Catalytic hydrocarbon dehydrogenation
US-2021069677-A1 · Mar 11, 2021 · US
US11097257B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11097257-B2 |
| Application number | US-201916566801-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 10, 2019 |
| Priority date | Sep 10, 2019 |
| Publication date | Aug 24, 2021 |
| Grant date | Aug 24, 2021 |
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A catalyst for dehydrogenation of hydrocarbons includes a support including zirconium oxide and Linde type L zeolite (L-zeolite). A concentration of the zirconium oxide in the catalyst is in a range of from 0.1 weight percent (wt. %) to 20 wt. %. The catalyst includes from 5 wt. % to 15 wt. % of an alkali metal or alkaline earth metal. The catalyst includes from 0.1 wt. % to 10 wt. % of tin. The catalyst includes from 0.1 wt. % to 8 wt. % of a platinum group metal. The alkali metal or alkaline earth metal, tin, and platinum group metal are disposed on the support.
Opening claim text (preview).
What is claimed is: 1. A method of dehydrogenating hydrocarbons, the method comprising: forming a catalyst comprising: a support comprising zirconium oxide and L-zeolite, wherein a concentration of the zirconium oxide in the catalyst is in a range of from 0.1 weight percent (wt. %) to 20 wt. %; from 5 wt. % to 15 wt. % of an alkali metal or alkaline earth metal in the catalyst, the alkali metal or alkaline earth metal disposed on the support; from 0.1 wt. % to 10 wt. % of tin in the catalyst, the tin disposed on the support; and from 0.1 wt. % to 8 wt. % of a platinum group metal in the catalyst, the platinum group metal disposed on the support; applying pressure to the catalyst to form catalyst grains of about 200 micrometers (μm) to about 500 μm in size; disposing the catalyst grains in a reactor; subjecting hydrocarbons to be dehydrogenated to an operating temperature in a range of from about 500 degrees Celsius (° C.) to about 800° C. within the reactor, wherein the hydrocarbons to be dehydrogenated comprise n-pentane; subjecting the hydrocarbons to be dehydrogenated to an operating pressure in a range of from about 0.01 bar to about 10 bar within the reactor; and while subjecting the hydrocarbons to be dehydrogenated to the operating temperature and operating pressure within the reactor, introducing a diluent gas to the hydrocarbons to be dehydrogenated, the diluent gas comprising hydrogen and inert gas. 2. The method of claim 1 , wherein the alkali metal or alkaline earth metal is selected from the group consisting of lithium, sodium, potassium, rubidium, cesium, beryllium, magnesium, calcium, and barium. 3. The method of claim 2 , wherein the alkali metal is potassium or cesium. 4. The method of claim 2 , wherein a volume ratio of hydrogen to inert gas in the diluent gas is in a range of from 11:70 to 71:10. 5. The method of claim 2 , further comprising, before using the catalyst to dehydrogenate the hydrocarbons to be dehydrogenated, activating the catalyst, wherein activating the catalyst comprises: placing the catalyst grains within the reactor; flowing a stream comprising oxygen to the catalyst grains within the reactor; while flowing the stream comprising oxygen to the catalyst grains, increasing a temperature within the reactor to 450° C.; after the temperature within the reactor reaches 450° C., flowing a stream comprising an inert gas to the catalyst grains within the reactor; while flowing the stream comprising the inert gas to the catalyst grains, decreasing the temperature within the reactor to 400° C.; after the temperature within the reactor reaches 400° C., flowing a stream comprising hydrogen to the catalyst grains within the reactor; and adjusting the temperature within the reactor to the operating temperature.
Addition of matrix or binder particles · CPC title
Crystalline aluminosilicate zeolites; Isomorphous compounds thereof · CPC title
Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof · CPC title
of the type L, as exemplified by patent document US3216789 · CPC title
Zirconium or hafnium; Oxides or hydroxides thereof · CPC title
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