Two column hydrocarbon recovery from carbon dioxide enhanced oil recovery streams

1. A method for use in an enhanced oil recovery (EOR) process, comprising:

receiving, by a first heat exchanger, a carbon dioxide recycle stream from the EOR process and producing a cooled carbon dioxide recycle stream, wherein the carbon dioxide recycle stream comprises carbon dioxide and C 1 -C 8 hydrocarbons;

receiving, by a first distillation column, the cooled carbon dioxide recycle stream from the first heat exchanger and separating the cooled carbon dioxide recycle stream to produce a first top effluent stream and a first bottom effluent stream, wherein the first top effluent stream comprises carbon dioxide, C 1 -C 4 hydrocarbons, and trace amounts of C 5 -C 8 hydrocarbons, and wherein the first bottom effluent stream comprises carbon dioxide, C 3 -C 8 hydrocarbons, and trace amounts of C 1 -C 2 hydrocarbons;

receiving, by a second distillation column, the first bottom effluent stream from the first distillation column and producing a second top effluent stream and a second bottom effluent stream, wherein the second top effluent stream comprises carbon dioxide, C 2 -C 4 hydrocarbons, and is substantially free of C 5 -C 8 hydrocarbons, wherein the second bottom effluent stream comprises C 3 -C 8 hydrocarbons and is substantially free of carbon dioxide and C 1 -C 2 hydrocarbons, and wherein the first distillation column and the second distillation column are the only two distillation columns used in the method; and

receiving, by an expansion valve, the second top effluent stream from the second distillation column and producing an expanded second top effluent stream.

2. The method of claim 1 , wherein the carbon dioxide recycle stream comprises nitrogen, wherein the first top effluent stream comprises nitrogen, wherein the first bottom effluent stream is substantially free of nitrogen, wherein the second top effluent stream is substantially free of nitrogen, and wherein the second bottom effluent stream is substantially free of nitrogen.

3. The method of claim 1 , wherein the second distillation column comprises a reboiler configured to reboil a portion of the second bottom effluent stream.

4. The method of claim 1 , wherein no cryogenic conditions are used in the process.

5. The method of claim 1 , wherein the method does not use any carbon dioxide recovery solvents.

6. The method of claim 1 , further comprising removing, by a dehydrator, water from the carbon dioxide recycle stream.

7. The method of claim 1 , further comprising receiving, by a second heat exchanger, the first bottom effluent stream, processing the first bottom effluent stream, and passing the first bottom effluent stream to the second distillation column.

8. The method of claim 1 , wherein the carbon dioxide recycle stream comprises hydrogen sulfide (H 2 S), and wherein the H 2 S is removed from the second bottom effluent stream.

9. The method of claim 1 , further comprising injecting, by a compressor, the first top effluent stream into a well of the EOR process.

10. The method of claim 1 , further comprising, separating C 9+ hydrocarbons from the carbon dioxide recycle stream.

11. A set of equipment for use in an enhanced oil recovery (EOR) process, the set of equipment comprising:

a first heat exchanger configured to receive a carbon dioxide recycle stream from the EOR process and produce a cooled carbon dioxide recycle stream, wherein the carbon dioxide recycle stream comprises carbon dioxide and C 1 -C 8 hydrocarbons;

a first distillation column configured to receive the cooled carbon dioxide recycle stream from the first heat exchanger and separate the cooled carbon dioxide recycle stream to produce a first top effluent stream and a first bottom effluent stream, wherein the first top effluent stream comprises carbon dioxide, C 1 -C 4 hydrocarbons, and trace amounts of C 5 -C 8 hydrocarbons, and wherein the first bottom effluent stream comprises carbon dioxide, C 3 -C 8 hydrocarbons, and trace amounts of C 1 -C 2 hydrocarbons;

a second distillation column configured to receive the first bottom effluent stream from the first distillation column and produce a second top effluent stream and a second bottom effluent stream, wherein the second top effluent stream comprises carbon dioxide, C 2 -C 4 hydrocarbons, and is substantially free of C 5 -C 8 hydrocarbons, wherein the second bottom effluent stream comprises C 3 -C 8 hydrocarbons and is substantially free of carbon dioxide and C 1 -C 2 hydrocarbons, and wherein the first distillation column and the second distillation column are the only two distillation columns in the set of equipment; and

an expansion valve configured to receive the second top effluent stream from the second distillation column and produce an expanded second top effluent stream.

12. The set of equipment of claim 11 , wherein the carbon dioxide recycle stream comprises nitrogen, wherein the first top effluent stream comprises nitrogen, wherein the first bottom effluent stream is substantially free of nitrogen, wherein the second top effluent stream is substantially free of nitrogen, and wherein the second bottom effluent stream is substantially free of nitrogen.

13. The set of equipment of claim 11 , wherein the second distillation column comprises a reboiler configured to reboil a portion of the second bottom effluent stream.

14. The set of equipment of claim 11 , wherein no cryogenic conditions are used in the set of equipment.

15. The set of equipment of claim 11 , wherein the set of equipment does not use any carbon dioxide recovery solvents.

16. The set of equipment of claim 11 , further comprising a dehydrator configured to remove water from the carbon dioxide recycle stream.

17. The set of equipment of claim 11 , further comprising a second heat exchanger configured to receive the first bottom effluent stream, process the first bottom effluent stream, and pass the first bottom effluent stream to the second distillation column.

18. The set of equipment of claim 11 , wherein the carbon dioxide recycle stream comprises hydrogen sulfide (H 2 S), and wherein the H 2 S is removed from the second bottom effluent stream.

19. The set of equipment of claim 11 , further comprising a compressor configured to inject the first top effluent stream into a well of the EOR process.

20. The set of equipment of claim 11 , further comprising an additional separator configured to separate C 9+ hydrocarbons from the carbon dioxide recycle stream.