초록 ▼

A process and catalyst is disclosed for converting a heavy hydrocarbon feed stream into lighter hydrocarbon products using a two component catalyst. The catalyst comprises iron and molybdenum containing catalyst. Alumina may be a third catalyst component. The molybdenum is present in the heavy hydro

A process and catalyst is disclosed for converting a heavy hydrocarbon feed stream into lighter hydrocarbon products using a two component catalyst. The catalyst comprises iron and molybdenum containing catalyst. Alumina may be a third catalyst component. The molybdenum is present in the heavy hydrocarbon feed stream at about 500 wppm or less and the weight ratio of iron to the molybdenum is less than 5. Much lower concentrations of expensive molybdenum can be used due to the addition of iron in the catalyst.

대표청구항 ▼

1. A process for converting a heavy hydrocarbon feed stream into lighter hydrocarbon products comprising: mixing said heavy hydrocarbon feed stream with catalyst and hydrogen to provide a heavy hydrocarbon slurry, said catalyst comprising an iron component and a solid molybdenum component; wherein s

1. A process for converting a heavy hydrocarbon feed stream into lighter hydrocarbon products comprising: mixing said heavy hydrocarbon feed stream with catalyst and hydrogen to provide a heavy hydrocarbon slurry, said catalyst comprising an iron component and a solid molybdenum component; wherein said solid molybdenum component comprises molybdenum in a hydrocarbon matrix and said molybdenum is present in the hydrocarbon feed stream at about 500 wppm or less and the weight ratio of iron to the molybdenum is less than 5; andhydrocracking hydrocarbons in said heavy hydrocarbon slurry in the presence of hydrogen and said catalyst to produce a hydrocracked slurry product comprising lighter hydrocarbon products. 2. The process of claim 1 wherein the iron component is provided as bauxite, red mud, iron sulfate, limonite, laterite or iron salt particles. 3. The process of claim 1 wherein the iron is provided with alumina in the iron component. 4. The process of claim 1 wherein the iron in the iron component is no more than about 1.0 wt % in the hydrocarbon feed. 5. The process of claim 1 wherein the iron component is provided as bauxite particles which comprise no more than 2.5 wt % of the hydrocarbon feed. 6. The process of claim 1 wherein the iron component is provided as particles that are mixed with the molybdenum component. 7. The process of claim 6 further comprising mixing a molybdenum compound with a hydrocarbon material and a sulfiding agent to provide a catalyst precursor concentrate comprising the molybdenum component, heating the catalyst precursor concentrate to an elevated temperature to produce a catalyst concentrate, and adding particles comprising the iron component to the hydrocarbon material. 8. The process of claim 7 further comprising adding particles comprising the iron component to the hydrocarbon material before heating the catalyst precursor concentrate to an elevated temperature. 9. The process of claim 8 further comprising mixing said catalyst concentrate with said heavy hydrocarbon feed stream. 10. A process for converting a heavy hydrocarbon feed stream into lighter hydrocarbon products comprising: mixing said heavy hydrocarbon feed stream with catalyst and hydrogen to provide a heavy hydrocarbon slurry, said catalyst comprising iron and alumina particles mixed with molybdenum; wherein said molybdenum is prepared by mixing said molybdenum with a heavy hydrocarbon material and heating the mixture to an elevated temperature to provide molybdenum in a hydrocarbon matrix and said molybdenum is present in the hydrocarbon feed stream at about 250 wppm or less and the weight ratio of iron to the molybdenum is less than 5 after mixing said heavy hydrocarbon feed stream with said catalyst; andhydrocracking hydrocarbons in said heavy hydrocarbon slurry in the presence of hydrogen and said catalyst to produce a slurry hydrocracked product comprising lighter hydrocarbon products. 11. The process of claim 10 wherein the iron is provided on bauxite particles which comprise no more than 2.5 wt % of the hydrocarbon feed. 12. The process of claim 10 wherein the iron in the catalyst is no more than about 1.0 wt % in the heavy hydrocarbon feed stream.