Process and system for cleaning a gas stream

1. A process for cleaning a gas stream containing carbon dioxide, comprising:

a) removing, in a at least a first gas-liquid contacting device, a part of the carbon dioxide contained in the gas stream by bringing the gas stream into contact with a first ammoniated liquid, to form a liquid enriched in carbon dioxide and a gas stream partly depleted in carbon dioxide;

b) removing, in a CO 2 removal vessel, at least a part of, the carbon dioxide contained in the gas stream partly depleted in carbon dioxide by bringing the gas stream partly depleted in carbon dioxide leaving step a) into contact with at least a second ammoniated liquid, to form a carbon dioxide depleted gas stream enriched in ammonia; and

c) removing, in at least a second gas-liquid contacting device, at least a part of, the ammonia of the carbon dioxide depleted gas stream enriched in ammonia by bringing the carbon dioxide depleted gas stream enriched in ammonia leaving step b) into contact with the liquid enriched in carbon dioxide formed in step a), to absorb, into the liquid, ammonia from the gas stream, such that a carbon dioxide depleted gas stream at least partly depleted in ammonia and a liquid enriched in ammonia are formed, wherein the liquid enriched in ammonia is the first ammoniated liquid used in step a);

d) contacting, in the second gas-liquid contacting device, the carbon dioxide depleted gas stream at least partly depleted in ammonia prior with a heated liquid to form a heated gas stream; and

e) releasing the heated as stream to the atmosphere.

2. The process according to claim 1 , wherein the carbon dioxide depleted gas stream enriched in ammonia formed in step b) is passed directly to step c) without being subjected to intermediate washing.

3. The process according to claim 1 , wherein the first ammoniated liquid formed in step c) has a R-value of 2.0 to 3.0.

4. The process according to claim 1 , wherein step a) provides a partial removal of carbon dioxide from the gas stream of between 1 and 10%.

5. The process according to claim 4 , wherein the liquid enriched in carbon dioxide formed in step a) has a R-value of 1.5 to 1.9.

6. The process according to claim 1 , further comprising, prior to step a), adjusting the temperature of the gas stream containing carbon dioxide to a temperature of 0-20 C.

7. The process according to claim 1 , further comprising, prior to step a), adjusting the temperature of the gas stream containing carbon dioxide to below 5° C.

8. The process according to claim 1 , further comprising

d) removing, in the post-conditioning stage, at least a part of, the ammonia of the carbon dioxide depleted gas stream at least partly depleted in ammonia by bringing the carbon dioxide depleted gas stream at least partly depleted in ammonia from step c) into contact with a post-conditioning liquid, to absorb, into the liquid, ammonia from the gas stream, such that a gas stream depleted in ammonia and a liquid enriched in ammonia are formed.

9. The process according to claim 8 , wherein the post-conditioning liquid has a pH of equal to or less than 5.

10. The process according to claim 8 , wherein the post-conditioning liquid comprises sulfuric acid.

11. The process according to claim 8 , further comprising:

heating, in the post-conditioning stage, the gas stream depleted in ammonia by bringing it into contact with a heating liquid to form a heated gas stream; and

releasing the heated gas stream to the atmosphere.