CA2156868A1 - Process for stabilizing polymeric material - Google Patents

Process for stabilizing polymeric material

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Publication number
CA2156868A1
CA2156868A1 CA002156868A CA2156868A CA2156868A1 CA 2156868 A1 CA2156868 A1 CA 2156868A1 CA 002156868 A CA002156868 A CA 002156868A CA 2156868 A CA2156868 A CA 2156868A CA 2156868 A1 CA2156868 A1 CA 2156868A1
Authority
CA
Canada
Prior art keywords
phosphite
carrier solution
butyl
styrene
weight
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
CA002156868A
Other languages
French (fr)
Inventor
James A. Mahood
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
General Electric Co
Original Assignee
General Electric Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US08/307,545 external-priority patent/US5424348A/en
Application filed by General Electric Co filed Critical General Electric Co
Publication of CA2156868A1 publication Critical patent/CA2156868A1/en
Abandoned legal-status Critical Current

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Classifications

    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/04—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins
    • D01F6/06—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins from polypropylene
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic System
    • C07F9/02—Phosphorus compounds
    • C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
    • C07F9/6564—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms
    • C07F9/6571—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms having phosphorus and oxygen atoms as the only ring hetero atoms
    • C07F9/6574—Esters of oxyacids of phosphorus
    • C07F9/65742—Esters of oxyacids of phosphorus non-condensed with carbocyclic rings or heterocyclic rings or ring systems
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/16—Making expandable particles
    • C08J9/18—Making expandable particles by impregnating polymer particles with the blowing agent
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/49—Phosphorus-containing compounds
    • C08K5/51—Phosphorus bound to oxygen
    • C08K5/52—Phosphorus bound to oxygen only
    • C08K5/527—Cyclic esters
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00—General methods for the manufacture of artificial filaments or the like
    • D01F1/02—Addition of substances to the spinning solution or to the melt
    • D01F1/10—Other agents for modifying properties
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/04—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment

Abstract

A polymerization process is provided involving a carrier solution containing an organic solvent and a phosphite. The phosphite is highly soluble in the solvent and allows for an incorporation of a minimum of solvent in the carrier solution. The phosphite is of the formula:

Description

PROCESS FOR STABILIZING POLYMERIC MATERIAL

BA~O~Nv OF THE l~V~. ~ lON
Fleld of the Inventlon The present invention relates to solvent utilizing polymerization processes, and more particularly relates to solvent based delivery systems for phosphites.
DESCRIPTION OF RELATED ART
Solvent utilizing polymerization processes are generally known. Such processes are useful for manufacturing polymers such as homopolymers, block copolymers and graft copolymers, and include processes commonly referred to as bulk, mass, suspension and emulsion processes. Some of the processes attempt to incorporate antioxidants such as phosphites into the polymer material by introducing a solvent containing the antioxidant into the reaction process. These solvents generally need to be removed at some point in the process, and consequently there is at times a desire to m;n;m;ze the amount of solvent in the process. Many phosphites, however, do not exhibit high levels of solubility in various organic solvents, for example, aliphatic or aromatic liquid (25C) hydrocarbons, for further example, cyclohexane.
Accordingly, there is a desire to provide a phosphite which exhibits high levels of solubility in organic solvents, and to provide a solvent deliverY
system for the phosphite which m;nimizes the amount of solvent required.

SUMMARY OF THE lNVk~ ~lON
The present invention involves a polymerization process involving the delivery of a phosphite into the process via a solvent carrier, and further S involves a solvent carrier solution containing a phosphite wherein the phosphite is of the formula:

