Transition metal-catalyzed production of alcohol and carbonyl compounds from hydrocarbons

US11780786B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11780786-B2
Application numberUS-202117470066-A
CountryUS
Kind codeB2
Filing dateSep 9, 2021
Priority dateSep 14, 2020
Publication dateOct 10, 2023
Grant dateOct 10, 2023

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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.

Processes for converting a hydrocarbon reactant into an alcohol compound and/or a carbonyl compound are disclosed in which the hydrocarbon reactant and a supported transition metal catalyst—containing molybdenum, tungsten, or vanadium—are irradiated with a light beam at a wavelength in the UV-visible spectrum, optionally in an oxidizing atmosphere, to form a reduced transition metal catalyst, followed by hydrolyzing the reduced transition metal catalyst to form a reaction product containing the alcohol compound and/or the carbonyl compound.

First claim

Opening claim text (preview).

We claim: 1. A process for converting a hydrocarbon reactant into an alcohol compound and/or a carbonyl compound, the process comprising: (i) irradiating the hydrocarbon reactant and a supported transition metal catalyst comprising molybdenum, tungsten, vanadium, or a combination thereof, with a light beam at a wavelength in the UV-visible spectrum to reduce at least a portion of the supported transition metal catalyst to form a reduced transition metal catalyst; and (ii) hydrolyzing the reduced transition metal catalyst to form a reaction product comprising the alcohol compound and/or the carbonyl compound. 2. The process of claim 1 , wherein step (i) comprises irradiating the hydrocarbon reactant and the supported transition metal catalyst in an oxidizing atmosphere. 3. The process of claim 1 , wherein the hydrocarbon reactant comprises a C 1 to C 36 linear, branched, or cyclic alkane compound. 4. The process of claim 1 , wherein the hydrocarbon reactant comprises a C 2 to C 36 olefin compound, a C 6 to C 36 aromatic compound, or any combination thereof. 5. The process of claim 1 , wherein the supported transition metal catalyst contains from 0.01 to 50 wt. % of molybdenum, tungsten, vanadium, or a combination thereof, based on the weight of the supported transition metal catalyst. 6. The process of claim 1 , wherein: the supported transition metal catalyst comprises a solid oxide, a chemically-treated solid oxide, a zeolite, or a combination thereof; the supported transition metal catalyst has a pore volume from 0.1 to 5 mL/g and a BET surface area from 50 to 2000 m 2 /g; and the irradiating step is conducted at a temperature from −100° C. to 100° C. 7. The process of claim 1 , wherein; the light beam is from a blue light source or a UV light source; the light beam comprises wavelengths above 350 nm and below 500 nm; the hydrocarbon reactant and the supported transition metal catalyst are irradiated with an illuminance of at least 5000 lux; or any combination thereof. 8. The process of claim 1 , wherein the process comprises: contacting the hydrocarbon reactant with a fluidized bed of the supported transition metal catalyst, and irradiating while contacting; or contacting the hydrocarbon reactant with a fixed bed of the supported transition metal catalyst, and irradiating while contacting. 9. The process of claim 1 , wherein: hydrolyzing is conducted at a temperature from 0° C. to 100° C.; and hydrolyzing comprises contacting the reduced transition metal catalyst with a hydrolysis agent comprising water, steam, an alcohol agent, an acid agent, an alkaline agent, or any combination thereof. 10. The process of claim 1 , further comprising a step of separating at least a portion of the alcohol compound and/or the carbonyl compound from the reaction product after step (ii). 11. The process of claim 1 , further comprising a step of separating at least a portion of the hydrocarbon reactant from the reaction product after step (ii), and wherein the at least a portion of the hydrocarbon reactant is recycled and irradiated with the supported transition metal catalyst again. 12. The process of claim 1 , further comprising: separating at least a portion of the reduced transition metal catalyst from the reaction product after step (ii); and calcining the at least a portion of the reduced transition metal catalyst to regenerate the supported transition metal catalyst. 13. The process of claim 1 , wherein: a conversion of the hydrocarbon reactant is at least 10 wt. %; and/or a molar yield of the alcohol compound and/or the carbonyl compound is from 0.01 to 5 moles of the alcohol compound and/or the carbonyl compound per mole of transition metal in the supported transition metal catalyst. 14. The process of claim 1 , wherein the supported transition metal catalyst comprises vanadium. 15. A process for converting a hydrocarbon reactant into an alcohol compound and/or a carbonyl compound, the process comprising: (I) irradiating the hydrocarbon reactant and a supported transition metal catalyst comprising molybdenum, tungsten, vanadium, or a combination thereof, with a light beam at a wavelength in the UV-visible spectrum to reduce at least a portion of the supported transition metal catalyst to form a reduced transition metal catalyst; (II) subjecting the reduced transition metal catalyst to an oxidizing atmosphere; and (III) hydrolyzing the reduced transition metal catalyst to form a reaction product comprising the alcohol compound and/or the carbonyl compound. 16. The process of claim 15 , wherein; the light beam is from a blue light source or a UV light source; the light beam comprises wavelengths above 350 nm and below 500 nm; the hydrocarbon reactant and the supported transition metal catalyst are irradiated with an illuminance of at least 5000 lux; or any combination thereof. 17. The process of claim 15 , wherein: a conversion of the hydrocarbon reactant is at least 10 wt. %; and/or a molar yield of the alcohol compound and/or the carbonyl compound is from 0.01 to 5 moles of the alcohol compound and/or the carbonyl compound per mole of transition metal in the supported transition metal catalyst.

Assignees

Inventors

Classifications

  • Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves {; Ionic sputtering; Flame or plasma spraying; Particle radiation} · CPC title

  • Reducing · CPC title

  • by oxidation (C07C51/145 takes precedence) · CPC title

  • by oxidation (with ozone C07C45/40) · CPC title

  • by oxidation reactions with formation of hydroxy groups · CPC title

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What does patent US11780786B2 cover?
Processes for converting a hydrocarbon reactant into an alcohol compound and/or a carbonyl compound are disclosed in which the hydrocarbon reactant and a supported transition metal catalyst—containing molybdenum, tungsten, or vanadium—are irradiated with a light beam at a wavelength in the UV-visible spectrum, optionally in an oxidizing atmosphere, to form a reduced transition metal catalyst, f…
Who is the assignee on this patent?
Chevron Phillips Chemical Co Lp
What technology area does this patent fall under?
Primary CPC classification B01J23/22. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Oct 10 2023 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 12 related publications on this page (citations in our corpus or others sharing the same primary CPC).