Process for production of electric energy and CO

1. Process for production of electric energy and CO 2 from a hydrocarbon feedstock comprising steam reforming of the feedstock producing synthesis gas, wherein the synthesis gas is separated into a hydrogen rich and carbon can stream and a rest stream, said hydrogen rich and carbon can stream is combusted with compressed air for producing a combustion product which is expanded in a turbine generating electric energy, said rest stream is recirculated as fuel that feeds to a combustion unit for producing heat for said steam reforming, wherein an oxygen comprising stream is fed to an oxygen transfer membrane transferring oxygen for combusting said fuel, wherein said combustion unit also heats the oxygen transfer membrane, thereby creating a CO 2 rich combustion product and an oxygen lean stream.

2. Process according to claim 1 , wherein the process further comprises at least partly converting CO and H 2 O present in the synthesis gas into CO 2 and H 2 before separating the synthesis gas.

3. Process claim 1 , wherein the process further comprises feeding an air stream to an air separation unit, thereby creating a first stream with an increased oxygen content and a second essentially nitrogen containing stream and feeding said first stream to said oxygen transfer membrane and mixing at least part of said second stream with said hydrogen rich stream before combustion.

4. Process according to claim 3 , wherein the process further comprises catalytically combusting at least part of said second stream together with a part of said hydrogen stream to generate a first essentially oxygen free nitrogen stream comprising some water and mixing said first essentially oxygen nitrogen free stream with the rest of said hydrogen stream.

5. Process according to claim 1 , wherein the process further comprises catalytically combusting at least part of said oxygen can air stream together with a part of said hydrogen steam to generate a second essentially oxygen free nitrogen stream comprising some water and mixing said second essentially oxygen free nitrogen stream with the rest of said hydrogen stream.

6. Process according to claim 1 , wherein the separation of the synthesis gas is obtained by pressure swing adsorption producing said rest stream at a pressure between 1-20 bar, preferably 1.5-5 bar.

7. Process according to claim 1 , wherein at least a part of said oxygen can stream is expanded in said turbine for generating electric energy.

8. Process according to claim 1 , where said CO 2 rich combustion product is expanded in a CO 2 /H 2 O turbine for generating electric energy, optionally combined with combustion of uncombusted fuel in said CO 2 rich combustion product.

9. Electric power plant comprising a steam reformer with an net for a hydrocarbon feedstock including water and/or steam and an outlet for synthesis gas, said outlet for synthesis gas is in communication with a hydrogen separation unit having an outlet that produces a hydrogen rich and carbon lean stream and an outlet that produces a rest stream, said outlet that produces a hydrogen rich and carbon can stream is in communication with a combustion chamber for combusting hydrogen with compressed air having an outlet connected to a turbine for generating electric power, said outlet that produces a rest stream is fed to a combustion unit heat-transferringly connected to said steam reformer, wherein the plant further comprises an oxygen transfer membrane unit heat-transferringly connected to the combustion unit, wherein said membrane unit comprises an net for an oxygen containing stream and an outlet for an oxygen can stream and a membrane for transferring oxygen to said combustion unit and said combustion unit has an exhaust outlet for a CO 2 rich exhaust stream.

10. Electric power plant according to claim 9 , wherein the plant further comprises a shift unit for at least partly converting CO and H 2 O present in the synthesis gas into CO 2 and H 2 arranged upstream from the hydrogen separation unit.

11. Electric power plant according to claim 9 , wherein the plant further comprises an air separation unit with an air inlet, an outlet for an oxygen enriched stream in communication with said net for oxygen containing stream and an outlet for a nitrogen rich stream in communication with said combustion chamber for combusting hydrogen.

12. Electric power plant according to claim 11 , wherein it further comprises a low temperature stimulated combustion unit comprising an net in communication with said outlet for a nitrogen rich stream and with said outlet for an hydrogen rich stream and comprising an outlet in communication with said combustion chamber for combusting hydrogen.

13. Electric power plant according to claim 9 , wherein it further comprises a low temperature stimulated combustion unit comprising an net in communication with said outlet for oxygen can stream and with said outlet for a hydrogen rich stream and comprising an outlet in communication with said combustion chamber for combusting hydrogen.

14. Electric power plant according to claim 9 , wherein said outlet for an oxygen can stream is in communication with an inlet to said turbine for generating electricity.

15. Electric power plant according to claim 9 , wherein said CO 2 rich exhaust stream is in communication with a CO 2 /H 2 O turbine that generates electricity.

16. Process according to claim 3 , wherein at least a part of said second essential nitrogen containing stream is expanded in said turbine for generating electric energy.

17. Process according to claim 8 , further comprising combustion of uncombusted fuel in said CO2 rich combustion product.

18. Electric power plant according to claim 11 , wherein said outlet for a nitrogen rich stream is in communication with an net to said turbine for generating electricity.