C(CH3)3 H3C-CH2-CH2-CH2 ~ ~CH2-O \ ~ y2 CH3-CH2/ CH2-O yl wherein yl is an alkyl and y2 iS selected from tert-butyl and sec-butyl. The solvent is an organic solvent.
DETAILED DESCRIPTION OF T~E l~V' .. lON
A process is provided for making polymeric materials. One embodiment of the process involves introducing a carrier solution into a reaction mass.
The carrier solution contains an organic solvent and a phosphite that exhibits a high degree of solubility in the organic solvent.
The process is useful for making polymeric materials cont~; nl ng (desired from) diene compounds.
The diene rubber polymers which can be used in the present invention are characterized by the following types (a) and (b): (a) ABA-type or ABA'-type copolymer (or their combination); (b) AB type di block copolymer.
In the aforementioned types, A and A' are blocks derived from comonomers consisting of unsaturated alkenyl aromatic compounds (e.g., styrene, a-methylstyrene, vinyltoluene, vinylxylene, vinylnaphthalene, etc.) or their mixtures, B is a block derived from comonomers consisting of diene compounds (e.g., butadiene, chlorobutadiene, isoprene, l,3-pentadiene, 2,3-dimethylbutadiene, etc.) or their mixtures.
The ABA-type or ABA'-type copolymer may be a so-called "tapered" block copolymer, in which threeblocks are directly connected to each other or via a "random copolymer" consisting of an alkenyl aromatic compound and a diene compound constituting each block, or a radial teleblock copolymer consisting of an alkenyl aromatic compound and a diene compound.
The AB type di block copolymer is a "tapered" block copolymer in which two blocks are directly connected to one each other or via a "random copolymer"
consisting of an alkenyl aromatic compound and a diene compound constituting each block.
Examples of especially desirable rubber polymers correspo~ing to the aforementioned type (a) include a styrene-ethylene-butadiene-styrene blockcopolymer, styrene-butadiene-styrene block copolymer, styrene-isoprene-styrene block copolymer, etc. Examples of especially rubber polymers corresponding to the aforementioned type (b) include a stYrene-ethYlene-propylene block copolymer, styrene-butadiene block copolymer, etc.
The aforementioned rubber polymers may be totally hydrogenated, partially hydrogenated, or acid-modified using maleic anhydride, etc. In particular, hydrogenated polymers are especially desirable in consideration of the thermal ageing resistance.
It is desirable that the quantity of rubber polymer content be 1-80 parts by weight (with respect to lO0 parts by weight) of the resin composition of the present invention. Then, it is desirable that 21568~8 the relative quantities of components (a) and (b) be 3-97 wt % and 97-3-wt %, respectively.
If necessary, furthermore, other rubbers (e.g., ethylene-propylene rubber, etc.) may be used in combination with the aforementioned rubber polymers of components (a) and (b).
The process is also useful for making graft copolymer having a diene rubber component. Rubber modified monovinylidene aromatic resins comprising (a) a rubber modified monovinylidene aromatic graft copolymer and (b) an ungrafted rigid copolymer, are generally prepared by graft polymerization of a mixture of a monovinylidene aromatic monomer and one or more comonomers in the presence of one or more rubbery polymeric substrates. Depen~ing on the amount of rubber present, a separate matrix or continuous rigid phase of ungrafted rigid (co)polymer may be simultaneously obtained along with the rubber modified monovinylidene aromatic graft polymer. The resins may also be produced by blending a rigid monovinylidene aromatic copolymer with one or more rubber modified monovinylidene aromatic graft copolymers. Typically, the rubber modified resins comprise the rubber modified graft copolymer at a level of from 5 to lO0 percent by weight based on the total weight of the resin, more preferably from lO to 95 percent by weight thereof, more-preferably 20 to 90 percent by weight thereof, and most preferably from l5 to 85 percent by weight thereof; and the rubber modified resin comprises the ungrafted rigid polymer at a level of from 0 to 95 percent by weight based on the total weight of the resin, more preferably from 5 to 90 percent by weight thereof, more preferably from lO to 80 percent by weight 2156~68 thereof and most preferably from 15 to 85 percent by weight thereof.
Monovinylidene aromatic monomers which may be employed include styrene, alpha-methyl styrene, halostyrenes i.e. dibromostyrene, mono or di alkyl, alkoxy or hydroxy substitute groups on the nuclear ring of the monovinylidene aromatic monomer i.e.
vinyl toluene, vinylxylene, butylstyrene, para-hydroxystyrene or methoxystyrene or mixtures thereof.
The monovinylidenearomatic monomers utilized are generically described by the following formula:

