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WO1993020117A1 - Copolymeres d'olefines et d'olefines aromatiques et d'olefines et de composes aromatiques polymeres - Google Patents

Copolymeres d'olefines et d'olefines aromatiques et d'olefines et de composes aromatiques polymeres Download PDF

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Publication number
WO1993020117A1
WO1993020117A1 PCT/US1993/003200 US9303200W WO9320117A1 WO 1993020117 A1 WO1993020117 A1 WO 1993020117A1 US 9303200 W US9303200 W US 9303200W WO 9320117 A1 WO9320117 A1 WO 9320117A1
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Prior art keywords
copolymer
monomer
alkyl
vinyl
formula
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PCT/US1993/003200
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English (en)
Inventor
Anthony Jay Dias
Sudhin Datta
Joseph Alexander Olkusz
Fred Thomas Morrar
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Exxon Chemical Patents Inc.
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Application filed by Exxon Chemical Patents Inc. filed Critical Exxon Chemical Patents Inc.
Priority to EP93912128A priority Critical patent/EP0635032A1/fr
Priority to JP5517760A priority patent/JPH07505661A/ja
Priority to CA002132305A priority patent/CA2132305A1/fr
Publication of WO1993020117A1 publication Critical patent/WO1993020117A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond

Definitions

  • Amorphous graft copolymers based, for example, on a polyisobutylene or ethylene/propylene backbone chain exhibit elastomeric properties are also useful for similar applications.
  • these copolymers cannot be readily vulcanized or co- vulcanized with other elastomers due to the lack of unsaturation in the polymeric backbone.
  • Another technique for rendering "essentially saturated" elastomeric polymers amenable to vulcanization and other reactions involves the inclusion of functional substituent groups, such as halogen, in the polymer chain.
  • One such technique is disclosed in U.S. Patent No. 4,074,035, which discloses the polymerization of isobutylene with a halomethylstyrene using a Lewis Acid-type catalyst system.
  • European Patent No. 240,638 teaches a block copolymer useful for sheeting caulks, sealants, gaskets and lubricating oil additives comprising ethylene, and ⁇ -olefin, and an olefinic halide with the formula RR'X where R is a Ziegler copolymerizable olefin R' is a 10 to 20 carbon atom hydrocarbyl and X is halogen.
  • Ethylene-propylene-5-[p-(chloromethyl)phenyl]- 2-norbornene block and graft copolymers are disclosed.
  • the block copolymer is prepared by first polymerizing ethylene with propylene in hexane using VCl4-VCl4Et2Al2Cl2 Et 2 Al 2 Cl 2 catalyst at 0-200 # psi (obtaining 49% conversion) and then adding 5-[(p- chloromethyl)phenyl]-2-norbornene to give the block copolymer with a polydispersity of 1.7.
  • R and Ri are selected from the group consisting of hydrogen and C1-C4 alkyl
  • R2 is a Ci to Ci8 alkylene radical.
  • Subsequent halogenation of the terpolymers to selectively halogenate one or more benzylic sites in R or Rj. or halogenate the aromatic ring when R is hydrogen and R2 is not * . present may be done.
  • halogen containing polymers may be readily vulcanized under mild conditions using conventional vulcanization recipes for halogenated elastomers .
  • the presence of the aromatic or benzylic halide functional group also permits easy transformation into a variety of other functionalities as desired for specific applications to enhance adhesion and compatibility as well as co- vulcanization and grafting with other copolymers.
  • the present invention provides for copolymers of ⁇ -olefins and C3 to C1 0 0 0 ethylenically unsaturated alkylaromatic hydrocarbons which can be functionalized by halogenation by methods known in the art.
  • the alkylaromatic monomer may also be a polymeric "macromonomer", formula IV, such as a norbornene-terminated macromonomer containing polymerized alkyl substituted styrene. Subsequent halogenation of the graft copolymer to selectively halogenate a portion of the benzylic sites present in the graft chain may be done.
  • a polymeric "macromonomer" such as a norbornene-terminated macromonomer containing polymerized alkyl substituted styrene.
  • R3 , R4 and R5 are independently hydrogen or alkyl and X is hydrogen, halogen or a mixture of . hydrogen and halogen.
