US20060270814A1 - Polyolefin functional at one end - Google Patents

Polyolefin functional at one end Download PDF

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US20060270814A1
US20060270814A1 US10/569,604 US56960406A US2006270814A1 US 20060270814 A1 US20060270814 A1 US 20060270814A1 US 56960406 A US56960406 A US 56960406A US 2006270814 A1 US2006270814 A1 US 2006270814A1
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chain
group
olefin
polymer
end functionalized
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Haruyuki Makio
Terunori Fujita
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Mitsui Chemicals Inc
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Mitsui Chemicals Inc
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Assigned to MITSUI CHEMICALS, INC. reassignment MITSUI CHEMICALS, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FUJITA, TERUNORI, MAKIO, HARUYUKI
Publication of US20060270814A1 publication Critical patent/US20060270814A1/en
Priority to US12/468,303 priority Critical patent/US7897709B2/en
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/18Introducing halogen atoms or halogen-containing groups
    • C08F8/20Halogenation

Definitions

  • the present invention relates to a novel single-chain-end functionalized polyolefin.
  • Polyolefins such as polyethylene (PE) and polypropylene (PP) are light and inexpensive and further have characteristics of having excellent physical properties and workability.
  • high chemical stability of polyolefins is an obstacle for giving, thereto, high functionalities, typical examples of which include printability, paintability, heat resistance and impact resistance, and a function for improving compatibility thereof with other polar polymers.
  • Examples thereof include a method of polymerizing an olefin with a polar monomer such as vinyl acetate or a methacrylic acid ester by radical polymerization; and a method of grafting a polar monomer such as maleic anhydride to a polyolefin in the presence of a peroxide.
  • a polar monomer such as vinyl acetate or a methacrylic acid ester by radical polymerization
  • grafting a polar monomer such as maleic anhydride
  • a process using living polymerization is useful as a process for producing such a polymer.
  • a growing terminal of the polymer quantitatively keeps reactivity. It is therefore known that the reactivity is used to cause the terminal to react directly with a polar-group-containing monomer, whereby a polymer having a functional group at its terminal position can be effectively produced.
  • the Applicant already discloses a transition metal compound having a salicylaldimine ligand as a novel catalyst for olefin polymerization (see Japanese Patent Application Laid-Open No. 11-315109), and further suggests a process of using the transition metal compound to produce a novel single-terminal vinyl-group-containing copolymer or a novel polar-group-containing block copolymer (see Japanese Patent Application Laid-Open Nos. 2003-73412 and 2003-40953).
  • the two published documents neither disclose any polymer having a polar functional group only at its single terminal (single-chain-end functionalized polymer) nor any process for the production thereof.
  • the present Applicant has eagerly searched a single-chain-end functionalized polymer which can be used for various purposes and has overcome the above-mentioned problems, and has then made the present invention.
  • the present invention relates to a polyolefin which has a polar functional group at its single-terminal position and is useful for various purposes.
  • the single-chain-end functionalized polyolefin (F) of the present invention is represented by the following general formula (I): P—X (I) wherein X is a group containing at least one element selected from oxygen, sulfur, nitrogen, phosphorus and halogens, P represents a polymer chain made mainly of an olefin composed only of carbon and hydrogen atoms, and X is bonded to a terminal of P, wherein the molecular weight distribution (Mw/Mn) obtained by gel permeation chromatography (GPC) is from 1.0 to 1.5.
  • Mw/Mn molecular weight distribution obtained by gel permeation chromatography
  • a preferred embodiment of the polymer chain (P) is a polymer chain made of units of at least one olefin selected from ethylene and olefins having 3 to 20 carbon atoms.
  • the invention also relates to the single-chain-end functionalized polyolefin (F) produced by a specific production process.