X R H

X - C C

X \ X H

wherein X is selected from the group consisting of hydrogen, alkyl groups of 1 to 5 carbon atoms, cycloalkyl, aryl, alkaryl, aralkyl, alkoxy, aryloxy, lS and halogens. R is selected from the group consisting of hydrogen, alkyl groups of 1 to 5 carbon atoms and halogens such as bromine and chlorine.
Examples of substituted vinylaromatic compounds include styrene, 4-methylstyrene, 3,5-diethylstyrene, 4-n-propylstyrene, a-methylstyrene, a-methyl vinyltoluene, a-chlorostyrene, a-bromostyrene, dichlorostyrene, dibromostyrene, tetrachlorostyrene, mixtures thereof and the like. The preferred `_ 215S8~8 monovinylidene aromatic monomers used are styrene and/or a-methylstyrene.
Comonomers which may be used with the monovinylidene aromatic monomer includes acrylonitrile, methacrylonitrile, Cl to C8 alkyl or aryl substituted acrylate, C~ to C8 alkyl, aryl or haloaryl substituted methacrylate, acrylic acid, methacrylic acid, itaconic acid, acrylamide, N-substituted acrylamide or methacrylamide, maleic anhydride, maleimide, N-alkyl, aryl or haloaryl substituted maleimide, glycidyl (meth)acrylates, hydroxy alkyl (meth)acrylates or mixtures thereof.
The acrylonitrile, substituted acrylonitrile, or acrylic acid esters are described generically by the following formula:

H R

C = C - Y

wherein Rlmay be selected from the same group set out for R as previously defined and Y is selected from the group consisting of cyano and carbalkoxy groups wherein the alkoxy group of the carbalkoxy contains from one or about twelve carbon atoms. Examples of such monomers include acrylonitrile, ethacrylonitrile, methacrylonitrile, a-chloroacrylonitrile, a-bromoacrylonitrile, methyl acrylate, methyl methacrylate, ethyl acrylate, butyl acrylate, propylacrylate, isopropyl acrylate and mixtures thereof. The preferred monomer is acrylonitrile and the preferred acrylic acid esters are ethyl acrylate and methyl methacrylate. It lS

215 6 8 ~ 8 08SC12217/08SC12197 also preferred that the acrylic acid esters, when included, are employed in combination with styrene or acrylonitrile.
The rubber modified graft copolymer comprises (i) the rubber substrate, and (ii) a rigid polymeric superstrate portion grafted to the rubber substrate.
The rubber substrate is preferably present in the graft copolymer at a level of from 5 to 85 percent by weight based on the total weight of the graft copolymer, more preferably from 10 to 80 percent by weight thereof, and most preferably 20 to 70 percent by weight thereof; and the rigid superstrate is preferably present at a level of from 15 to 95 percent by weight based on the total weight of the graft copolymer, more preferably from 20 to 90 percent by weight thereof, and most preferably from 30 to 80 percent by weight thereof.
For high rubber graft emulsion resins, the rubber level will range from 50 to 85% by weight based on the total weight of the rubber modified resin. For mass polymerization, the rubber level ranges from 4 to 40% by weight based on the total weight of the rubber modified resin. For blends of an ungrafted rigid copolymer (such as styrene-acrylonitrile copolymer) with an emulsion high rubbergraft (HRG) copolymer (such as acrylonitrile-butadiene-styrene graft copolymers), the rubber loading will typically range from 10 to 40% rubber based on the total weight of the rubber modified resin.
Examples of rubbery polymers for the substrate include: conjugated dienes, copolymers of a diene with styrene, acrylonitrile, methacrylonitrile or C
to C8 alkyl acrylate which contain at least 50%
(preferably at least 65% by weight) conjugated 21568~8 ~ 08SC12217/08SC12197 dienes, polyisoprene or mixtures thereof; olefin rubbers i.e. ethylene propylene copolymer (EPR) or ethylene propylene non-conjugated diene ~EPDM);
silicone rubbers; or Cl or C8 alkyl acrylate s homopolymers or copolymers with butadiene and/or styrene. The acrylic polymer may also contain up to 5% of one or more polyfunctional crosslinking agents such as alkylenediol di(meth)acrylates, alkylenetriol tri(meth)acrylates, polyester di(meth)acrylates, divinylbenzene, trivinylbenzene, butadiene, isoprene and optionally graftable monomers such as, triallyl cyanurate, triallyl isocyanurate, allyl (meth)acrylate, diallyl maleate, diallyl fumarate, diallyl adipate, triallyl esters of citric acid or mixtures of these agents.
The diene rubbers may preferably be polybutadiene, polyisoprene and copolymers of butadiene with up to 35% by weight of comonomers such as styrene, acrylonitrile, methylmethacrylate or C~-C6-alkylacrylate which are produced by aqueous radical emulsion polymerisation. The acrylate rubbers may be cross-linked, particulate emulsion copolymers substantially of Cl-C8-alkylacrylate, in particular C2-C6-alkylacrylate, optionally in admixture with up to 15% by weight of comonomers such as styrene, methylmethacrylate, butadiene, vinyl methyl ether or acrylonitrile and optionally up to 5% by weight of a polyfunctional crosslinking comonomer, e.g.
divinylbenzene,glycol-bis-acrylates,bisacrylamides, phosphoric acid triallylester, citric acid triallylester, allylesters of acrylic acid or - methacrylic acid, triallylcyanurate, triallylisocyanurate. Also suitable are mixtures of diene- and alkylacrylate rubbers and rubbers which have a so-called core/sheath structure, e.g. a core of diene rubber and a sheath of acrylate or vice versa.
Specific conjugated diene monomers normally utilized in preparing the rubber substrate of the graft polymer are generically described by the following formula:

