comprises compressing and/or cooling at least a portion of said recovered CO 2 -rich off-gas stream to thereby provide said CO 2 -rich liquid stream.
13. The process of claim 12 , wherein said circulating liquid solvent is selected from a group consisting of methanol, SELEXOL solvent (DEPG), PURISOL solvent (NMP), MORPHYSORB solvent (NFM and NAM), Sulfinol solvent (Solfolane and di-isopropanolamine or Solfolane and methyldiethanolamine), reversible ionic liquids, propylene carbonate, hot potassium carbonate, amines, chilled ammonia, ammonium carbonate, and combinations thereof.
14. The process of claim 1 , wherein said recovering of step (b) comprises freezing CO 2 from said uncondensed CO 2 -lean fraction to thereby provide a plurality of CO 2 solids and melting at least a portion of said CO 2 solids to thereby provide said CO 2 -rich liquid stream.
15. The process of claim 1 , further comprising, prior to said cooling of step (a), passing at least a portion of said high-pressure gas stream through at least one membrane separation device to thereby provide a first permeate stream and a first CO 2 -enriched non-permeate stream, wherein said high-pressure feed gas stream at least partially condensed in step (a) comprises at least a portion of said first CO 2 -enriched non-permeate stream.
16. A method of recovering carbon dioxide (CO 2 ) in a liquid state from a high-pressure gas stream, said method comprising:
(a) cooling and partially condensing a high-pressure feed gas stream to thereby provide a condensed CO 2 -rich fraction and an uncondensed CO 2 -lean fraction;
(b) recovering a CO 2 -rich liquid stream from at least a portion of said uncondensed CO 2 -lean fraction, wherein said recovering comprises one or more of the following steps—
(i) absorbing CO 2 from said uncondensed CO 2 -lean fraction using a circulating liquid solvent to thereby provide a CO 2 -rich off-gas stream, wherein said recovering further comprises compressing and/or cooling at least a portion of said recovered CO 2 -rich off-gas stream to thereby provide said CO 2 -rich liquid stream, and/or
(ii) adsorbing CO 2 from said uncondensed CO 2 -lean fraction using a solid adsorbent material to thereby provide a CO 2 -rich tail gas stream, wherein said CO 2 -rich liquid stream recovered comprises at least a portion of said CO 2 -rich tail gas stream, and/or
(iii) freezing CO 2 from said uncondensed CO 2 -lean fraction using one or more direct or indirect heat exchange methods to thereby provide a plurality of CO 2 solids and melting at least a portion of said CO 2 solids to thereby provide said CO 2 -rich liquid stream;
(c) introducing at least a portion of said CO 2 -rich liquid stream recovered in step (b) and/or at least a portion of said condensed CO 2 -rich fraction resulting from said cooling and partially condensing of step (a) into a purification zone; and
(d) separating at least a portion of the non-CO 2 components from said CO 2 -rich liquid stream and/or said condensed CO 2 -rich fraction introduced into said purification zone to thereby provide a purified CO 2 -rich liquid stream,
wherein each of said high-pressure feed gas stream, said condensed CO 2 -rich fraction, and said purified CO 2 -rich liquid stream has a pressure greater than 77 psia.
17. The process of claim 16 , wherein said high-pressure feed gas stream comprises a natural gas or a synthesis gas stream.
18. The process of claim 16 , wherein said purified CO 2 liquid stream comprises at least 75 percent of the CO 2 originally present in said high-pressure feed gas stream.
19. The process of claim 16 , wherein not more than 90 percent of the CO 2 present in said purified CO 2 -rich liquid stream was subjected to compression during said recovering of step (b).
20. The process of claim 16 , wherein said high-pressure feed gas stream has a pressure of at least 350 psia and comprises at least 20 mole percent CO 2 prior to said cooling of step (a), wherein said high-pressure feed gas stream has been pre-treated for the removal of non-methane hydrocarbons, sulfur-containing compounds, and water prior to said cooling of step (a).
21. The process of claim 16 , wherein said recovering of step (b) comprises adsorbing CO 2 from said uncondensed CO 2 -lean fraction, wherein said CO 2 -rich liquid stream recovered in step (b) has a pressure of at least 77 psia.
22. The process of claim 16 , wherein said recovering of step (b) comprises absorbing CO 2 from said uncondensed CO 2 -lean fraction wherein said CO 2 -rich liquid stream has a pressure of at least 77 psia, wherein said circulating liquid solvent is selected from a group consisting of methanol, SELEXOL solvent (DEPG), PURISOL solvent (NMP), MORPHYSORB solvent (NFM and NAM), Sulfinol solvent (Solfolane and di-isopropanolamine or Solfolane and methyldiethanolamine), Flexsorb SE solvent (Solfolane and sterically-hindered amine), reversible ionic liquids, propylene carbonate, hot potassium carbonate, amines, chilled ammonia, ammonium carbonate, and combinations thereof.
23. The process of claim 16 , wherein said recovering of step (b) comprises freezing said CO 2 from said uncondensed CO 2 -lean fraction, wherein said CO 2 -rich liquid stream has a pressure of at least 77 psia.
24. The process of claim 16 , further comprising, prior to said cooling of step (a), passing at least a portion of said high-pressure gas stream through at least one membrane separation device to thereby provide a first permeate stream and a first CO 2 -enriched non-permeate stream, wherein said high-pressure feed gas stream at least partially condensed in step (a) comprises at least a portion of said first CO 2 -enriched non-permeate stream.
25. A method of recovering carbon dioxide (CO 2 ) in a liquid state from a high-pressure gas stream, said method comprising:
(a) cooling and partially condensing a high-pressure feed gas stream to thereby provide a condensed CO 2 -rich fraction and an uncondensed CO 2 -lean fraction;
(b) passing at least a portion of said uncondensed CO 2 -lean fraction though at least one membrane separation device to thereby provide a second permeate stream and a second CO 2 -enriched non-permeate stream
(c) recovering a CO 2 -rich liquid stream from at least a portion of said second CO 2 -enriched non-permeate stream, wherein said recovering comprises one or more of the following steps—
(i) absorbing CO 2 from said uncondensed CO 2 -lean fraction, and/or
(ii) adsorbing CO 2 from said uncondensed CO 2 -lean fraction, and/or
(iii) freezing CO 2 from said uncondensed CO 2 -lean fraction;
(d) introducing at least a portion of said CO 2 -rich liquid stream recovered in step (d) and/or at least a portion of said condensed CO 2 -rich fraction resulting from said cooling and partially condensing of step (a) into a purification zone; and
(e) separating at least a portion of the non-CO 2 components from said CO 2 -rich liquid stream and/or said condensed CO 2 -rich fraction introduced into said purification zone to thereby provide a purified CO 2 -rich liquid stream,
wherein each of said high-pressure feed gas stream, said condensed CO 2 -rich fraction, and said purified CO 2 -rich liquid stream has a pressure greater than 77 psia.