Polyolefin production with chromium-based catalysts
US-2017274356-A1 · Sep 28, 2017 · US
US11780786B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11780786-B2 |
| Application number | US-202117470066-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 9, 2021 |
| Priority date | Sep 14, 2020 |
| Publication date | Oct 10, 2023 |
| Grant date | Oct 10, 2023 |
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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.
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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.
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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