Process and plant for producing hydrocarbons with reduced CO

1. A process for producing a hydrocarbon product, said process comprising the steps of:

i) passing a feedstock originating from a fossil fuel source through a hydroprocessing stage for producing a main hydrotrotreated stream;

ii) passing the main hydrotreated stream to a separation stage for producing:

an aqueous stream;

a hydrogen-rich stream, at least a portion of the hydrogen-rich stream being a first recycle gas stream;

an off-gas stream comprising hydrocarbons;

and said hydrocarbon product, boiling at above 50° C.;

iii) passing the first recycle gas stream untreated from the separation stage to the hydroprocessing stage;

iv) passing the off-gas stream as a second recycle gas stream to a hydrogen producing unit for producing a hydrogen stream as a make-up hydrogen stream; and

v) passing the make-up hydrogen stream to the hydroprocessing stage;

wherein prior to conducting step iv), said off-gas stream passes to a separation stage for removing H 2 S and thereby producing said second recycle gas stream.

2. The process according to claim 1 , wherein the separation stage is at least one of an amine absorption stage, a caustic scrubber, and a sulfur absorbent.

3. The process according to claim 1 , wherein the feedstock originating from the fossil fuel source is one or more of diesel, kerosene, naphtha, and vacuum gas oil (VGO).

4. The process according to claim 1 , wherein step i) also comprises adding a feedstock originating from a renewable source and/or recycling a hydrocarbon product.

5. The process according to claim 4 , wherein the feedstock originating from the renewable source and/or recycling the hydrocarbon product is obtained from a raw material of renewable origin originating from plants, algae, animals, fish, vegetable oil refining, domestic waste, waste rich in plastic, industrial organic waste, or a feedstock derived from one or more oxygenates taken from the group consisting of triglycerides, fatty acids, resin acids, ketones, aldehydes or alcohols where said oxygenates originate from one or more of a biological source, a gasification process, a pyrolysis process, Fischer-Tropsch synthesis, or methanol based synthesis.

6. The process of claim 1 , wherein in step i) the hydroprocessing stage comprises:

i-1) passing the feedstock through a first catalytic hydrotreating unit under the addition of hydrogen for producing a first hydrotreated stream; and

i-2) passing the first hydrotreated stream to a dewaxing section comprising a second catalytic hydrotreating unit under the addition of hydrogen for producing said main hydrotreated stream.

7. The process according to claim 6 , wherein between step i-1) and i-2) the process further comprises passing the first hydrotreated stream to a separator for removing H 2 S, NH 3 , and H 2 O, thereby producing said first hydrotreated stream.

8. The process according to claim 6 , wherein in step v) the make-up hydrogen stream passes to at least one of:

said first catalytic hydrotreating unit;

a separator between step i-1) and i-2);

second catalytic hydrotreating unit;

and an additional catalytic hydrotreating unit.

9. The process according to claim 1 , wherein the hydrogen producing unit comprises feeding: said second recycle gas stream, and a hydrocarbon feedstock with at least a part of said hydrocarbon product.

10. The process according to claim 1 , wherein the hydrogen producing unit comprises subjecting the hydrocarbon feedstock to: cleaning in a cleaning unit; catalytic steam methane reforming in a steam reforming unit; water gas shift conversion in a water gas shift unit and hydrogen purification in a hydrogen purification unit.

11. The process according to claim 10 , wherein said second recycle gas stream is fed to the cleaning unit.

12. The process according to claim 10 , wherein the steam reforming unit is: a convection reformer, a tubular reformer, autothermal reformer (ATR), electrically heated steam methane reformer (e-SMR), or any combinations thereof.

13. The process according to claim 1 , wherein the hydrogen-rich stream comprises hydrogen in a concentration of 50 vol % or higher, the process comprising:

splitting said hydrogen-rich stream into the first recycle stream and a third recycle stream.

14. The process according to claim 13 , wherein said third recycle gas stream is passed through a hydrogen purification unit prior to being passed to the hydroprocessing stage.

15. The process according to claim 14 , wherein the hydrogen purification unit is a Pressure Swing Adsorption unit (PSA unit), said PSA unit producing an off-gas stream which is used as fuel in a stream reforming unit of the hydrogen producing unit, and/or in fired heaters in any of the catalytic hydrotreating units of the hydroprocessing stage, separation units of the separation stage, and/or for steam production.

16. The process according to claim 1 , wherein prior to passing the make-up hydrogen stream to the hydroprocessing stage, the make-up hydrogen stream passes through a compressor section comprising a make-up compressor, the make-up compressor also producing a hydrogen recycle stream which is added to the hydrogen producing unit.

17. The process of claim 1 further comprising:

vi) splitting said hydrogen-rich stream into said first recycle gas stream and a third recycle gas stream, and passing said third recycle gas stream to said hydrogen producing unit.

18. The process of claim 1 , wherein the first recycle gas stream is not subjected to a separation stage for removing H 2 S and/or CO 2 , prior to being passed to the hydroprocessing stage.

19. The process of claim 18 , wherein the first recycle gas stream is not subjected to a separation stage for removing NH 3 and/or CO, prior to being passed to the hydroprocessing stage.

20. The process according to claim 18 , wherein in step ii) the separation stage comprises:

ii-1) passing the main hydrotreated stream to a cold separator, for producing said aqueous stream, said hydrogen-rich stream, and a heavy hydrocarbon stream; and

ii-2) passing the heavy hydrocarbon stream to a fractionation section for producing said off-gas stream, and said hydrocarbon product.

21. A plant for producing a hydrocarbon product, comprising:

a hydroprocessing section arranged to receive a feedstock originating from a fossil fuel source and a compressed hydrogen-rich feed stream for producing a main hydrotreated stream;

a separation section arranged to receive said main hydrotreated stream for producing an aqueous stream, a hydrogen-rich stream as a first recycle gas stream, an off-gas stream comprising hydrocarbons as a second recycle stream, and said hydrocarbon product, boiling at above 50° C.;

a separation section for removing H 2 S and thereby producing said second recycle gas stream;

a hydrogen producing unit (HPU) arranged to receive said second recycle gas stream and a hydrocarbon feedstock for producing a make-up hydrogen stream;

a compressor section arranged to receive said first recycle gas stream and at least a portion of the make-up hydrogen stream produced in said HPU, for generating said compressed hydrogen-rich feed stream and a make-up hydrogen recycle stream;

a conduit for passing said first recycle gas stream to said compressor section; and

a conduit for passing said make-up hydrogen stream from the HPU to said compressor section.