Modified y-type zeolites having a trimodal intracrystalline structure, method for making same, and use thereof
US-2015328625-A1 · Nov 19, 2015 · US
US9675967B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9675967-B2 |
| Application number | US-201514827873-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 17, 2015 |
| Priority date | Jun 20, 2007 |
| Publication date | Jun 13, 2017 |
| Grant date | Jun 13, 2017 |
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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.
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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.
Y-type faujasite · CPC title
in or on refractory materials · CPC title
Alumina · CPC title
Operations & Transport · mapped topic
Clays or other mineral silicates · CPC title
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