EP2688954A2 - Polymères triséquencés à base d'oléfines obtenus par polymérisation par ouverture de cycle par métathèse - Google Patents

Polymères triséquencés à base d'oléfines obtenus par polymérisation par ouverture de cycle par métathèse

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Publication number
EP2688954A2
EP2688954A2 EP12764275.9A EP12764275A EP2688954A2 EP 2688954 A2 EP2688954 A2 EP 2688954A2 EP 12764275 A EP12764275 A EP 12764275A EP 2688954 A2 EP2688954 A2 EP 2688954A2
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Prior art keywords
mol
hydrocarbyl
multiblock
polyolefin
composition
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EP12764275.9A
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German (de)
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EP2688954A4 (fr
Inventor
Ian C. STEWART
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ExxonMobil Chemical Patents Inc
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ExxonMobil Chemical Patents Inc
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Priority claimed from US13/072,432 external-priority patent/US8669330B2/en
Application filed by ExxonMobil Chemical Patents Inc filed Critical ExxonMobil Chemical Patents Inc
Priority to EP12764275.9A priority Critical patent/EP2688954A4/fr
Publication of EP2688954A2 publication Critical patent/EP2688954A2/fr
Publication of EP2688954A4 publication Critical patent/EP2688954A4/fr
Withdrawn legal-status Critical Current

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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
    • C08F32/00—Homopolymers and copolymers of cyclic compounds having no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system
    • 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
    • C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
    • C08F297/06—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type
    • C08F297/08—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type polymerising mono-olefins
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G61/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G61/02—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes
    • C08G61/04—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes only aliphatic carbon atoms
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G61/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G61/02—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes
    • C08G61/04—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes only aliphatic carbon atoms
    • C08G61/06—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes only aliphatic carbon atoms prepared by ring-opening of carbocyclic compounds
    • C08G61/08—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes only aliphatic carbon atoms prepared by ring-opening of carbocyclic compounds of carbocyclic compounds containing one or more carbon-to-carbon double bonds in the ring
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L65/00—Compositions of macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain; Compositions of derivatives of such polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G2261/10—Definition of the polymer structure
    • C08G2261/12—Copolymers
    • C08G2261/126—Copolymers block
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G2261/30—Monomer units or repeat units incorporating structural elements in the main chain
    • C08G2261/33—Monomer units or repeat units incorporating structural elements in the main chain incorporating non-aromatic structural elements in the main chain
    • C08G2261/332—Monomer units or repeat units incorporating structural elements in the main chain incorporating non-aromatic structural elements in the main chain containing only carbon atoms
    • C08G2261/3323—Monomer units or repeat units incorporating structural elements in the main chain incorporating non-aromatic structural elements in the main chain containing only carbon atoms derived from other monocyclic systems
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G2261/40—Polymerisation processes
    • C08G2261/41—Organometallic coupling reactions
    • C08G2261/418—Ring opening metathesis polymerisation [ROMP]

Definitions

  • This invention relates to metathesis preparation of triblock polymers from vinyl- terminated polyolefins.
  • Metathesis is generally thought of as the interchange of radicals between two compounds during a chemical reaction. There are several varieties of metathesis reactions, such as ring opening metathesis, acyclic diene metathesis, ring closing metathesis and cross metathesis.
  • Methods for the production of polyolefins with end-functionalized groups are typically multi-step processes that often create unwanted by-products and waste of reactants and energy.
  • metathesis reactions can provide functionalized polyolefins that have end-functionalization.
  • polymerize polyolefins having end-functionalization to each other it has not been feasible to polymerize polyolefins having end-functionalization to each other.
  • Triblock polymers prepared by metathesis from multiblocks of vinyl-terminated polyolefins feature a chemically reactive internal site of unsaturation and are of interest for use in a broad range of applications as compatibilizers, tie-layer modifiers, surfactants, and surface modifiers. Hydrogenation leads to unique triblock polymers that can be used in applications such as those noted for the unhydrogenated materials.
  • a novel method for their production by the metathesis of multiblocks of vinyl-terminated polyolefins is useful in a range of polyolefins, including isotactic polypropylene (iPP), atactic polypropylene (aPP), ethylene propylene copolymer (EP), and polyethylene (PE).
  • This invention relates to a composition
  • a composition comprising a multiblock polyolefin represented by the formula:
  • Z is the portion of a "cyclic monomer having at least one internal double bond" that remains after a ring-opening metathesis reaction, preferably a Q to hydrocarbyl or substituted hydrocarbyl;
  • PO and PO* are polyolefins, preferably PO and PO* are each, independently, a substituted or unsubstituted hydrocarbyl group having 9 to 10,000 carbon atoms; and n is 1 to about 10,000.
  • This invention also relates to multiblock polyolefins represented by the formula la that have been hydrogenated.
  • polyolefin as used herein means an oligomer or polymer of two or more olefin mer units and specifically includes oligomers and polymers as defined below.
  • An "olefin,” alternatively referred to as “alkene,” is a linear, branched, or cyclic compound of carbon and hydrogen having at least one double bond.
  • a higher olefin is an olefin having four or more carbon atoms.
  • Ethylene shall be considered an alpha-olefin.
  • a propylene polymer or oligomer contains at least 50 mol% of propylene, an ethylene polymer or oligomer contains at least 50 mol% of ethylene, and so on.
  • a polymer or copolymer when referred to as comprising an olefin, including, but not limited to ethylene, propylene, and butene, the olefin present in such polymer or copolymer is the polymerized form of the olefin.
  • a copolymer when a copolymer is said to have an "ethylene" content of 35 wt% to 55 wt%, it is understood that the mer unit in the copolymer is derived from ethylene in the polymerization reaction and said derived units are present at 35 wt% to 55 wt%, based upon the weight of the copolymer.
  • a “polymer” has two or more of the same or different mer units.
  • a “homopolymer” is a polymer having mer units that are the same.
  • a “copolymer” is a polymer having two or more mer units that are different from each other.
  • a “terpolymer” is a polymer having three mer units that are different from each other.
  • the term “different” as used to refer to mer units indicates that the mer units differ from each other by at least one atom or are different isomerically. Accordingly, the definition of copolymer, as used herein, includes terpolymers and the like.
  • An oligomer is typically a polymer having a low molecular weight (such an Mn of less than 25,000 g/mol, preferably less than 2,500 g/mol) or a low number of mer units (such as 75 mer units or less).
  • Mn is number average molecular weight (measured by ⁇ NMR unless stated otherwise)
  • Mw is weight average molecular weight (measured by Gel Permeation Chromatography)
  • Mz is z average molecular weight (measured by Gel Permeation Chromatography)
  • wt% is weight percent
  • mol% is mole percent.
  • Molecular weight distribution (MWD) is defined to be Mw (measured by Gel Permeation Chromatography) divided by Mn (measured by l R NMR). Unless otherwise noted, all molecular weight units (e.g., Mw, Mn, Mz) are g/mol.
  • Allyl chain ends (also referred to as “vinyl termination”, “vinyl chain ends” “allylic vinyl end group” or “vinyl content”) is defined to be a polyolefin (oligomer or polymer) having at least one terminus represented by formula I: allylic vinyl end group
  • the amount of allyl chain ends is determined using NMR at 120°C using deuterated tetrachloroethane as the solvent on a 500 MHz machine, and in selected cases confirmed by 13 C NMR.
  • Resconi has reported proton and carbon assignments (neat perdeuterated tetrachloroethane used for proton spectra while a 50:50 mixture of normal and perdeuterated tetrachloroethane was used for carbon spectra; all spectra were recorded at 100°C on a Bruker AM 300 spectrometer operating at 300 MHz for proton and 75.43 MHz for carbon) for vinyl terminated propylene oligomers in J American Chemical Soc, 1 14, 1992, pp. 1025- 1032 that are useful herein.
  • Isobutyl chain end also referred to as an “isobutyl end group” is defined to be a polyolefin (oligomer or polymer) having at least one terminus represented by the formula:
  • M represents the polyolefin (oligomer or polymer) chain.
  • isobut l chain end is represented by one of the following formulae:
  • M represents the polyolefin chain
  • the "isobutyl chain end to allylic vinyl group ratio" is defined to be the ratio of the percentage of isobutyl chain ends to the percentage of allylic vinyl groups.
  • inter unsaturation means a double bond that is not an allyl chain end as defined above, a vinylene, or vinylidene unsaturation.
  • diblock is defined to mean that there are at least two polyolefin different portions in the multiblock polyolefin, e.g., PO and PO* are different.
  • the term "different" as used to refer to polyolefins indicates that the mer units of the polyolefins differ from each other by at least one atom, the mer units of the polyolefins differ isomerically, or the polyolefins differ in Mn, Mw, Mz, tacticity, Mw/Mn, g'vis, vinyl, vinylidene, vinylene, or internal unsaturation content, amount of comonomer (when the comonomer is the same or different in the polyolefins), density (ASTM D 1505), melting point, heat of fusion, Brookfield viscosity, specific gravity (ASTM D 4052), or any other fluid or polyolefin property described in US 2008/0045638, paragraphs [0593] to [0636]
  • multiblock is defined to mean more than one polyolefin portion is present in the multiblock polyolefin.
  • the term "vinyl terminated polyolefin” also referred to as “vinyl terminated macromer” or “VTM” is defined to be a polyolefin (oligomer or polymer) having at least 30% allyl chain ends (relative to total unsaturation), preferably having an Mn of at least 300 g/mol, preferably from 500 to 100,000 g/mol.
  • substituted means that a hydrogen group has been replaced with a hydrocarbyl group, a heteroatom or a heteroatom containing group.
  • methyl cyclopentadiene (Cp) is a Cp group substituted with a methyl group and ethyl alcohol is an ethyl group substituted with an -OH group.
  • hydrocarbyl radical is used interchangeably throughout this document.
  • group and “substituent” are also used interchangeably in this document.
  • hydrocarbyl radical is defined to be C C2o radicals, that may be saturated or unsaturated, linear, branched, or cyclic (aromatic or non-aromatic); and include substituted hydrocarbyl radicals as defined below.
  • Substituted hydrocarbyl radicals are radicals in which at least one hydrogen atom has been substituted with a heteroatom or heteroatom containing group, preferably with at least one functional group, such as halogen (CI, Br, I, F), R*2, OR*, SeR*, TeR*, PR*2, AsR* 2 , SbR* 2 , SR*, BR* 2 , SiR* 3 , GeR* 3 , SnR* 3 , PbR* 3 , and the like or where at least one heteroatom has been inserted within the hydrocarbyl radical, such as halogen (CI, Br, I, F), O, S, Se, Te, NR*, PR*, AsR*, SbR*, BR*, SiR* 2 , GeR* 2 , SnR* 2 , PbR* 2 , and the like, where R* is, independently, hydrogen or a hydrocarbyl.
  • halogen CI, Br, I, F
  • a " substituted alkyl” or “substituted aryl” group is an alkyl or aryl radical made of carbon and hydrogen where at least one hydrogen is replaced by a heteroatom, a heteroatom containing group, or a linear, branched, or cyclic substituted or unsubstituted hydrocarbyl group having 1 to 30 carbon atoms.
  • reactive termini is meant a polymer having a vinyl, vinylidene, vinylene or other terminal group that can be polymerized into a growing polymer chain.
  • Me is methyl
  • Ph is phenyl
  • Et is ethyl
  • Pr is propyl
  • iPr is isopropyl
  • n-Pr normal propyl
  • Bu is butyl
  • iBu is isobutyl
  • tBu is tertiary butyl
  • p-tBu is para-tertiary butyl
  • nBu is normal butyl
  • TMS is trimethylsilyl
  • TIBAL is triisobutylaluminum
  • TNOAL is triisobutyl n- octylaluminum
  • MAO is methylalumoxane
  • pMe is para-methyl
  • Ar* is 2,6-diisopropylaryl
  • Bz is benzyl
  • THF is tetrahydrofuran
  • RT room temperature
  • tol is toluene.