  • the single-chain-end functionalized polyolefin of the invention comprises a single-chain-end functionalized polyolefin obtained by: performing the following steps 1 and 2 in any order in the presence of an olefin polymerizing catalyst containing a compound (A) which contains a transition metal in the groups IV to V; and subsequently performing the following step 3 if necessary:
  • the single-chain-end functionalized polyolefin (F) of the invention is represented by the following general formula (I): P—X (I)
  • X is a group containing at least one element selected from oxygen, sulfur, nitrogen, phosphorus and halogens, that is, a polar functional group. Specific examples thereof include an oxy group; a peroxy group; a hydroxyl group; a hydroperoxy group; alkoxy groups such as methoxy, ethoxy, propoxy and butoxy; aryloxy groups such as phenoxy, methylphenoxy, dimethylphenoxy, and naphthoxy; arylalkoxy groups such as phenylmethoxy, and phenylethoxy; an acetoxy group; a carbonyl group; groups wherein an element in the group XIII or XIV is bonded to an oxygen, such as silyloxy, boryloxy, and aluminoxy; an amino group; N-mono-substituted amino groups such as methylamino, N-benzylamino, and N-cyclohexylamino; N,N-di-substit
  • Examples of the phosphorus-containing group include phosphines such as phenylphosphino, methylphosphino, ethylphosphino, diphenylphosphino, dimethylphosphino, diethylphosphino, methylphenylphosphino, and dibenzylphosphino; phosphine oxides; phosphine sulfides; and phosphinous acids.
  • Examples of the halogens include fluorine, chlorine, bromine, and iodine.
  • P represents a polymer chain made mainly of an olefin composed only of carbon and hydrogen atoms.
  • olefin polymer chains preferred is a polyolefin polymer chain made of structural units derived from at least one selected from ethylene and olefins having 3 to 10 carbon atoms.
  • X is bonded to a terminal of P.
  • the molecular weight distribution (Mw/Mn) is usually 1.2 or less.
  • the polymer chain (P) is a polyethylene chain, that is, a chain wherein the concentration of a skeleton originating from ethylene is 80% or more by mol
  • the weight-average molecular weight (Mw) of the single-chain-end functionalized polyolefin of the invention is 5,000 or more, preferably 7,000 or more.
  • the polymer chain P in the single-chain-end functionalized polyolefin (F) of the invention contains an ⁇ -olefin chain having 3 to 20 carbon atoms
  • the ⁇ -olefin chain has a feature of exhibiting syndiotacticity.
  • the fact that the ⁇ -olefin chain is syndiotactic can be identified by various spectral analyses. The following will describe the fact that the polymer chain (P) of the single-chain-end functionalized polyolefin in the invention is syndiotactic on the basis of analytic findings, giving a case in which the ⁇ -olefin is propylene as an example.
  • the 13 C NMR spectrum of polypropylene is measured, and attention is paid to a range of methyl groups of side chains (19.5-21.7 ppm).
  • the syndiotacticity [rr] of a triad can be obtained by substituting an integrated value of plural peaks (19.5-20.2 ppm) corresponding to an rr triad in this range and an integrated value of peaks (20.2-21.7 ppm) corresponding to a different mm or mr triad for I(rr)/ ⁇ I(rr)+I(mr)+I(mm) ⁇ wherein I represents the integrated intensity of each chain in the 13 C NMR.
  • the [rr] can be controlled into any value from 0.25 to 1.0 by catalytic structure or other polymerizing conditions.
  • the regularity is particularly high ([rr]>0.80)
  • a sharp peak (20.0-20.1 ppm) corresponding to an rrrr pentad makes its appearance at a higher intensity than peaks resulting from other chains.
  • the syndiotacticity can be more precisely evaluated by the [rrrr]
  • syndiotacticity is kept when chains of propylene are present therein.
  • the value of the [rr] can be obtained from a value obtained by amending overlap of methyl groups which originates from chains of EPE and EPP wherein E and P represent an ethylene unit and a propylene unit, respectively, in each polymer.
  • polyolefins wherein X is an oxygen-containing group or nitrogen-containing group or is the two groups from the viewpoint of exhibiting high reactivity with various chemical species.
  • the single-chain-end functionalized polyolefin of the invention can be effectively obtained by carrying out steps which will be detailed below successively in the presence of an olefin polymerizing catalyst containing a compound (A) which contains a transition metal in the groups IV to V in the periodic table.
