Process for removing carbon dioxide from gas mixtures
View Patent ↗The present invention relates to a process for removing carbon dioxide and optionally hydrogen sulphide and/or COS from a gas stream containing these compounds by washing the gas with an aqueous washing solution containing water, sulfolane and a secondary or tertiary amine derived from ethanolamine. More particularly the invention relates to the process described above, the process being carried out in the presence of a primary or secondary amine compound in an amount between 0.5 and 15 wt. % based on water, sulfolane and amine. The invention further relates to an absorbent liquid to be used in the above process.
1. A process for the removal of carbon dioxide from a gas stream containing carbon dioxide by washing the gas stream in an absorption zone having from 5-80 contacting trays with an aqueous washing solution, at an aqueous washing solution to gas ratio of between 2 and 6 (weight/weight), said aqueous washing solution containing between 20 and 45 parts by weight water, between 20 and 35 parts by weight sulfolane and between 40 and 55 parts by weight of an amine selected from the group of amines consisting of MEA, DEA, TEA, DIPA and MDEA, wherein the parts by weights are based on the amounts of water, sulfolane and amine together being 100 parts by weight, and, further, wherein the aqueous washing solution contains piperazine in an amount of from 0.7 mol/l to 0.9 mol/l, thereby obtaining an aqueous washing solution loaded with carbon dioxide, and a purified gas stream having a substantially reduced concentration of carbon dioxide, said carbon dioxide loaded aqueous washing solution being substantially free of insoluble carbamates.
2. The process of claim 1 , wherein the gas stream is natural gas or synthesis gas.
3. The process of claim 2 , wherein the gas stream includes an amount of carbon dioxide that is between 1 and 45 mol %, an amount of hydrogen sulphide that is between 0 and 25 mol %, and an amount of COS that is between 0 and 2 mol % (all % based on total gas stream).
4. The process of claim 3 , wherein the aqueous washing solution includes an amount of water that is between 20 and 45 parts by weight, an amount of sulfolane that is between 20 and 35 parts by weight, and an amount of the amine that is between 40 and 55 parts by weight, wherein the parts by weights are based on the amounts of water, sulfolane and amine together being 100 parts by weight.
5. The process of claim 4 , wherein the piperazine is present in the aqueous washing solution in an amount in the range of from 0.6 to 0.8 mol/l.
6. The process of claim 5 wherein the process is carried out at a temperature of at least 20° C.
7. The process of claim 6 , wherein the process also comprises a regeneration of the loaded solvent.
8. The process of claim 7 , wherein the process is carried out at a pressure between 25 and 90 bara.
9. An absorbent liquid containing between 20 and 45 parts by weight water, between 20 and 35 parts by weight sulfolane and between 40 and 55 parts by weight of an amine selected from the group of amines consisting of MEA, DEA, TEA, DIPA and MDEA, wherein the parts by weights are based on the amounts of water, sulfolane and amine together being 100 parts by weight, and, further, wherein the aqueous washing solution contains piperazine in an amount of from 0.7 mol/l to 0.9 mol./l, and wherein said absorbent liquid after absorption of carbon dioxide is substantially free of insoluble carbamates.
10. The absorbent liquid of claim 9 , wherein the piperazine is present in the aqueous washing solution in an amount in the range of from 0.6 to 0.8 mol/l.
11. The absorbent liquid of claim 10 , wherein the amine is MDEA.
12. The process of claim 1 , wherein carbon dioxide is produced at an intermediate pressure of between 3 and 15 bara.
13. The process of claim 1 , wherein the amine in the aqueous washing solution is DIPA.
14. The absorbent liquid of claim 9 , wherein the amine is DIPA.
15. The process of claim 12 , wherein carbon dioxide is produced at an intermediate pressure of between 5 and 10 bara.