  • This invention relates multiblock polyolefins and processes to prepare a multiblock polyolefin represented by the formula:
  • Z is the portion of a cyclic monomer having at least one internal double bond that remains after a ring-opening metathesis reaction, preferably Z is a Q to hydrocarbyl or substituted hydrocarbyl (including olefins and substituted olefins), preferably a C to hydrocarbyl or substituted hydrocarbyl, preferably a Q to hydrocarbyl or substituted hydrocarbyl (preferably the substituent on the substituted hydrocarbyl is a C [ to C 5 hydrocarbyl or a Cj to C5 substituted hydrocarbyl (such as methyl, ethyl, propyl, butyl, pentyl or an isomer thereof), a halogen (such as Br, CI, I or F), an ether or ester (such as an alkyl ether, an alkyl ester, an aryl ether or an aryl ester, where the alkyl is a Q to C20 alkyl group and the aryl is a
  • PO and PO* are polyolefins, preferably PO and PO* are each, independently, a substituted or unsubstituted hydrocarbyl group having 9 to 10,000 carbon atoms (preferably 20 to 7500 carbon atoms, preferably 30 to 4000, preferably from 40 to 2000), preferably at least one of PO and PO* has from 20 to 10,000 carbon atoms, preferably 30 to 2000; and
  • n is 1 to about 10,000, in particular from about 10 to about 7500, more particularly from about 50 to about 5000 and in one aspect from about 100 to about 2000.
  • a preferred embodiment, for the multiblock polyolefin of formula (I), has PO and PO* being different.
  • An example of this would be having PO being isotactic PP and PO* being an EP copolymer, with the ethylene content in the PO* being about 50% by weight.
  • a preferred embodiment for the multiblock polyolefin of formula (X) has PO and PO* being different, with PO being immiscible with PO*. By immiscible is meant that if the vinyl terminated polyolefins that became PO and PO* were blended together they would form a heterogeneous composition.
  • homogeneous composition a composition having substantially one morphological phase.
  • a co-continuous morphology is considered a single state for purposes of this invention and the claims thereto.
  • a blend of two polymers where one polymer is miscible with another polymer is said to be homogeneous in the solid state.
  • Such morphology is determined using optical microscopy, scanning electron microscopy (SEM) or atomic force microscopy (AFM), in the event the optical microscopy, SEM and AFM provide different data, then the SEM data shall be used.
  • SEM scanning electron microscopy
  • AFM atomic force microscopy
  • two separate phases would be observed for an immiscible blend.
  • a miscible blend is homogeneous, while an immiscible blend is heterogeneous.
  • PO and PO* comprise about 15 wt% to about 95 wt% ethylene and have more than 80% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 30 wt% to about 95 wt% ethylene and have more than 70% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 30 wt% to about 95 wt% ethylene and have more than 90% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 15 wt% to about 95 wt% propylene and have more than 80% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 30 wt% to about 95 wt% propylene and have more than 70% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 30 wt% to about 95 wt% propylene and have more than 90% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 15 wt% to about 95 wt% ethylene-propylene copolymer and have more than 80% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 30 wt% to about 95 wt% ethylene-propylene copolymer and have more than 70% allyl chain ends (relative to total unsaturations).
  • PO and PO* comprise about 30 wt% to about 95 wt% ethylene-propylene copolymer and have more than 90% allyl chain ends (relative to total unsaturations).
  • the multiblock polyolefin has an average of about 0.75 to about 4.0 internal unsaturation sites per polyolefin chain, as determined by NMR of the polyolefin for multiblock polymers having an Mn of up to 60,000 g/mol as determined by NMR.
  • the multiblock polyolefin is hydrogenated and the multiblock polyolefin has an average of less than 1.25 internal unsaturation sites per polyolefin chain, as determined by NMR of the polyolefin for multiblock polymers having an Mn of up to 60,000 g/mol as determined by l R NMR.
  • PO* is PO and/or PO is PO*.
  • the multiblock polyolefin is polyolefin is a mixture of at least three forms of formula I, for example: the multiblock polyolefin can be a mixture of:
  • the mixture of I, II and III comprises about 30% to about 70% of multiblock polyolefin (I), about 1% to about 30% of multiblock polyolefin (II), and about 1% to about 30% multiblock polyolefin (III).
  • the multiblock polyolefin is polyolefin is a mixture of at least three forms of formula la, for example: the multiblock polyolefin can be a mixture of:
  • the mixture of la, Ila, and Ilia comprises about 30% to about 70% of multiblock polyolefin (la), about 1% to about 30% of multiblock polyolefin (Ila), and about 1% to about 30% multiblock polyolefin (Ilia), where Z, PO, PO*, and n are as described above.
  • PO and PO* may be the same or different.
  • the multiblock polyolefin mixture of I, II, and III or of la, Ila, and Ills may be fractionated into the three individual components (I), (II), and (III) or la, Ila, or Ilia using preparative fractionation by dissolution or crystallization temperature, which includes preparative temperature rising elution fractionation (Prep-TREF) and related methods (e.g., using a PREP-mc2 instrument from Polymer ChAR in the TREF or CRYSTAF mode).
  • Prep-TREF preparative temperature rising elution fractionation
  • related methods e.g., using a PREP-mc2 instrument from Polymer ChAR in the TREF or CRYSTAF mode.
  • Mn of PO and PO* are significantly different, then three individual components may be separated by preparative fractionation by molecular weight, which includes using a solvent- nonsolvent extraction or precipitation method (e.g., using the PREP-mc2 instrument from Polymer ChAR in the MW mode).
  • a solvent- nonsolvent extraction or precipitation method e.g., using the PREP-mc2 instrument from Polymer ChAR in the MW mode.
  • the fraction of intermediate crystallinity will also have a number average molecular weight (Mn), as determined by gel permeation chromatography with a triple detector (GPC-3D), that is intermediate to the Mn of each of the other two fractions.
  • Mn number average molecular weight
  • Typical separations can be accomplished when the elution temperature of the intermediate crystalline fraction is at least 5°C, in particular about 10°C, more particularly 20°C different than the elution temperature of each of the other two fractions.
  • the various components of the multiblock polyolefin can be separated from each other (e.g., (I) can be separated from (II) and (III)) using the preparative TREF procedure below.
  • the fraction containing the largest mass is selected (and is presumed to be the multiblock polyolefin produced herein) and subjected to characterization, such as DSC (as described below).
  • the multiblock polyolefin shows two or more peak melting temperatures (Tm), preferably three Tm's, according to the DSC and the Tm's are different by at least 5°C each from the other, preferably by at least 10°C, preferably by at least 20°C, preferably by at least 30°C, preferably by at least 40°C, preferably by at least 50°C, preferably by at least 60°C, preferably by at least 70°C, preferably by at least 80°C.
  • Tm peak melting temperatures
  • the multiblock polyolefin shows at least two crystallization temperatures (Tc) according to the DSC, preferably three Tc's, and the Tc's are different by at least 5°C each from the other, preferably by at least 10°C, preferably by at least 20°C, preferably by at least 30°C, preferably by at least 40°C, preferably by at least 50°C, preferably by at least 60°C, preferably by at least 70°C, preferably by at least 80°C.
  • Tc crystallization temperatures
  • the heat of fusion (Hf), determined by DSC, of the multiblock polyolefin is between the Hfs of the starting dimer polyolefins.
  • the Hf of the multiblock polyolefin e.g., the selected fraction with the largest mass
  • the Hf of the multiblock polyolefin is at least 5 J/g different than the Hf of the starting dimer polyolefin (if two or more dimers are used, then the Hf of the dimer having the highest Hf is used), preferably at least 10 J/g different, preferably at least 20 J/g different, preferably at least 50 J/g different, preferably at least 80 J/g different.
  • the Hf of the multiblock polyolefin (e.g., the selected fraction with the largest mass) is at least 5 J/g less than the Hf of the starting dimer polyolefin having the highest Hf, preferably at least 10 J/g less, preferably at least 20 J/g less, preferably at least 30 J/g less, preferably at least 40 J/g less, preferably at least 50 J/g less, preferably at least 60 J/g less, preferably at least 70 J/g less, preferably at least 80 J/g less, preferably at least 90 J/g less.
  • the comonomer content of the multiblock polyolefin is at least 5 mol% different than the comonomer content of the starting dimer polyolefin (if two or more dimers are present then the dimer having the highest comonomer content is used for this comparison), preferably at least 10 mol% different, preferably at least 20 mol% different, preferably at least 30 mol% different, preferably at least 40 mol% different.
  • a homopolymer shall be considered to have 0 mol% comonomer.
  • Comonomer content can be measured by Fourier Transform Infrared Spectroscopy (FTIR) in conjunction with samples collected by GPC as described in Wheeler and Willis, Applied Spectroscopy, 1993, vol. 47, pp. 1128-1 130.
  • FTIR Fourier Transform Infrared Spectroscopy
  • a commercial preparative TREF instrument (Model MC2, Polymer Char S.A.) is used to fractionate the resin into Chemical Composition Fractions. Approximately 2 g of polymer is placed into a reactor and dissolved in 200 mL of xylene, stabilized with 600 ppm of BHT, at 130°C for approximately 60 minutes. The mixture is allowed to equilibrate for 45 minutes at 90°C, and then cooled to either 30°C (standard procedure) or 15°C (cryo procedure) using a cooling rate of 0.1°C/min. The temperature of the cooled mixture is increased until it is within the lowest Isolation Temperature Range to be used (see Table 2) and the mixture is heated to maintain its temperature within the specified range for 20 minutes.
  • the mixture is sequentially filtered through a 75 micron column filter and then a 2 micron disk filter using 10 psi to 50 psi of pressurized nitrogen.
  • the reactor is washed twice with 50 ml of xylene heated to maintain the temperature of the wash mixture within the designated temperature range and held at that temperature for 20 minutes during each wash cycle.
  • the fractionation process is continued by introducing fresh xylene (200 mL of xylene, stabilized with 600 ppm of BHT) into the reactor, increasing the temperature of the mixture until it reaches the next highest Isolation Temperature Range in the sequence indicated in Table 2 and heating the mixture to maintain its temperature within the specified range for 20 minutes prior to filtering it as described above.
  • the extraction cycle is sequentially repeated in this manner until the mixture has been extracted at all Isolation Temperature Ranges shown in Table 2.
  • the extracts are independently precipitated with methanol to recover the individual polymer fractions. Table 2
  • the Isolation Temperature Range for the Standard Procedure is 0 to 36°C
  • the multiblock polyolefin has an Mn of up to 200,000 g/mol, preferably from 400 to 120,000 g/mol, preferably 1000 to about 60,000 g/mol, preferably 10,000 to 45,000 g/mol, preferably from 20,000 to 42,000 g/mol, preferably about 40,000 g/mol, alternately about 20,000 alternately about 1000 g/mol.
  • PO is has an Mn of greater than 300, preferably from 400 to 120,000, preferably from 500 to 100,000, preferably form 600 to 60,000 g/mol.
  • PO is a polypropylene of a Mn of about 300 to about 20,000 g/mol or PO is an ethylene/propylene copolymer of a Mn of about 300 to about 20,000 g/mol.
  • at least one of the substituted or unsubstituted hydrocarbyl groups of PO and PO* contain from about 2 to about 18 carbon atoms.
  • the PO is tactic, preferably isotactic, alternately syndiotactic.
  • Particularly useful PO and PO*'s may be isotactic, highly isotactic, syndiotactic, or highly syndiotactic propylene polymer, particularly isotactic polypropylene.
  • isotactic is defined as having at least 10% isotactic pentads, preferably having at least 40% isotactic pentads of methyl groups derived from propylene according to analysis by 13 C-NMR.
  • “highly isotactic” is defined as having at least 60% isotactic pentads according to analysis by 13 C-NMR.
  • PO* and/or the vinyl terminated polyolefins used to produce PO and PO* have at least 85% isotacticity.
  • “syndiotactic” is defined as having at least 10% syndiotactic pentads, preferably at least 40%, according to analysis by 13 C-NMR.
  • “highly syndiotactic” is defined as having at least 60% syndiotactic pentads according to analysis by 13 C-NMR.
  • PO, and/or PO* and/or the vinyl terminated polyolefins used to produce PO and PO* have has at least 85% syndiotacticity.