  • transition metal compounds described in the above-mentioned Japanese Patent Application Laid-Open No. 2003-40953, which was filed by the Applicant can be used without any limitation. Of these transition metal compounds, preferred transition metal compounds are illustrated below.
  • an organic aluminum oxy compound (B) can be used together with the group IV to V transition metal containing compound (A).
  • the organic aluminum oxy compound (B) may be an aluminoxane known in the prior art, or an organic aluminum oxy compound insoluble in benzene, as exemplified in Japanese Patent Application Laid-Open No. 2-78687.
  • the known aluminoxane can be produced by, for example, a process as described below, and is usually obtained as a solution containing a solvent of a hydrocarbon.
  • a compound containing absorbed water or a salt containing crystal water such as magnesium chloride hydrate, copper sulfate hydrate, aluminum sulfate hydrate, nickel sulfate hydrate or cerium (I) chloride hydrate
  • organic aluminum compound used when the aluminoxane is prepared include tri-n-alkylaluminums such as trimethylaluminum, triethylaluminum, tri-n-butylaluminum, tripropylaluminum, tripentylaluminum, trihexylaluminum, and trioctylaluminum; branched-trialkyl aluminums such as triisopropylaluminum, triisobutylaluminum, tri-sec-butylaluminum, and tri-2-ethylhexylaluminum; tricycloalkylaluminums such as tricyclohexylaluminum, and tricyclooctylaluminum; triarylaluminums such as triphenylaluminum, and tritolylaluminum; and trialkenylaluminums such as triisoprenylaluminum represented by (i-C 4 H 9 ) x Al y (C
  • At least one selected from the following can be caused to be present together with the group IV to V transition metal containing compound (A) and the organic aluminum oxy compound (B): an organic metal compound, a compound which can react with the transition metal compound (A) to form an ion pair, a carrier, and an organic compound.
  • an organic metal compound a compound which can react with the transition metal compound (A) to form an ion pair
  • a carrier a compound which can react with the transition metal compound (A) to form an ion pair
  • an organic compound a compound which can react with the transition metal compound (A) to form an ion pair
  • the single-chain-end functionalized polyolefin (F) of the invention is obtained by performing the following steps 1 and 2 in any order in the presence of an olefin polymerizing catalyst containing a compound (A) which contains a transition metal in the groups IV to V, and subsequently performing the following step 3 if necessary; that is, the single-chain-end functionalized polyolefin (F) of the invention is obtained [i] by carrying out the steps 1 and 2 in this order, and carrying out the step 3 if necessary; or [ii] by carrying out the step 2 and step 1 in this order, and carrying out the step 3 if necessary:
  • Y′ in the general formula (II) used in the step 1 is a group containing at least one element from oxygen, sulfur, nitrogen, phosphorus and halogens.
  • a group include an oxy group; a peroxy group; a hydroxyl group; a hydroperoxy group; alkoxy groups such as methoxy, ethoxy, propoxy and butoxy; aryloxy groups such as phenoxy, methylphenoxy, dimethylphenoxy, and naphthoxy; arylalkoxy groups such as phenylmethoxy, and phenylethoxy; an acetoxy group; a carbonyl group; groups wherein an element in the group XIII or XIV is bonded to an oxygen, such as silyloxy, boryloxy, and aluminoxy; an amino group; N-mono-substituted amino groups such as methylamino, N-benzylamino, and N-cyclohexylamino; N,N-di-substit
  • Examples of the phosphorus-containing group include phosphines such as phenylphosphino, methylphosphino, ethylphosphino, diphenylphosphino, dimethylphosphino, diethylphosphino, methylphenylphosphino, and dibenzylphosphino; phosphine oxides; phosphine sulfides; and phosphinous acids.
  • Examples of the halogens include fluorine, chlorine, bromine, and iodine.
  • silyloxy aluminoxy, boryloxy, and N,N-disiyl-substituted amino groups, which do not poison the catalyst easily and which generate active hydrogen in the case that hydrolysis is performed after the end of the step 2.
  • Q is an alkylene group which may have a substituent, a carbonyl group, or bivalent oxygen.
