Systems and methods for the separation of carbon dioxide and water
Systems and methods for the separation and capture of carbon dioxide from water are generally described. In some embodiments, a vapor stream containing carbon dioxide and water is separated using a cascade of at least two flash drums. Additional flash steps may be incorporated to remove atmospheric gases, such as nitrogen and argon, from the feed. Carbon dioxide may be condensed and pressurized at purities suitable for pipeline transport and eventual storage in geological formations. In addition, water may be recovered at high purity. In some embodiments, fuel cells may be used in combination with fuel reforming or gasification to produce syngas. Certain aspects of the invention involve innovations related to the combined reforming and fuel cell process, that, in certain embodiments, do not depend upon water and carbon dioxide separation. It should be understood, however, that the invention is not limited to the applications described above, and may be used with any suitable system in which the separation of carbon dioxide and water is desired.
1. A method of separating carbon dioxide and water, comprising:
separating a first fluid stream comprising carbon dioxide and water within a first flash drum to create a second fluid stream enriched in water relative to the first fluid stream and a third fluid stream enriched in carbon dioxide relative to the first fluid stream, wherein the third fluid stream contains at least about 99 wt % carbon dioxide; and
separating at least a portion of the second fluid stream comprising carbon dioxide and water within a second flash drum to create a fourth fluid stream enriched in water relative to the second fluid stream, wherein the fourth fluid stream contains at least about 99 wt % water.
2. A method of separating carbon dioxide and water, comprising:
separating a first fluid stream comprising carbon dioxide and water within a first flash drum to create a second fluid stream enriched in water relative to the first fluid stream;
separating at least a portion of the second fluid stream comprising carbon dioxide and water within a second flash drum to create a third fluid stream enriched in carbon dioxide relative to the second fluid stream; and
recycling and directly combining at least a portion of the third fluid stream with the first fluid stream.
3. The method of claim 1 , wherein the fourth fluid stream contains at least about 99.8 wt % water.
4. The method of claim 1 , wherein at least one of the first and second separation steps is performed essentially adiabatically.
5. The method of claim 1 , comprising creating from the second fluid stream in the second flash drum a fifth fluid stream enriched in carbon dioxide relative to the second fluid stream.
6. The method of claim 1 , comprising sequestering the third fluid stream.
7. The method of claim 1 , wherein the pressure in the first flash drum is between about 2 bar and about 35 bar.
8. The method of claim 1 , wherein the pressure in the second flash drum is between about 2 bar and about 35 bar.
9. The method of claim 1 , wherein the first fluid stream contains less than about 1.5 wt % carbon monoxide.
10. The method of claim 1 , wherein the first fluid stream consists essentially of carbon dioxide and water.
11. The method of claim 1 , wherein the weight ratio of carbon dioxide to carbon monoxide in the first fluid stream is at least about 30:1.
12. The method of claim 1 , wherein the first fluid stream comprises or is derived from at least a portion of a fluid product of a chemical reactor.
13. The method of claim 1 , wherein the first fluid stream comprises or is derived from a syngas.
14. The method of claim 1 , wherein the second flash drum is operated at ambient temperature.
15. The method of claim 5 , comprising recycling and combining at least a portion of the fifth fluid stream with the first fluid stream.
16. The method of claim 1 , wherein the third fluid stream contains at least about 99.9 wt % carbon dioxide.
17. The method of claim 1 , wherein the fourth fluid stream contains at least about 99.99 wt % water.
18. The method of claim 2 , wherein the first fluid stream contains less than about 1.5 wt % carbon monoxide.
19. The method of claim 2 , wherein the first fluid stream comprises or is derived from a syngas.
20. The method of claim 2 , wherein the second flash drum is operated at ambient temperature.