Catalyst and process for the conversion of oxygenates to olefins
US-2016310934-A1 · Oct 27, 2016 · US
US11247198B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11247198-B2 |
| Application number | US-201716767300-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 20, 2017 |
| Priority date | Nov 29, 2017 |
| Publication date | Feb 15, 2022 |
| Grant date | Feb 15, 2022 |
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The present application discloses a catalyst, the catalyst contains a molecular sieve, there is at least one-dimension 8-membered ring channel in the molecular sieve structure, the diameter of a diffusible substance in the direction of the 8-membered ring channel is no less than 2.0 Å, the diameter of a substance that can be accommodated in the molecular sieve structure is no more than 6 Å; the catalyst is used for a methanol and/or dimethyl ether to propylene reaction, comprising contacting methanol and/or dimethyl ether with a methanol-to-propylene catalyst to obtain propylene.
Opening claim text (preview).
The invention claimed is: 1. A method for preparing propylene from methanol and/or dimethyl ether, comprising bringing methanol and/or dimethyl ether into contact with a methanol to propylene catalyst to obtain propylene; the methanol to propylene catalyst comprises a catalyst, wherein the catalyst comprises a molecular sieve with at least one-dimensional 8-membered ring channel in the molecular sieve structure, and the diameter of a sphere that can diffuse along the direction of the 8-membered ring channel is no less than 2.0 Å, the diameter of the sphere that can be included in the molecular sieve structure is no more than 6 Å. 2. The method of claim 1 , wherein the molecular sieve is at least one selected from aluminosilicate molecular sieve, silicoaluminophosphate molecular sieve and transition metal-substituted aluminophosphate molecular sieve. 3. The method of claim 2 , wherein a reaction temperature for bringing methanol and/or dimethyl ether into contact with the methanol to propylene catalyst is in a range of 300° C. to 500° C. 4. The method of claim 2 , wherein a conversion rate of raw material is greater than 75% in the method. 5. The method of claim 2 , wherein a single pass selectivity to propylene is greater than 60% in the method. 6. The method of claim 1 , wherein the molecular sieve structure contains two-dimensional or three-dimensional 8-membered ring channels. 7. The method of claim 1 , wherein the diameter of the sphere that can be included in the molecular sieve structure is in a range of 4.8 Å to 6 Å. 8. The method of claim 1 , wherein a topology of the molecular sieve structure is at least one selected from AFN, DFT, PHI, SIV, THO, APD, CAS, EDI, GIS and VNI.
A-type · CPC title
Silicoaluminophosphates [SAPO compounds] · CPC title
Ethene · CPC title
Aluminophosphates containing other elements, e.g. metals, boron · CPC title
of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65 · CPC title
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