  • Q is usually an alkylene group which may have a substituent wherein the total number of carbon atoms is from 1 to 20.
  • an unsubstituted linear alkylene group represented by the following formula (III) is preferably used: —[CH 2 ]n- (III) wherein n is a positive integer of 1 to 15.
  • a and R each represent a hydrogen atom or a hydrocarbon group which may have a substituent, and A or R may be bonded together to Q to form a ring.
  • a cycloolefin represented by the following formula (IV) or (IV′) is preferably used: wherein p represents an integer of 1 to 10, and is bonded to Y at any position, q is an integer of 0 to 10, and when q is 0, the cycloolefin is a monocycloolefin.
  • Examples of the olefin having 3 to 20 carbon atoms, used in the step 2, include linear or branched ⁇ -olefins having 3 to 20 carbon atoms, such as propylene, 1-butene, 2-butene, 1-pentene, 3-methyl-1-butene, 1-hexene, 4-methyl-1-pentene, 3-methyl-1-pentene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, and 1-eicocene; and cyclic olefins having 3 to 20 carbon atoms, such as cyclopentene, cycloheptene, norbornene, 5-methyl-2-norbornene, tetracyclododecene, and 2-methyl 1,4,5,8-dimethano-1,2,3,4,4a,5,8,8a-octahydronaphthalene.
  • olefin having 3 to 20 carbon atoms examples include vinylcyclohexane, dienes and polyenes. Additional examples of the olefin include such as aromatic vinyl compounds styrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, o,p-dimethylstyrene, o-ethylstyrene, m-ethylstyrene, and p-ethylstyrene, and other mono- or poly-alkylstyrenes; and 3-phenylpropylene, 4-phenylbutene, and ⁇ -methylstyrene. These olefins may each contain in the molecule thereof a heteroatom such as an oxygen, nitrogen, or silicon atom. The olefins may be used alone or in combination of two or more thereof.
  • the polymer chain (P) in the single-chain-end functionalized polyolefin (F) represented by the general formula (I) can be rendered a block type chain composed of two kinds of olefin chains each having a controlled molecular weight (the wording “different in kind or composition” in the step 2 related to the invention means the following: “different in kind”; “different in composition”; and further “different in kind and composition”).
  • the resultant single-chain-end functionalized polyolefin is a single-chain-end functionalized block polymer represented by the following general formula (V): X-PE-PP (V) wherein X has the same meanings as in the formula (I), and PE and PP represent a polyethylene chain and a polypropylene chain, respectively.
  • the resultant single-chain-end functionalized polyolefin is a single-chain-end functionalized block polymer represented by the following formula (VI): X-PE-EPR (VI) wherein X has the same meanings as in the formula (I), and PE and EPR represent a polyethylene chain and an ethylene/polypropylene copolymer chain, respectively.
  • the step 3 which may be performed if necessary, is a step for converting the group (Y′) in the general formula (II) to a different group by a reaction such as hydrolysis, oxidization, reduction, or nucleophilic substitution.
  • a reaction such as hydrolysis, oxidization, reduction, or nucleophilic substitution.
  • hydrolysis reaction is used to convert a Y′ group: Me 2 Al—O— to a different group (hydroxyl group).
  • the conversion is not limited to this chemical conversion.
  • the polymerization can be carried out by any one of liquid-phase polymerizations, such as dissolution polymerization, suspension polymerization, and gas-phase polymerizations.
  • an inert hydrocarbon medium used in the liquid-phase polymerization examples include aliphatic hydrocarbons such as propane, butane, pentane, hexane, heptane, octane, decane, dodecane, and kerosene; alicyclic hydrocarbons such as cyclopentane, cyclohexane, and methylcyclopentane; aromatic hydrocarbons such as benzene, toluene, and xylene; halogenated hydrocarbons such as ethylene chloride, chlorobenzene, and dichloromethane; and mixtures thereof.
  • the olefin itself can be used as the solvent.
  • the operations composed of the steps 1 and 2 are usually carried out without isolating any product in each of the steps.
  • the catalyst is once charged when the initial step 1 is started.