  • Pi and P2 independently represent a polymer or copolymer segment derived from an ⁇ -olefin monomer or mixture of ⁇ -olefin monomers copolymerizable with norbornene-type monomers, R2 is a straight or branched chain alkylene radical having from 1 to about 17 carbon atoms and P is a homopolymeric or copolymeric segment comprising an anionically polymerized vinyl alkylaromatic monomer or mixture of vinyl aromatic monomers or other anionically polymerizable vinyl monomers wherein at least one of the P repeating units is represented by formula V:
  • Examples of.ethylenically unsaturated alkylaromatic hydrocarbon represented by the formula "monomer II”, include but are not limited to, allyl benzenes or substituted allyl benzenes wherein R is located in the para position, such as allyl (4- methyl) benzene, allyl (4-ethyl) benzene and allyl (4-propyl) benzene.
  • Allyl benzene and allyl (4- methyl) benzene are especially preferred because they are most readily copolymerizable with ethylene and other ⁇ -olefin monomers under coordination polymerization conditions to provide high molecular weight elastomeric copolymers wherein the aromatic monomer is randomly dispersed along the polymer chain.
  • the polymers of formula II may then be selectively halogenated either at sites on the aromatic ring or through reactions with benzylic hydrogen wherein R is other than hydrogen.
  • the monomers of formulas monomer Ilia and monomer Illb may be readily prepared by a conventional Diels-Alder addition reaction of an ethylenically unsaturated aromatic or substituted aromatic compound and cyclopentadiene.
  • styrene or alkyl styrenes when added to cylcopentadiene will yield monomer materials of formula monomer Ilia when Ri is hydrogen and R is hydrogen or alkyl.
  • Diels Alder addition of 4- methylstyrene and cyclopentadiene yields 5- norbornene-2-(4-methylphenyl) . Allyl benzenes will add to cyclopentadiene to yield compounds of formula wherein is methylene and is hydrogen.
  • phenyl substituted ⁇ -olefins or internal olefins having from 1 to 18 carbon atoms will add to cyclopentadiene to yield monomers with specific variations of the end substituent groups depending on the location of the double bond in the olefin compound.
  • a reaction with p-phenyl-1- butene will yield a compound of formula monomer Illb wherein R2 is ethylidene and 3. and R are hydrogen.
  • Particularly preferred ⁇ - olefins are mixtures of ethylene and propylene which give rise to polymers having elastomeric properties when copolymerized in the presence of Ziegler-Natta coordination catalysts.
  • the resulting graft copolymers are then halogenated such that the P in formula VI is modified to contain compounds represented by formula V, wherein X is either halogen or H.
  • R is a straight or branched chain ⁇ to C j ⁇ alkylene radical.
  • Preferred examples of compounds represented by Formula VII include, but are not limited to, 2-methylene-5-norbornene.
  • These initiators may be generally prepared by contacting dicyclopentadiene with a mono-halogen containing olefinically unsaturated alkyl compound containing from 3 to 20 carbon atoms under Diels Alder reaction conditions to form the addition product which is an alkyl norbornene containing a halogen substituent group on the alkyl chain.
  • This reaction product may then be reacted under conditions known in the art with an alkali metal such as lithium, sodium or potassium such that the halogen atom is displaced to form the alkali- metallated, alkyl substituted norbornene initiator.
  • Suitable halogen-substituted olefins which may be employed to form the Diels-Alder adduct include allyl.bromide, 3-chloro-l-butene, 3-bromo-l-pentene, l-chloro-2-butene, 5-chloro-l-pentene, 3-chloro-l- propene, 4-bromo-l-butene and 2-chloro-l-butene.
  • Suitable initiators are those of formula VIII above wherein n is 0 and X ⁇ is lithium. These are preferred because they are readily synthesized using a relatively inexpensive and available reactant (ally bromide) and the resulting intermediate alkyl norbornene halide is recovered in relatively high yields because of a minimization of side reactions including decomposition and unwanted cyclization reactions. Accordingly while the invention will be further described with a focus on these preferred initiators and their method of preparation, it should be understood that such description is equally applicable to the preparation of other initiators within the scope of formula VIII above.
  • X is an alkali metal selected from the group consisting of lithium, potassium and sodium.
