Light treatment of chromium catalysts and related catalyst preparation systems and polymerization processes

Patent metadata

Field	Value
Publication number	US-11338278-B2
Application number	US-202117468820-A
Country	US
Kind code	B2
Filing date	Sep 8, 2021
Priority date	Sep 17, 2018
Publication date	May 24, 2022
Grant date	May 24, 2022

Abstract

Catalyst preparation systems and methods for preparing reduced chromium catalysts are disclosed, and can comprise irradiating a supported chromium catalyst containing hexavalent chromium with a light beam having a wavelength within the UV-visible light spectrum. Such reduced chromium catalysts have improved catalytic activity compared to chromium catalysts reduced by other means. The use of the reduced chromium catalyst in polymerization reactor systems and olefin polymerization processes also is disclosed, resulting in polymers with a higher melt index.

First claim

What is claimed is:

1. A method for reducing a chromium catalyst for olefin polymerization, the method comprising:
irradiating a reductant comprising a C—H bond and a supported chromium catalyst comprising chromium in a hexavalent oxidation state with a light beam having a flux of at least 5,000 lux at a wavelength in the UV-visible spectrum to reduce at least a portion of the supported chromium catalyst to form a reduced chromium catalyst.

2. The method of claim 1 , wherein:
the reductant comprises ethylene, 1-butene, 1-hexene, 1-octene, methane, ethane, propane, isobutane, n-pentane, isopentane, n-hexane, tetrafluoroethane, cyclohexane, adamantane, decalin, benzene, toluene, or any combination thereof; and
the supported chromium catalyst comprises a solid oxide selected from silica, alumina, silica-alumina, silica-coated alumina, aluminum phosphate, aluminophosphate, heteropolytungstate, titania, zirconia, magnesia, boria, zinc oxide, silica-titania, silica-zirconia, alumina-titania, alumina-zirconia, zinc-aluminate, alumina-boria, silica-boria, aluminophosphate-silica, titania-zirconia, or any combination thereof.

3. The method of claim 1 , wherein the supported chromium catalyst comprises chromium/silica, chromium/silica-titania, chromium/silica-titania-magnesia, chromium/silica-alumina, chromium/silica-coated alumina, chromium/aluminophosphate, or any combination thereof.

4. The method of claim 1 , wherein the supported chromium catalyst has:
a total pore volume in a range from about 0.9 to about 3 mL/g;
a BET surface area in a range from about 200 to about 700 m 2 /g; and
an average particle size in a range from about 25 to 250 μm.

5. The method of claim 1 , further comprising a step of calcining to form the supported chromium catalyst comprising chromium in the hexavalent oxidation state.

6. The method of claim 1 , wherein:
the reductant comprises an alkane or aromatic hydrocarbon compound with up to 36 carbon atoms; and
the wavelength comprises a single wavelength or a range of wavelengths in a range from about 300 nm to about 500 nm.

7. The method of claim 1 , wherein:
the reductant comprises a compound with a C—C bond and a C—H bond; and
the wavelength comprises a single wavelength or a range of wavelengths below about 500 nm.

8. The method of claim 1 , wherein:
the light beam comprises wavelengths above 350 nm and below 500 nm.

9. The method of claim 1 , wherein:
less than or equal to about 50 wt % of the chromium in the reduced chromium catalyst is in the hexavalent oxidation state; and
the chromium in the reduced chromium catalyst has an average valence of less than or equal to about 5.

10. The method of claim 1 , wherein:
the reduced chromium catalyst has a catalyst activity at least 10% greater than that of the supported chromium catalyst, under slurry polymerization conditions at a temperature of 105° C. and a pressure of 550 psig; and/or
the reduced chromium catalyst has a catalyst activity at least 10% greater than an otherwise identical catalyst prepared using the reductant at 400° C. without light irradiation, under slurry polymerization conditions at a temperature of 105° C. and a pressure of 550 psig.

