Method for producing gasoline alternative fuel and gasoline alternative fuel
US-2024043753-A1 · Feb 8, 2024 · US
US9382169B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9382169-B2 |
| Application number | US-201113333383-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 21, 2011 |
| Priority date | Jun 22, 2009 |
| Publication date | Jul 5, 2016 |
| Grant date | Jul 5, 2016 |
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A lower olefin producing catalyst which has high olefin production efficiency and maintains its activity for a long period of time when lower olefins are produced from an oxygen-containing compound, which is a solid catalyst used in producing lower olefins from an oxygen-containing compound, includes a solid-state catalyst component containing an MFI-type zeolite, in which, at a position where the shortest distance to the outer surface is maximum among all positions inside a structure of the solid catalyst, the thickness defined as a distance twice the shortest distance from the point to the outer surface is in a range of from 0.1 to 2.0 mm, and a method for producing lower olefins.
Opening claim text (preview).
The invention claimed is: 1. A lower olefin producing catalyst comprising: a solid-state catalyst component comprising an MFI-type zeolite, the thickness of the catalyst being in a range of from 0.1 to 2.0 mm, where the thickness is defined as a distance twice the shortest distance from the outer surface to a position where the shortest distance to the outer surface is maximum among all positions inside a structure of the solid catalyst, and the compacted bulk density (CBD) of the catalyst being 800 kg/m 3 or less, wherein the lower olefin producing catalyst is of a shape selected from the group consisting of honeycomb-shaped, three-leaf-shaped and four-leaf-shaped, the solid-state catalyst component contains an alkaline-earth metal component in an amount of 0.3 to 10 parts by weight in terms of metal relative to 100 parts by weight of the MFI-type zeolite. 2. The lower olefin producing catalyst according to claim 1 , wherein the lower olefin producing catalyst is obtained by a process comprising shaping a mixture comprising the solid-state catalyst component comprising an MFI-type zeolite, and at least one binder selected from the group consisting of an oxide of aluminum, a hydroxide of aluminum, an oxide of silicon, a hydroxide of silicon and clay. 3. The lower olefin producing catalyst according to claim 2 , wherein the alkaline-earth metal is calcium. 4. The lower olefin producing catalyst according to claim 1 , wherein the lower olefin producing catalyst is honeycomb-shaped. 5. The lower olefin producing catalyst according to claim 1 , wherein the atomic ratio Si/Al in the zeolite framework of the MFI-type zeolite is in a range of from 10 to 2,000. 6. A method for producing a lower olefin producing catalyst comprising: preparing a mixture by mixing/kneading a solid-state catalyst component comprising an MFI-type zeolite and at least one binder selected from the group consisting of an oxide of aluminum, a hydroxide of aluminum, an oxide of silicon, a hydroxide of silicon, and clay in the presence of a polar solvent; and shaping the mixture and calcining the shaped mixture, to obtain the catalyst having a thickness in a range of from 0.1 to 2.0 mm, where the thickness is defined as a distance twice the shortest distance from the outer surface to a position where the shortest distance to the outer surface is maximum among all positions inside a structure of the solid catalyst, and the catalyst having the compacted bulk density (CBD) of 800 kg/m 3 or less, wherein the lower olefin producing catalyst is of a shape selected from the group consisting of honeycomb-shaped, three-leaf-shaped and four-leaf-shaped, the solid-state catalyst component contains an alkaline-earth metal component in an amount of 0.3 to 10 parts by weight in terms of metal relative to 100 parts by weight of the MFI-type zeolite. 7. A method for producing lower olefins comprising: contacting an oxygen-containing compound with the lower olefin producing catalyst according to claim 1 in a reactor into which the catalyst has been packed at 500° C. to 650° C. of outlet temperature under 0.12 MPa to 1.0 MPa of inlet pressure. 8. The method for producing lower olefins according to claim 7 , wherein the oxygen-containing compound comprises dimethyl ether and/or methanol. 9. The method for producing lower olefins according to claim 7 , wherein the catalyst packing density in the reactor is 800 kg/m 3 or less. 10. The method for producing lower olefins according to claim 8 , wherein the catalyst packing density in the reactor is 800 kg/m 3 or less. 11. The lower olefin producing catalyst according to claim 1 , wherein the alkaline-earth metal is calcium. 12. The lower olefin producing catalyst according to claim 1 , wherein the atomic ratio Si/Al in the zeolite framework of the MFI-type zeolite is in a range of 50 to 1,000. 13. The lower olefin producing catalyst according to claim 1 , wherein the compacted bulk density (CBD) of the catalyst is 729 kg/m 3 or less. 14. The lower olefin producing catalyst according to claim 1 , wherein the compacted bulk density (CBD) of the catalyst is 700 kg/m 3 or less. 15. The lower olefin producing catalyst according to claim 1 , wherein the compacted bulk density (CBD) of the catalyst is 650 kg/m 3 or less. 16. The lower olefin producing catalyst according to claim 1 , wherein the compacted bulk density (CBD) of the catalyst ranges from 200 to 650 kg/m 3 .
Scanning electron microscopy; Transmission electron microscopy · CPC title
Bulk density · CPC title
Cylinders or rings · CPC title
Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title
characterised by their shape or configuration · CPC title
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