Catalytic hydrocarbon dehydrogenation

US11097257B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11097257-B2
Application numberUS-201916566801-A
CountryUS
Kind codeB2
Filing dateSep 10, 2019
Priority dateSep 10, 2019
Publication dateAug 24, 2021
Grant dateAug 24, 2021

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

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.

First claim

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.

Assignees

Inventors

Classifications

  • Addition of matrix or binder particles · CPC title

  • B01J29/06Primary

    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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What does patent US11097257B2 cover?
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. Th…
Who is the assignee on this patent?
Saudi Arabian Oil Co
What technology area does this patent fall under?
Primary CPC classification B01J29/06. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Aug 24 2021 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).