X~ H H X

C = C - C = C

X~ X~

wherein X~ is selected from the group consisting of hydrogen, alkyl groups containing from one to five carbon atoms, chlorine or bromine. Examples of dienes that may be used are butadiene, isoprene, 1,3-heptadiene, methyl-1,3-pentadiene, 2,3-dimethylbutadiene, 2-ethyl-1,3-pentadiene 1,3- and 2,4-hexadienes, chloro and bromo substituted butadienes s~ch as dichlorobutadiene, bromobutadiene, dibromobutadiene, mixtures thereof, and the like. A
preferred conjugated diene is 1,3 butadiene.
The substrate polymer, as mentioned, is preferably a conjugated diene polymer such as polybutadiene, polyisoprene, or a copolymer, such as butadiene-styrene, butadiene-acrylonitrile, or the like. The rubbery polymeric substrate portion must exhibit a glass transition temperature (Tg) of less than about 0C.
Mixtures of one or more rubbery polymers previously described for preparing the monovinylidene aromatic graft polymers, or mixtures of one or more rubber modified monovinylidene aromatic graft polymers disclosed herein may also be employed.

21~6~68 Furthermore, the rubber may comprise either a block or random copolymer. The rubber particle size used in this invention as measured by simple light transmission methods or capillary hydrodynamic chromatography (CHDF) may be described as having an average particle size by weight of select one of the following: 0.05 to 1.2 microns, preferably .2 to .8 microns, for emulsion based polymerized rubber latices or 0.5 to 10 microns, preferably 0.6 to 1.5 microns, for mass polymerized rubber substrates which also have included grafted monomer occlusions. The rubber substrate is preferably a particulate, highly crosslinked diene or alkyl acrylate rubber, and preferably has a gel content greater than 70%.
Preferred graft superstrates include copolymers of styrene and acrylonitrile, copolymers of a-methylstyrene and acrylonitrile and methylmethacrylate polymers or copolymers with up to 50% by weight of C~-C6 alkylacrylates, acrylonitrile or styrene. Specific examples of monovinylidene aromatic graft copolymers include but are not limited to the following: acrylonitrile-butadiene-styrene (ABS ), acrylonitrile-styrene-butyl acrylate (ASA), methylmethacrylate-acrylonitrile-butadiene-styrene (MABS ), acrylonitrile-ethylene-propylene-non-conjugated diene-styrene (AES ) .
The ungrafted rigid polymers (typically free of rubber) are resinous, thermoplastic polymers of styrene, -methylstyrene, styrenes substituted in the nucleus such as p-methylstyrene, methyl acrylate, methylmethacrylate,acrylonitrile,methacrylonitrile, maleic acid anhydride, N-substituted maleimide, vinyl acetate or mixtures thereof. Styrene/acrylonitrile copolymers, a-methylstyrene/acrylonitrile copolymers and methylmethacrylate/acrylonitrile copolymers are preferred.
The ungrafted rigid copolymers are known and may be prepared by radical polymerisation, in particular by emulsion, suspension, solution or bulk polymerisation. They preferably have number average molecular weights of from 20,000 to 200,000 and limiting viscosity numbers [~] of from 20 to 110 ml/g (determined in dimethylformamide at 25C).
10The number average molecular weight of the grafted rigid superstrate of the monovinylidene aromatic resin is designed to be in the range of 20,000 to 350,000. The ratio of monovinylidene aromatic monomer to the second and optionally third 15monomer may range from 90/10 to 50/50 preferably 80/20 to 60/40. The third monomer may optional replace 0 to 50~ of one or both of the first and second monomers.