  • PO is a polypropylene of a Mn of about 300 to about 20,000 g/mol and PO * is not a polypropylene.
  • This invention presumes that PO and PO* are derived from dimers of one or more vinyl terminated polyolefins used to make the dimers that are used to make the multiblock polyolefins.
  • the multiblock polyolefin is a liquid at 25°C.
  • the multiblock polyolefin has a viscosity index (ASTM 2270) of 120 or more, alternately 130 or more, alternately 150 or more, alternately 200 or more, alternately 250 or more, alternately 300 or more.
  • the multiblock polyolefins described herein have a viscosity at 60°C of greater than 1000 cP, greater than 12,000 cP, or greater than 100,000 cP. In other embodiments, the multiblock polyolefins have a viscosity of less than 200,000 cP, less than 150,000 cP, or less than 100,000 cP. Viscosity is measured using a Brookfield Digital Viscometer.
  • one or both of PO and PO* are not a polyaromatic monomer material, such as polystyrene.
  • PO and PO* comprise less than 0.1 wt% aromatic monomer, such as a vinyl aromatic, such as styrene or derivatives thereof.
  • the multiblock polyolefin produced herein comprises less than 0.1 wt% aromatic monomer (such as styrene), preferably 0 wt%.
  • the polyolefin multiblock product containing internal unsaturation such as those described by Formulae I, II, or III can be catalytically hydrogenated using typical conditions to afford a fully saturated polyolefin product of interest due to increased stability toward unwanted oxidation and other chemical reactions. Hydrogenation may be performed in the melt state, in solution, or as a slurry in the presence of 0.01 to 100 MPa of hydrogen and a suitable hydrogenation catalyst, such as Group 8 through 10 supported metals. [0065] In another embodiment, any of the multiblock polyolefins described herein may be hydrogenated.
  • the multiblock polyolefin is optionally treated to reduce heteroatom containing compounds to less than 600 ppm, and then contacted with hydrogen and a hydrogenation catalyst to produce a multiblock polyolefins having a bromine number less than 1.8.
  • the treated multiblock polyolefins comprises 100 ppm of heteroatom containing compounds or less, preferably 50 ppm of heteroatom containing compounds or less.
  • a heteroatom containing compound is a compound containing at least one atom other than carbon and hydrogen.
  • the hydrogenation catalyst is selected from the group consisting of supported Group 7, 8, 9, and 10 metals, preferably the hydrogenation catalyst selected from the group consisting of one or more of i, Pd, Pt, Co, Rh,-74-Fe, Ru, Os, Cr, Mo, and W, supported on silica, alumina, clay, titania, zirconia, or mixed metal oxide supports.
  • a preferred hydrogenation catalsyt is nickel supported on kieselguhr, or platinum or palladium supported on alumina, or cobalt- molydenum supported on alumina.
  • a high nickel content catalyst such as 60% Ni on Keiselguhr catalyst is used, or a supported catalyst with high amount of Co-Mo loading.
  • the hydrogenation catalyst is nickel supported on keisleghur, silica, alumina, clay or silica-alumina.
  • the multiblock polyolefin is contacted with hydrogen and a hydrogenation catalyst at a temperature from 25 to 350°C, preferably 100 to 300°C. In another preferred embodiment the multiblock polyolefin is contacted with hydrogen and a hydrogenation catalyst for a time period from 5 minutes to 100 hours, preferably from 5 minutes to 24 hours. In another preferred embodiment, the multiblock polyolefin is contacted with hydrogen and a hydrogenation catalyst at a hydrogen pressure of from 25 psi to 2500 psi, preferably from 100 to 2000 psi.
  • This hydrogenation process can be accomplished in a slurry reactor in a batch operation or in a continuous stirred tank reactor (CSTR), where the catalyst in 0.001 wt% to 20 wt% of the multiblock polyolefin feed or preferably 0. 01 to 10 wt%, hydrogen and the multiblock polyolefins are continuously added to the reactor to allow for certain residence time, usually 5 minutes to 10 hours to allow complete hydrogenation of the unsaturated olefins.
  • the amount of catalyst added is usually very small just to compensate for the catalyst deactivation.
  • the catalyst and hydrogenated multiblock polyolefins are continuously withdrawn from the reactor.
  • the product mixture is then filtered, centrifuged or settled to remove the solid hydrogenation catalyst.
  • the catalyst can be regenerated and reused.
  • the hydrogenated multiblock polyolefins can be used as is or further distilled.
  • any of the multiblock polyolefins produced herein are hydrogenated and have a Bromine number of 1.8 or less as measured by ASTM D 1 159 (or ASTM 2710 if so directed by ASTM D 1159), preferably 1.7 or less, preferably 1.6 or less, preferably 1.5 or less,-15-preferably 1.4 or less, preferably 1.3 or less, preferably 1. 2 or less, preferably 1.1 or less, preferably 1.0 or less, preferably 0.5 or less, preferably 0.1 or less.
  • the multiblock polyolefins produced herein may be used in a broad range of applications, such as compatibilizers, tie-layer modifiers, surfactants, surface modifiers, lubricants, detergents, flocculants, viscosity modifiers, Viscosity Index modifiers, emulsifiers, de-emulsifiers, dispersants, plasticizers, surfactants for soaps, detergents, fabric softeners, antistatics, oil additives, anti-fogging or wetting additives, adhesion promoters, adhesives, additives for lubricants and/or fuels, thermoplastic elastomers, thermoplastics, elastomers, and the like.
  • the multiblock polyolefins produced herein may be used in blends and article of manufacture, such as films, fibers, nonwovens, or molded articles (injection molded and/or blow molded), such as those described in paragraphs [0197 to 0257] of US 2004/0106723.
  • the invention also provides suitable methods to prepare multiblock polyolefins of formula (I) comprising contacting an alkene metathesis catalyst, and a cyclic hydrocarbyl monomer comprising at least one internal double bond with dimer(s) of vinyl terminated polyolefin(s) (VTP), each vinyl terminated polyolefins having at least 30% allyl chain ends, relative to total unsaturations (preferably least 40%, preferably at least 50%, preferably at least 60%, preferably at least 65%, preferably at least 75%, preferably at least 80%, preferably at least 85%, preferably at least 90%, preferably at least 95%).
  • the dimer(s) may be dimers of the same VTP or may be dimers of 2, 3, 4 or more VTP's, preferably one or two. For example, if two VTP's (A and B) are used, the dimer(s) may be A-A, A-B, B-B; or if three VTP's (A, B and C) are used then the dimer(s) may be A-A, A-B, A-C, B-B, B-C, C-C; or if four VTP's (A, B, C and D) are used, then the dimer(s) may be A-A, A-B, A-C, A-D, B- B, B-C, B-D, C-C, C-D, D-D, etc.
  • the reactants are typically combined in a reaction vessel at a temperature of 20 to 200°C (preferably 50 to 160°C, preferably 60 to 140°C) and a pressure of 1 Pa to 1000 MPa (preferably 0.5 to 500 MPa, preferably 1 to 250 MPa) for a residence time of 0.5 seconds to 10 hours (preferably 1 second to 5 hours, preferably 1 minute to 1 hour).
  • 0.00001 to 0.1 moles, preferably 0.0001 to 0.02 moles, preferably 0.0005 to 0.01 moles of catalyst are charged to the reactor per mole of dimer charged.
  • from about 0.7 to about 4.0 (e.g., 0.8 to 2.6), preferably from about 1.0 to about 2.0, and most preferably from about 1.1 to about 1.7 moles of cyclic hydrocarbyl monomer comprising at least 1 internal double bond are charged to the reactor per mole of dimer charged.
  • the ratio of moles of cyclic hydrocarbon monomer to moles of dimer charged to the reactor are > 1 : 1, preferably 50: 1, preferably 100: 1, preferably 200: 1.
  • the process is typically a solution process, although it may be a bulk or high pressure process. Homogeneous processes are preferred. (A homogeneous process is defined to be a process where at least 90 wt% of the product is soluble in the reaction media.)
  • a bulk homogeneous process is particularly preferred.
  • a bulk process is defined to be a process where reactant concentration in all feeds to the reactor is 70 volume % or more.
  • Suitable diluents/solvents for the process include non-coordinating, inert liquids.
  • Examples include straight and branched-chain hydrocarbons, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof such as can be found commercially (IsoparTM); perhalogenated hydrocarbons, such as perfluorinated C4 0 alkanes, chlorobenzene, and aromatic and alkylsubstituted aromatic compounds, such as benzene, toluene, mesitylene, and xylene.
  • straight and branched-chain hydrocarbons such as isobutane,
  • aliphatic hydrocarbon solvents are preferred, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof.
  • the solvent is not aromatic, preferably aromatics are present in the solvent at less than 1 wt%, preferably at 0.5 wt%, preferably at 0 wt% based upon the weight of the solvents.
  • the process is a slurry process.
  • slurry polymerization process means a polymerization process where a supported catalyst is employed and monomers are polymerized on the supported catalyst particles. At least 95 wt % of polymer products derived from the supported catalyst are in granular form as solid particles (not dissolved in the diluent).
  • the feed concentration for the process is 60 volume % solvent or less, preferably 40 volume % or less, preferably 20 volume % or less.
  • the process may be batch, semi-batch, or continuous.
  • continuous means a system that operates without interruption or cessation.
  • a continuous process to produce a polymer would be one where the reactants are continually introduced into one or more reactors and polymer product is continually withdrawn.
  • Useful reaction vessels include reactors (including continuous stirred tank reactors, batch reactors, reactive extruder, pipe or pump).
  • the productivity of the process is at least 200 g of multiblock polyolefin of formula (I) per mmol of catalyst per hour, preferably at least 5000 g/mmol/hour, preferably at least 10,000 g/mmol/hr, preferably at least 300,000 g/mmol/hr.
  • a "reaction zone” also referred to as a "polymerization zone” is defined as an area where activated catalysts and monomers are contacted and a polymerization reaction takes place.
  • each reactor is considered as a separate polymerization zone.
  • each polymerization stage is considered as a separate polymerization zone. Room temperature is 23 °C unless otherwise noted.
  • This invention further relates to a process, preferably an in-line process, preferably a continuous process, to produce multiblock polyolefin of formula (I), comprising introducing monomer and catalyst system into a reactor, obtaining a reactor effluent containing vinyl terminated polyolefins, optionally removing (such as flashing off) solvent, unused monomer and/or other volatiles, obtaining two vinyl terminated polyolefins (such as those described herein), introducing vinyl terminated polyolefins and alkene metathesis catalyst into a reaction zone, obtaining dimer of vinyl terminated polyolefins; introducing said dimer, cyclic monomer having at least one unsaturation and an alkene metathesis catalyst into a reaction zone, (such as a reactor, an extruder, a pipe, and/or a pump) and obtaining multiblock polyolefin of formula (I) (such as those described herein), thereafter optionally hydrogenating the multiblock polyolefin of formula (I), thereafter
  • the alkene metathesis catalysts described herein are compounds that catalyze: 1) the reaction between a first vinyl terminated polyolefin with a second vinyl terminated polyolefin to produce a dimer, typically with the elimination of ethylene; or 2) the reaction between the dimers with a cyclic monomer having at least one unsaturation to produce the multiblock polyolefins described herein.
  • the alkene metathesis catalyst is represented by the Formula (IA):
  • M is a Group 8 metal, preferably Ru or Os, preferably Ru;
  • X and X 1 are, independently, any anionic ligand, preferably a halogen (preferably CI), an alkoxide or a triflate, or X and X 1 may be joined to form a dianionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non- hydrogen atoms;
  • L and L 1 are, independently, a neutral two electron donor, preferably a phosphine or a N- heterocyclic carbene, L and L 1 may be joined to form a single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • L and X may be joined to form a multidentate monoanionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • L 1 and X 1 may be joined to form a multidentate monoanionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • R and R 1 are, independently, hydrogen or Q to C30 substituted or unsubstituted hydrocarbyl (preferably a C to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl);
  • R 1 and L 1 or X 1 may be joined to form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • R and L or X may be joined to form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms.