  • the preferred metal is lithium since the lithium- containing compound can be more readily prepared by simple lithiation of the corresponding 2-halomethyl- 5-norbornene compound and is quite soluble in solvents used for anionic polymerization reactions.
  • the initiators of formula IX may be typically prepared by a two stage process. In the first stage an allyl halide, preferably allyl bromide, may be reacted with cyclopentadiene to give the bicyloheptenyl-2 methyl halide derivative, i.e., 2- halomethyl-5-norbornene.
  • the crude product of the first stage reaction is then purified using conventional distillation techniques to further separate the 2-halomethyl-5- norbornene from any unreacted reactants and isomers thereof.
  • the second stage of the preparation of the initiator involves the reaction of lithium, sodium or potassium metal with the 2-halomethyl-5- norbornene to form the 2-metalomethyl-5-norbornene having the structure of formula IX above.
  • This reaction is conducted in a solvent which is inert under reaction conditions and which is free of materials which are detrimental to the reaction such as water, oxygen, carbon dioxide and/or alcohols.
  • the reaction is best conducted by gradual drop- wise addition of norbornene compound to a finely divided suspension of the metal present in excess and in solvent.
  • the reaction is preferably conducted at temperatures below O'C. preferably below -3O'C, and reaction times may vary between about 3 to 8 hours.
  • These reaction conditions are especially important to avoid thermally induced ring cleavage reactions and unwanted addition reactions which can lead to a low yield of the desired product as well as the formation of isomers which are difficult to separate.
  • essentially all of the bromomethyl norbornene is reacted to give a mixture which is substantially the lithiomethyl norbornene containing less than 5% by weight of unidentified oligomeric products.
  • the reaction product may then be recovered by filtering out residual metal particles and removal of the solvent by evaporation.
  • the macromonomers of this invention are preferably produced by living polymerization.
  • the anionically polymerizable monomer or mixture of monomers is contacted with the norbornene initiator prepared as above in the presence of an organic solvent which does not participate in or interfere with the polymerization reaction.
  • the living polymers prepared in accordance with this invention using any of the above initiators may be generally characterized by the structure X:
  • P represents a polymeric chain selected from the group consisting of homopolymers, random copolymers and block copolymers derived from an alkylstyrene monomer, preferably para allyl styrene, having the formula V above, wherein X is H, alone or in admixture with one or more other anionically polymerizable vinyl monomers ;
  • n is 0 or an integer ranging from 1-17
  • y and yl are either 0 or 1 , provided that where yl is 1 then y is 0, further provided that where yl is 0 , then n is an integer ranging from 1-17 and (n-1) of the y substituents are also 0 the remaining y substituent is a 1 , and further provided that where n is 0 , then yl is 1.
  • anionically polymerizable vinyl monomer as mentioned in formula X, are well known in the art.
  • anionically polymerizable vinyl monomers include vinyl aromatic monomers such as styrene and ⁇ -methyl styrene; vinyl unsaturated amides such as aery 1 amide, methacrylamide, N,N- dialkyl acrylamides, e.g.
  • solvents are the saturated aliphatic and cycloaliphatic hydrocarbons such as n- hexane, n-heptane, n-octane, cyclohexane and the like.
  • aliphatic and cyclic ether solvents can be used, for example, dimethyl ether, diethyl ether, dibutyl ether, tetrahydrofuran, dioxane, anisole, tetrahydropyran, diglyme, glyme, etc.
  • the rates of polymerization are faster in the ether solvents than in the hydrocarbon solvents.
  • a polymer of narrow molecular weight distribution is generally prepared by introducing all of the reactive species into the system at the same time.
  • polymer growth by consecutive addition of monomer to an active terminal group takes place at the same rate without chain transfer or termination reaction.
  • high concentrations of initiator leads to the formation of low molecular weight polymers, whereas, low concentrations of initiator leads to the production of high molecular weight polymers.
  • the temperature of the polymerization will depend on the monomer. Generally, the reaction can be carried out at temperatures ranging from about - 100*C up to about lOO'C. When using aliphatic and hydrocarbon solvents, the preferred temperature range is from about -10*C to about 100*C. With ethers as the solvent, the preferred temperature range is from about -100'C to about lOO'C.
  • the polymerization of styrene monomer for example is generally carried out at slightly above room temperature.