These rubber modified monovinylidene aromatic graft polymers may be polymerized either by mass, emulsion, suspension, solution or combined processes such as bulk-suspension, emulsion-bulk, bulk-solution or other techniques well known in the art.
Furthermore, these rubber modified monovinylidene aromatic graft copolymers may be produced either by continuous, semibatch or batch processes.
The organic solvent may be any suitable organic solvent, which preferably has a melt temperature below 25C, and suitable examples include C3 to C20 hydrocarbons, more preferably C4 to Cl0 hydrocarbons, such as benzene, tetrahydrofuran, dioxane, 1,2-dimethoxyethane and n-hexane, and most preferably is cyclohexane. Other suitable solvents include aliphatic or aromatic hydrocarbons, mineral oil, and hydrocarbon monomers such as styrene. The carrier solution is a solution of organic solvent and phosphite. The phosphite is preferably present at a level of from 1 to 50 percent by weight based on the total weight of the carrier solution, more preferably from 10 to 50 percent by weight thereof, and most preferably from 20 to 40 percent by weight thereof.
The organic solvent is preferably present in the carrier solution at a level of from 50 to 99 percent by weight based on the total weight of the carrier solution, more preferably from 50 to 90 percent by weight thereof, and most preferably from 60 to 80 percent by weight thereof.
One embodiment of the process involves feeding the carrier solution into a reaction mass. The reaction mass comprises vinyl monomers and diene monomers and/or diene derived polymers. The phosphite serves to enhAnce the oxidative stability of the polymeric materials during processing and post-processing. Another embodiment of the process involves introducing the carrier solution into the polymeric material, and then removing the solvent therefrom.
Other suitable processes for using the present invention include processes for making vinylic polymers including, for example, polystyrene, polyvinylchloride, anionic polymers, polybutadiene, polyisoprene, and polymethylmethacrylate.
Mass, bulk, mass-suspension, suspension and emulsion processes are well known in the art. The present invention involves improving the phosphite delivery system of those processes by utilizing a carrier solution that contains a phosphite which exhibits high levels of solubility in organic solvents.

`~ 21~6868 ~ 08SC12217/08SC12197 Polymeric material as used herein refers to either the final polymer product or the final polymeric product in solution or dispersion.
The phosphite preferably has a melt temperature 5 above 25C.
EXAMPLES
Table 1 Ex Phos SolubilitY %
1 Phos 1 50.1 A Phos A <10 B Phos B 15.7 C Phos C 12.4 Solubility for example 1 and comparative example A is measured as solubiiity in hexane with each percentage value being equal to grams of phos per milliliter of hexane (20% = 2 g/ml, 10% = lg~ml.
Phos A isTetrakis(2,4-di-tert-butylphenyl)4,4'-diphenylylenediphosphonite.
Phos 1 is of the formula ~X~P ~

The examples of Table 2 illustrate the in polymer solubility of the present phosphites which should facilitate phosphite dispersion in the polymer compositions.
Phos B is bis(2,4-di-t-butylphenyl) pentaerythritol diphosphite.
Phos C is tris(2,4-di-tert-butylphenyl) phosphite.
Phos D is trisnonylphenyphosphite.

