Process for producing hydrocarbons

1. A process for producing hydrocarbons, wherein starting material comprising tall oil material and polar co-feed, which polar co-feed comprises at least 75 wt. % of C12-C22 fatty acids, is diluted with a non-polar diluent to obtain feedstock, the feedstock is hydroprocessed by a catalyst system comprising a combination of a HDO catalyst and HDW catalyst, at a temperature of 270-450° C. and under the pressure of 10-250 bar to obtain a hydroprocessing product, at least one hydrocarbon fraction boiling in the liquid fuel range is separated from the hydroprocessing product, and the non-polar diluent comprises the hydroprocessing product or hydrocarbon fraction or a hydrocarbon blend or a combination thereof.

2. The process according to claim 1 , wherein the tall oil material is crude tall oil or purified tall oil.

3. The process according to claim 1 , wherein the polar co-feed comprises at least 75 wt. % of C14-C20 fatty acids.

4. The process according to claim 1 , wherein the polar co-feed comprises at least 75 wt. % of free fatty acids.

5. The process according to claim 1 , wherein the polar co-feed has acid value of 150-220.

6. The process according to claim 1 , wherein the polar co-feed is selected from the group consisting of palm oil fatty acid distillate, soy acid oil, tall oil fatty acid, crude tall oil fatty acid, fatty acid containing residues obtained from degumming of plant oils, residues obtained from refining of plant oils, used cooking oils, animal fat residues and distillers corn oil, and combinations thereof.

7. The process according to claim 1 , wherein the starting material comprises 45-95 wt. % of the tall oil material, and 5-55 wt. % of the polar co-feed.

8. The process according to claim 1 , wherein the starting material is diluted with the non-polar diluent in the ratio from 1:1 to 1:10 of starting material to diluent.

9. The process according to claim 1 , wherein the feedstock has sodium content of not more than 170 ppm.

10. The process according to claim 1 , wherein the feedstock has phosphorus content of not more than 80 ppm.

11. The process according to claim 1 , wherein the feedstock has silicon content of not more than 50 ppm.

12. The process according to claim 1 , wherein the non-polar diluent comprises hydroprocessing product boiling in the range of 30-450° C. or hydrocarbon fraction boiling in the range of 150-450° C., or a combination thereof, or the non-polar diluent comprises a hydrocarbon fraction separated from gaseous recycle streams, or a hydrocarbon fraction separated from another process, or a combination thereof.

13. The process according to claim 1 , wherein the ratio of the starting material to non-polar diluent is from 2:1 to 1:10.

14. The process according to claim 1 , wherein the tall oil material is crude tall oil and it is purified by evaporation comprising one, two or three evaporation steps.

15. The process according to claim 1 , wherein the HDO catalyst is a catalyst comprising a metal selected from the group consisting of Ni, Co and Mo and combinations thereof.

16. The process according to claim 1 , wherein the HDW catalyst a catalyst comprising NiW, or zeolite with medium or large pore sizes, or a combination thereof.

17. The process according to claim 1 , wherein the tall oil material is purified tall oil.

18. The process according to claim 1 , wherein the polar co-feed comprises at least 75 wt. % of C14-C18 fatty acids.

19. The process according to claim 1 , wherein the polar co-feed comprises 75-100 wt. % of free fatty acids.

20. The process according to claim 1 , wherein the starting material comprises 50-90 wt. % of the tall oil material, and 10-50 wt. % of the polar co-feed.

21. The process according to claim 1 , wherein the feedstock has sodium content of not more than 160 ppm.

22. The process according to claim 1 , wherein the feedstock has phosphorus content of not more than 70 ppm.

23. The process according to claim 1 , wherein the feedstock has silicon content of not more than 40 ppm.