  • the preparation of the living polymer can be carried out by adding a solution of the alkali metal hydrocarbon initiator in an inert organic solvent to a mixture of a monomer and diluent at the desired polymerization temperature and allowing the mixture to stand with or without agitation until the polymerization is completed.
  • a preferred alternative procedure is to add monomer to a solution of the catalyst in the diluent at the desired polymerization temperature at the same rate. In this method the monomer is converted quantitatively to a living polymer as long as the system remains free of impurities which inactivate the anionic species.
  • the anionic polymerization must be carried out under carefully controlled conditions, so as to exclude substances which destroy the catalytic effect of the catalyst or initiator. For example such impurities as water, oxygen, carbon monoxide, carbon dioxide, and the like should be excluded from the system.
  • the polymerizations are generally carried out in dry equipment, using anhydrous reactants, and under inert gas atmosphere, such as nitrogen, helium argon, methane, and the like.
  • the above-described living polymers are susceptible to further reactions including further polymerization.
  • additional monomer such as para alkyl styrene
  • the living paraalkylstyryl polymer the polymerization is renewed and the chain grows until no more monomeric styrene remains.
  • the living polymers employed in the present invention are characterized by relatively uniform molecular weight, i.e., the distribution of molecular weights of the mixture of living polymers produced is quite narrow. This is in marked contrast to the typical polymer, where the molecular weight distribution is quite broad. The difference in molecular weight distribution is particularly evident from analysis of the gel permeation chro atogram of commercial polystyrene (Dow '666) prepared by free-radical polymerization and polystyrene produced by the anionic polymerization process utilized in accordance with the practice of the present invention.
  • Dow '666 commercial polystyrene
  • graft copolymers provide thermoplastic polymer composition(s) having balanced beneficial properties of both the backbone polymer and the macromonomer components alone and provides a technique for chemically linking these polymers which might otherwise be mutually incompatible when physically mixed or grafted by other techniques.
  • the present graft copolymers differ structurally from conventional graft copolymers since the macromolecular monomer is interposed between polymeric segments of the backbone polymer rather than being arbitrarily attached to the backbone in a random manner. These characteristics contribute materially to the advantageous properties which inure in these novel graft copolymers.
  • Especially preferred backbone monomer is a mixture of ethylene and propylene present at a level such that the copolymer backbone contains from about 15 to about 80 mole percent polymerized ethylene, the balance being propylene and the interpolymerized norbornene head monomer of the macromonomer.
  • Most preferred are elastomeric copolymers containing from 30 to about 70 percent of polymerized ethylene.
  • the copolymerization of the polymerizable macromolecular monomers with the comonomers may be conducted in a wide range of proportions.
  • a sufficient amount of the macromolecular monomer should be present to provide the chemical joining of at least one of the uniform molecular weight side chain polymers to each backbone polymer, so that noticeable effect on the properties of the graft copolymeric properties can be obtained.
  • the chemically joined, phase separated thermoplastic graft copolymers may be prepared by copolymerizing a mixture containing up to about 95 percent by weight, or more, of the polymerizable macromolecular monomers of this invention, although mixtures containing up to about 60 percent by weight of the polymerizable macromolecular monomer are preferred and mixtures containing up to 25 percent by weight of the polymerizable macromolecular monomer are most preferred.
  • the thermoplastic chemically joined, phase separated graft copolymer of the invention is comprised of: (1) from 1 to about 95 percent by weight of the polymerizable macromolecular monomer having a narrow molecular weight distribution (i.e., a Mw/Mn of less than 1.25), more preferably from about 1 to about 60 percent by weight, and most preferably from about 1 to about 25 percent by weight and; (2) from about 99 to about 5 percent by weight of a copolymerization ⁇ -olefin monomer or mixture of ⁇ -olefin monomers defined herein above, more preferably from about 99 to about 40 percent by weight of the latter, and most preferably from about 99 to about 75% by weight of the latter.
  • the solvent, reaction conditions and feed rate will be partially dependent upon the type of catalyst system utilized in the copolymerization process.
  • the macromolecular monomer be dissolved in the solvent system utilized.
  • the most preferred organo-aluminium compound is an aluminum alkylsequichloride such as Al2Et3Cl3 or Al 2 (iBu) 3 Cl 3 .
