초록 ▼

The present invention pertains to a method for hydroprocessing a heavy hydrocarbon oil, comprising bringing a heavy hydrocarbon oil into contact with hydroprocessing catalyst I in the presence of hydrogen in a first stage, after which the effluent of the first stage is contacted in whole or in part

The present invention pertains to a method for hydroprocessing a heavy hydrocarbon oil, comprising bringing a heavy hydrocarbon oil into contact with hydroprocessing catalyst I in the presence of hydrogen in a first stage, after which the effluent of the first stage is contacted in whole or in part with hydroprocessing catalyst II in the presence of hydrogen in a second stage. The method according to the invention combines efficient contaminant removal with high cracking rate and low sediment formation. The invention also pertains to the combination of catalysts.

대표청구항 ▼

The invention claimed is: 1. A method for hydroprocessing a heavy hydrocarbon oil, comprising bringing a heavy hydrocarbon oil having at least 70 wt % vacuum residue which boils above 538° C. into contact with hydroprocessing catalyst I in the presence of hydrogen in a first stage, after which the

The invention claimed is: 1. A method for hydroprocessing a heavy hydrocarbon oil, comprising bringing a heavy hydrocarbon oil having at least 70 wt % vacuum residue which boils above 538° C. into contact with hydroprocessing catalyst I in the presence of hydrogen in a first stage, after which the effluent of the first stage is contacted in whole or in part with hydroprocessing catalyst II in the presence of hydrogen in a second stage, wherein catalyst I comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of at least 100 m2/g, a total pore volume of at least 0.55 ml/g, and a pore size distribution for inhibiting sediment formation and promoting asphaltene removal, such that at least 50% of the total pore volume in pores with a diameter of at least 20 nm (200 Å), 10-30% of the total pore volume in pores with a diameter of at least 200 nm (2000 Å), less than 85% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), less than 0.2 ml/g of total pore volume in pores with a diameter of 50-150 nm (500-1500 Å), and less than 25% of the total pore volume in pores with a diameter of 10 nm (100 Å) or less, and catalyst II comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of at least 100 m2/g, a total pore volume of at least 0.55 ml/g, and a pore size distribution for providing catalytic activity and inhibiting sediment, such that at least 75% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å), and less than 25% of the total pore volume in pores with a diameter of 10 nm (100 Å) or less. 2. The method of claim 1 wherein catalyst II comprises a catalyst IIa, which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of 100-180 m2/g, a total pore volume of at least 0.55 ml/g, at least 85% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å). 3. The method of claim 2 wherein the carrier of catalyst IIa consists essentially of alumina. 4. The method of claim 1 wherein catalyst II comprises a catalyst IIb, which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier comprising at least 3.5 wt. % of silica, calculated on the weight of the final catalyst, said catalyst having a specific surface area of at least 150 m2/g, a total pore volume of at least 0.55 ml/g, at least 75% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å). 5. The method of claim 4 wherein catalyst IIb additionally comprises a Group IA metal component. 6. The method of claim 1 wherein at least one of the stages is carried out in an ebullating bed. 7. The method of claim 1 wherein catalyst II may comprise catalyst IIa and/or catalyst IIb, catalyst IIa, which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of 100-180 m2/g, a total pore volume of at least 0.55 ml/g, at least 85% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å), catalyst IIb, which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier comprising at least 3.5 Wt. % of silica, calculated on the weight of the final catalyst, said catalyst having a specific surface area of at least 150 m2/g, a total pore volume of at least 0.55 ml/g, at least 75% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å). 8. The method of claim 7 wherein Catalyst II comprises both catalyst IIa and catalyst IIb, catalyst IIb being present in an amount of at least 1 wt. % of the total catalyst mixture. 9. The method of claim 8 wherein catalyst ha has at least 50% of its pore volume in pores with a diameter above 200 Å, and catalyst IIb has at most 50% of its pore volume in pores with a diameter above 200 Å. 10. The method of claim 8 wherein catalyst IIb comprises a Group VA metal component, in particular phosphorus. 11. A combination of catalysts comprising a catalyst I which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of at least 100 m2/g, a total pore volume of at least 0.55 ml/g, and a pore size distribution for inhibiting sediment formation and promoting asphaltene removal, such that at least 50% of the total pore volume in pores with a diameter of at least 20 nm (200 Å), 10-30% of the total pore volume in pores with a diameter of at least 200 nm (2000 Å), less than 85% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), less than 0.2 ml/g of total pore volume in pores with a diameter of 50-150 nm (500-1500 Å), and less than 25% of the total pore volume in pores with a diameter of 10 nm (100 Å) or less, and a catalyst II which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of at least 100 m2/g, a total pore volume of at least 0.55 ml/g, and a pore size distribution for providing catalytic activity and inhibiting sediment, such that at least 75% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å), and less than 25% of the total pore volume in pores with a diameter of 10 nm (100 Å) or less. 12. The catalyst combination of claim 11 wherein catalyst II comprises a catalyst IIa, which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of 100-180 m2/g, a total pore volume of at least 0.55 ml/g, at least 85% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å). 13. The catalyst combination of claim 12 wherein the carrier of catalyst IIa consists essentially of alumina. 14. The catalyst combination of claim 11 wherein catalyst II comprises a catalyst IIb, which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier comprising at least 3.5 wt. % of silica, calculated on the weight of the final catalyst, said catalyst having a specific surface area of at least 150 m2/g, a total pore volume of at least 0.55 ml/g, at least 75% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å). 15. The catalyst combination of claim 11 wherein catalyst IIb additionally comprises a Group IA metal component. 16. The catalyst combination of claim 12 wherein catalyst II comprises catalyst IIa and/or catalyst IIb, wherein catalyst IIa comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of 100-180 m2/g, a total pore volume of at least 0.55 ml/g, at least 85% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å), and wherein catalyst IIb, which comprises 7 to 20 wt. % of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt. % of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier comprising at least 3.5 wt. % of silica, calculated on the weight of the final catalyst, said catalyst having a specific surface area of at least 150 m2/g, a total pore volume of at least 0.55 m2/g, at least 75% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å). 17. The catalyst combination of claim 16 wherein catalyst II comprises both catalyst ha and catalyst IIb, catalyst IIb being present in an amount of at least 1 wt. % of the total catalyst mixture. 18. The catalyst combination of claim 17 wherein catalyst IIa has at least 50% of its pore volume in pores with a diameter above 200 Å, and catalyst IIB has at most 50% of its pore volume in pores with a diameter above 200 Å. 19. The catalyst combination of claim 18 wherein catalyst IIb comprises a Group VA metal component, in particular phosphorus.