  • Preferred alkoxides include those where the alkyl group is a phenol, substituted phenol (where the phenol may be substituted with up to 1, 2, 3, 4, or 5 Q to (3 ⁇ 4 hydrocarbyl groups) or a to C ⁇ o hydrocarbyl, preferably a to C ⁇ Q alkyl group, preferably methyl, ethyl, propyl, butyl, or phenyl.
  • Preferred triflates are represented by the Formula (IIA):
  • R 2 is hydrogen or a Q to C30 hydrocarbyl group, preferably a Ci to alkyl group, preferably methyl, ethyl, propyl, butyl, or phenyl.
  • N-heterocyclic carbenes are represented by the Formula (IIIA) or the
  • each R 4 is independently a hydrocarbyl group or substituted hydrocarbyl group having 1 to 40 carbon atoms, preferably methyl, ethyl, propyl, butyl (including isobutyl and n-butyl), pentyl, cyclopentyl, hexyl, cyclohexyl, octyl, cyclooctyl, nonyl, decyl, cyclodecyl, dodecyl, cyclododecyl, mesityl, adamantyl, phenyl, benzyl, tolulyl, chlorophenyl, phenol, substituted phenol, or CH 2 C(CH 3 ) 3 ; and
  • each R 5 is hydrogen, a halogen, or a Q to (3 ⁇ 4 hydrocarbyl group, preferably hydrogen, bromine, chlorine, methyl, ethyl, propyl, butyl, or phenyl.
  • one of the N groups bound to the carbene in formula (IIIA) or (IV A) is replaced with an S, O or P atom, preferably an S atom.
  • N-heterocyclic carbenes include the compounds described in Hermann, W. A. Chem. Eur. J. 1996, 2, pp. 772 and 1627; Enders, D. et al. Angew. Chem. Int. Ed. 1995, 34, pg. 1021 ; Alder R. W., Angew. Chem. Int. Ed. 1996, 35, pg. 1121 ; and Bertrand, G. et al. Chem. Rev. 2000, 100, pg. 39.
  • the alkene metathesis catalyst is one or more of tricyclohexylphosphine[l,3-bis(2,4,6-trimethylphenyl)imidazol-2-ylidene][3-phenyl-lH- inden-l-ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[3 -phenyl- lH-inden-1 - ylidene][l,3-bis(2,4,6-trimethylphenyl)-4,5-dihydro-imidazol-2-ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[l,3-bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2- ylidene] [(phenylthio)methylene]ruthenium(II) dichloride, bis(tricyclohexylphosphine
  • the alkene metathesis catalyst is represented in Formula (IA) above, where: M is Os or Ru; R 1 is hydrogen; X and X 1 may be different or the same and are any anionic ligand; L and L 1 may be different or the same and are any neutral electron donor; and R may be hydrogen, substituted or unsubstituted alkyl, or substituted or unsubstituted aryl.
  • R is preferably hydrogen, alkyl, or aryl.
  • the C C2o alkyl may optionally be substituted with one or more aryl, halide, hydroxy, C C2o alkoxy, or C2-C20 alkoxycarbonyl groups.
  • the aryl may optionally be substituted with one or more C C2o alkyl, aryl, hydroxyl, Ci ⁇ C 5 alkoxy, amino, nitro, or halide groups.
  • L and L 1 are preferably phosphines of the formula PR 3 ' R 4 ' R 5 ', where R 3 ' is a secondary alkyl or cycloalkyl, and R 4 ' and R 5 ' are aryl, C C ⁇ o primary alkyl, secondary alkyl, or cycloalkyl.
  • R 4 ' and R 5 ' may be the same or different.
  • L and L 1 preferably the same and are -P(cyclohexyl)3, -P(cyclopentyl)3, or -P(isopropyl)3.
  • X and X 1 are most preferably the same and are chlorine.
  • the ruthenium and osmium carbene compounds have the Formula (V):
  • R 9 and R 10 may be different or the same and may be hydrogen, substituted or unsubstituted alkyl, or substituted or unsubstituted aryl.
  • the R 9 and R 10 groups may optionally include one or more of the following functional groups: alcohol, thiol, ketone, aldehyde, ester, ether, amine, imine, amide, nitro, carboxylic acid, disulfide, carbonate, isocyanate, carbodiimide, carboalkoxy, and halogen groups.
  • Such compounds and their synthesis are described in U.S. Patent No. 6, 1 11,121.
  • the alkene metathesis catalyst useful herein may be any of the catalysts described in U.S. Patent Nos. 6, 11 1,121 ; 5,312,940; 5,342,909; 7,329,758; 5,831, 108; 5,969, 170; 6,759,537; 6,921,735; and U.S. Publication No.
  • 2005-0261451 Al including, but not limited to, benzylidene-bis(tricyclohexylphosphine)dichlororuthenium, benzylidene[l,3- bis(2,4,6-trimethylphenyl)-2- imidazolidinylidene] dichloro(tricyclohexylphosphine)ruthenium, dichloro(o- isopropoxyphenylmethylene)(tricyclohexylphosphine)ruthenium(II), (l,3-Bis-(2,4,6- trimethylphenyl)-2-imidazolidinylidene)dichloro(o-isopropoxyphenylmethylene)ruthenium, l,3-Bis(2-methylphenyl)-2-imidazolidinylidene]dichloro(2-isopropoxyphenylmethylene) ruthenium(II), [l,3-Bis(2,4,6-trimethylphenyl)-2
  • the alkene metathesis catalyst is represented by the formula:
  • M* is a Group 8 metal, preferably Ru or Os, preferably Ru;
  • X* and X 1 * are, independently, any anionic ligand, preferably a halogen (preferably C j ), an alkoxide or an alkyl sulfonate, or X and X 1 may be joined to form a dianionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • L* is N, O, P, or S, preferably N or O;
  • R* is hydrogen or a to C30 hydrocarbyl or substituted hydrocarbyl, preferably methyl;
  • R 1 *, R 2 *, R 3 *, R 4 *, R 5 *, R 6 *, R 7 *, and R 8 * are, independently, hydrogen or a C ⁇ to C 30 hydrocarbyl or substituted hydrocarbyl, preferably methyl, ethyl, propyl or butyl, preferably R 1 *, R 2 *, R 3 *, and R 4 * are methyl;
  • each R 9 * and R 13 * are, independently, hydrogen or a Q to C30 hydrocarbyl or substituted hydrocarbyl, preferably a C2 to hydrocarbyl, preferably ethyl;
  • R 10 *, R 1 1 *, R 12 * are, independently hydrogen or a to C30 hydrocarbyl or substituted hydrocarbyl, preferably hydrogen or methyl;
  • each G is, independently, hydrogen, halogen or Q to C30 substituted or unsubstituted hydrocarbyl (preferably a Q to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl);
  • any two adjacent R groups may form a single ring of up to 8 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms.
  • any two adjacent R groups may form a fused ring having from 5 to 8 non hydrogen atoms.
  • the non-hydrogen atoms are C and/or O.
  • the adjacent R groups form fused rings of 5 to 6 ring atoms, preferably 5 to 6 carbon atoms.
  • adjacent is meant any two R groups located next to each other, for example R 3 * and R 4 * can form a ring and/or R 1 !* and R 12 * can form a ring.
  • the metathesis catalyst compound comprises one or more of: 2-(2,6-diethylphenyl)-3,5,5,5-tetramethylpyrrolidine[2-(i-propoxy)-5-(N,N- dimethylaminosulfonyl)phenyl]methylene ruthenium dichloride; 2-(mesityl)-3, 3,5,5- tetramethylpyrrolidine[2-(i-propoxy)-5-(N,N-dimethylaminosulfonyl)phenyl]methylene ruthenium dichloride; 2-(2-isopropyl)-3,3,5,5-tetramethylpyrrolidine[2-(i-propoxy)-5-(N,N- dimethylaminosulfonyl)phenyl]methylene ruthenium dichloride; 2-(2,6-diethyl-4- fluorophenyl)-3,3,5,5-tetramethylpyrrolidine[2-(i-propoxy)-5-(N,N- dimethyl
  • catalysts are generally available from Sigma-Aldrich Corp. (St. Louis, MO) or Strem Chemicals, Inc. (Newburyport, MA).
  • Suitable cyclic hydrocarbyl monomers having at least one internal double bond include C3 through C20 cyclic hydrocarbyl monomers that have one or more internal double bonds.
  • the cyclic hydrocarbyl monomer can be substituted or unsubstituted.
  • Suitable substituents include Ci through C5 hydrocarbyl substituents, such may also be substituted (such as methyl, ethyl, propyl, butyl, pentyl, and isomers thereof), halogen atoms (such as Br, CI, I, or F), ether substituents, and the like.
  • Preferred cyclic hydrocarbyl monomers include a C3 to C20 hydrocarbyls or substituted hydrocarbyls, preferably C3 to C 14 hydrocarbyls or substituted hydrocarbyls, preferably C3 to C ⁇ hydrocarbyls or substituted hydrocarbyls (preferably the substituent on the substituted hydrocarbyl is a Q to C 5 hydrocarbyl or a Q to C 5 substituted hydrocarbyl (such as methyl, ethyl, propyl, butyl, pentyl, or an isomer thereof), a halogen (such as Br, CI, I, or F) or an ether (such as an alkyl ether or an aryl ether), where the alkyl is a Q to C20 alkyl group and the aryl is a C ⁇ to C20 aryl group, preferably methyl ether, ethyl ether, methyl ethyl ether, butyl ether, propyl ether, and
  • Preferred cyclic hydrocarbyl monomers include bi cyclic and tricylic monomers.
  • Preferred cyclic hydrocarbyl monomers include, for example, cyclopropene, cyclobutene, cyclopentene, cyclohexene, methylcyclohexene, cycloheptene, cyclooctadiene, cyclooctene, norbornadiene, norbornene, cyclobutadiene, cyclohexadiene, cycloheptadiene, cyclooctatetraene, 1,5-cyclooctadiene, l,5-dimethyl-l,5-cyclooctadiene, dicyclopentadiene, and isomers thereof.
  • internal double bond is meant that the double bond is within the cyclic structure and is not pendent thereto.
  • vinyl cyclohexane is not a cyclic hydrocarbyl monomers having at least one internal double bond
  • cyclohexene is a cyclic hydrocarbyl monomers having at least one internal double bond.
  • PO and PO* are any combination described herein.
  • dimer when used, it means two mer units which may be the same or different, e.g., PO and PO* may be the same or different.
  • PO and PO* are each, independently, polyolefins, preferably derived from vinyl terminated polyolefins, preferably PO and PO* are each, independently, a substituted or unsubstituted hydrocarbyl group having 9 to 4000 carbon atoms, provided that at least one of PO and PO* are C 20 or greater, said dimer having:
  • an Mn ratio "Z” 0.1 to 10, preferably 0.25 to 4, preferably 0.5 to 2, preferably 0.75 to 1.5, where Z is the Mn (as determined by 13 C NMR) divided by Mn (as determined according to Gel Permeation Chromotography using polystyrene standards); and
  • J is the number of reactive groups per 1000 carbons for the mixture of vinyl terminated polyolefins, that preferably become PO and PO*, before they are coupled by an alkene metathesis catalyst.
  • a preferred embodiment for the dimer of formula (X) has PO and PO* being different.
  • PO and PO* in Formula (X) may by any PO and PO* as described herein.
  • the dimer has 0.10 to 35 internal unsaturations per 1,000 carbon atoms, as determined by 13 C NMR (as described in concurrently filed USSN 13/072,383, filed March 25, 2011, entitled “Diblock Copolymers Prepared by Cross Metathesis"), alternately from 0.2 to 20, preferably 0.3 to 10.
  • Dimers of vinyl terminated polyolefins can be produced by a process comprising contacting an alkene metathesis catalyst with two or more vinyl terminated polyolefins, each having at least 30% allyl chain ends (relative to total unsaturations).
  • the reactants are typically combined in a reaction vessel at a temperature of 20 to 200°C (preferably 50 to 160°C, preferably 60 to 140°C) and a pressure of 0 to 1000 MPa (preferably 0.5 to 500 MPa, preferably 1 to 250 MPa) for a residence time of 0.5 seconds to 10 hours (preferably 1 second to 5 hours, preferably 1 minute to 1 hour).
