Structurally enhanced cracking catalysts

US9675967B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9675967-B2
Application numberUS-201514827873-A
CountryUS
Kind codeB2
Filing dateAug 17, 2015
Priority dateJun 20, 2007
Publication dateJun 13, 2017
Grant dateJun 13, 2017

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

A cracking catalyst contains a substantially inert core and an active shell, the active shell containing a zeolite catalyst and a matrix. Methods of making and using the cracking catalyst are also described.

First claim

Opening claim text (preview).

What is claimed is: 1. A process of forming a fluidizable cracking catalyst, the process comprising: forming a slurry by combining at least water, about 1 to about 70 parts by weight kaolin, about 1 to about 70 parts by weight of substantially inert core microspheres comprising alpha-alumina, and a zeolite catalyst precursor comprising germanium oxide, tin oxide, phosphorus oxide, boron oxide, iron oxide, gallium oxide, indium oxide, gallosilicates, borosilicates, ferrosilicates, or a mixture of two or more thereof; and spray drying the slurry to form spray dried particles containing the substantially inert core microspheres with an active catalytic shell at least partially surrounding the substantially inert core microspheres; and crystallizing a zeolite in the active catalytic shell to form the fluidizable cracking catalyst. 2. The process of claim 1 , wherein the fluidizable cracking catalyst comprises from about 30 wt % to about 70 wt % of the active catalytic shell. 3. The process of claim 1 further comprising calcining the spray dried particles. 4. The process of claim 1 , wherein the inert core microsphere have an average diameter of from about 35 μm to about 75 μm. 5. The process of claim 1 , wherein the inert core microsphere have an average diameter of about 45 μm. 6. The process of claim 1 , wherein the slurry further comprises an inorganic binder. 7. The process of claim 6 , wherein the inorganic binder comprises an aluminum stabilized SiO 2 hydrosol, a dispersible pseudo-boehmite binder reinforced with silica, or an aluminum chlorohydrol binder. 8. A cracking process comprising: contacting a hydrocarbon feedstream and a fluidizable cracking catalyst; wherein the fluidizable cracking catalyst comprises: a substantially inert core comprising at least one of mullite or alpha-alumina; and an active catalytic shell around the substantially inert core, the active catalytic shell comprising a zeolite catalyst incorporated in a matrix, wherein said zeolite catalyst is formed by in-situ crystallization of the zeolite within the matrix, wherein the active catalytic shell comprises 30 to 70 wt. % of said fluidizable cracking catalyst and the zeolite is formed from a zeolite catalyst precursor comprising germanium oxide, tin oxide, phosphorus oxide, boron oxide, iron oxide, gallium oxide, indium oxide, gallosilicates, borosilicates, ferrosilicates, or a mixture of two or more thereof. 9. A cracking process comprising: contacting a hydrocarbon feedstream and a fluidizable cracking catalyst; wherein the fluidizable cracking catalyst comprises: a substantially inert core; and an active catalytic shell around the core, the active catalytic shell comprising: an alumina having a metals passivation function and a zeolite catalyst incorporated in a matrix, wherein the zeolite catalyst is formed by in-situ crystallization of the zeolite within the matrix, wherein the active catalytic shell comprises 30 to 70 wt. % of said fluidizable cracking catalyst and the zeolite is formed from a zeolite catalyst precursor comprising germanium oxide, tin oxide, phosphorus oxide, boron oxide, iron oxide, gallium oxide, indium oxide, gallosilicates, borosilicates, ferrosilicates, or a mixture of two or more thereof.

Assignees

Inventors

Classifications

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US9675967B2 cover?
A cracking catalyst contains a substantially inert core and an active shell, the active shell containing a zeolite catalyst and a matrix. Methods of making and using the cracking catalyst are also described.
Who is the assignee on this patent?
Basf Corp
What technology area does this patent fall under?
Primary CPC classification B01J29/084. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Jun 13 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).