Gas-phase and liquid-gas-phase nitrilation process
US-2016016153-A1 · Jan 21, 2016 · US
US11452995B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11452995-B2 |
| Application number | US-201816956677-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 20, 2018 |
| Priority date | Dec 20, 2017 |
| Publication date | Sep 27, 2022 |
| Grant date | Sep 27, 2022 |
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The invention relates to a catalyst and catalyst layer and process for preparing dimethyl ether from synthesis gas or methanol as well as the use of the catalyst or catalyst layer in this process.
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The invention claimed is: 1. A catalyst admixture of catalyst 2 particles comprising an acidic aluminosilicate zeolite with an SiO 2 :Al 2 O 3 molar ratio of from 10 to 1500:1, 10 to 90 weight % of at least one binder material and 0.01 to 20 weight % of copper, based on the total weight of catalyst 2 particles, which is 100 weight %, and catalyst 1 particles comprising 5 to 80 weight % CuO, ZnO, Al 2 O 3 and optionally ZrO 2 . 2. The catalyst admixture according to claim 1 , formed of a packed bed of an admixture of the catalyst 1 particles and the catalyst 2 particles in a weight ratio of from 1:9 to 9:1. 3. The catalyst admixture according to claim 1 , wherein in the catalyst 2 particles the amount of copper is 0.3 to 5 weight %, based on the total weight of the catalyst 2 particles. 4. The catalyst admixture according to claim 1 , wherein, in the catalyst 2 particles, the binder material is an inorganic oxide binder material different from the aluminosilicate zeolite and copper. 5. The catalyst admixture according to claim 4 , wherein the inorganic oxide binder material is selected from the group consisting of Al 2 O 3 , SiO 2 , TiO 2 , ZrO 2 , or mixtures thereof. 6. The catalyst according to claim 4 , wherein the amount of the inorganic oxide binder material is 20 to 70 weight %, based on the total weight of the catalyst 2 particles. 7. The catalyst admixture according to claim 1 , wherein the catalyst 2 particles are formed of 30 to 80 weight % of at least one acidic aluminosilicate of framework type MFI, 20 to 70 weight % of at least one binder material selected from Al 2 O 3 , SiO 2 , TiO 2 and ZrO 2 , and 0.1 to 5 weight % of copper, based on the total weight of the catalyst 2 particles, which is 100 weight %. 8. The catalyst admixture according to claim 1 , wherein the catalyst 2 particles comprise ZSM-5 aluminosilicate, Al 2 O 3 as binder material, and copper. 9. The catalyst admixture according to claim 1 , wherein the catalyst 1 and catalyst 2 particles have an average maximum particle diameter of from 0.5 to 5 mm. 10. A process for preparing dimethyl ether from methanol, comprising contacting methanol with the catalyst admixture according to claim 1 under dehydrating conditions. 11. The process according to claim 10 , wherein the temperature is in the range of from 200 to 400° C. 12. The process according to claim 10 , wherein the temperature is in the range of from 270 to 280° C. 13. A synthesis gas-to-dimethyl ether process comprising contacting synthesis gas with the catalyst admixture according to claim 1 . 14. The catalyst admixture according to claim 9 , wherein the catalyst 1 and catalyst 2 particles are present as a packed bed of extrudates with an average maximum diameter of from 1 to 3.5 mm and a ratio of average length to average maximum diameter of from 0.5:1 to 10:1.
Cylinders or rings · CPC title
Copper · CPC title
Constitutive chemical elements of heterogeneous catalysts · CPC title
Dimethyl ether · CPC title
by dehydration of compounds containing hydroxy groups · CPC title
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