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US4853426A Expired / Lapsed US ⏱️ 0.0 years remaining

In-reactor stabilization of polyolefins via coated stabilizers

Assignee: Union Carbide Chemicals and Plastics Technology LLC
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Filing: 1988-01-25
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Granted: 1989-08-01
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Expires: 2008-01-25
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Abstract

Abstract The present invention includes: (i) a method for making a coated particulate comprising the steps of heating until liquid a polyolefin wax; fluidizing with a hot gas, additive particles selected from the group comprising an antioxidant, a processing stabilizer, an acid acceptor, and mixtures thereof; spraying the liquid polyolefin wax on the heated fluidized additive particles, and maintaining the fluidized additive particles at a temperature which is sufficient to prevent the formation of fibers and adequate to form discrete substantially coated additive particles; (ii) a coated particulate made by the above process; and (iii) a process for providing in-reactor stabilization of a polyolefin during a polymerization reaction, using the coated additives prepared by the above described method.

Inventors

  • 👤 Ananda M. Chatterjee

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 16:36
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/20; C08J3/201; C08F; C08F10/00; C08J3/22; C08J3/226; C08K; C08K9/00; C08K9/08; C08J2391/00; C08J2391/06

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 264 words
A process for providing in-reactor stabilization of a polyolefin during a polymerization reaction comprising the steps of: forming a particulate adapted for use in polyolefin polymerization reactions, by the steps consisting of heating until liquid a polyolefin wax; fluidizing with a hot gas, additive particles selected from the group consisting of an antioxidant, a processing stabilizer, an acid acceptor, and mixtures thereof; spraying the liquid polyolefin wax on the heated fluidized additive particles; and maintaining the fluidized additive particles at a temperature which is sufficient to prevent the formation of fibers and adequate to form discrete substantially coated additive particles; adding said discrete substantially coated additive containing particles to a polymerization reactor and using a magnesium supported titanium halide/aluminum alkyl catalyst system wherein said system comprises (i) a procatalyst compound obtained by halogenating a magnesium compound of the formula MgR'R" wherein R' is an alkoxide or aryloxide group or halogen, and R" is an alkoxide, alkyl carbonate, aryloxide, or halogen with a halide of tetravalent titanium and electron donor, contacting the halogenated product with a tetravalent titanium halide, washing it to remove unreacted titanium and an electron donor, contacting the halogenated product with a tetravalent titanium halide, washing it in an inert solvent to remove unreacted titanium compounds and recovering the solid product; (ii) a cocatalyst component comprising an organoaluminum compound selected from the group comprising diethyl aluminum chloride, ethyl aluminum dichloride, ethyl aluminum sesquichloride and tri-ethyl aluminum; and (iii) a selectivity control agent selected from the group comprising; diphenyl dimethoxy silane, paraethoxy benzoate, ethyl paratoluate, paramethoxy ethyl benzoate, phenyl triethoxysilane and 2,2,6,6-tetramethyl piperidine.
Claim 2
Dependent Claim 264 words
A process for providing in-reactor stabilization of a polyolefin during a polymerization reaction comprising the steps of: forming a particulate adapted for use in polyolefin polymerization reactions, by the steps consisting of heating until liquid a polyolefin wax; fluidizing with a hot gas, additive particles selected from the group consisting of an antioxidant, a processing stabilizer, an acid acceptor, and mixtures thereof; spraying the liquid polyolefin wax on the heated fluidized additive particles; and maintaining the fluidized additive particles at a temperature which is sufficient to prevent the formation of fibers and adequate to form discrete substantially coated additive particles; adding said discrete substantially coated additive containing particles to a polymerization reactor and using a magnesium supported titanium halide/aluminum alkyl catalyst system wherein said system comprises (i) a procatalyst compound obtained by halogenating a magnesium compound of the formula MgR'R" wherein R' is an alkoxide or aryloxide group or halogen, and R" is an alkoxide, alkyl carbonate, aryloxide, or halogen with a halide of tetravalent titanium and electron donor, contacting the halogenated product with a tetravalent titanium halide, washing it to remove unreacted titanium and an electron donor, contacting the halogenated product with a tetravalent titanium halide, washing it in an inert solvent to remove unreacted titanium compounds and recovering the solid product; (ii) a cocatalyst component comprising an organoaluminum compound selected from the group comprising diethyl aluminum chloride, ethyl aluminum dichloride, ethyl aluminum sesquichloride and tri-ethyl aluminum; and (iii) a selectivity control agent selected from the group comprising; diphenyl dimethoxy silane, paraethoxy benzoate, ethyl paratoluate, paramethoxy ethyl benzoate, phenyl triethoxysilane and 2,2,6,6-tetramethyl piperidine.
Claim 3
Dependent Claim 21 words
The process of claim 1, wherein the olefin polymerization reaction is for the polymerization of an olefin having 2-18 carbon atoms.
Claim 4
Dependent Claim 15 words
The process of claim 1, wherein the olefin polymerization reaction is a 1-butene polymerization reaction.
Claim 5
Dependent Claim 15 words
The process of claim 1, wherein the olefin polymerization reaction is a propylene polymerization reaction.
Claim 6
Dependent Claim 44 words
The process of claim 1, wherein the additive used to form said particulate is a member of the group; 1,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl) benzene; octadecyl 3-(3',5'-di-tert-butyl-4'-hydroxphenyl)propionate; tetrakis[methylene (3,5-di-tert-butyl-4-hydroxyhydrocinnamate)]methane; tris(3,5-di-t-butyl-4-hydroxybenzyl)isocyanurate; 3,5-di-tert-butyl-4-hydroxyhydrocinnamic acid triester with 1,3,5-tris(2-hydroxyethyl)-s-triazine-2,4,6(1H,3H,5H)-trione; 1,3,5-tris(4-tert-butyl-3-hydroxy-2,6-dimethylbenzyl) 1,3,5-triazine-2,4,6-(1H,3H,5H)-trione; bis-[3,3-bis(4'hydroxy-3'tert-butyl-phenyl)-butanoic acid]-glycolester; 2,2'-methylene-bis-[(4-methyl-6-tertiary-butyl-phenyl)-terephthalate]; 2,2-bis[4-(2-(3,5-di-tert-butyl-4-hydroxyhydrocinnamoyloxy)) ethoxy-phenyl]propane; calcium bis[monoethyl(3,5-di-tert-butyl-4-hydroxybenzyl)phosphonate]; 1,2-bis(3,5-di-tert-butyl-4-hydroxyhydrocinnamoyl)hydrazine; and 2,2'-oxamidobis-[ethyl 3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate].
Claim 7
Dependent Claim 25 words
The process of claim 1, wherein the polyolefin wax coating used to form said particulate comprises a polyolefin having 2-18 carbon atoms per repeat unit.
Claim 8
Dependent Claim 30 words
The process of claim 1, wherein said fluidization of the bed of solid additive is performed using a member of the group consisting of air, inert gas, and mixtures thereof.
Claim 9
Dependent Claim 15 words
The process of claim 1, wherein said polymerization reactor is a gas phase polymerization reactor.
Claim 10
Dependent Claim 15 words
The process of claim 1, wherein said polymerization reactor is a liquid pool polymerization reactor.
Claim 11
Dependent Claim 14 words
The process of claim 1, wherein said polymerization reactor is a solvent/slurry polymerization reactor.
Claim 12
Dependent Claim 14 words
The process of claim 1, wherein said polymerization reactor is a solution polymerization reactor.

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Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-07-31 1993-01-30 1993-08-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-07-31 1997-01-30 1997-08-01 $3760.00 Window Closed / Lapsed
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