Methods of preparing a catalyst

Patent metadata

Field	Value
Publication number	US-9587048-B2
Application number	US-201514699533-A
Country	US
Kind code	B2
Filing date	Apr 29, 2015
Priority date	Apr 29, 2015
Publication date	Mar 7, 2017
Grant date	Mar 7, 2017

Abstract

A method comprising a) calcining a silica support at temperature in the range of from about 100° C. to about 500° C. to form a precalcined silica support; b) contacting the precalcined silica support with a titanium alkoxide to form a titanated support; c) subsequent to b), contacting the titanated support with a polyol to form a polyol associated titanated support (PATS); d) contacting at least one of the silica support, pre-calcined silica support, the titanated support, the PATS, or combinations thereof with a chromium-containing compound to form a polymerization catalyst precursor; e) drying the polymerization catalyst precursor to form a dried polymerization catalyst precursor; and f) calcining the dried polymerization catalyst precursor to produce a polymerization catalyst, wherein less than about 0.1 wt. % of a highly reactive volatile organic compound (HRVOC) is emitted during the calcining of the dried polymerization catalyst precursor.

First claim

What is claimed is:

1. A method comprising:
a) calcining a silica support at temperature in the range of from about 100° C. to about 500° C. to form a precalcined silica support;
b) contacting the precalcined silica support with a titanium alkoxide to form a titanated support;
c) subsequent to b), contacting the titanated support with a polyol to form a polyol associated titanated support (PATS);
d) contacting at least one of the silica support, pre-calcined silica support, the titanated support, the PATS, or combinations thereof with a chromium-containing compound to form a polymerization catalyst precursor;
e) drying the polymerization catalyst precursor to form a dried polymerization catalyst precursor; and
f) calcining the dried polymerization catalyst precursor to produce a polymerization catalyst, wherein less than about 0.1 wt. % of a highly reactive volatile organic compound (HRVOC) is emitted during the calcining of the dried polymerization catalyst precursor.

2. The method of claim 1 wherein the polyol comprises ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, tripropylene glycol, polyethylene glycols with a molecular weight of from 106 to 1000, 1,2-propanediol, 1,3-propanediol, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, neopentyl glycol, 1,2-hexanediol, 1,6-hexanediol, 1,2-cyclohexanediol, 1,4-cyclohexanediol, 1,2-octanediol, 1,8-octanediol, 1,2-decanediol, 1,10-decanediol, glycerol, 2,2-dimethylolpropane, trimethylolethane, trimethylolpropane, pentaerythritol, dipentaerythritol, sorbitol, 1,2,4-butanediol, 2,2,4-trimethyl-1,3-pentanediol, 1-phenyl-1,2-ethanediol, 1,2-benzenediol (pyrocatechol), 1,3-benzenediol (resorcinol), 1,4-benzenediol, methyl catechol, methyl resorcinol, 1,2,4-benzenetriol, 2-hydroxybenzylalcohol, 3-hydroxybenzylalcohol, 4-hydroxybenzylalcohol, 3,5-dihydroxybenzylalcohol, 1,2-benzenedimethanol, 1,3-benzenedimethanol, 1,4-benzenedimethanol, 2-(2-hydroxyphenyl)ethanol, 2-(3-hydroxyphenyl)ethanol, 2-(4-hydroxyphenyl)ethanol, 2-phenyl-1,2-propanediol, bisphenol A (2,2-di(4-hydroxyphenyl)propane), bisphenol F (bis(4-hydroxyphenyl)methane), bisphenol S (4,4′-dihydroxydiphenylsulfone), bisphenol Z (4,4′-cyclohexylidenebisphenol), bis(2-hydroxyphenyl)methane, or combinations thereof.

3. The method of claim 1 wherein the polyol is present in an amount of from about 0.1 to about 10 molar equivalents per mole of titanium.

4. The method of claim 1 wherein the HRVOC is an alkene compound.

5. The method of claim 4 wherein the alkene compound is propylene.

6. The method of claim 1 wherein an emission of the HRVOC is reduced by from about 50% to about 100% when compared to the emission of the HRVOC from a polymerization catalyst prepared by an otherwise similar process in the absence of the polyol.

7. The method of claim 1 wherein the titanium alkoxide is a titanium tetra-alkoxide.

8. The method of claim 1 wherein the titanium alkoxide comprises titanium isopropoxide.

9. The method of claim 1 wherein the titanium alkoxide is present in an amount of from about 0.1 wt. % to about 10 wt. %.

10. The method of claim 1 wherein the chromium-containing compound is added to the silica support.

11. A method comprising contacting the polymerization catalyst produced by the method of claim 1 with (i) an olefin monomer and (ii) an optional comonomer in a reaction zone under conditions suitable to produce a polymer; and
recovering the polymer.

