FCC catalyst compositions containing boron oxide and phosphorus

Patent metadata

Field	Value
Publication number	US-9796932-B2
Application number	US-201314134640-A
Country	US
Kind code	B2
Filing date	Dec 19, 2013
Priority date	Dec 19, 2013
Publication date	Oct 24, 2017
Grant date	Oct 24, 2017

Abstract

Described are fluid catalytic cracking (FCC) compositions, methods of manufacture and use. FCC catalyst compositions comprise particles first particle type comprising one or more boron oxide components and a first matrix component and a second particle type having a composition different from the first particle type, the second particle type comprising a second matrix component, a phosphorus component and 20% to 95% by weight of a zeolite component. The FCC catalyst compositions can be used to crack hydrocarbon feeds, particularly resid feeds containing high V and Ni, resulting in lower hydrogen and coke yields.

First claim

What is claimed is:

1. An FCC catalyst composition for cracking hydrocarbons, the FCC catalyst composition comprising:
a first particle type comprising one or more boron oxide components, and a first matrix component wherein the first particle type does not incorporate a zeolite; and
a second particle type comprising a second matrix component, a phosphorus component, and 20% to 95% by weight of a zeolite component;
wherein the second particle type is different from the first particle type and the first particle type and second particle type are mixed together.

2. The FCC catalyst composition 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.

3. The FCC catalyst composition of claim 2 , wherein the phosphorus component is present in an amount in the range of about 0.5% to 10.0% by weight on an oxide basis.

4. The FCC catalyst composition of claim 1 , wherein at least one of the first matrix component and the second matrix component comprise at least one 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.

5. The FCC catalyst composition of claim 4 , wherein the second particle type further comprises an oxide selected from the group consisting of yttria, and a rare earth component selected from ceria, lanthana, praseodymia, neodymia, and combinations thereof.

6. The FCC catalyst composition of claim 5 , 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.

7. The FCC catalyst composition of claim 4 , wherein the second particle type further comprises a transition alumina component present in a range of 1 wt. % to 35 wt. %.

8. The FCC catalyst composition of claim 7 , wherein the zeolite component is intergrown with the second matrix component.

9. The FCC catalyst composition of claim 8 , 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.

10. The FCC catalyst composition of claim 9 , 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.

11. The FCC catalyst composition of claim 10 , wherein the rare-earth component is selected from the group consisting of ceria, lanthana, praseodymia, and neodymia.

12. The FCC catalyst composition of claim 11 , 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.

13. The FCC catalyst composition of claim 12 , 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.

14. A method of cracking a hydrocarbon feed under fluid catalytic cracking conditions, the method comprising contacting the hydrocarbon feed with the catalyst composition of claim 13 .

15. A method of cracking a hydrocarbon feed under fluid catalytic cracking conditions, the method comprising contacting the hydrocarbon feed with the catalyst composition of claim 1 .

Assignees

• Basf Corp

Inventors

• Smith Gary M
• Mcguire Jr Robert
• Yilmaz Bilge

Classifications

• B01J2229/186

  not in framework positions · CPC title

• B01J37/0045

  Drying a slurry, e.g. spray drying · CPC title

• C10G11/18

  according to the "fluidised-bed" technique · CPC title

• B01J37/28

  Phosphorising · CPC title

• B01J37/04

  Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title