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A process for the sulfiding of a hydrodesulfurization catalyst for example in a distillation column reactor. The catalyst in the distillation column reactor is first dried using nitrogen and the reactor is filled with a sulfiding solvent and circulation begun. The reactor is heated to a temperature

A process for the sulfiding of a hydrodesulfurization catalyst for example in a distillation column reactor. The catalyst in the distillation column reactor is first dried using nitrogen and the reactor is filled with a sulfiding solvent and circulation begun. The reactor is heated to a temperature above the decomposition temperature of the sulfiding agent to be used and the sulfiding agent charged to the reactor. When sulfiding agent breakthrough is noted in the overheads the temperature is raised and held until sulfiding is complete.

대표청구항 ▼

1. A process for the sulfiding of a hydrodesulfurization catalyst in a distillation column reactor comprising the steps of: (a) drying the catalyst with an inert gas; (b) filling the distillation column reactor with a sulfiding solvent containing sulfur; (c) establishing hydrocarbon feed and hy

1. A process for the sulfiding of a hydrodesulfurization catalyst in a distillation column reactor comprising the steps of: (a) drying the catalyst with an inert gas; (b) filling the distillation column reactor with a sulfiding solvent containing sulfur; (c) establishing hydrocarbon feed and hydrogen flow rates; (d) begin recycling of sulfiding solvent; (e) heating the distillation column reactor to a temperature above the decomposition temperature of the sulfiding agent; (f) introducing a sulfiding agent; (g) observing the water by-product azeotrope overhead and collecting the water; (h) observing said sulfiding agent breakthrough in the overhead; (i) increasing temperature to a second temperature; and (j) holding said second temperature for a period of time. 2. The process according to claim 1 wherein said sulfiding agent comprises tertiary nonyl poly sulfide. 3. The process according to claim 1 wherein said sulfiding agent comprises dimethyl disulfide. 4. The process according to claim 1 wherein the solvent is moving upflow through said catalyst. 5. The process according to claim 1 wherein the solvent is moving downflow through said catalyst. 6. The process according to claim 1 wherein the sulfiding agent and solvent are co-currently fed. 7. The process according to claim 1 wherein the sulfiding is carried out at a pressure that it is above the vapor pressure of the solvent at the first temperature. 8. The process according to claim 1 wherein the first temperature is in the range between 300 and 500° F. 9. The process according to claim 1 wherein the second temperature is in the range between 500-700° F. 10. The process according to claim 1 wherein said sulfiding agent comprises H2S. 11. The process according to claim 10 wherein said catalyst comprises components selected from the group consisting of Group V, VIB and VIII metals of the Periodic Table. 12. The process according to claim 11 wherein said catalyst comprises an oxide of said components selected from the group consisting of Group V, VIB and VIII metals of the Periodic Table. 13. The process according to claim 1 wherein said solvent comprises a sulfur containing naphtha stream. 14. The process according to claim 13 wherein the sulfiding solvent and sulfiding agent are fed downflow. 15. The process according to claim 11 wherein the sulfiding solvent and sulfiding agent are fed downflow. 16. The process according to claim 1 wherein heating of step (e) is obtained by heating a bottom portion in the column. 17. The process according to claim 16 wherein the reboiler is operated at a temperature sufficient to dissociate the sulfiding agent into its constituent elements.