  • the group IV to V transition metal compound (A) is used in an amount ranging usually from 10 ⁇ 12 to 1 mole, preferably from 10 ⁇ 10 to 10 ⁇ 1 mole per liter of the reaction volume.
  • the organic aluminum oxy compound (B) is used in such an amount that the mole ratio of aluminum atoms in the component (B) to transition metal atoms (M) in the transition metal compound (A) (Al/M) will be a value ranging usually from 10 to 500,000, preferably from 50 to 100,000.
  • the step 1 can be finished by the contact usually at ⁇ 20 to 50° C., preferably at ⁇ 10 to 25° C. for 1 to 300 minutes, preferably for 20 to 200 minutes.
  • the polymerization reaction is advanced by the contact usually at ⁇ 20 to 75° C., preferably at 0 to 50° C. for 1 to 600 minutes, preferably for 5 to 180 minutes.
  • the pressure in the step 2 is usually from a normal pressure to 100 kg/cm 2 , preferably from a normal pressure to 50 kg/cm 2 .
  • the polymerization reaction can be conducted by any one of batch type, semi-continuous type, and continuous type processes. The polymerization can be conducted at two or more separated stages wherein reaction conditions are different.
  • the single-chain-end functionalized polyolefin of the invention can be developed into various applications.
  • the polyolefin can be applied to, for example, a high molecular weight additive; a compatibility accelerator; a diblock copolymer useful as a compatibility accelerator or modifier for polymer; a precursor of a triblock copolymer useful as thermoplastic elastomer or the above-mentioned articles; or a surface modifier for improving paintability, adhesive property and other properties of resin.
  • the polyolefin can be used, in the form of a macromonomer, as raw material of a polymer having a specific structure such as a comb-shaped or star-shaped structure, and applied to a viscosity adjustor for oil, or some other agents.
  • water or alcohol is usually used as a hydrolyzing agent, and the hydrolysis is conducted under an acidic or basic condition.
  • the hydrolysis may be conducted in the presence of an organic solvent in a two-phase system, or conducted in a gas phase using steam. Usually, the following conditions are adopted: a temperature of 0 to 800° C. and a time of 1 minute to 24 hours.
  • the polymerization activity per mmol of titanium was 30.9 g
  • the number-average molecular weight (Mn) of the polymer was 13,000
  • the ratio of the weight-average molecular weight (Mn) to the number-average molecular weight (Mn), (Mw/Mn) was 1.08
  • the melting peak temperature based on DSC was 133.8° C.
  • FT, 270 MHz, in C 2 D 2 Cl 4 , at 120° C. a triplet corresponding to a methylene group adjacent to an OH group made its appearance near 3.64 ppm, and an overlap of methyl groups of two types at terminals made its appearance near 0.95 ppm.
  • the integration ratio therebetween was 2:6.
  • the reactant was poured into 600 mL of methanol containing a small amount of hydrochloric acid to precipitate the entire amount of a polymer.
  • the polymer was collected by filtration.
  • the polymer was dried at 80° C. under a reduced pressure for 10 hours so as to be yielded in an amount of 0.354 g.
  • the polymerization activity per mmol of titanium was 3.04 g
  • the number-average molecular weight (Mn) of the polymer was 8, 820
  • the ratio of the weight-average molecular weight (Mw) to the number-average molecular weight (Mn), (Mw/Mn) was 1.05
  • the melting peak temperature based on DSC was 144.4° C.
  • Propylene was polymerized under the same conditions as in Example 2 except that Me 2 AlO—(CH 2 ) 9 CH ⁇ CH 2 was used instead of Me 2 AlO—(CH 2 ) 4 CH ⁇ CH 2 .
  • the polymerization activity per mmol of titanium was 3.03 g
  • the number-average molecular weight (Mn) of the polymer was 8,200
  • the ratio of the weight-average molecular weight (Mw) to the number-average molecular weight (Mn), (Mw/Mn) was 1.09.
  • FT 270 MHz in C 2 D 2 Cl 4 , at 120° C.
  • Propylene was polymerized under the same conditions as in Example 2 except that Me 3 SiO—(CH 2 ) 9 CH ⁇ CH 2 was used instead of Me 2 AlO—(CH 2 ) 4 CH ⁇ CH 2 .
