One exemplary embodiment can be a slurry hydrocracking process. The process can include providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone. The slurry catalyst may have about 32-about
One exemplary embodiment can be a slurry hydrocracking process. The process can include providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone. The slurry catalyst may have about 32-about 50%, by weight, iron; about 3-about 14%, by weight, aluminum; no more than about 10%, by weight, sodium; and about 2-about 10%, by weight, calcium. Typically, all catalytic component percentages are as metal and based on the weight of the dried slurry catalyst.
대표청구항▼
1. A slurry hydrocracking process, comprising: providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone, wherein the slurry catalyst comprises: 1) about 40-about 50%, by weight, iron;2) abo
1. A slurry hydrocracking process, comprising: providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone, wherein the slurry catalyst comprises: 1) about 40-about 50%, by weight, iron;2) about 3-about 14%, by weight, aluminum;3) no more than about 10%, by weight, sodium; and4) about 3-about 8%, by weight, calcium;wherein all catalytic component percentages are as metal and based on the weight of a dried slurry catalyst. 2. The slurry hydrocracking process according to claim 1, wherein the slurry hydrocracking zone comprises an upflow tubular reactor. 3. The slurry hydrocracking process according to claim 1, wherein the iron, aluminum, sodium, and calcium are present as oxides, hydroxides, or oxide hydrates. 4. The slurry hydrocracking process according to claim 1, wherein the slurry catalyst comprises about 40-about 50%, by weight, iron as metal and based on the weight of the dried slurry catalyst. 5. The slurry hydrocracking process according to claim 1, wherein the dried slurry catalyst comprises no more than about 1%, by weight, water. 6. The slurry hydrocracking process according to claim 1, wherein the dried slurry catalyst has a loss on ignition at 900° C. of no more than about 0.01%, by weight. 7. The slurry hydrocracking process according to claim 1, wherein the one or more hydrocarbons comprises a light vacuum gas oil, a heavy vacuum gas oil, or a pitch. 8. The slurry hydrocracking process according to claim 1, wherein the slurry catalyst comprises a red mud. 9. The slurry hydrocracking process according to claim 1, wherein the slurry catalyst has an average particle size of no more than about 75 microns. 10. The slurry hydrocracking process according to claim 1, wherein the slurry catalyst comprises about 45-about 50%, by weight, iron as metal and based on the weight of the dried slurry catalyst. 11. A slurry hydrocracking process, comprising: providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone, wherein the slurry catalyst comprises: 1) about 15-about 25%, by weight, iron;2) about 3.5-about 5%, by weight, aluminum;3) no more than about 5%, by weight, sodium; and4) greater than about 3%, by weight, calcium;wherein all catalytic component percentages are as metal and based on the weight of the slurry catalyst with a loss on ignition at 900° C. of about 40-about 60%, by weight. 12. The slurry hydrocracking process according to claim 11, wherein the slurry catalyst has a loss on ignition at 900° C. of about 50%, by weight. 13. The slurry hydrocracking process according to claim 11, wherein the slurry catalyst comprises about 2-about 5%, by weight, calcium and about 0.5-about 5%, by weight, titanium as metal based on the weight of the slurry catalyst. 14. The slurry hydrocracking process according to claim 11, wherein the slurry hydrocracking zone comprises an upflow tubular reactor. 15. The slurry hydrocracking process according to claim 11, wherein the iron, aluminum, sodium, and calcium are present as oxides, hydroxides, or oxide hydrates. 16. The slurry hydrocracking process according to claim 11, wherein the one or more hydrocarbons comprises a light vacuum gas oil, a heavy vacuum gas oil, or a pitch. 17. A slurry hydrocracking process, comprising: providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone, wherein the slurry catalyst comprises: 1) about 57-about 72%, by weight, iron oxide;2) about 6-about 27%, by weight, aluminum oxide;3) no more than about 14%, by weight, sodium oxide; and4) about 4-about 12%, by weight, calcium oxide;wherein all catalytic component percentages are as oxide and based on the weight of a dried slurry catalyst. 18. The slurry hydrocracking process according to claim 17, wherein the dried slurry catalyst comprises no more than about 1%, by weight, water. 19. The slurry hydrocracking process according to claim 17, wherein the dried slurry catalyst has a loss on ignition at 900° C. of no more than about 0.01%, by weight. 20. The slurry hydrocracking process according to claim 17, wherein the slurry hydrocracking zone comprises an upflow tubular reactor.
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