초록 ▼

A process is provided for producing low sulfur diesel by hydrotreatment of suitable feed in the presence of a bulk metal catalyst. The feed is exposed under effective hydrotreating conditions to a catalyst including at least one Group VI metal, at least one Group VIII metal, and Niobium. Treatment o

A process is provided for producing low sulfur diesel by hydrotreatment of suitable feed in the presence of a bulk metal catalyst. The feed is exposed under effective hydrotreating conditions to a catalyst including at least one Group VI metal, at least one Group VIII metal, and Niobium. Treatment of the feed results in production of a liquid diesel product, which is separated from a gas phase product that is also produced during the hydrotreatment.

대표청구항 ▼

The invention claimed is: 1. A process for producing low sulfur diesel products from a diesel boiling range feedstream comprising: a) contacting a diesel boiling range feedstream containing aromatics, nitrogen and organically bound sulfur contaminants in a reaction stage with a bulk metal hydrotrea

The invention claimed is: 1. A process for producing low sulfur diesel products from a diesel boiling range feedstream comprising: a) contacting a diesel boiling range feedstream containing aromatics, nitrogen and organically bound sulfur contaminants in a reaction stage with a bulk metal hydrotreating catalyst having metals consisting of Nb, Mo, and at least one metal selected from Group VIII metals in the presence of hydrogen-containing treat gas thereby producing a reaction product comprising at least a vapor product and a liquid diesel boiling range product, wherein said diesel boiling range feedstream is contacted with said catalyst under effective hydrotreating conditions, wherein said bulk metal hydrotreating catalyst comprises about 15 to about 20 wt. % Nb, about 15 to about 30 wt. % Mo, and about 30 to about 40 wt. % of said at least one Group VIII metal selected from Co, Ni, Rh, Pt, Pd, Ir, and mixtures thereof. 2. The process according to claim 1 wherein said reaction stage comprises one or more reactors or reaction zones each of which can comprise one or more catalyst beds selected from the group consisting of fluidized beds, ebullating beds, slurry beds, fixed beds, and moving beds wherein each of said one or more catalyst beds contains a catalyst suitable for the reaction zone in which the catalyst bed is located. 3. The process according to claim 2 wherein said reaction stage comprises one or more fixed catalyst beds. 4. The process according to claim 2 wherein said process further comprises cooling between catalyst beds, reactors, or reaction zones in said reaction stage. 5. The process according to claim 1 wherein said diesel boiling range feedstream boils in the range of about 300° F. to about 775° F. 6. The process according to claim 5 wherein said diesel boiling range feedstream is selected from (i) diesel boiling range feedstreams that are not hydrotreated; (ii) are a blend of non-hydrotreated diesel boiling range feedstreams; (iii) are previously hydrotreated diesel boiling range feedstreams; (iv) are blends of hydrotreated diesel boiling range feedstreams; and (v) are blends of non-hydrotreated and hydrotreated diesel boiling range feedstreams. 7. The process according to claim 1 wherein said at least one Group VIII metal is selected from Co, Ni, and mixtures thereof. 8. The process according to claim 1 wherein said bulk metal hydrotreating catalyst is selected from CoMoNb and CoNiMoNb catalysts. 9. The process according to claim 1 wherein said process further comprises: b) separating said vapor product from said liquid diesel boiling range product; and c) recovering said liquid diesel boiling range product. 10. The process according to claim 1 wherein said effective hydrotreating conditions are selected in such a manner that at least a portion of said nitrogen and organically bound sulfur contaminants are removed from said diesel boiling range feedstream and at least a portion of said aromatics are hydrogenated. 11. The process according to claim 10 wherein said liquid diesel boiling range product has a sulfur, nitrogen, and aromatics concentration lower than said diesel boiling range feedstream. 12. The process according to claim 10 wherein said effective hydrotreating conditions comprise temperatures ranging from about 150° C. to about 425° C., weight hourly space velocities range from about 0.1 to about 20 hr−1, and pressures ranging from about 4 to about 70 atmospheres. 