  • the copolymerization reaction may be conducted at any suitable temperature, depending on the particular catalyst, macromolecular monomer, monomer feed, resulting graft copolymer and solvent used. Generally, the graft copolymerization will be conducted at a temperature of from about O'C to lOO'C.
  • the graft copolymers prepared in accordance with the invention generally may have a weight average molecular weight in the range of from about 10,000 up to 3,000,000 more preferably in the range of from about 25,000 to 250,000.
  • copolymers prepared as described above provide an excellent substrate for further functionalization reactions such as halogenation. It is generally desirable to treat the polymerization product in an appropriate manner, prior to halogenation, in order to quench the catalyst and/or remove catalyst residues, remove residual unconverted monomers and place the polymer in a convenient form for the halogenation reaction.
  • Halogenation of the copolymers of this invention using a source of halogen and in the presence of a free radical initiator is highly selective towards halogenation of benzylic sites, i.e., sites present in the alkylstyrene sidechains, than sites present in the backbone chain.
  • almost exclusive halogen substitution occurs on one or more of the alkylaromatic groups present in the pendent chain as consequence of hydrogen atom extraction from these groups. This is significant because halogenation of the backbone polymer chain is undesirable due to the possibility of facile dehydrohalogenation reactions leading to backbone unsaturation and resulting environmental instability, i.e., decreased ozone resistance and thermal instability.
  • halogen bromine
  • the presence of halogen (bromine) on the ring alkyl groups leads to several additional significant advantages, such as facile functionalization by substitution of other functional groups at that site. More particularly, the highly reactive nature of the halogen in the haloalkyl group attached to an aromatic ring makes it a particularly desirable functionality to enhance and extend the usefulness of these copolymers in a range of applications.
  • the presence of aromatic haloalkyl groups in the copolymer permits cross linking in a variety of ways under mild conditions.
  • a second advantage offered by the copolymerized macromonomers with respect to the halogenation is that the terpolymers of the invention contain relatively little residual unreacted volatile monomer content.
  • Residual unreacted monomer, such as para-methylstyrene, left in the copolymer will react curing halogenation to both consume halogen and produce generally undesirable toxic by-products, and their presence thus renders it difficult to control and measure the amount of desired functionality introduced into the copolymer.
  • Unreacted olefin monomers in the backbone polymer ar volatile enough to be easily removed in any of a variety of stripping operations, but para- methylstyrene, with its high boiling point of 170'C, is much more difficult to remove.
  • the graft copolymers prepared in accordance with this invention are relatively free of such difficult to remove unreacted monomers due to the fact that essentially all of the aromatic monomer used to prepare the norbornene-terminated macromolecules is consumed in the anionic polymerization process and also as a consequence of the very high (90% or greater) conversion of the macromolecule when copolymerized with the olefin monomers forming the backbone.
  • the halogenation reaction itself can be carried out in the bulk phase or on the graft copolymer either in solution or in a finely dispersed slurry.
  • Bulk halogenation can be effected in an ex «truder, or other internal mixer, suitably modified to provide adequate mixing and for handling the halogen and corrosive by-products of the reaction. It has the advantages of permitting complete removal of residual unreacted para-methylstyrene by conventional finishing operations prior to halogenation, and of avoiding possible diluent halogenation as an undesirable side reaction.
  • Solution halogenation is advantageous in that it permits good mixing and control of halogenation conditions to be achieved, easier removal of undesired halogenation by-products, and a wider range of initiators of halogenation to be employed.
  • the halogenation is preferably conducted in solvent in the presence of a free radical initiator and a source of halogen.
  • Suitable indicators include heat, light or initiators which have a half life of between about 0.5 and 2500 minutes under the desired reaction conditions, more preferably about 10 to 300 minutes.
  • the amount of initiator employed will usually vary between 0.02 and 1% by weight on the copolymer. preferably between about 0.02 and 0.3%.
  • the preferred initiators are bis azo compounds, such as:
  • radical indicators such as peroxides can also be used, but it. is preferred to use a radical initiator which is relatively poor at hydrogen abstraction, so that it reacts preferentially with the bromine molecules to form bromine atoms rather than with the copolymer or solvent to form alkyl radicals.
  • the halogenating agent can be gaseous, liquid or solid and may be added either in a pure state or diluted with a suitable inert solvent.