2 15 6 ~ S 8 08SC12217/08SC12197 CEX D-G were comparative examples and examples 2 and 3 were examples of the present invention.
Phos 2 was of the formula ~~ ~

Values are set out as concentration in parts per million based on the total weight of the linear low density polyethylene. The greatly increasing values with time for examples 2 and 3 compared to CEX D-G
illustrates the greatly enhAnced solubility of the present phosphites.

r r~ o r ~D r u~ ~ o r-X ,C ~ o o a~
P~ o _I ~ ~ 0 ~ I C~ 0 ~n r u~ 0 ~
ou~ ~ ~ cn ~ 0 X
~ ~O ~ _~ ~1 _I

X O ~ o In U ~ O ~ I o~ ~ ~ I I r~

~q 0 L cq ~ ~7 E~ X O ~ a o r~ r o ~ ~~ ~ ~ ~ ~ o X O
.C~ _I U~ o U P~ o I I ~ ~ o~

~ tQ
X O ~ ~
p~ o I I r~ r ~, _ O ~

Claims (13)

1. A polymerization process comprising:
(a) introducing a carrier solution into a monomeric reaction mass, said carrier solution comprising a liquid organic solvent and a phosphite of the formula:

wherein Y1 is an alkyl and Y2 is selected from tert-butyl and sec-butyl, (b) polymerizing said monomeric reaction mass to produce a phosphite stabilized polymeric material.
2. The process of Claim 1 wherein said solvent is removed from said polymeric material.
3. The process of Claim 1 wherein said reaction mass comprised a diene compound.
4. The process of Claim 1 wherein said reaction mass comprises a vinyl aromatic monomer.
5. The process of Claim 1 wherein said polymeric material comprises vinyl aromatic-diene copolymers.
6. The process of Claim 5 wherein said copolymer is a styrene-butadiene-styrene block copolymer.
7. A carrier solution for introducing a phosphite into a reaction mass of a polymerization process, said carrier solution comprising:
(a) an organic solvent, and (b) a phosphite of the formula wherein Y1 is an alkyl and Y2 is selected from tert-butyl and sec-butyl.
8. The carrier solution of Claim 7 wherein said solvent is cyclohexane.
9. The carrier solution of Claim 7 wherein Y1 and Y2 are each tert-butyl.
10. The carrier solution of Claim 7 wherein said phosphite is present at a level of from 1 to 50 percent by weight based on the total weight of the composition.
11. The carrier solution of Claim 7 wherein said phosphite is present at a level of from 2 to 25 percent by weight based on the total weight of the composition.
12. The carrier solution of Claim 7 wherein said phosphite is present at a level of from 2 to 15 percent by weight based on the total weight of the composition.
13. A polymerization process comprising:
(a) polymerizing a monomeric reaction mass to produce a polymeric material;
(b) introducing a carrier solution into said polymeric material, said carrier solution comprising a liquid organic solvent and a phosphite of the formula:

wherein Y1 is an alkyl and Y2 is selected from tert-butyl and sec-butyl.
CA002156868A 1994-09-16 1995-08-24 Process for stabilizing polymeric material Abandoned CA2156868A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US08/307,545 1994-09-16
US08/307,545 US5424348A (en) 1993-07-22 1994-09-16 Neo-diol phosphites as polymer stabilizers
US08/361,786 1994-12-21
US08/361,786 US5500468A (en) 1993-07-22 1994-12-21 Process for stabilizing polymeric material

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CA002156866A Abandoned CA2156866A1 (en) 1994-09-16 1995-08-24 Liquid neo-diol phosphites as polymer stabilizers

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EP (1) EP0702053B1 (en)
JP (1) JPH08208718A (en)
AT (1) ATE174943T1 (en)
CA (2) CA2156868A1 (en)
DE (1) DE69506815T2 (en)
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US6891117B1 (en) * 2003-11-07 2005-05-10 Cooper Wiring Devices, Inc. Modular block switch assembly

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ATE174943T1 (en) 1999-01-15
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CA2156866A1 (en) 1996-03-17
DK0702053T3 (en) 1999-08-23
EP0702053B1 (en) 1998-12-23
US5500468A (en) 1996-03-19
JPH08208718A (en) 1996-08-13
ES2124966T3 (en) 1999-02-16
EP0702053A1 (en) 1996-03-20

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