FCC catalyst compositions containing boron oxide and phosphorus

1. A method of cracking a hydrocarbon feed under fluid catalytic cracking conditions, the method comprising adding FCC compatible inorganic particles comprising a first particle type comprising one or more boron oxide components and a first matrix component into a FCC unit and adding cracking microspheres comprising a second particle type comprising a second matrix component, a phosphorus component and 20% to 95% by weight of a zeolite component into the FCC unit;

wherein the second particle type is different from the first particle type and the first particle type does not incorporate a zeolite.

2. The method of claim 1 , wherein the one or more boron oxides present in the FCC composition is in the in the range of 0.005% to 8% by weight on an oxide basis and the phosphorus content is present on the cracking microspheres in the range of 0.5% and 10.0% by weight on an oxide basis.

3. The method of claim 2 , wherein the cracking microspheres further comprise a rare earth component selected from the group consisting of yttria, ceria, lanthana, praseodymia, neodymia, and combinations thereof.

4. The method of claim 3 , wherein the rare earth component is lanthana, and the lanthana is present in a range of 0.5 wt. % to about 10.0 wt. % on an oxide basis based on the weight of the FCC catalyst composition.

5. The method of claim 4 , wherein the cracking microspheres further comprise a transition alumina component present in a range of 1 wt. % to 35 wt. %.

6. The method of claim 1 , wherein the first particle type does not incorporate a zeolite.

7. The method of claim 1 , wherein the one or more boron oxide components are present in an amount in the range of 0.005% to 8% by weight of the FCC catalyst composition.

8. The method of claim 1 , wherein the phosphorus component is present in an amount in the range of about 0.5% to 10.0% by weight of the second particle type on an oxide basis.

9. The method of claim 1 , wherein at least one of the first matrix component and the second matrix component comprises at least one of member of the group consisting of kaolinite, halloysite, montmorillonite, bentonite, attapulgite, kaolin, amorphous kaolin, metakaolin, mullite, spinel, hydrous kaolin, clay, gibbsite (alumina trihydrate), boehmite, titania, alumina, silica, silica-alumina, silica-magnesia, magnesia, and sepiolite.

10. The method of claim 9 , wherein the second particle type further comprises a transition alumina component present in a range of 1 wt. % to 35 wt. %.

11. The method of claim 10 , wherein the zeolite component is intergrown with the second matrix component.

12. The method of claim 11 , wherein the second particle type comprises microspheres obtained by forming rare earth-containing microspheres containing the second matrix component, the transition alumina, the zeolite component intergrown within the second matrix component, an oxide selected from the group consisting of yttria, and a rare earth component selected from ceria, lanthana, praseodymia, neodymia, and combinations thereof, and further adding the phosphorus component to the rare earth-containing microspheres to provide catalytic microspheres.

13. The method of claim 12 , wherein the phosphorus component is in the range of 0.5 wt. % to about 10.0 wt. % P 2 O 5 on an oxide basis.

14. The method of claim 13 , wherein the rare-earth component is selected from the group consisting of ceria, lanthana, praseodymia, and neodymia.

15. The method of claim 14 , wherein the rare earth component is lanthana, and the lanthana is present in a range of 0.5 wt. % to about 10.0 wt. % on an oxide basis.

16. The method of claim 15 , wherein the microsphere has a phosphorus level of about 2-4 wt. % P 2 O 5 on an oxide basis of the FCC catalyst composition and the rare earth metal component is present in an amount of about 1-5 wt. % on an oxide basis of the FCC catalyst composition.