초록 ▼

A process for selectively producing para-xylene from a feedstock enriched in C8isoalkanes and/or isoalkenes is disclosed. The feed is contacted with Group VIII metal loaded molecular sieve catalyst of low acidity under dehydrocyclization conditions wherein the molecular sieve has a channel size rang

A process for selectively producing para-xylene from a feedstock enriched in C8isoalkanes and/or isoalkenes is disclosed. The feed is contacted with Group VIII metal loaded molecular sieve catalyst of low acidity under dehydrocyclization conditions wherein the molecular sieve has a channel size ranging from about 5-8 Angstroms and a 10 to 12 membered ring structure containing at least two elements selected from the group consisting of Si, Al, P, Ge, Ga and Ti.

대표청구항 ▼

1. A process for producing para-xylene from a feedstock enriched in C8isoalkane or isoalkene components comprising: contacting said feedstock with a dehydrocyclization catalyst under dehydrocyclization conditions of temperature and hydrogen partial pressure to convert C8isoalkane or isoalkene com

1. A process for producing para-xylene from a feedstock enriched in C8isoalkane or isoalkene components comprising: contacting said feedstock with a dehydrocyclization catalyst under dehydrocyclization conditions of temperature and hydrogen partial pressure to convert C8isoalkane or isoalkene components into para-xylene; and recovering a reformate rich in para-xylene, wherein said catalyst comprises a molecular sieve support having low acidity and a channel size in the range of about 5-8 angstroms and having a 10 to 12 membered ring structure containing at least two elements selected from Si, Al, P, Ge, Ga or Ti, wherein said molecular sieve further contains at least one Periodic Table Group VIII metal, and wherein said molecular sieve is selected from zeolite ETS-10 or ETAS-10. 2. The process of claim 1 wherein said feedstock contains at least about 5 wt % of said C8components. 3. The process of claim 2 wherein said C8components are selected from 2,5-dimethylhexane, 2,5-dimethylhexene, 2,5-dimethylhexadiene, 2,5-dimethylhexatriene or mixtures thereof. 4. The process of claim 1 wherein said molecular sieve contains at least two elements selected from Si, Al or Ti. 5. The process of claim 1 wherein said group VIII metal is platinum. 6. The process of claim 1 wherein said feedstock contains at least 10 wt % of said C8components. 7. The process of claim 6 wherein said feedstock contains at least 50 wt % of said C8components. 8. The process of claim 7 wherein said feedstock contains seater than 90 wt % of said C8components. 9. The process of claim 1 wherein said catalyst comprises a Group VIII metal-loaded ETAS-10. 10. The process of claim 1 wherein said molecular sieve support has a alpha value of less than 10. 11. The process of claim 10 wherein said alpha value is less than 1. 12. The process of claim 11 wherein said alpha value is less than 0.1. 13. The process of claim 1 wherein said reformate contains para-xylene in an amount greater than the thermodynamic equilibrium concentration thereof in the total xylenes present. 14. The process of claim 1 wherein the ratio of para-xylene to total xylenes present in said reformate is at least about 50%. 15. The process of claim 14 wherein said ratio is at least about 75%. 16. The process of claim 1, wherein the Group VIII metal is one of platinum, rhenium or iridium. 17. The process of claim 16, wherein the molecular sieve further contains a promoter selected from tin, iron, germanium or tungsten.