Pre-carburized molybdenum-modified zeolite catalyst and use thereof for the aromatization of lower alkanes
US-2016121314-A1 · May 5, 2016 · US
US11517884B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11517884-B2 |
| Application number | US-202016744383-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 16, 2020 |
| Priority date | Feb 4, 2019 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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A catalyst that includes heterogeneous metal carbide nanomaterials and a novel preparation method to synthesize the metal carbide nanomaterials under relatively mild conditions to form an encapsulated transition metal and/or transition metal carbide nanoclusters in a support and/or binder. The catalyst may include confined platinum carbide nanoclusters. The preparation may include the treatment of encapsulated platinum nanoclusters with ethane at elevated temperatures. The catalysts may be used for catalytic hydrocarbon conversions, which include but are not limited to, ethane aromatization, and for selective hydrogenation, with negligible green oil production.
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The invention claimed is: 1. A method for synthesizing a catalyst for catalytic hydrogenation of alkynes and alkadienes to olefins, which comprises steps of: step (1): mixing a support with an aqueous solution of a platinum precursor, to form a mixture; step (2): drying the mixture to form a dry product; step (3): calcinating the dry product obtained after the drying; step (4): reducing a dry product obtained after the calcination to form a catalyst precursor comprising multiple encapsulated platinum nanoclusters within the support; and step (5): activating the catalyst precursor obtained in step (4) in an ethane atmosphere to form the catalyst comprising a plurality of platinum carbide nanoclusters encapsulated in a plurality of micropores of the support; wherein in step (5), the catalyst obtained in step (4) is activated as follows: the catalyst precursor obtained in step (4) is purged with an inert gas, and an ethane activation occurs at temperatures between 300-750° C., for a certain period, cooled to 100° C. in ethane flow, and further cooled to room temperature in an inert atmosphere, wherein the support is an aluminosilicate zeolite and the catalyst comprises 300-25000 ppm of platinum. 2. The method according to claim 1 , further comprising after reducing the dry product obtained after the calcination, a step of cooling the catalyst precursor obtained in step (4) in a hydrogen atmosphere. 3. The method according to claim 1 , wherein the calcinating comprises an air calcination. 4. The method according to claim 3 , wherein the calcinating occurs at a temperature between 300-800° C., for a certain period. 5. The method according to claim 1 , wherein the catalyst contains between 300-500 ppm of platinum. 6. The method according to claim 1 , wherein the dry product obtained after the calcination is reduced in hydrogen between 300-800° C. for a certain period. 7. The method according to claim 1 , wherein an inert binder can be added before or after the calcinating step. 8. The method according to claim 1 , wherein the encapsulated platinum nanoclusters have a size close to 1 nm. 9. The method according to claim 1 , wherein the catalyst has a platinum dispersion greater than 90%. 10. The method according to claim 1 , wherein the catalyst comprises the encapsulated platinum carbide nanoclusters having a size close to 1 nm.
by condensation of hydrocarbons with partial elimination of hydrogen · CPC title
Reducing · CPC title
Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Reaction with organic or organometallic compounds · CPC title
of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11 · CPC title
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