Process for removing polyunsaturated hydrocarbons from C4 hydrocarbon streams in the presence of mercaptans, disulfides and C5 hydrocarbons

1. A process for removing polyunsaturated hydrocarbons from an olefin-containing C4 hydrocarbon stream that, in addition to C4 hydrocarbons, also contains C5 hydrocarbons in a range between 0.01 and 5% by weight and mercaptans and/or disulfides in a range between 0.01 and 200 ppm by weight,

wherein the process comprises a first step and a second step as follows:

in the first step, at least some of the polyunsaturated hydrocarbons from the olefin-containing C4 hydrocarbon stream are hydrogenated and reacted with the mercaptans and/or disulfides from the olefin-containing C4 hydrocarbon stream in a first reaction zone in a presence of a molar ratio of hydrogen to polyunsaturated hydrocarbons between 0.01 and 0.8,

wherein the first reaction zone comprises one or more reactors connected in parallel and/or in series,

wherein the first step is carried out using a first catalyst comprising an alumina support material and a metal, where the metal comprises a combination of palladium and platinum having a palladium concentration of up to 2.0% by weight and a platinum concentration of up to 1.0% by weight,

wherein the concentration of the palladium is at least a factor of 2 higher than that of platinum,

wherein no carbon monoxide is added to the C4 hydrocarbon stream in the first step, and

wherein not more than 80 mol % of the available polyunsaturated hydrocarbons from the C4 hydrocarbon stream are hydrogenated and reacted in the first step; and

in the second step, remaining polyunsaturated hydrocarbons in the olefin-containing C4 hydrocarbon stream are selectively hydrogenated using a second catalyst in the presence of hydrogen and carbon monoxide in a second reaction zone, which comprises one or more reactors connected in parallel and/or in series;

wherein the second catalyst contains only a single metal of the 10th group of the periodic table, wherein the single metal is palladium; and

wherein at least one removal of high boilers takes place between the first step and the second step.

2. The process according to claim 1 , wherein the molar ratio of hydrogen to polyunsaturated hydrocarbons in the first step is between 0.1 and 0.5.

3. The process according to claim 1 , wherein an inlet temperature of the C4 hydrocarbon stream in an inflow of the first reaction zone, is between 0° C. and 180° C.

4. The process according to claim 1 , wherein the first step is carried out in a liquid phase and the hydrogen present has been dissolved in the liquid phase.

5. The process according to claim 1 , wherein, in the second step, the content of carbon monoxide in the C4 hydrocarbon stream in the inflow of the second reaction zone, is 0.05 to 20 ppm based on a total amount of the hydrocarbon stream.

6. The process according to claim 1 , wherein an inlet temperature of the C4 hydrocarbon stream in an inflow of the second reaction zone, is between 0° C. and 100° C.

7. The process according to claim 1 , wherein a pressure in the second reaction zone, is in the range from 2 to 50 bar.

8. The process according to claim 1 , wherein the second step is carried out exclusively in a liquid phase.

9. The process according to claim 1 , wherein the first reaction zone comprises a single reactor.

10. The process according to claim 1 , wherein the second reaction zone comprises at least two reactors connected in parallel or in series.

11. The process according to claim 1 , wherein the at least one removal of high boilers is done with a distillation column having 40 to 100 theoretical plates and the distillation column has a reflux ratio of between 1 and 2.5.

12. The process according to claim 1 , wherein an inlet temperature of the C4 hydrocarbon stream in an inflow of the first reaction zone, is between 60° C. and 150° C.

13. The process according to claim 1 , wherein an inlet temperature of the C4 hydrocarbon stream in an inflow of the first reaction zone, is between 80° C. and 130° C.

14. The process according to claim 1 , wherein an inlet temperature of the C4 hydrocarbon stream in an inflow of the second reaction zone, is between 20° C. and 80° C.

15. The process according to claim 1 , wherein an inlet temperature of the C4 hydrocarbon stream in an inflow of the second reaction zone, is between 30° C. and 60° C.

16. The process according to claim 1 , wherein a pressure in the second reaction zone, is in the range from 6 to 30 bar.

17. The process according to claim 1 , wherein a pressure in the second reaction zone, is in the range from 10 to 25 bar.

18. The process according to claim 1 , wherein the first catalyst comprises a palladium concentration of up to 1.0% by weight and a platinum concentration of up to 0.5% by weight.

19. The process according to claim 1 , wherein the first catalyst comprises a palladium concentration of up to 0.5% by weight and a platinum concentration of up to 0.2% by weight.

20. The process according to claim 1 , wherein the first catalyst comprises a palladium concentration of about 0.5% by weight and a platinum concentration of about 0.2% by weight.

21. The process according to claim 1 , wherein the C4 hydrocarbon stream contains mercaptans.

22. The process according to claim 1 , wherein the C4 hydrocarbon stream contains disulfides.

23. The process according to claim 1 , wherein the C4 hydrocarbon stream contains mercaptans and disulfides and the C4 hydrocarbon stream reacts with the mercaptans and the disulfides.

24. The process according to claim 1 , wherein the metal consists of the combination of palladium and platinum.

25. The process according to claim 1 , wherein between the first and second step, at least some of the C5 hydrocarbons are removed from the C4 hydrocarbon stream.