System and process for synthesis gas production

1. A hydrogen production system comprising:

optionally, one or more gas conditioning stages chosen between the following stages: a hydrogenation stage, a desulfurization stage and a prereforming stage, where the most upstream stage of the one or more gas conditioning stages is arranged to receive a hydrogen enriched hydrocarbon stream and to process said hydrocarbon feed stream into a conditioned hydrocarbon stream,

a steam reformer unit downstream the one or more optional gas conditioning units,

a steam addition line arranged to add steam upstream the steam reformer unit, and

said steam reformer unit being arranged to process the hydrogen enriched hydrocarbon stream or the conditioned hydrocarbon stream together with added steam into a reformed stream,

a hydrogen membrane unit downstream said steam reformer unit, said hydrogen membrane unit comprising a hydrogen permeable membrane and being arranged to allow at least a part of the reformed stream to pass on a first side of said hydrogen permeable membrane and a hydrocarbon feed stream to pass on a second side of said hydrogen permeable membrane, so that during operation of the system hydrogen passes from the reformed stream on the first side into the hydrocarbon feed stream on the second side, thereby forming said hydrogen enriched hydrocarbon stream, and

a separation unit downstream the first side of said hydrogen membrane unit, said separation unit being arranged for separating the reformed stream exiting the first side of the hydrogen membrane unit into a hydrogen product gas and an off-gas.

2. The hydrogen production system according to claim 1 , wherein said separation unit is a pressure swing adsorption unit, a temperature swing adsorption unit, or a combination of a carbon dioxide separation unit and a cold box.

3. The hydrogen production system according to claim 1 , wherein the hydrogen membrane unit comprises a polymeric membrane or a ceramic membrane.

4. The hydrogen production system according to claim 1 , wherein the reformed stream and the hydrocarbon feed stream are arranged to pass in counter-current or co-currently in the hydrogen membrane unit.

5. The hydrogen production system according to claim 1 , wherein said membrane unit comprises an outer tube and a plurality of hollow hydrogen permeable membranes.

6. The hydrogen production system according to claim 1 , further comprising a water gas shift unit downstream said steam reformer unit and upstream said hydrogen membrane unit, said water gas shift unit being arranged to convert steam and carbon monoxide in the reformed stream to hydrogen and carbon dioxide.

7. A process for hydrogen gas production, said process comprising the steps of:

optionally, passing a hydrogen enriched hydrocarbon stream through one or more gas conditioning stages chosen between the following stages: a hydrogenation stage, a desulfurization stage and a prereforming stage, where the one or more gas conditioning stages is/are arranged to receive the hydrogen enriched hydrocarbon stream and to process said hydrocarbon feed stream into a conditioned hydrocarbon stream,

adding steam to the hydrogen enriched hydrocarbon stream or to the conditioned hydrocarbon stream,

reforming said hydrogen enriched hydrocarbon stream or the conditioned hydrocarbon stream together with the added steam in a steam reformer unit downstream the one or more gas conditioning units, to a reformed stream,

directing at least a part of said reformed stream into a hydrogen membrane unit downstream said steam reformer unit, said hydrogen membrane unit comprising a hydrogen permeable membrane and being arranged to allow at least a part of the reformed stream to pass on a first side of said hydrogen permeable membrane and a hydrocarbon feed stream to pass on a second side of said hydrogen permeable membrane, so that hydrogen passes from the reformed stream on the first side into the hydrocarbon feed stream on the second side, thereby forming said hydrogen enriched hydrocarbon stream; and

separating the reformed stream exiting the first side of the hydrogen membrane unit into a hydrogen product gas and an off-gas in a separation unit downstream the first side of said hydrogen membrane unit.

8. The process according to claim 7 , wherein said separation unit is a pressure swing adsorption unit, a temperature swing adsorption unit, or a combination of a carbon dioxide separation unit and a cold box.

9. The process according to claim 7 , wherein the partial pressure of hydrogen in the reformed stream is between 5 and 25 barg.

10. The process according to claim 7 , wherein the hydrogen membrane unit comprises a polymeric membrane, or a ceramic membrane.

11. The process according to claim 7 , wherein the reformed stream and the hydrocarbon feed stream pass in counter-current or co-currently in the hydrogen membrane unit.

12. The process according to claim 7 , further comprising the step of dividing off a first part of the reformed stream and passing only said first part on to said first side of said hydrogen membrane unit.

13. The process according to claim 7 , wherein said membrane unit comprises an outer tube and a plurality of hollow hydrogen permeable membranes.

14. The process according to claim 7 , further comprising the step of:

converting steam and carbon monoxide in the reformed stream to hydrogen and carbon dioxide in a water gas shift unit downstream said steam reformer unit and upstream said hydrogen membrane unit.

15. The process according to claim 7 , further separating off water from the stream exiting a retentate side of the hydrogen membrane unit.