  • Suitable halogenating agents include chlorine, sulfuryl chloride, N-chloro-succinimide, l,3-dichloro-5, 5- dimethylhydantoin, bromine, bromine chloride, sodium hypochlorite, sulfur bromide and N-bromosuccinimide.
  • gaseous chlorine, bromine or bromine chloride gaseous diluents, e.g., nitrogen, argon, air, CO2 etc. , can be used when a diluent is desired. Mixtures of any of these halogenation agents may also be used.
  • the most preferred halogenating agent is liquid bromine.
  • Halogenation in solution may be conducted at any temperature between about 40*C and the reflux temperature of a solution of the polymer. It is preferred to conduct the halogenation at relatively low temperatures, i.e., 45 to 80'C, since selectively towards hydrogen displacement on the alkylaromatic groups on the chain is further enhanced at a lower temperatures. Since one mole of HX, wherein X is chlorine or bromine, is produced for each mole of halogen reacted or substituted on the enchained alkylstyrene moiety, it is desirable to neutralize or otherwise remove this HX during the reaction or at least during polymer recovery in order to prevent it from causing undesirable side reaction or corrosion of equipment.
  • Such neutralization and/or removal can be accomplished by having a base (which is relatively non-reactive with the halogen) such as, for example, calcium carbonate powder present in dispersed form during the halogenation reaction to absorb the HX as it is produced. Removal of HX can also be accomplished by stripping with an inert gas, e.g. N , preferably at elevated temperatures. Final traces of HX may be neutralized by incorporation of a suitable base, e.g. calcium stearate into the stripped halogenated copolymer.
  • a base which is relatively non-reactive with the halogen
  • an inert gas e.g. N
  • the degree of halogenation of the polymers is largely a function of the quantity of reactants used in the halogenation process and the structure and molecular weight of the graft polymer substrate.
  • the halogen content of the graft polymers may range from about 0.05 up to about 7.5 weight percent based on the total weight of copolymer, more preferably from about 0.1 up to about 5.0 weight percent.
  • halogenated neutralized copolymers of the present invention can be recovered and finished using conventional means with appropriate stabilizers being added to yield highly desirable and functional saturated halogenated copolymers suitable for many uses.
  • the halogenated copolymers of the present invention may be processed in standard equipment used for rubber such as internal mixers. These halogenated copolymers are amendable to conventional compounding practice and various fillers and extenders can be incorporated, e.g., carbon blacks, clays, silicas, carbonates, oils, resins, waxes, etc., to produce a composition.
  • the halogenated copolymers of the present invention can be cured alone or a composition comprising a halogenated copolymer of the present invention may be blended with other co-vulcanizable elastomers and thermoplastics.
  • Example 1 is illustrative of the invention.
  • ( ) MPN content is the weight percent of the incorporated 5-(4-methylphenyll)- 2-norbornene as determined by Hnmr.
  • Reactor 11 Continuous Flow Stirred Tank Reactor Temperature: 30'C Pressure: 500 kpa Agitation: 1200 kpa Residence: 9 min
  • the resulting crude mixture contained 75% 2- bromomethyl-5-norbornene, 9% dicyclopentadiene, 3% allylbromide and unidentified isomers of each.
  • Example 4 Svnthesis of 2-bromomethyl-5-norbornene
  • the crude reaction mixtures from Examples 1 and 2 were combined and purified by two distillation steps.
  • the first distillation was conducted in a 3 liter, 3 neck flask fitted with a nitrogen sweep, a thermocouple, and an efficient column.
  • the system pressure was kept at 700 mm Hg pressure and the pot temperature was slowly raised to 175'C. Under these conditions the dicyclopentadiene cracked and cyclopentadiene co-distilled with the allyl bromide. When it appeared that no more volatile products were distilling, the pressure was dropped and the contents of the flask were flashed into a receiver.
  • This distillate contained 2% dicyclopentadiene, 95% 2-bromomethyl-5-norbornene and higher boiling unidentified isomers.
  • a 2 liter 2 neck flask, fitted with a stirrer and a septum inlet was assembled in a dry box.
  • 700ml of diethyl ether (distilled from dibutylmagnesium) was placed in the flask along with 4g lithium (Lithco, 0.8% sodium, slivered from rod).
