Process and plant for removing carbon dioxide from synthesis gas

Patent metadata

Field	Value
Publication number	US-11826694-B2
Application number	US-202117524026-A
Country	US
Kind code	B2
Filing date	Nov 11, 2021
Priority date	Nov 11, 2020
Publication date	Nov 28, 2023
Grant date	Nov 28, 2023

Abstract

The present invention relates to a process for removing carbon dioxide from synthesis gas using a hygroscopic, physical absorption medium. The process includes cooling the absorption medium and the synthesis gas; water is at least partially removed from the synthesis gas by condensation; carbon dioxide is removed from the cooled synthesis gas via the cooled absorption medium in a physical absorption step at elevated pressure; laden absorption medium is treated in a plurality of serially arranged flash stages, wherein co-absorbed carbon monoxide and hydrogen are removed from the laden absorption medium in at least one first flash stage, and carbon dioxide is removed from the laden absorption medium in a flash stage arranged downstream of the first flash stage. The process features a high rate of separated carbon dioxide and a pure and dry (anhydrous) carbon dioxide product. The invention further relates to a plant for performing the process.

First claim

What is claimed is:

1. A process for removing carbon dioxide from synthesis gas, wherein the synthesis gas comprises at least hydrogen, carbon monoxide, carbon dioxide and water, comprising:
(a) providing a hygroscopic physical absorption medium;
(b) at least partially removing water from the synthesis gas by cooling the synthesis gas below the dew point of water and separating the condensed water;
(c) cooling the absorption medium;
(d) removing carbon dioxide from the cooled synthesis gas via the cooled absorption medium in a physical absorption step at elevated pressure, wherein the cooled synthesis gas and the cooled absorption medium are run in countercurrent, wherein synthesis gas at least partially freed of water and carbon dioxide is obtained and absorption medium laden with carbon dioxide and partially co-absorbed carbon monoxide and hydrogen is obtained;
(e) discharging the synthesis gas at least partially freed of water and carbon dioxide from the process;
(f) treating the laden absorption medium in a plurality of serially arranged flash stages, wherein co-absorbed carbon monoxide and hydrogen is removed from the laden absorption medium in at least one first flash stage and carbon dioxide is removed from the laden absorption medium in a flash stage arranged downstream of the first flash stage;
(g) compressing to absorption pressure and recycling to step (d) the carbon monoxide and hydrogen obtained in step (f); and
(h) discharging the carbon dioxide obtained in step (f) from the process.

2. The process according to claim 1 , wherein water is removed from the absorption medium in a distillation step arranged downstream of step (f).

3. The process according to claim 2 , wherein the distillation step for removal of water is operated temporarily.

4. The process according to claim 2 , wherein absorption medium vapours obtained in the distillation step are utilized as a stripping medium for removal of carbon dioxide in the downstream flash stage according to step (f).

5. The process according to claim 1 , wherein the downstream flash stage has a lower pressure compared to the first flash stage.

6. The process according to claim 1 , wherein absorption medium obtained in the downstream flash stage is recycled to the physical absorption step according to step (d) for reabsorption of carbon dioxide.

7. The process according to claim 1 , wherein the synthesis gas comprises no sulfur compounds as impurities.

8. The process according to claim 1 , wherein the synthesis gas comprises no hydrogen cyanide and/or no ammonia as an impurity.

9. The process according to claim 1 , wherein the carbon dioxide is not subjected to a drying step after discharging from the process according to step (h).

10. The process according to claim 1 , wherein the carbon dioxide is not subjected to a condensation step.

11. The process according to claim 1 , wherein the process comprises no hot regeneration step for regenerating the laden absorption medium.

12. The process according to claim 1 , wherein water is removed by cooled absorption medium in a further physical absorption step at elevated pressure.

13. The process according to claim 1 , wherein the provided hygroscopic, physical absorption medium comprises methanol or consists substantially of methanol or consists of methanol.

14. The process according to claim 1 , wherein after discharging from the process according to step (h) the carbon dioxide is compressed and subsequently stored or sent to a further use.

15. The process according to claim 1 , wherein an inert gas is utilized as stripping medium for removal of carbon dioxide in the downstream flash stage according to step (f).

16. A plant for removing carbon dioxide from synthesis gas, wherein the synthesis gas comprises at least hydrogen, carbon monoxide, carbon dioxide and water, comprising the following plant components in fluid connection with one another:
(a) a means for cooling the synthesis gas below the dew point of water;
(b) a means for separating water condensed out of the synthesis gas;
(c) a means for cooling a hygroscopic, physical absorption medium;
(d) an absorption column for running the cooled synthesis gas freed of water and the cooled absorption medium in countercurrent at elevated pressure for removal of carbon dioxide from the synthesis gas, wherein synthesis gas at least partially freed of water and carbon dioxide is obtainable and absorption medium laden with carbon dioxide and partially co-absorbed carbon monoxide and hydrogen is obtainable;
(e) a means for discharging the synthesis gas freed of water and carbon dioxide from the plant;
(f) a plurality of serially arranged flash stages comprising a first flash stage for removal of the co-absorbed carbon monoxide and hydrogen from the laden absorption medium and comprising a flash stage arranged downstream of the first flash stage for removal of carbon dioxide from the laden absorption medium;
(g) a compressor for compressing carbon monoxide and hydrogen removed from laden absorption medium and for recycling the compressed carbon monoxide and hydrogen to the absorption column (c); and
(h) a means for discharging carbon dioxide removed from laden absorption medium from the plant.

17. The plant according to claim 16 , wherein the plurality of serially arranged flash stages (f) has a distillation apparatus for removal of water from the absorption medium arranged downstream of it.

18. The plant according to claim 17 , wherein the plant comprises means for withdrawing absorption medium vapours from the distillation apparatus and means for introducing the absorption medium vapours into the flash stage arranged downstream of the first flash stage for use of the absorption medium vapours as stripping medium.

Assignees

• Air Liquide
• Lair Liquide Soc Letude Et Lexploitation Des Procedes Georges Claude

Inventors

• Schmidt Sophia
• Linicus Matthias
• Corbet Sharon

Classifications

• B01D53/1418 Primary

  Recovery of products · CPC title

• B01D3/143

  by two or more of a fractionation, separation or rectification step · CPC title

• B01D19/0005

  with one or more auxiliary substances · CPC title

• B01D19/0036

  Flash degasification (the other groups take precedence) · CPC title

• B01D53/145

  Pretreatment by separation of solid or liquid material · CPC title