Advanced intercooling and recycling in CO
View Patent ↗The present invention relates to a gas purification system for removal of acidic gases from a gas stream. The system comprises an absorption unit arranged for receiving a gas stream and contacting it with a wash solution stream and a cooling unit in fluid communication with the absorption unit. The cooling unit receives wash solution enriched with acidic gases from a first withdrawal level of said absorption unit, cools the enriched wash solution, and provides cooled, enriched wash solution to a first reintroduction level of the absorption unit upstream of the withdrawal level. The ratio of withdrawn wash solution is 10-90% of the total wash solution stream.
1. A gas purification system for removal of acidic gases from a gas stream, comprising:
an absorption unit arranged for receiving a gas stream and contacting it with a wash solution stream;
a cooling unit in variable fluid communication with the absorption unit, wherein the cooling unit receives wash solution enriched with acidic gases from a first withdrawal level of the absorption unit, cools the enriched wash solution, and provides cooled, enriched wash solution to a first reintroduction level of the absorption unit upstream of the first withdrawal level;
wherein the cooling unit further receives wash solution enriched with acidic gases from a second withdrawal level of the absorption unit, and provides cooled, enriched wash solution to a second reintroduction level corresponding to the second withdrawal level of the absorption unit; and
wherein the second reintroduction level corresponds to the first reintroduction level.
2. The gas purification system according to claim 1 , wherein the ratio of withdrawn wash solution from the first withdrawal level is 10-90% of the total wash solution stream.
3. The gas purification system according to claim 2 , wherein the ratio of withdrawn wash solution from the first withdrawal level is 30-70% of the total wash solution stream.
4. The gas purification system according to claim 1 , wherein the acidic gases are selected from the group consisting of CO 2 and H 2 S.
5. The gas purification system according to claim 1 , wherein said absorption unit is a packed bed column.
6. The gas purification system according to claim 1 wherein 100% of the total wash solution is withdrawn from the second withdrawal level of the absorption unit.
7. The gas purification system of claim 6 wherein the ratio of withdrawn wash solution from the second withdrawal level is 10-90% of the total wash solution.
8. The gas purification system according to claim 7 , wherein the ratio of withdrawn wash solution from the second withdrawal level is 30-70% of the total wash solution stream.
9. The gas purification system according to claim 1 wherein the wash solution provided at the first reintroduction level and the wash solution provided at the second reintroduction level are commonly reintroduced to the absorption unit.
10. The gas purification system according to claim 9 wherein the wash solution provided at the first reintroduction level and the wash solution provided at the second reintroduction level are reintroduced via the same line.
11. The gas purification system according to claim 1 wherein the cooling unit receives wash solution enriched with acidic gases from the first withdrawal level of the absorption unit, cools the enriched wash solution to a temperature in the range of 20-70° C., and provides the cooled, enriched wash solution to the first reintroduction level of the absorption unit upstream of the first withdrawal level.
12. The gas purification system of claim 1 wherein variable fluid communication further comprises either continuous or discontinuous fluid communication.
13. A gas purification system for removal of acidic gases from a gas stream, comprising:
an absorption unit arranged for receiving a gas stream and contacting it with a wash solution stream, the absorption unit having a first withdrawal level, wherein the wash solution stream divides into a first portion and a second portion;
a cooling unit in variable fluid communication with the absorption unit, wherein the cooling unit
receives the wash solution stream enriched with acidic gases from the first withdrawal level of said absorption unit,
cools the enriched wash solution stream,
provides the cooled, first portion of enriched wash solution stream to a first reintroduction level of the absorption unit upstream of the withdrawal level,
provides the cooled second portion of the enriched wash solution stream to a second reintroduction level of the absorption unit,
wherein the second reintroduction level corresponds to the first withdrawal level; and
a regenerator in fluid communication with the absorption unit, wherein the regenerator receives the wash solution from a second withdrawal level, wherein the CO 2 is separated from the wash solution.
14. The gas purification system of claim 13 wherein variable fluid communication further comprises either continuous or discontinuous fluid communication.