Hydroprocessing catalyst for the reduction of metals and sulfur in heavy feeds
A catalyst comprising a carrier and a metals component impregnated in the carrier, the carrier comprising alumina; and the metals component comprising a first metals fraction and a second metals fraction, the first metals fraction comprising at least one metal selected from chromium, molybdenum, or tungsten, and the second metals fraction comprising at least two metals selected from cobalt, rhodium, iridium, nickel, palladium, or platinum, wherein the catalyst has a first pore volume of 0.28 to 0.45 mL/g for pores having a pore diameter of 12 nm to less than 16 nm, and a second pore volume of 0.15 to 0.28 mL/g for pores of 2.0 nm to less than 12.0 nm.
1. A catalyst comprising a carrier and a metals component impregnated in the carrier,
the carrier comprising alumina; and
the metals component comprising a first metals fraction and a second metals fraction, the first metals fraction comprising at least one metal selected from chromium, molybdenum, or tungsten, and the second metals fraction comprising at least two metals selected from cobalt, rhodium, iridium, nickel, palladium, or platinum,
wherein the catalyst has a first pore volume of 0.28 to 0.45 mL/g for pores having a pore diameter of 12 nm to less than 16 nm, and a second pore volume of 0.15 to 0.28 mL/g for pores of 2.0 nm to less than 12.0 nm.
2. The catalyst of claim 1 further comprising a ratio of the first metals fraction to the second metals fraction ranging from 2.0 to 6.0.
3. The catalyst of claim 1 wherein the second metals fraction comprises at least one metal from a first metal subgroup selected from cobalt, rhodium or iridium, and at least one metal from a second metal subgroup selected from nickel, palladium, or platinum.
4. The catalyst of claim 3 wherein the first metal subgroup is present in an amount from 0.5 to 2.0 wt % based on the total weight of the catalyst and the second metal subgroup is present in an amount from 0.3 to 1.0 wt % based on the total weight of the catalyst.
5. The catalyst of claim 3 wherein the second metals fraction comprises one metal from the first metal subgroup and one metal from the second metal subgroup.
6. The catalyst of claim 1 wherein the total weight of the first metals fraction and the second metals fraction is from 3.0 to 12.0 wt % based on the total weight of the catalyst.
7. The catalyst of claim 1 wherein the first metals fraction is molybdenum.
8. The catalyst of claim 1 wherein the second metals fraction comprises cobalt and nickel.
9. The catalyst of claim 1 wherein the metals component comprises molybdenum, cobalt and nickel.
10. The catalyst of claim 1 wherein the first pore volume is 0.30 to 0.40 mL/g.
11. The catalyst of claim 10 wherein the first pore volume is 0.32 to 0.36 mL/g.
12. The catalyst of claim 1 where the second pore volume is 0.16 to 0.25 mL/g.
13. The catalyst of claim 1 further comprising a third pore volume of 0.01 to 0.20 mL/g for pores from 16 nm to 60 nm.
14. The catalyst of claim 13 wherein the total of the first pore volume and the third pore volume is from 0.32 to 0.60 mL/g.
15. The catalyst of claim 1 further comprising a total pore volume of 0.63 to 0.75 mL/g.
16. The catalyst of claim 1 further comprising a specific surface area of 180 to 230 m 2 /g.
17. The catalyst of claim 1 further comprising a median pore diameter of 10.0 to 16.0 nm.
18. The catalyst of claim 1 further comprising a maximum phosphorus content of 1000 ppm based on the total weight of the catalyst.
19. The catalyst of claim 18 wherein the maximum phosphorus content is 200 ppm.
20. A process for producing a catalyst, the process comprising impregnating a metals component onto a carrier,
the carrier comprising alumina; and
the metals component comprising a first metals fraction and a second metals fraction, the first metals fraction comprising at least one metal selected from chromium, molybdenum, tungsten, or mixtures thereof, and the second metals fraction comprising at least two different metals selected from cobalt, rhodium, iridium, nickel, palladium, platinum or mixtures thereof,
wherein the catalyst has a first pore volume of 0.28 to 0.45 mL/g for pores having a pore diameter of 12 nm to less than 16 nm, and a second pore volume of 0.15 to 0.28 mL/g for pores of 2.0 nm to less than 12.0 nm.