13. The process according to claim 1 wherein the nitrogen content of diesel boiling range feedstream is about 50 to about 1000 wppm nitrogen, the sulfur content of the diesel boiling range feedstream ranges from about 50 wppm to about 7000 wppm, and the aromatics content ranges from about 0.05 wt. % to about 2.5 wt. %, all based on the diesel boiling range feedstream. 14. The process according to claim 1 wherein the at least one Group VIII metal and Mo comprise from about 50 wt. % to about 100 wt. %, calculated as oxides, of the total weight of the bulk metal hydrotreating catalyst. 15. A process for producing low sulfur diesel products from a diesel boiling range feedstream comprising: a) contacting a diesel boiling range feedstream in the range of about 300° F. to about 775° F. and containing aromatics, nitrogen and organically bound sulfur contaminants in a reaction stage with a bulk metal hydrotreating catalyst having metals consisting of Nb, Mo and at least one Group VIII metal selected from Co, Ni, Rh, Pt, Pd, Ir, and mixtures thereof in the presence of hydrogen-containing treat gas thereby producing a reaction product comprising at least a vapor product and a liquid diesel boiling range product, wherein said diesel boiling range feedstream is contacted with said catalyst under hydrotreating conditions effective at removing at least a portion of said nitrogen and organically bound sulfur contaminants and hydrogenating at least a portion of said aromatics, wherein said bulk metal hydrotreating catalyst comprises about 10 to about 35 wt. % Nb, about 20 to about 40 wt. % Mo, and about 20 to about 40 wt. % of said at least one Group VIII metal selected from Co, Ni, Rh, Pt, Pd, Ir, and mixtures thereof. 16. The process according to claim 15 wherein the nitrogen content of diesel boiling range feedstream is about 50 to about 1000 wppm nitrogen, the sulfur content of the diesel boiling range feedstream ranges from about 50 wppm to about 7000 wppm, and the aromatics content ranges from about 0.05 wt. % to about 2.5 wt. %, all based on the diesel boiling range feedstream. 17. The process according to claim 16 wherein said reaction stage comprises one or more reactors or reaction zones each of which can comprise one or more catalyst beds selected from the group consisting of fluidized beds, ebullating beds, slurry beds, fixed beds, and moving beds wherein each of said one or more catalyst beds contains a catalyst suitable for the reaction zone in which the catalyst bed is located. 18. The process according to claim 17 wherein said reaction stage comprises one or more fixed catalyst beds. 19. The process according to claim 17 wherein said process further comprises cooling between catalyst beds, reactors, or reaction zones in said reaction stage. 20. The process according to claim 15 wherein said diesel boiling range feedstream boils in the range of about 400° F. to about 700° F. 21. The process according to claim 20 wherein said diesel boiling range feedstream is selected from (i) diesel boiling range feedstreams that are not hydrotreated; (ii) are a blend of non-hydrotreated diesel boiling range feedstreams; (iii) are previously hydrotreated diesel boiling range feedstreams; (iv) are blends of hydrotreated diesel boiling range feedstreams; and (v) are blends of non-hydrotreated and hydrotreated diesel boiling range feedstreams. 22. The process according to claim 15 wherein said at least one Group VIII metal is selected from Co, Ni, and mixtures thereof. 23. The process according to claim 15 wherein said bulk metal hydrotreating catalyst is selected from CoMoNb and CoNiMoNb catalysts. 24. The process according to claim 15 wherein said process further comprises: b) separating said vapor product from said liquid diesel boiling range product; and c) recovering said liquid diesel boiling range product. 25. The process according to claim 15 wherein said liquid diesel boiling range product has a sulfur, nitrogen, and aromatics concentration lower than said diesel boiling range feedstream. 26. The process according to claim 15 wherein said effective hydrotreating conditions comprise temperatures ranging from about 150° C. to about 425° C., weight hourly space velocities range from about 0.1 to about 20 hr−1, and pressures ranging from about 4 to about 70 atmospheres. 27. The process according to claim 15 wherein the at least one Group VIII metal and Mo comprise from about 50 wt. % to about 100 wt. %, calculated as oxides, of the total weight of the bulk metal hydrotreating catalyst.