초록 ▼

One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the

One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds including at least two rings obtaining a processed distillate product.

대표청구항 ▼

1. A process for converting a hydrocarbon stream, comprising: A) passing the hydrocarbon stream comprising one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream comprising one or more C9-C22 hydrocarbons; andB) passing the distillate hydrocarbon strea

1. A process for converting a hydrocarbon stream, comprising: A) passing the hydrocarbon stream comprising one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream comprising one or more C9-C22 hydrocarbons; andB) passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds comprising at least two rings obtaining a processed distillate product. 2. The process according to claim 1, wherein the slurry hydrocracking zone operates at a temperature of about 340-about 600° C. and a hydrogen partial pressure of about 3.5-about 30 MPa. 3. The process according to claim 1, wherein the hydrocarbon stream comprises at least one of a vacuum resid, a visbroken tar, an atmospheric resid, a slurry oil, a hydrotreated resid, a tar sand, and a pitch. 4. The process according to claim 1, wherein the selective hydrocracking zone operates at a temperature of about 230-about 460° C. and about 3.5-about 21 MPa. 5. The process according to claim 1, further comprising recycling the processed distillate product from the selective hydrocracking zone to a fluid catalytic cracking zone comprising at least one riser reactor to obtain a cracked naphtha stream. 6. The process according to claim 5, further comprising passing the cracked naphtha stream from the fluid catalytic cracking zone to a naphtha separation zone, separating an aromatic stream, and passing the aromatic stream to an aromatic zone for producing at least one of benzene and one or more xylenes. 7. The process according to claim 6, further comprising passing a hydrocracked heavy naphtha product produced from the selective hydrocracking zone to the aromatic zone. 8. The process according to claim 6, further obtaining from the naphtha separation zone a first naphtha portion and a second naphtha portion and providing the first and second naphtha portions to a selective hydrotreating zone for producing a gasoline blended-stock product. 9. The process according to claim 5, further comprising obtaining a light cycle oil stream from the fluid catalytic cracking zone and passing the light cycle oil stream to the selective hydrocracking zone. 10. The process according to claim 6, further comprising passing the aromatic stream through a hydrotreatment zone and a reforming zone prior to providing to the aromatic zone. 11. The process according to claim 5, wherein a mass ratio of a recycled distillate product to a feed to the selective hydrocracking zone is about 0.05:1-about 0.95:1. 12. The process according to claim 5, wherein a mass ratio of a recycled distillate product to a feed to the selective hydrocracking zone is about 0.1:1-about 0.5:1. 13. The process according to claim 1, further comprising passing a gas oil stream from the slurry hydrocracking zone to a gas oil hydrotreatment zone to obtain a hydrotreated gas oil stream. 14. A process for converting a hydrocarbon stream, comprising: A) passing the hydrocarbon stream comprising one or more C40+ hydrocarbons to a thermal conversion zone to obtain a distillate hydrocarbon stream comprising one or more C9-C22 hydrocarbons from the thermal conversion zone; andB) passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds comprising at least two rings obtaining a processed distillate product. 15. The process according to claim 14, wherein the thermal conversion zone comprises a slurry hydrocracking reactor. 16. The process according to claim 14, wherein the thermal conversion zone comprises a delayed coking zone. 17. The process according to claim 16, wherein the delayed coking zone comprises a plurality of coke drums and a coke fractionator. 18. The process according to claim 17, further comprising recycling the processed distillate product to a fluid catalytic cracking zone. 19. A process for producing a processed distillate product, comprising: A) passing a hydrocarbon stream comprising one or more C40+ hydrocarbons to a thermal conversion zone to obtain a distillate hydrocarbon stream and a gas oil stream;B) passing the gas oil stream to a gas oil hydrotreatment zone to obtain a hydrotreated gas oil;C) passing the hydrotreated gas oil to a fluid catalytic cracking zone to obtain a light cycle oil;D) passing the light cycle oil to a hydrocracking zone for selectively hydrocracking aromatic compounds comprising at least two rings obtaining the processed distillate product; andE) recycling at least a portion of the processed distillate product from the selective hydrocracking zone to the fluid catalytic cracking zone. 20. The process according to claim 19, wherein the thermal conversion zone comprises a delayed coking zone or a slurry hydrocracking zone.