  • the polymerization activity per mmol of titanium was 2.88 g
  • the number-average molecular weight (Mn) of the polymer was 7,700
  • the ratio of the weight-average molecular weight (Mw) to the number-average molecular weight (Mn), (Mw/Mn) was 1.06
  • the weight-average molecular weight (Mw) of the polymer was 9,250
  • the ratio of the weight-average molecular weight to the number-average molecular weight (Mn) was 1.06
  • the melting peak temperature based on DSC was 142.0° C.
  • the polymerization activity per mmol of titanium was 52.5 g, the number-average molecular weight (Mn) of the polymer was 13,700, and the ratio of the weight-average molecular weight (Mw) to the number-average molecular weight (Mn), (Mw/Mn), was 1.15.
  • FT 1 H NMR spectrum
  • FT 270 MHz, in C 2 D 2 Cl 4 , at 120° C.
  • a triplet corresponding to a methylene group adjacent to a phenyl group, aromatic protons, and an overlap of methyl groups of two types at terminals made their appearance near 2.53 ppm, 6.45-6.65 ppm and 7-7.13 ppm, at an integration ratio of 2:4:6. From the above, a structure of a polymer of the following formula was identified:
  • the polymerization activity per mmol of titanium was 44.1 g, the number-average molecular weight (Mn) of the polymer was 15,500, and the ratio of the weight-average molecular weight (Mw) to the number-average molecular weight (Mn), (Mw/Mn), was 1.10.
  • Propylene was polymerized under the same conditions as in Example 2 except that Me 2 AlO—(454644CH 2 ) 4 CH ⁇ CH 2 was not added.
  • the polymerization activity per mmol of titanium was 3.16 g, and the melting peak temperature based on DSC was 146.0° C.
  • the melting peak temperature based on DSC was 146.0° C.
  • FT, 270 MHz, in C 2 D 2 Cl 4 , at 120° C. no peak made its appearance near 3.64 ppm.
  • peaks at 22.5-24.0 ppm corresponding to isopentyl and isobutyl groups at the terminals made their appearance.
  • the polyolefin having a polar functional group at its single terminal position itself, or the polyolefin subjected to a further modifying treatment is useful for various purposes.

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US8399724B2 (en) 2011-03-25 2013-03-19 Exxonmobil Chemical Patents Inc. Vinyl terminated higher olefin copolymers and methods to produce thereof
US8426659B2 (en) 2011-03-25 2013-04-23 Exxonmobil Chemical Patents Inc. Vinyl terminated higher olefin polymers and methods to produce thereof
US8431662B2 (en) 2008-06-20 2013-04-30 Exxonmobil Chemical Patents Inc. Polymacromonomer and process for production thereof
US8455597B2 (en) 2011-03-25 2013-06-04 Exxonmobil Chemical Patents Inc. Catalysts and methods of use thereof to produce vinyl terminated polymers
US8501894B2 (en) 2011-03-25 2013-08-06 Exxonmobil Chemical Patents Inc. Hydrosilyation of vinyl macromers with metallocenes
US8604148B2 (en) 2011-11-29 2013-12-10 Exxonmobil Chemical Patents Inc. Functionalization of vinyl terminated polymers by ring opening cross metathesis
US8623974B2 (en) 2011-03-25 2014-01-07 Exxonmobil Chemical Patents Inc. Branched vinyl terminated polymers and methods for production thereof
US8623962B2 (en) 2008-06-20 2014-01-07 Exxonmobil Chemical Patents Inc. Olefin functionalization by metathesis reaction
US8653209B2 (en) 2008-06-20 2014-02-18 Exxonmobil Chemical Patents Inc. High vinyl terminated propylene based oligomers
US8669330B2 (en) 2011-03-25 2014-03-11 Exxonmobil Chemical Patents Inc. Olefin triblock polymers via ring-opening metathesis polymerization
US8669326B2 (en) 2011-03-25 2014-03-11 Exxonmobil Chemical Patents Inc. Amine functionalized polyolefin and methods for preparation thereof
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