  • 0.00001 to 1.0 moles, preferably 0.0001 to 0.05 moles, preferably 0.0005 to 0.01 moles of catalyst are charged to the reactor per mole of vinyl terminated polyolefin charged.
  • the process is typically a solution process, although it may be a bulk or high pressure process. Homogeneous processes are preferred. (A homogeneous process is defined to be a process where at least 90 wt% of the product is soluble in the reaction media.) A bulk homogeneous process is particularly preferred. (A bulk process is defined to be a process where reactant concentration in all feeds to the reactor is 70 volume % or more.) Alternately no solvent or diluent is present or added in the reaction medium, (except for the small amounts used as the carrier for the catalyst or other additives, or amounts typically found with the reactants; e.g., propane in propylene).
  • Suitable diluents/solvents for the process include non-coordinating, inert liquids.
  • Examples include straight and branched-chain hydrocarbons, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof such as can be found commercially (Isopar ); perhalogenated hydrocarbons, such as perfluorinated C4 0 alkanes, chlorobenzene, and aromatic and alkylsubstituted aromatic compounds, such as benzene, toluene, mesitylene, and xylene.
  • straight and branched-chain hydrocarbons such as isobutane,
  • aliphatic hydrocarbon solvents are preferred, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof.
  • the solvent is not aromatic, preferably aromatics are present in the solvent at less than 1 wt%, preferably at 0.5 wt%, preferably at 0 wt% based upon the weight of the solvents.
  • the process is a slurry process.
  • slurry polymerization process means a polymerization process where a supported catalyst is employed and monomers are polymerized on the supported catalyst particles. At least 95 wt% of polymer products derived from the supported catalyst are in granular form as solid particles (not dissolved in the diluent).
  • the feed concentration for the process is 60 volume % solvent or less, preferably 40 volume % or less, preferably 20 volume % or less.
  • the process may be batch, semi-batch or continuous.
  • continuous means a system that operates without interruption or cessation.
  • a continuous process to produce a polymer would be one where the reactants are continually introduced into one or more reactors and polymer product is continually withdrawn.
  • Useful reaction vessels include reactors (including continuous stirred tank reactors, batch reactors, reactive extruder, pipe, or pump).
  • the productivity of the process is at least 200 g of dimer of formula (X) per mmol of catalyst per hour, preferably at least 5000 g/mmol/hour, preferably at least 10,000 g/mmol/hr, preferably at least 300,000 g/mmol/hr.
  • Vinyl terminated olefin polyolefins (oligomers and polymers) useful herein to make the dimers used herein can include any vinyl-terminated polyolefin including those prepared from one or more of C2, C3, C4 through C ⁇ unsaturated monomers.
  • Suitable monomers include but are not limited to, for example, ethylene, propylenes, butylenes, pentylenes, hexylenes, heptylenes, octylenes, nonylenes, decyclenes, and the like, preferably each having at least 30% allyl chain ends, relative to total unsaturations (preferably least 40%, preferably at least 50%, preferably at least 60%, preferably at least 65%, preferably at least 75%, preferably at least 80%, preferably at least 85%, preferably at least 90%, preferably at least 95%).
  • the vinyl terminated polyolefin used herein comprises at least 10 mol% (alternately at least 20 mol%, alternately at least 40 mol%, alternately at least 60 mol%) of a C 4 or greater olefin (such as butene, pentene, octene, nonene, decene, undecene, dodecene) and has: 1) at least 30% allyl chain ends (relative to total unsaturations), preferably at least 40%, preferably at least 50%, preferably at least 60%, preferably at least 70%, preferably at least 75%, preferably at least 80%, preferably at least 85%, preferably at least 90%, preferably at least 95%; and 2) an Mn of from 200 to 60,000 g/mol, preferably from 200 to 50,000 g/mol, preferably from 500 to 40,000 g/mol.
  • a C 4 or greater olefin such as butene, pentene, octene, nonene, decene
  • Vinyl terminated olefin polyolefins useful in this invention include propylene polymers, comprising propylene and less than 0.5 wt% comonomer, preferably 0 wt% comonomer, wherein the oligomer has:
  • Mn a number average molecular weight (Mn) of about 500 to about 20,000 g/mol, as measured by ⁇ NMR (preferably 500 to 15,000, preferably 700 to 10,000, preferably 800 to 8,000 g/mol, preferably 900 to 7,000, preferably 1000 to 6,000, preferably 1000 to 5,000);
  • X is 80% or more, preferably 85% or more, preferably 90% or more, preferably 95% or more.
  • the polymer has at least 80% isobutyl chain ends (based upon the sum of isobutyl and n- propyl saturated chain ends), preferably at least 85% isobutyl chain ends, preferably at least 90% isobutyl chain ends.
  • the polymer has an isobutyl chain end to allylic vinyl group ratio of 0.8: 1 to 1.35: 1.0, preferably 0.9: 1 to 1.20: 1.0, preferably 0.9: 1.0 to 1.1 : 1.0.
  • Vinyl terminated olefin polymers useful in this invention also include propylene polymers, comprising more than 90 mol% propylene (preferably 95 to 99 mol%, preferably 98 to 9 mol%) and less than 10 mol% ethylene (preferably 1 to 4 mol%, preferably 1 to 2 mol%), wherein the polymer has:
  • Mn a number average molecular weight (Mn) of about 400 to about 30,000 g/mol, as measured by l R NMR (preferably 500 to 20,000, preferably 600 to 15,000, preferably 700 to 10,000 g/mol, preferably 800 to 9,000, preferably 900 to 8,000, preferably 1000 to 6,000);
  • Vinyl terminated olefin polymers and polymers useful in this invention also include propylene polymers, comprising: at least 50 (preferably 60 to 90, preferably 70 to 90) mol% propylene and from 10 to 50 (preferably 10 to 40, preferably 10 to 30) mol% ethylene, wherein the polymer has: i) at least 90% allyl chain ends (preferably at least 91%, preferably at least 93%, preferably at least 95%, preferably at least 98%);
  • Vinyl terminated olefin polymers useful in this invention also include propylene polymers, comprising:
  • mol% propylene at least 50 (preferably at least 60, preferably 70 to 99.5, preferably 80 to 99, preferably 90 to 98.5) mol% propylene, from 0.1 to 45 (alternately at least 35, preferably 0.5 to 30, preferably 1 to 20, preferably 1.5 to 10) mol% ethylene, and from 0.1 to 5 (preferably 0.5 to 3, preferably 0.5 to 1) mol% C 4 to olefin (such as butene, hexene or octene, preferably butene), wherein the polymer has :
  • At least 90% allyl chain ends preferably at least 91%, preferably at least 93%, preferably at least 95%, preferably at least 98%;
  • Mn a number average molecular weight of about 150 to about 15,000 g/mol, as measured by l K NMR (preferably 200 to 12,000, preferably 250 to 10,000, preferably 300 to 10,000, preferably 400 to 9500, preferably 500 to 9,000, preferably 750 to
  • Vinyl terminated olefin polymers useful in this invention also include propylene polymers, comprising:
  • mol% propylene at least 50 (preferably at least 60, preferably 70 to 99.5, preferably 80 to 99, preferably 90 to 98.5) mol% propylene, from 0.1 to 45 (alternately at least 35, preferably 0.5 to 30, preferably 1 to 20, preferably 1.5 to 10) mol% ethylene, and from 0.1 to 5 (preferably 0.5 to 3, preferably 0.5 to 1) mol% diene (such as C 4 to (3 ⁇ 4 alpha-omega dienes (such as butadiene, hexadiene, octadiene), norbornene, ethylidene norbornene, vinylnorbornene, norbornadiene, and dicyclopentadiene), wherein the polymer has:
  • diene such as C 4 to (3 ⁇ 4 alpha-omega dienes (such as butadiene, hexadiene, octadiene), norbornene, ethylidene norbornene, vinylnor
  • At least 90% allyl chain ends preferably at least 91%, preferably at least 93%, preferably at least 95%, preferably at least 98%
  • Mn number average molecular weight
  • the vinyl terminated polyolefin useful herein may be one or more vinyl terminated polymers having an Mn (measured by !fi NMR) of 200 g/mol or more, (preferably 300 to 60,000 g/mol, 400 to 50,000 g/mol, preferably 500 to 35,000 g/mol, preferably 300 to 15,000 g/mol, preferably 400 to 12,000 g/mol, or preferably 750 to 10,000 g/mol); and comprising: (i) from about 20 to about 99.9 mol% (preferably from about 25 to about 90 mol%, from about 30 to about 85 mol%, from about 35 to about 80 mol%, from about 40 to about 75 mol%, or from about 50 to about 95 mol%) of at least one C5 to C40 olefin (preferably C 5 to C30 a-olefins, more preferably C5-C20 a-olefins, preferably, Cs-C ⁇ a-olefins, preferably
  • the vinyl terminated polyolefins useful herein may be one or more vinyl terminated polyolefins having an Mn (measured by NMR) of 200 g/mol or more (preferably 300 to 60,000 g/mol, 400 to 50,000 g/mol, preferably 500 to 35,000 g/mol, preferably 300 to 15,000 g/mol, preferably 400 to 12,000 g/mol, or preferably 750 to 10,000 g/mol) and comprises: (i) from about 80 to 99.9 mol% (preferably 85 to 99.9 mol%, more preferably 90 to 99.9 mol%) of at least one C 4 olefin (preferably 1-butene); and (ii) from about 0.1 to 20 mol% of propylene, preferably 0.1 to 15 mol%, more preferably 0.1 to 10 mol%; wherein the vinyl terminated polyolefin has at least 40% allyl chain ends, preferably at least 50%, at least 60%, at least 70%; or at least 80%
  • the invention relates to a composition
  • a composition comprising vinyl terminated polyolefins having an Mn of at least 200 g/mol, (preferably 200 to 100,000 g/mol, preferably 200 to 75,000 g/mol, preferably 200 to 60,000 g/mol, preferably 300 to 60,000 g/mol, or preferably 750 to 30,000 g/mol) (measured by ⁇ NMR) comprising of one or more (preferably two or more, three or more, four or more, and the like) C 4 to C 4 Q (preferably C 4 to C30, C 4 to C20, or C 4 to C ⁇ , preferably butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene, norbornene, norbornadiene, dicyclopentadiene, cyclopentene, cycloheptene, cyclooctene, cycloocta
  • these higher olefin vinyl terminated polymers may comprise ethylene derived units, preferably at least 5 mol% ethylene (preferably at least 15 mol% ethylene, preferably at least 25 mol% ethylene, preferably at least 35 mol% ethylene, preferably at least 45 mol% ethylene, preferably at least 60 mol% ethylene, preferably at least 75 mol% ethylene, or preferably at least 90 mol% ethylene).
  • ethylene derived units preferably at least 5 mol% ethylene (preferably at least 15 mol% ethylene, preferably at least 25 mol% ethylene, preferably at least 35 mol% ethylene, preferably at least 45 mol% ethylene, preferably at least 60 mol% ethylene, preferably at least 75 mol% ethylene, or preferably at least 90 mol% ethylene).