  • the flask was stoppered and 5% of a solution of 38g 2-bromomethyl-5-norbornene was added. As soon as the reaction begins (lithium is very bright) the flask was cooled to -50*C or below. The addition was continued dropwise at -50*C over 6 hour period.
  • a two liter two neck flask, fitted with a stirrer and septum inlet is assembled in a dry box, nitrogen atmosphere.
  • 700ml ether distilled from dibutylmagnesium
  • 4g lithium Lithco, 0.8% sodium, cut from a rod.
  • the flask is stoppered and 5% of a solution of 38g 2-bromomethyl-5-norbornene is added.
  • the reaction begins (lithium brightens) the flask is cooled to -30'C or below.
  • the addition is continued dropwise over a 6 hour period.
  • Ethylene content using ASTM 1246 (2) Poly(4-methyIstyrene) , (P(4-MeS)) is the weight percent of the incorporated (2-(polyl ⁇ inethyIstyrene) ) ⁇ -norbornene as determined by GPC.
  • the graft copolymers prepared in Example 9 above are clear, tough thermoplastic elastomers. Transmission electron micrographs of the grafts indicate that they are microphase separated with spherical polystyrene domains averaging 30 nanometers. The rheology of the graft copolymers is typical for multiphase materials. A temperature sweep from 20 to 100 * C did not show a large change in viscosity, which indicates that the system likely remains biphasic in the melt. This corresponds to the non-newtonian shear behavior. The polymer undergoes a 4 order of magnitude drop in viscosity upon increasing the shear-rate from 10-2 to 10-2 rad/sec.
  • Free radical catalyzed bromination of the EP graft terpolymer was conducted on stabilizer free terpolymer prepared as in Example 9. 50 grams of the terpolymer was dissolved in 1 liter of heptane and refluxed under nitrogen for 30 minutes. The solution was cooled to 70'C and a solution of AIBN (azoisobutyronitrile) in heptane (0.2g in 20ml) was added. A solution of bromine (8g in 100ml heptane) was added over 4.5 minutes. After the addition, the polymer was washed with 10% aqueous sodium bicarbonate solution followed by two washes with 10% aqueous isopropanol. The polymer cement was then precipitated into acetone and vacuum dried at 40'C overnight. Analysis by NMR indicated that there is 2.6st% benzylbromide which is the same value observed by X-ray florescence.
  • a mixture was prepared on a cold mill containing Tetrone A (1 pph) , Zinc oxide (lpph), stearic acid (2 pph) , carbon black (60 pph) and graft polymer (100 pph). The mixture was then placed in a Monsanto rheometer and a cure curve (Document 1) at 160*C was obtained. The torque increase as a function of time provides an indication of cure-state and cure time.

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Abstract

L'invention se rapporte à des copolymères halogénés sélectivement contenant au moins une αoléphine polymérisée et un comonomère contenant un alkylbenzene monomère ou polymère, ainsi que la préparation de compositions réticulées à partir desdits copolymères.
PCT/US1993/003200 1992-04-07 1993-04-06 Copolymeres d'olefines et d'olefines aromatiques et d'olefines et de composes aromatiques polymeres WO1993020117A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP93912128A EP0635032A1 (fr) 1992-04-07 1993-04-06 Copolymeres d'olefines et d'olefines aromatiques et d'olefines et de composes aromatiques polymeres
JP5517760A JPH07505661A (ja) 1992-04-07 1993-04-06 オレフィンと芳香族オレフィンのコポリマー及びオレフィンと高分子芳香族化合物のコポリマー
CA002132305A CA2132305A1 (fr) 1992-04-07 1993-04-06 Copolymeres d'olefines et d'olefines aromatiques, ainsi que d'olefines et de composes aromatiques polymeres

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US86498192A 1992-04-07 1992-04-07
US07/864,981 1992-04-07

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EP0095787A1 (fr) * 1982-05-26 1983-12-07 Shell Internationale Researchmaatschappij B.V. Procédé de couplage des polymères vivants
US4599384A (en) * 1984-07-23 1986-07-08 The University Of Akron Novel EPDM-isobutylene graft copolymers
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EP0635032A1 (fr) 1995-01-25
CA2132305A1 (fr) 1993-10-14

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