Catalyst for conversion of hydrocarbons, process of making and process of using thereof—bimetallic deposition
This invention is for a catalyst for conversion of hydrocarbons. The catalyst is a non-acidic germanium zeolite, such as Ge-ZSM-5, on which at least two metals, platinum and at least one other metal selected from Group 7, Group 8, Group 9, Group 10 and tin, are deposited on the germanium zeolite. Examples of the other metal are iridium, rhenium, palladium, ruthenium, rhodium, iron, cobalt and tin. The catalyst is prepared by synthesizing a germanium zeolite; depositing platinum and at least one other metal on the germanium zeolite; and calcining after preparation of the zeolite, before depositing the metals or after depositing the metals. The catalyst may be used in a process for the conversion of hydrocarbons, such as propane to aromatics, by contacting the catalyst with a hydrocarbon stream containing alkanes, olefins and mixtures thereof having 2 to 12 carbon atoms per molecule and recovering the product.
1. A catalyst for conversion of hydrocarbons, comprising:
a non-acidic germanium zeolite, wherein the zeolite comprises MFI, BEA, MWW, MOR, LTL, MTT, MTW, TON, MEL, or a combination comprising one or more of the foregoing; and
platinum and a metal deposited on the germanium zeolite, wherein the metal comprises rhenium, ruthenium, rhodium, iridium, palladium, cobalt, iron, tin, or a combination comprising one or more of the foregoing.
2. The catalyst of claim 1 , wherein the metal is rhenium, ruthenium, rhodium, iridium, palladium, cobalt, and/or iron.
3. The catalyst of claim 2 , wherein the metal is rhenium, ruthenium, rhodium, iridium, and/or palladium.
4. A process for synthesizing a germanium zeolite catalyst comprising:
preparing a non-acidic germanium zeolite, wherein the zeolite comprises MFI, BEA, MWW, MOR, LTL, MTT, MTW, TON, MEL, or a combination comprising one or more of the foregoing;
depositing platinum and a metal, wherein the metal comprises rhenium, ruthenium, rhodium, iridium, palladium, cobalt, iron, tin, or a combination comprising one or more of the foregoing on the zeolite; and
calcining the zeolite.
5. The process of claim 4 , wherein the calcining occurs after preparation of the zeolite and before depositing platinum and the metal on the zeolite.
6. The process of claim 4 , wherein the calcining occurs after preparation of the zeolite and before or after depositing platinum and the metal on the zeolite.
7. The process of claim 4 , wherein the other metal is rhenium, ruthenium, rhodium, iridium, palladium, cobalt, and/or iron.
8. A process for the conversion of hydrocarbons comprising:
contacting a hydrocarbon stream containing alkanes, olefins or mixtures thereof having 2to 12 carbon atoms per molecule with a non-acidic germanium zeolite catalyst comprising platinum and a metal deposited on the germanium zeolite; and
recovering the product;
wherein the zeolite comprises MFI, BEA, MWW, MOR, LTL, MTT, MTW, TON, MEL, or a combination comprising one or more of the foregoing, and wherein the metal comprises rhenium, ruthenium, rhodium, iridium, palladium, cobalt, iron, tin, or a combination comprising one or more of the foregoing.
9. The process of claim 8 wherein the metal is rhenium, ruthenium, rhodium, iridium, palladium, cobalt, and/or iron.
10. The process of claim 8 , wherein the metal is rhenium, ruthenium, rhodium, iridium, and/or palladium.
11. The process of claim 8 , wherein alkanes or olefins are straight.
12. The catalyst of claim 1 , wherein the zeolite is MFI.
13. The catalyst of claim 1 , further comprising one or more of boron, gallium, indium, tin, titanium, zirconium, vanadium, chromium, iron, niobium and phosphorus, in the framework.
14. The catalyst of claim 1 , wherein the zeolite has no more than 0.4 wt % aluminum.
15. The catalyst of claim 1 , wherein the zeolite has an aluminum content of no more than 0.4 wt % or was made non-acidic by exchange with a base.