  • the vinyl terminated polyolefin useful herein is a branched polyolefin having an Mn of 7,500 to 60,000 g/mol (and optionally a Tm of greater than 60°C (preferably greater than 100°C), and or, optionally, a AHf of greater than 7 J/g (preferably greater than 50 J/g)) comprising one or more alpha olefins (preferably ethylene and/or propylene and optionally a C 4 to Qo alpha olefin), said branched polyolefin having: (i) 50 mol% or greater allyl chain ends, relative to total unsaturated chain ends (preferably 60% or more, preferably 70% or more, preferably 80% or more, preferably 90% or more, preferably 95% or more); (ii) a g'(vis) of 0.90 or less (preferably 0.85 or less, preferably 0.80 or less); (iii) optionally, an allyl chain end to internal vinylidene ratio of
  • the vinyl terminated polyolefin useful herein is a branched polyolefin having an Mn of 60,000 g/mol or more (and optionally a Tm of greater than 60°C (preferably greater than 100°C), and or, optionally, a AHf of greater than 7 J/g (preferably greater than 50 J/g)) comprising one or more alpha olefins (preferably ethylene and/or propylene and optionally a C 4 to C ⁇ Q alpha olefin), and having: (i) 50 mol% or greater allyl chain ends, relative to total unsaturated chain ends (preferably 60% or more, preferably 70% or more, preferably 80% or more, preferably 90% or more, preferably 95% or more); (ii) a g'(vis) of 0.90 or less (preferably 0.85 or less, preferably 0.80 or less); (iii) a bromine number which, upon complete hydrogenation, decreases by at least 50% (preferably at least 75%);
  • the vinyl terminated polyolefin useful herein is a branched polyolefin having an Mn of less than 7,500 g/mol, preferably from 100 to 7,500 g/mol (and optionally a Tm of greater than 60°C (preferably greater than 100°C), and/or, optionally, a AHf of greater than 7 J/g (preferably greater than 50 J/g)) comprising one or more alpha olefins (preferably ethylene and or propylene and optionally a C 4 to CIQ alpha olefin), and having: (i) 50 mol% or greater allyl chain ends, relative to total unsaturated chain ends (preferably 60% or more, preferably 70% or more, preferably 80% or more, preferably 90% or more, preferably 95% or more); (ii) a ratio of percentage of saturated chain ends to percentage of allyl chain ends of 1.2 to 2.0 (preferably a ratio of percentage of saturated chain ends (preferably isobutyl chain ends) to percentage of
  • Cio alpha olefin monomers useful in the branched polymers described above include butene, pentene, hexene, heptene, octene, nonene, decene, cyclopentene, cycloheptene, cyclooctene, and isomers thereof.
  • Particularly useful vinyl terminated polyolefins may be isotactic, highly isotactic, syndiotactic, or highly syndiotactic propylene polymer, particularly isotactic polypropylene.
  • isotactic is defined as having at least 10% isotactic pentads, preferably having at least 40% isotactic pentads of methyl groups derived from propylene according to analysis by 13 C-NMR.
  • “highly isotactic” is defined as having at least 60% isotactic pentads according to analysis by 13 C-NMR.
  • PO, and/or PO* and/or the vinyl terminated polyolefins used to produce PO and PO* have at least 85% isotacticity.
  • “syndiotactic” is defined as having at least 10% syndiotactic pentads, preferably at least 40%, according to analysis by 13 C-NMR.
  • “highly syndiotactic” is defined as having at least 60% syndiotactic pentads according to analysis by 13 C-NMR.
  • PO, and/or PO* and/or the vinyl terminated polyolefins used to produce PO and PO* have has at least 85% syndiotacticity.
  • Any of the vinyl terminated polyolefins described herein preferably have less than 1400 ppm aluminum, preferably less than 1000 ppm aluminum, preferably less than 500 ppm aluminum, preferably less than 100 ppm aluminum, preferably less than 50 ppm aluminum, preferably less than 20 ppm aluminum, preferably less than 5 ppm aluminum.
  • cross-metathesis products disclosed herein have little or no reactive termini as shown by a ratio of 2.0 or greater for the intensity of the internal unsaturation peaks at about 128 to 132 ppm to the reactive termini peaks at about 114 and 137 ppm in the 13 C NMR spectrum.
  • any vinyl terminated polyolefin described herein comprises less than 3 wt% of functional groups selected from hydroxide, aryls and substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, preferably less than 2 wt%, more preferably less than 1 wt%, more preferably less than 0.5 wt%, more preferably less than 0.1 wt%, more preferably 0 wt%, based upon the weight of the oligomer.
  • Preferred vinyl terminated polyolefins described herein may have an M n as determined by l R NMR of 150 to 25,000 g/mole, 200 to 20,000 g/mol, preferably 250 to 15,000 g/mol, preferably 300 to 15,000 g/mol, preferably 400 to 12,000 g/mol, preferably 750 to 10,000 g/mol.
  • M n is determined according to the methods described below in the examples section.
  • Any vinyl terminated polyolefin described herein preferably has a glass transition temperature (Tg) of less than 0°C or less (as determined by differential scanning calorimetry as described below), preferably -10°C or less, more preferably -20°C or less, more preferably -30°C or less, more preferably -50°C or less.
  • Tg glass transition temperature
  • Any vinyl terminated polyolefin described herein preferably contains less than 80 wt% of C 4 olefin(s), (such as isobutylene n-butene, 2-butene, isobutylene, and butadiene), based upon the weight of the oligomer, preferably less than 10 wt%, preferably 5 wt%, preferably less than 4 wt%, preferably less than 3 wt%, preferably less than 2 wt%, preferably less than 1 wt%, preferably less than 0.5 wt%, preferably less than 0.25 wt% of C 4 olefin(s) based upon the weight of the polyolefin.
  • C 4 olefin(s) such as isobutylene n-butene, 2-butene, isobutylene, and butadiene
  • any vinyl terminated polyolefin described herein preferably contains less than 20 wt% of C 4 or more olefin(s), (such as C 4 to C30 olefins, typically such as C 4 to C12 olefins, typically such as C 4 , Cg, C ⁇ , olefins, etc.), based upon the weight of the polyolefin, preferably less than 10 wt%, preferably 5 wt%, preferably less than 4 wt%, preferably less than 3 wt%, preferably less than 2 wt%, preferably less than 1 wt%, preferably less than 0.5 wt%, preferably less than 0.25 wt% of C 4 olefin(s) based upon the weight of the polyolefin, as determined by 13 C NMR.
  • C 4 to C30 olefins typically such as C 4 to C12 olefins, typically such as C 4 , Cg, C ⁇ ,
  • any vinyl terminated polyolefin described herein comprises at least 50 wt% (preferably at least 75 wt%, preferably at least 90 wt%, based upon the weight of the oligomer composition) olefins having at least 36 carbon atoms (preferably at least 51 carbon atoms, preferably at least 102 carbon atoms) as measured by NMR assuming one unsaturation per chain.
  • any vinyl terminated polyolefin described herein comprises less than 20 wt% dimer and trimer (preferably less than 10 wt%, preferably less than 5 wt%, more preferably less than 2 wt%, based upon the weight of the oligomer composition), as measured by Gas Chromatography. Products are analyzed by gas chromatography (Agilent 6890N with auto-injector) using helium as a carrier gas at 38 cm/sec.
  • a column having a length of 60 m (J & W Scientific DB-1, 60 m x 0.25 mm I.D.x 1.0 ⁇ film thickness) packed with a flame ionization detector (FID), an Injector temperature of 250°C, and a Detector temperature of 250°C are used.
  • the sample was injected into the column in an oven at 70°C, then heated to 275°C over 22 minutes (ramp rate 10°C/min to 100°C, 30°C/min to 275°C, hold).
  • An internal standard usually the monomer, is used to derive the amount of dimer or trimer product that is obtained. Yields of dimer and trimer product are calculated from the data recorded on the spectrometer. The amount of dimer or trimer product is calculated from the area under the relevant peak on the GC trace, relative to the internal standard.
  • any vinyl terminated polyolefin described herein here contains less than 25 ppm hafnium, preferably less than 10 ppm hafnium, preferably less than 5 ppm hafnium based on the yield of polymer produced and the mass of catalyst employed.
  • any vinyl terminated polyolefin described herein may have a melting point (DSC first melt) of from 60 to 130°C, alternately 50 to 100°C.
  • the polyolefins described herein have no detectable melting point by DSC following storage at ambient temperature (23°C) for at least 48 hours.
  • T m and Tg are measured using Differential Scanning Calorimetry (DSC) using commercially available equipment such as a TA Instruments 2920 DSC.
  • DSC Differential Scanning Calorimetry
  • the sample is equilibrated at 25°C, then it is cooled at a cooling rate of 10°C/min to -80°C.
  • the sample is held at -80°C for 5 min and then heated at a heating rate of 10°C/min to 25°C.
  • the glass transition temperature is measured from the heating cycle.
  • the sample is equilibrated at 25°C, then heated at a heating rate of 10°C/min to 150°C.
  • the endothermic melting transition if present, is analyzed for onset of transition and peak temperature.
  • the melting temperatures reported are the peak melting temperatures from the first heat unless otherwise specified.
  • the melting point is defined to be the peak melting temperature (i.e., associated with the largest endothermic calorimetric response in that range of temperatures) from the DSC melting trace.
  • any vinyl terminated polyolefin described herein is a liquid at 25°C.
  • Bromine number is determined by ASTM D 1 159.
  • ICPES Inductively Coupled Plasma Emission Spectrometry
  • J. W. Olesik “Inductively Coupled Plasma-Optical Emission Spectroscopy” in the Encyclopedia of Materials Characterization, C. R. Brundle, C. A. Evans, Jr. and S. Wilson, eds., Butterworth-Heinemann, Boston, Mass., 1992, pp. 633-644, is used to determine the amount of an element in a material.
  • the vinyl terminated polymers described herein have a viscosity at 60°C of greater than 1000 cP, greater than 12,000 cP, or greater than 100,000 cP. In other embodiments, the vinyl terminated polymers have a viscosity of less than 200,000 cP, less than 150,000 cP, or less than 100,000 cP. Viscosity is measured using a Brookfield Digital Viscometer.
  • any of the vinyl terminated polyolefins described or useful herein have 3-alkyl vinyl end groups (where the alkyl is a Q to C38 alkyl), also referred to as a "3-alkyl chain ends" or a "3-alkyl vinyl termination", represented by the formula:
  • R b is a to C38 alkyl group, preferably a Ci to C20 alkyl group, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, docecyl, and the like.
  • the amount of 3-alkyl chain ends is determined using 13 C NMR as set out below.
  • any of the vinyl terminated polyolefins described or useful herein have at least 5% 3-alkyl chain ends (preferably at least 10% 3-alkyl chain ends, at least 20% 3-alkyl chain ends, at least 30% 3-alkyl chain ends; at least 40% 3-alkyl chain ends, at least 50% 3-alkyl chain ends, at least 60% 3-alkyl chain ends, at least 70% 3-alkyl chain ends; at least 80% 3-alkyl chain ends, at least 90% 3-alkyl chain ends; at least 95% 3- alkyl chain ends), relative to total unsaturation.
  • 3-alkyl chain ends preferably at least 10% 3-alkyl chain ends, at least 20% 3-alkyl chain ends, at least 30% 3-alkyl chain ends; at least 40% 3-alkyl chain ends, at least 50% 3-alkyl chain ends, at least 60% 3-alkyl chain ends, at least 70% 3-alkyl chain ends; at least 80% 3-alkyl chain ends, at least 90% 3-alkyl chain ends; at least 95% 3- alkyl chain ends
  • any of the vinyl terminated polyolefins described or useful herein have at least 5% of 3-alkyl + allyl chain ends, (e.g., all 3-alkyl chain ends plus all allyl chain ends), preferably at least 10% 3-alkyl + allyl chain ends, at least 20% 3-alkyl + allyl chain ends, at least 30% 3-alkyl + allyl chain ends; at least 40% 3-alkyl + allyl chain ends, at least 50% 3-alkyl + allyl chain ends, at least 60% 3-alkyl + allyl chain ends, at least 70% 3-alkyl + allyl chain ends; at least 80%3-alkyl + allyl chain ends, at least 90% 3-alkyl + allyl chain ends; at least 95% 3-alkyl + allyl chain ends, relative to total unsaturation.
  • 3-alkyl + allyl chain ends e.g., all 3-alkyl chain ends plus all allyl chain ends
  • at least 10% 3-alkyl + allyl chain ends
  • the vinyl terminated polyolefins described herein have an Mw (measured as described below) of 1,000 to about 30,000 g/mol, alternately 2000 to 25,000 g/mol, alternately 3,000 to 20,000 g/mol and/or an Mz of about 1700 to about 150,000 g/mol, alternately 800 to 100,000 g/mol.
  • Mw, Mn, Mz, number of carbon atoms, and g' vjs are determined by using a High Temperature Size Exclusion Chromatograph (either from Waters Corporation or Polymer Laboratories), equipped with three in-line detectors, a differential refractive index detector (DRI), a light scattering (LS) detector, and a viscometer.