11. An olefin polymerization process comprising:
(I) irradiating a reductant comprising a C—H bond and a supported chromium catalyst comprising chromium in a hexavalent oxidation state with a light beam having a flux of at least 5,000 lux at a single wavelength or a range of wavelengths in a range from about 300 nm to about 500 nm to convert at least a portion of the supported chromium catalyst to form a reduced chromium catalyst; and
(II) contacting the reduced chromium catalyst and an optional co-catalyst with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization reaction conditions to produce an olefin polymer.

12. The process of claim 11 , wherein:
the reductant comprises a hydrocarbon compound with up to 36 carbon atoms; and
the polymerization reactor system comprises a loop slurry reactor, a fluidized bed reactor, a solution reactor, or a combination thereof.

13. The process of claim 12 , wherein the light beam is from a blue light source or a UV light source.

14. The process of claim 12 , wherein the reductant and the supported chromium catalyst are irradiated with a light beam having a flux of from about 50,000 to about 500,000 lux.

15. The process of claim 11 , wherein:
the reductant comprises a compound with a C—C bond; and
a molar ratio of the reductant to chromium in the hexavalent oxidation state is at least about 1:1.

16. The process of claim 11 , wherein:
the olefin polymer comprises an ethylene homopolymer, an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, an ethylene/1-octene copolymer, a propylene homopolymer, a propylene-based copolymer, or a combination thereof;
the HLMI of the olefin polymer produced by the process is greater than 80% of that of (i) an olefin polymer obtained using the supported chromium catalyst instead of the reduced chromium catalyst, and/or (ii) an olefin polymer obtained using an otherwise identical reduced chromium catalyst prepared using the reductant at 400° C. without light irradiation, under the same polymerization conditions.

17. A catalyst preparation system comprising:
(a) a catalyst preparation vessel configured to irradiate a slurry of a supported chromium catalyst in a diluent with a light beam at a wavelength in the UV-visible spectrum;
(b) a catalyst inlet configured to introduce the slurry of the supported chromium catalyst into the catalyst preparation vessel, wherein at least a portion of the chromium is in the hexavalent oxidation state;
(c) a reduced catalyst outlet configured to withdraw a slurry of a reduced chromium catalyst from the catalyst preparation vessel; and
(d) a controller that controls a residence time of the slurry of the supported chromium catalyst in the catalyst preparation vessel, a temperature of the catalyst preparation vessel, an intensity of the light beam, the wavelength of the light beam, an amount of the reduced chromium catalyst, a molar ratio of a reductant to chromium of the supported chromium catalyst, or any combination thereof.

18. The catalyst preparation system of claim 17 , wherein:
a source of the light beam is sunlight, a fluorescent white light, a UV lamp, a LED diode, or any combination thereof;
the wavelength comprises a single wavelength or a range of wavelengths below 600 nm;
the diluent comprises a hydrocarbon;
the system further comprises a lamp assembly inside or outside the catalyst preparation vessel; and
the catalyst preparation system further comprises a co-catalyst inlet configured to introduce a co-catalyst feed stream into the catalyst preparation vessel.

19. A polymerization reactor system comprising:
the catalyst preparation system of claim 17 ; and
a reactor configured to contact the reduced chromium catalyst with an olefin monomer and an optional olefin comonomer under polymerization reaction conditions to produce an olefin polymer, wherein the reactor is a loop slurry reactor, a fluidized bed reactor, or a combination thereof.

20. The polymerization reactor system of claim 19 , wherein the polymerization reactor system comprises a single reactor.

21. The polymerization reactor system of claim 19 , wherein the polymerization reactor system comprises two or more reactors.

22. The polymerization reactor system of claim 19 , w

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Clear Kathy S
• Mcdaniel Max P
• Ellis William C
• Schwerdtfeger Eric D
• Gagan Deloris R
• Cruz Carlos A
• Monwar Masud M

Classifications

• C08F4/025

  Metal oxides · CPC title

• B01J8/085

  Feeding reactive fluids (for solid material, see B01J8/0015) · CPC title

• B01J31/34

  of chromium, molybdenum or tungsten · CPC title

• C08F110/02

  Ethene · CPC title

• B01J19/123

  Ultraviolet light · CPC title