Catalyst for conversion of hydrocarbons, process of making and process of using thereof—bimetallic deposition
US-9233884-B2 · Jan 12, 2016 · US
US10207255B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10207255-B2 |
| Application number | US-201415035505-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 6, 2014 |
| Priority date | Nov 22, 2013 |
| Publication date | Feb 19, 2019 |
| Grant date | Feb 19, 2019 |
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In an embodiment, a method for making a catalyst, comprises: forming a mixture comprising a germanium source, an alkali metal source, an aluminum source, and a silica source, wherein the mixture has a pH; adjusting the pH of the mixture to a value of greater than or equal to 9.5; crystallizing and calcining the mixture to form a zeolite; depositing platinum on the zeolite; and calcining the zeolite to form the final catalyst. The final catalyst is non-acidic and has an aluminum content of less than or equal to 0.75 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide and a Si:Al2 mole ratio of greater than or equal to 125.
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We claim: 1. A method for making a catalyst, comprising: forming a mixture comprising a germanium source, an alkali metal source, an aluminum source, and a silica source, wherein the mixture has a pH; adjusting the pH of the mixture to a value of 9.5 to less than 13; crystallizing and calcining the mixture to form a zeolite; a medium pore zeolite having an average pore size of 5 to 8 Å; depositing platinum on the zeolite; and calcining the zeolite to form the final catalyst; wherein the final catalyst is non-acidic and has an aluminum content of less than or equal to 0.75 wt % based on the total weight of the final catalyst excluding any binder or extrusion aide, and a final Si:Al 2 mole ratio of 125 to 211; wherein the final catalyst has a Ge content of 0.1 to 3 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide. 2. The method of claim 1 , wherein the forming of the mixture comprises: forming a first aqueous solution, wherein the first solution comprises the germanium source and the alkali metal source; forming a second aqueous solution, wherein the second solution comprises the aluminum source; combining the first and second aqueous solutions to form a combined solution; and adding the silica source to the combined solution to form the mixture. 3. The method of claim 1 , wherein the mixture has a mixture Si:Al 2 mole ratio of 175 to 290, a mixture Si:Ge mole ratio of 5 to 100, and a mixture Na:Al mole ratio of 10 to 60. 4. The method of claim 1 , wherein the zeolite is a ZSM-5 zeolite. 5. The method of claim 1 , wherein the final catalyst has one or both of a final Si:Ge mole ratio of 40 to 400 and a final Na:Al mole ratio of 0.9 to 2.5. 6. The method of claim 1 , wherein the Ge content is 0.4 to 2.5 wt %, or wherein the final catalyst has an Na content of 0.5 to 2 wt %, or wherein the final catalyst has a Pt content of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the final catalyst excluding any binder and extrusion aide. 7. The method of claim 1 , wherein the method does not include an ion-exchange step with an alkali metal. 8. The method of claim 1 , wherein the final catalyst is free of cesium. 9. The method of claim 1 , wherein the alkali metal source comprises at least one of a sodium source and a potassium source. 10. The method of claim 1 , wherein the alkali metal source comprises at least one of NaOH and NaCl. 11. The method of claim 1 , wherein the pH is 9.5 to 12.5. 12. The method of claim 1 , wherein the final catalyst has a Ge content of 0.4 to 1.5 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide. 13. The method of claim 1 , wherein the final catalyst comprises Al in an amount of 0.45 to 0.7 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide. 14. The method of claim 1 , wherein the Ge content is 0.4 to 2.5 wt %, wherein the final catalyst has an Na content of 0.5 to 2 wt %, and wherein the final catalyst has a Pt content of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the final catalyst excluding any binder and extrusion aide. 15. The method of claim 1 , wherein the final Si:Al 2 mole ratio is 125 to 200.
containing crystalline alumino-silicates, e.g. molecular sieves · CPC title
Platinum · CPC title
containing platinum group metals or compounds thereof · CPC title
by condensation of hydrocarbons with partial elimination of hydrogen · CPC title
of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11 · CPC title
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