  • DRI differential refractive index detector
  • LS light scattering
  • Solvent for the experiment is prepared by dissolving 6 grams of butylated hydroxy toluene as an antioxidant in 4 liters of Aldrich reagent grade 1, 2, 4 trichlorobenzene (TCB). The TCB mixture is then filtered through a 0.7 ⁇ glass pre-filter and subsequently through a 0.1 ⁇ Teflon filter. The TCB is then degassed with an online degasser before entering the Size Exclusion Chromatograph. Polymer solutions are prepared by placing dry polymer in a glass container, adding the desired amount of TCB, then heating the mixture at 160°C with continuous agitation for about 2 hours. All quantities are measured gravimetrically.
  • the TCB densities used to express the polymer concentration in mass/volume units are 1.463 g/ml at room temperature and 1.324 g/ml at 145°C.
  • the injection concentration is from 0.75 to 2.0 mg/ml, with lower concentrations being used for higher molecular weight samples.
  • the DRI detector and the injector Prior to running each sample the DRI detector and the injector are purged. Flow rate in the apparatus is then increased to 0.5 ml/minute, and the DRI is allowed to stabilize for 8 to 9 hours before injecting the first sample.
  • the LS laser is turned on 1 to 1.5 hours before running the samples.
  • the concentration, c, at each point in the chromatogram is calculated from the baseline-subtracted DRI signal, I DR[ , using the following equation:
  • K D RJ is a constant determined by calibrating the DRI
  • (dn/dc) is the refractive index increment for the system.
  • (dn/dc) 0.104 for propylene polymers, 0.098 for butene polymers and 0.1 otherwise.
  • concentration is expressed in g/cm 3
  • molecular weight is expressed in g/mole
  • intrinsic viscosity is expressed in dL/g.
  • the LS detector is a Wyatt Technology High Temperature mini-DAW .
  • the molecular weight, M, at each point in the chromatogram is determined by analyzing the LS output using the Zimm model for static light scattering (M.B. Huglin, LIGHT SCATTERING FROM POLYMER SOLUTIONS, Academic Press 1971):
  • ⁇ ( ⁇ ) is the measured excess Rayleigh scattering intensity at scattering angle ⁇
  • c is the polymer concentration determined from the DRI analysis
  • A2 is the second virial coefficient for purposes of this invention
  • a 2 0.0006 for propylene polymers, 0.0015 for butene polymers and 0.001 otherwise
  • (dn/dc) 0.104 for propylene polymers, 0.098 for butene polymers and 0.1 otherwise
  • ⁇ ( ⁇ ) is the form factor for a monodisperse random coil
  • K 0 is the optical constant for the system:
  • a high temperature Viscotek Corporation viscometer which has four capillaries arranged in a Wheatstone bridge configuration with two pressure transducers, is used to determine specific viscosity.
  • One transducer measures the total pressure drop across the detector, and the other, positioned between the two sides of the bridge, measures a differential pressure.
  • the specific viscosity, n s for the solution flowing through the viscometer is calculated from their outputs.
  • the intrinsic viscosity, [ ⁇ ], at each point in the chromatogram is calculated from the following equation:
  • ⁇ 8 ⁇ [ ⁇ ] + 0.3( ⁇ [ ⁇ ]) 2
  • the branching index (g' v i s ) is calculated using the output of the SEC-DRI-LS-VIS method as follows.
  • ] aV g, of the sample is calculated by:
  • M v is the viscosity-average molecular weight based on molecular weights determined by LS analysis. See Macromolecules, 2001, 34, pp. 6812-6820 and Macromolecules, 2005, 38, pp. 7181-7183, for guidance on selecting a linear standard having similar molecular weight and comonomer content, and determining k coefficients and a exponents.
  • Molecular weight distribution (Mw/Mn - both by GPC-DRI) is determined by the method above.
  • the vinyl terminated polyolefins of this invention have an Mw/Mn (by GPC-DRI) of 1.5 to 20, alternately 1.7 to 10.
  • this invention can be practiced with any vinyl containing materials, preferably with vinyl terminated materials (including vinyl terminated polymers, vinyl terminated polyolefins (such as vinyl terminated ethylene homo- and co-polymers, and vinyl terminated propylene homo- and co-polymers)).
  • vinyl terminated materials including vinyl terminated polymers, vinyl terminated polyolefins (such as vinyl terminated ethylene homo- and co-polymers, and vinyl terminated propylene homo- and co-polymers).
  • vinyl terminated materials include homo-and co-polymers of heteroatom containing monomers, as well as polymers of olefin monomers only.
  • vinyl terminated polymers includes vinyl terminated oligomers.
  • Preferred vinyl terminated polyolefins include vinyl terminated isotactic polypropylene (preferably having a melting point of 100°C or more, preferably 155°C or more), polyethylene (preferably having a melting point of 100°C or more, preferably 155°C or more).
  • the vinyl terminated polyolefins described above are typically prepared in a homogeneous process, preferably a bulk process as described in WO 2009/155471, which is incorporated by reference herein.
  • propylene and optional comonomers such as ethylene
  • a catalyst system comprising metallocene compound(s), and one or more activators
  • Other additives may also be used, as desired, such as scavengers and/or hydrogen.
  • Any conventional suspension, homogeneous bulk, solution, slurry, or high-pressure oligomerization process can be used. Such processes can be run in a batch, semi-batch, or continuous mode.
  • homogeneous polymerization processes are preferred.
  • a homogeneous polymerization process is defined to be a process where at least 90 wt% of the product is soluble in the reaction media.
  • a bulk homogeneous process is particularly preferred.
  • a bulk process is defined to be a process where monomer concentration in all feeds to the reactor is 70 volume % or more.
  • no solvent or diluent is present or added in the reaction medium, (except for the small amounts used as the carrier for the catalyst system or other additives, or amounts typically found with the monomer; e.g., propane in propylene).
  • Monomers useful in the polymerization processes described herein to produce the vinyl terminated polyolefins include one or more (preferably two or more, three or more, four or more, and the like) of C2 to C40 (preferably C3 to C30, C 4 to C20, or C 5 to ( 3 ⁇ 4, preferably ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene, norbornene, norbornadiene, dicyclopentadiene, cyclopentene, cycloheptene, cyclooctene, cyclooctadiene, cyclododecene, 7-oxanorbornene, 7-oxanorbornadiene, substituted derivatives thereof, and isomers thereof).
  • C2 to C40 preferably C3 to C30, C 4 to C20, or C 5 to ( 3 ⁇ 4, preferably
  • the butene source may be a mixed butene stream comprising various isomers of butene.
  • the 1 -butene monomers are expected to be preferentially consumed by the polymerization process.
  • Use of such mixed butene streams will provide an economic benefit, as these mixed streams are often waste streams from refining processes, for example C 4 raffinate streams, and can therefore be substantially less expensive than pure 1 -butene.
  • Suitable diluents/solvents for polymerization include non-coordinating, inert liquids.
  • examples include straight and branched-chain hydrocarbons, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof such as can be found commercially (Isopars); perhalogenated hydrocarbons, such as perfluorinated C4 0 alkanes, chlorobenzene, and aromatic and alkylsubstituted aromatic compounds, such as benzene, toluene, mesitylene, and xylene.
  • straight and branched-chain hydrocarbons such as isobutane
  • Suitable solvents also include liquid olefins which may act as monomers or comonomers including ethylene, propylene, 1 -butene, 1 -hexene, 1 -pentene, 3-methyl-l-pentene, 4-methyl-l-pentene, 1-octene, and 1-decene. Mixtures of the foregoing are also suitable.
  • aliphatic hydrocarbon solvents are preferred, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof.
  • the solvent is not aromatic, preferably aromatics are present in the solvent at less than 1 wt%, preferably at 0.5 wt%, preferably at 0 wt% based upon the weight of the solvents.
  • the process is a slurry process.
  • slurry polymerization process means a polymerization process where a supported catalyst is employed and monomers are polymerized on the supported catalyst particles. At least 95 wt % of polymer products derived from the supported catalyst are in granular form as solid particles (not dissolved in the diluent).
  • scavenger is present at zero mol%, alternately the scavenger is present at a molar ratio of scavenger metal to transition metal of less than 100: 1, preferably less than 50: 1, preferably less than 15: 1, preferably less than 10: 1.
  • hydrogen is present in the polymerization reactor at a partial pressure of 0.001 to 50 psig (0.007 to 345 kPa), preferably from 0.01 to 25 psig (0.07 to 172.4 kPa), more preferably 0.1 to 10 psig (0.7 to 68.95 kPa). It has been found that in the present systems, hydrogen can be used to provide increased activity without significantly impairing the catalyst's ability to produce allylic chain ends.
  • the catalyst activity (calculated as g/mmolcatalyst/hr) is at least 20% higher than the same reaction without hydrogen present, preferably at least 50% higher, preferably at least 100% higher.
  • Catalyst productivity is a measure of how many grams of polymer (P) are produced using a polymerization catalyst comprising W g of catalyst (cat), over a period of time of T hours; and may be expressed by the following formula: P/(T x W) and expressed in units of gPgcaHhr 1 . Conversion is the amount of monomer that is converted to polymer product, and is reported as mol% and is calculated based on the polymer yield and the amount of monomer fed into the reactor. Catalyst activity is a measure of how active the catalyst is and is reported as the mass of product polymer (P) produced per mole of catalyst (cat) used (kgP/molcat).
  • the activity of the catalyst is at least 50 g/mmol/hour, preferably 500 or more g/mmol/hour, preferably 5000 or more g/mmol/hr, preferably 50,000 or more g/mmol/hr.
  • the conversion of olefin monomer is at least 10%, based upon polymer yield and the weight of the monomer entering the reaction zone, preferably 20% or more, preferably 30% or more, preferably 50% or more, preferably 80% or more.
  • the productivity at least 4500 g/mmol/hour, preferably 5000 or more g/mmol/hour, preferably 10,000 or more g/mmol/hr, preferably 50,000 or more g/mmol/hr.
  • the productivity is at least 80,000 g/mmol/hr, preferably at least 150,000 g/mmol/hr, preferably at least 200,000 g/mmol/hr, preferably at least 250,000 g/mmol/hr, preferably at least 300,000 g/mmol/hr.
  • the productivity of the process is at least 200 g of vinyl terminated polyolefin per mmol of catalyst per hour, preferably at least 5000 g/mmol/hour, preferably at least 10,000 g/mmol/hr, preferably at least 300,000 g/mmol/hr.
  • Preferred polymerizations can be run at typical temperatures and/or pressures, such as from 25 to 150°C, preferably 40 to 120°C, preferably 45 to 80°C, and preferably from 0.35 to 10 MPa, preferably from 0.45 to 6 MPa, preferably from 0.5 to 4 MPa.
  • the residence time of the reaction is up to 60 minutes, preferably between 5 to 50 minutes, preferably 10 to 40 minutes.
  • alumoxane is present at zero mol%, alternately the alumoxane is present at a molar ratio of aluminum to transition metal less than 500: 1, preferably less than 300: 1, preferably less than 100: 1, preferably less than 1 : 1.
  • alumoxane is used to produce the vinyl terminated polyolefins then, the alumoxane has been treated to remove free alkyl aluminum compounds, particularly trimethyl aluminum.
  • the activator used herein to produce the vinyl terminated polyolefins is bulky as defined herein and is discrete.
  • scavenger such as trialkyl aluminum
  • scavenger is present at zero mol%, alternately the scavenger is present at a molar ratio of scavenger metal to transition metal of less than 100: 1, preferably less than 50: 1, preferably less than 15: 1, preferably less than 10: 1.
  • scavenger such as tri alkyl aluminum
  • the scavenger is present at zero mol%, alternately the scavenger is present at a molar ratio of scavenger metal to transition metal of less than 100: 1, preferably less than 50: 1, preferably less than 15: 1, preferably less than 10: 1.
  • the polymerization 1) is conducted at temperatures of 0 to 300°C (preferably 25 to 150°C, preferably 40 to 120°C, preferably 45 to 80°C); 2) is conducted at a pressure of atmospheric pressure to 10 MPa (preferably 0.35 to 10 MPa, preferably from 0.45 to 6 MPa, preferably from 0.5 to 4 MPa); 3) is conducted in an aliphatic hydrocarbon solvent (such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof; preferably where aromatics are present in the solvent at less than 1 wt%, preferably at 0.5 wt%, preferably at 0
  • the catalyst system used in the polymerization comprises no more than one catalyst compound.