12. The method of claim 11 wherein the olefin monomer comprises ethylene and the polymer comprises polyethylene.

13. The method of claim 11 wherein the reaction zone is a loop reactor.

14. A method comprising:
a) calcining a silica support at temperature in the range of from about 100° C. to about 500° C. to form a precalcined silica support;
b) contacting the precalcined silica support with a titanium alkoxide to form a titanated support;
c) subsequent to b), contacting the titanated support with a polyol to form a polyol associated titanated support (PATS);
d) contacting the PATS with a chromium-containing compound to form a polymerization catalyst precursor;
e) drying the polymerization catalyst precursor to form a dried polymerization catalyst precursor; and
f) calcining the dried polymerization catalyst precursor to produce a polymerization catalyst, wherein less than about 0.1 wt. % of a highly reactive volatile organic compound (HRVOC) is emitted during the calcining of the dried polymerization catalyst precursor.

15. The method of claim 14 wherein the polyol comprises ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, tripropylene glycol, polyethylene glycols with a molecular weight of from 106 to 1000, 1,2-propanediol, 1,3-propanediol, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, neopentyl glycol, 1,2-hexanediol, 1,6-hexanediol, 1,2-cyclohexanediol, 1,4-cyclohexanediol, 1,2-octanediol, 1,8-octanediol, 1,2-decanediol, 1,10-decanediol, glycerol, 2,2-dimethylolpropane, trimethylolethane, trimethylolpropane, pentaerythritol, dipentaerythritol, sorbitol, 1,2,4-butanediol, 2,2,4-trimethyl-1,3-pentanediol, 1-phenyl-1,2-ethanediol, 1,2-benzenediol (pyrocatechol), 1,3-benzenediol (resorcinol), 1,4-benzenediol, methyl catechol, methyl resorcinol, 1,2,4-benzenetriol, 2-hydroxybenzylalcohol, 3-hydroxybenzylalcohol, 4-hydroxybenzylalcohol, 3,5-dihydroxybenzylalcohol, 1,2-benzenedimethanol, 1,3-benzenedimethanol, 1,4-benzenedimethanol, 2-(2-hydroxyphenyl)ethanol, 2-(3-hydroxyphenyl)ethanol, 2-(4-hydroxyphenyl)ethanol, 2-phenyl-1,2-propanediol, bisphenol A (2,2-di(4-hydroxyphenyl)propane), bisphenol F (bis(4-hydroxyphenyl)methane), bisphenol S (4,4′-dihydroxydiphenylsulfone), bisphenol Z (4,4′-cyclohexylidenebisphenol), bis(2-hydroxyphenyl)methane, or combinations thereof.

16. The method of claim 14 wherein the polyol is present in an amount of from about 0.1 to about 10 molar equivalents per mole of titanium.

17. The method of claim 14 wherein the HRVOC is hydrocarbons, aromatic compounds, alcohols, ketones, or combinations thereof.

18. The method of claim 17 wherein HRVOC is propylene.

19. The method of claim 14 wherein an emission of the HRVOC is reduced by from about 50% to about 100% when compared to the emission of the HRVOC from a polymerization catalyst prepared by an otherwise similar process in the absence of the polyol.

20. The method of claim 18 wherein propylene emissions range from about 50 wt. % to about less than 1 wt. % based on the weight percent titanium.

21. The method of claim 8 wherein the titanium isopropoxide is present in an amount of from about 0.1 wt. % to about 10 wt. %.

22. A method comprising:
a) calcining a silica support at temperature in the range of from about 100° C. to about 500° C. to form a precalcined silica support;
b) contacting the precalcined silica support with a chromium-containing compound to form a Cr/silica support;
c) contacting the Cr/silica support with a titanium alkoxide to form a titanated support;
d) subsequent to c), contacting the titanated support with a polyol to form a polymerization catalyst precursor;
e) drying the polymerization catalyst precursor to form a dried polymerization catalyst precursor; and
f) calcining the dried polymerization catalyst precursor to produce a polymerization catalyst, wherein less than about 0.1 wt. % of a highly reactive volatile organic compound (HRVOC) is emitted during the calcining of the dried polymerization catalyst p

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Praetorius Jeremy M
• Schwerdtfeger Eric D
• Mcdaniel Max P
• Cymbaluk Ted H
• Boxell Connor D
• Collins Kathy S
• Solenberger Alan L

Classifications

• C08F10/02 Primary

  Ethene · CPC title

• C08F4/24

  Oxides · CPC title

• B01J37/08

  Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• B01J31/38

  of titanium, zirconium or hafnium · CPC title

• C08F4/02

  Carriers therefor · CPC title