Hydrotreating catalyst sulphiding agent and its use for in situ and ex situ presulphidation
View Patent ↗The present invention relates to a sulphiding agent for a hydrotreating catalyst which makes possible faster sulphiding of the catalyst but which also makes possible to very significantly limit solid deposits, in particular of sulphur. The sulphiding agent according to the invention is essentially composed of diethyl disulphide (DEDS) or dipropyl disulphide(s) (DPDS) or dibutyl disulphide(s) (DBDS) and can be employed in “in situ” and “ex situ” presulphidation processes.
1. A method of hydrotreating a hydrocarbon material to reduce its sulphur content which comprises
contacting the hydrocarbon material with a hydrotreating catalyst comprising an active metal catalyst supported on a catalyst base of an oxide of a metal or semi-metal, said hydrotreating catalyst having been presulphided with a sulphiding agent consisting essentially of diethyl disulphide (DEDS) dissolved in a solvent composition consisting essentially of a solvent selected from the group consisting of light or heavy petrols, alkanes, aromatic hydrocarbons, and hydrocarbon or non-hydrocarbon fractions thereof, and optionally 0.1 to 1% by weight of at least one odour-masking agent,
wherein the hydrotreating catalyst achieves the same level of desulphurization at a lower temperature than the same catalyst presulphided with dimethyl disulphide (DMDS).
2. The method of claim 1 , wherein the hydrotreating catalyst was presulphided in situ.
3. The method of claim 2 , wherein the hydrotreating catalyst was presulphided by contacting the sulphiding agent with the hydrotreating catalyst under a hydrogen pressure at a temperature of up to 350° C.
4. The method of claim 2 , wherein the hydrotreating catalyst was presulphided in two stages comprising a primary sulphidation stage wherein the sulphiding agent is contacted with the hydrotreating catalyst at a temperature ranging from 150 to 250° C., followed by a secondary sulpidation stage wherein the sulphiding agent is contacted with the hydrotreating catalyst at a temperature ranging from 250 to 350° C.
5. The method of claim 4 , wherein the hydrotreating catalyst was presulphided under a pressure of 4.5 MPa, an hourly space velocity of 1 h −1 , and an H 2 /hydrocarbon ratio of 200 Sl/l.
6. The method of claim 1 , wherein the hydrotreating catalyst was presulphided ex situ.
7. The method of claim 6 , wherein the hydrotreating catalyst was presulphided by contacting the sulphiding agent with the hydrotreating catalyst in the absence of hydrogen at a temperature between 0 and 50° C.
8. A method of presulphiding a hydrotreating catalyst comprising an active metal catalyst supported on a catalyst base of an oxide of a metal or semi-metal, which comprises
contacting the hydrotreating catalyst with a sulphiding agent consisting essentially of diethyl disulphide (DEDS) dissolved in a solvent composition consisting essentially of a solvent selected from the group consisting of light or heavy petrols, alkanes, aromatic hydrocarbons, and hydrocarbon or non-hydrocarbon fractions thereof, and optionally 0.1 to 1% by weight of at least one odour-masking agent,
wherein, when used in a method of hydrotreating a hydrocarbon material to reduce its sulphur content, the hydrotreating catalyst is able to achieve the same level of desulphurization at a lower temperature than the same catalyst presulphided with dimethyl disulphide (DMDS).
9. The method of claim 8 , wherein the hydrotreating catalyst is presulphided in situ.
10. The method of claim 8 , wherein the hydrotreating catalyst is presulphided ex situ.
11. The method of claim 8 , which comprises contacting the hydrotreating catalyst with the sulphiding agent under a hydrogen pressure at a temperature of up to 350° C.
12. The method of claim 8 , which comprises contacting the hydrotreating catalyst with the sulphiding agent at a first temperature range of 150 to 250° C., and then at a second temperature range of 250 to 350° C.
13. The method of claim 12 , which comprises contacting the hydrotreating catalyst with the sulphiding agent under a pressure of 4.5 MPa, an hourly space velocity of 1 h −1 , and an H 2 /hydrocarbon ratio of 200 Sl/l.
14. The method of claim 8 , wherein the hydrotreating catalyst was presulphided by contacting the sulphiding agent with the hydrotreating catalyst in the absence of hydrogen at a temperature between 0 and 50° C.
15. A method of decreasing the desulphurization temperature required for hydrotreating a hydrocarbon material to reduce its sulphur content which comprises
contacting the hydrocarbon material with a hydrotreating catalyst comprising an active metal catalyst supported on a catalyst base of an oxide of a metal or semi-metal, said hydrotreating catalyst having been presulphided with diethyl disulphide (DEDS) instead of dimethyl disulphide (DMDS),
wherein the hydrotreating catalyst achieves the same level of desulphurization at a lower temperature than the same catalyst presulphided with DMDS.
16. A method of hydrotreating a hydrocarbon material to reduce its sulphur content which comprises
contacting the hydrocarbon material with a hydrotreating catalyst comprising an active metal catalyst supported on a catalyst base of an oxide of a metal or semi-metal, said hydrotreating catalyst having been presulphided with a sulphiding agent consisting essentially of diethyl disulphide (DEDS) dissolved in a solvent composition consisting essentially of a solvent selected from the group consisting of light or heavy petrols, alkanes, aromatic hydrocarbons, and hydrocarbon or non-hydrocarbon fractions thereof, and optionally 0.1 to 1% by weight of at least one odour-masking agent,
wherein the hydrotreating catalyst outperforms the same catalyst presulphided with DMDS, with respect to desulphurization, across a temperature range of 340° C. to 360° C.
17. The method of claim 16 , wherein the hydrotreating catalyst outperforms the same catalyst presulphided with DMDS, with respect to desulphurization, across the entire temperature range of 340° C. to 360° C.
18. The method of claim 16 , wherein the hydrotreating catalyst was presulphided by contacting the sulphiding agent with the hydrotreating catalyst under a hydrogen pressure at a temperature of up to 350° C.
19. The method of claim 16 , wherein the hydrotreating catalyst was presulphided in two stages comprising a primary sulphidation stage wherein the sulphiding agent is contacted with the hydrotreating catalyst at a temperature ranging from 150 to 250° C., followed by a secondary sulpidation stage wherein the sulphiding agent is contacted with the hydrotreating catalyst at a temperature ranging from 250 to 350° C.
20. The method of claim 18 , wherein the hydrotreating catalyst was presulphided under a pressure of 4.5 MPa, an hourly space velocity of 1 h −1 , and an H 2 /hydrocarbon ratio of 200 Sl/l.