  • a "reaction zone” also referred to as a "polymerization zone” is a vessel where polymerization takes place, for example a batch reactor. When multiple reactors are used in either series or parallel configuration, each reactor is considered as a separate polymerization zone. For a multi-stage polymerization in both a batch reactor and a continuous reactor, each polymerization stage is considered as a separate polymerization zone. In a preferred embodiment, the polymerization occurs in one reaction zone. Room temperature is 23 °C unless otherwise noted.
  • a "catalyst system” is combination of at least one catalyst compound, at least one activator, an optional co-activator, and an optional support material, where the system can polymerize monomers to polymer.
  • catalyst systems are described as comprising neutral stable forms of the components, it is well understood by one of ordinary skill in the art, that the ionic form of the component is the form that reacts with the monomers to produce polymers.
  • the metallocene catalyst may be described as a catalyst precursor, a pre-catalyst compound, or a transition metal compound, and these terms are used interchangeably.
  • An "anionic ligand” is a negatively charged ligand which donates one or more pairs of electrons to a metal ion.
  • a “neutral donor ligand” is a neutrally charged ligand which donates one or more pairs of electrons to a metal ion.
  • a metallocene catalyst is defined as an organometallic compound with at least one ⁇ -bound cyclopentadienyl moiety (or substituted cyclopentadienyl moiety) and more frequently two ⁇ -bound cyclopentadienyl moieties or substituted cyclopentadienyl moieties. This includes other ⁇ -bound moieties such as indenyls or fluorenyls or derivatives thereof.
  • Catalyst compounds useful herein to produce the vinyl terminated polyolefins include one or more metallocene com ound(s) represented by the formulae:
  • Hf is hafnium
  • each X is, independently, selected from the group consisting of hydrocarbyl radicals having from 1 to 20 carbon atoms, hydrides, amides, alkoxides, sulfides, phosphides, halogens, dienes, amines, phosphines, ethers, or a combination thereof, preferably methyl, ethyl, propyl, butyl, phenyl, benzyl, chloride, bromide, iodide, (alternately two X's may form a part of a fused ring or a ring system);
  • each Q is, independently carbon or a heteroatom, preferably C, N, P, S (preferably at least one Q is a heteroatom, alternately at least two Q's are the same or different heteroatoms, alternately at least three Q's are the same or different heteroatoms, alternately at least four Q's are the same or different heteroatoms);
  • each R 1 is, independently, hydrogen or a Q to Cg alkyl group, preferably a Q to Cg linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, or octyl, R 1 may the same or different as R 2 ;
  • each R 2 is, independently, hydrogen or a Q to Cg alkyl group, preferably a Q to Cg linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, or octyl, provided that at least one of R 1 or R 2 is not hydrogen, preferably both of R 1 and R 2 are not hydrogen, preferably R 1 and/or R 2 are not branched;
  • each R 3 is, independently, hydrogen, or a substituted or unsubstituted hydrocarbyl group having from 1 to 8 carbon atoms, preferably 1 to 6 carbon atoms, preferably a substituted or unsubstituted Q to Cg linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, provided, however, that at least three R 3 groups are not hydrogen (alternately four R 3 groups are not hydrogen, alternately five R 3 groups are not hydrogen); ⁇ Alternately, when the catalyst compound is to used to make the homo-polymer then each R 3 is, independently, hydrogen, or a substituted or unsubstituted hydrocarbyl group having from 1 to 8 carbon atoms, preferably 1 to 6 carbon atoms, preferably a substituted or unsubstituted Q to Cg linear alkyl group, preferably methyl ethyl, propyl
  • 1 to 8 carbon atoms preferably 1 to 6 carbon atoms, preferably a substituted or unsubstituted Ci to Cg linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, provided however that: 1) all five R 3 groups are methyl; or 2) four R 3 groups are not hydrogen and at least one R 3 group is a C2 to Cg substituted or unsubstituted hydrocarbyl (preferably at least two, three, four, or five R 3 groups are a C2 to Cg substituted or unsubstituted hydrocarbyl) ⁇ ;
  • each R 4 is, independently, hydrogen or a substituted or unsubstituted hydrocarbyl group, a heteroatom or heteroatom containing group, preferably a substituted or unsubstituted hydrocarbyl group having from 1 to 20 carbon atoms, preferably 1 to 8 carbon atoms, preferably a substituted or unsubstituted Q to Cg linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, substituted phenyl (such as propyl phenyl), phenyl, silyl, substituted silyl, (such as CH 2 SiR' ; where R' is a to (3 ⁇ 4 hydrocarbyl, such as methyl, ethyl, propyl, butyl, phenyl);
  • R 5 is hydrogen or a Q to Cg alkyl group, preferably a Q to Cg linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, or octyl;
  • R 6 is hydrogen or a Q to Cg alkyl group, preferably a Q to Cg linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, or octyl;
  • each R 7 is, independently, hydrogen, or a C to Cg alkyl group, preferably a Q to Cg linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, or octyl, provided however that at least seven R 7 groups are not hydrogen, alternately at least eight R 7 groups are not hydrogen, alternately all R 7 groups are not hydrogen, (preferably the R 7 groups at the 3 and 4 positions on each Cp ring of Formula IV are not hydrogen);
  • N is nitrogen
  • R2 a T is a bridge, preferably T is Si or Ge, preferably Si, and each R a , is independently, hydrogen, halogen or a Q to C20 hydrocarbyl, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, phenyl, benzyl, substituted phenyl, and two R a can form a cyclic structure including aromatic, partially saturated, or saturated cyclic or fused ring system; and further provided that any two adjacent R groups may form a fused ring or multicenter fused ring system where the rings may be aromatic, partially saturated or saturated.
  • At least one R 4 group is not hydrogen, alternately at least two R 4 groups are not hydrogen, alternately at least three R 4 groups are not hydrogen, alternately at least four R 4 groups are not hydrogen, alternately all R 4 groups are not hydrogen.
  • Catalyst compounds that are particularly useful in this invention include one or more of:
  • the "dimethyl" after the transition metal in the list of catalyst compounds above is replaced with a dihalide (such as dichloride, dibromide, or difluoride) or a bisphenoxide, particularly for use with an alumoxane activator.
  • a dihalide such as dichloride, dibromide, or difluoride
  • a bisphenoxide particularly for use with an alumoxane activator.
  • Preferred activators useful with the above include:
  • each X is, independently, selected from the group consisting of hydrocarbyl radicals having from 1 to 20 carbon atoms, hydrides, amides, alkoxides, sulfides, phosphides, halides, dienes, amines, phosphines, ethers, and a combination thereof, (two X's may form a part of a fused ring or a ring system) (preferably each X is independently selected from halides and to C 5 alkyl groups, preferably each X is a methyl group); each R 8 is, independently, a Q to alkyl group (preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, or isomers thereof, preferably each R 8 is a methyl group); each R 9 is, independently, a Q to alkyl group (preferably methyl, ethyl, propyl, but
  • Catalyst compounds that are particularly useful in this invention include one or more of: rac -dimethy lsilyl bis(2-methyl,3 -propylindenyl)hafniumdimethyl, rac -dimethy lsilyl bis(2-methyl,3 -propylindenyl)zirconiumdimethyl, rac ⁇ dimethy lsilyl bis(2-ethyl,3 -propylindenyl)hafniumdimethyl, rac ⁇ dimethy lsilyl bis(2-ethyl,3 -propylindenyl)zirconiumdimethyl, rac ⁇ dimethy lsilyl bis(2-methyl,3 -ethylindenyl)hafniumdimethyl, rac ⁇ dimethy lsilyl bis(2-methyl,3 -ethylindenyl)zirconiumdimethyl, rac ⁇ dimethy lsilyl bis(2-
  • the "dimethyl" after the transition metal in the list of catalyst compounds above is replaced with a dihalide (such as dichloride or difluoride) or a bisphenoxide, particularly for use with an alumoxane activator.
  • a dihalide such as dichloride or difluoride
  • a bisphenoxide particularly for use with an alumoxane activator.
  • the catalyst compound is rac-dimethylsilylbis(2- methyl,3-propylindenyl)hafniumdimethyl or dichloride, or rac-dimethylsilylbis(2-methyl,3- propylindenyl)zirconiumdimethyl or dichloride.
  • Preferred activators useful with the above include:
  • Preferred combinations of catalyst and activator include: N,N-dimethylanilinium tetrakis(perfluorobiphenyl)borate and rac-dimethylsilylbis(2-methyl,3- propylindenyl)hafniumdimethyl, or rac-dimethylsilylbis(2-methyl,3- propylindenyl)zirconiumdimethyl.
  • the vinyl terminated polyolefins useful here in may be produced using the catalyst com ound represented by the formula:
  • each X is, independently, selected from the group consisting of hydrocarbyl radicals having from 1 to 20 carbon atoms, hydrides, amides, alkoxides, sulfides, phosphides, halogens, dienes, amines, phosphines, ethers, or a combination thereof; each R 15 and R 17 are, independently, a C ⁇ to Cg alkyl group (preferably a Ci to Cg linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, or octyl); and each R , R ⁇ , R20 ; R21 ; R22 ; R23 ; R24 ; R25 ; R26 ; R27 ; and R 28 ⁇ ⁇ independently, hydrogen, or a substituted or unsubstituted hydrocarbyl group having from 1 to 8 carbon atoms (
  • R 24 -R 28 groups are not hydrogen (alternately four of R 24 -R 28 groups are not hydrogen, alternately five of R 24 -R 28 groups are not hydrogen). In a preferred embodiment, all five groups of R 24 -R 28 are methyl. In a preferred embodiment, four of the R 24 -R 28 groups are not hydrogen and at least one of the R24.R28 g r0U p S 1S a C2 to Cg substituted or unsubstituted hydrocarbyl (preferably at least two, three, four, or five of R 24 -R 28 groups are a C2 to Cg substituted or unsubstituted hydrocarbyl).
  • R 15 and R 17 are methyl groups
  • R 16 is a hydrogen
  • R 18 -R 23 are all hydrogens
  • R 24 -R 28 are all methyl groups
  • each X is a methyl group.
  • Catalyst compounds that are particularly useful in this invention include (CpMe 5 )( 1 ,3 -Me 2 benz[e]indenyl)HfMe 2 , (CpMe 5 )( 1 -methyl-3-n- propylbenz[e]indenyl)HfMe2, (CpMe5)(l-n-propyl,3-methylbenz[e]indenyl)HfMe2, (CpMe 5 )( 1 -methyl-3 -n-butylbenz[e]indenyl)HfMe 2 , (CpMe 5 )( 1 -n-butyl,3 - methylbenz[e]indenyl)HfMe 2 , (CpMe 5 )(l-ethyl,3-methylbenz[e]indenyl)HfMe 2 , (CpMe 5 )(l- methyl, 3-ethylbenz[e]indendenyl
  • the "dimethyl" (Me 2 ) after the transition metal in the list of catalyst compounds above is replaced with a dihalide (such as dichlonde or difluoride) or a bisphenoxide, particularly for use with an alumoxane activator.
  • a dihalide such as dichlonde or difluoride
  • a bisphenoxide particularly for use with an alumoxane activator.
  • the branched polymers described herein may be produced as described in concurrently filed USSN 61/467,681, filed March 25, 201 1, entitled "Branched Vinyl Terminated Polymers and Methods for Production Thereof.
  • substituted means that a hydrogen group has been replaced with a hydrocarbyl group, a heteroatom or a heteroatom containing group.
  • methyl cyclopentadiene (Cp) is a Cp group substituted with a methyl group and ethyl alcohol is an ethyl group substituted with an -OH group.
  • activator is used herein interchangeably and are defined to be any compound which can activate any one of the catalyst compounds described above by converting the neutral catalyst compound to a catalytically active catalyst compound cation.
  • Non-limiting activators include alumoxanes, aluminum alkyls, ionizing activators, which may be neutral or ionic, and conventional-type cocatalysts.
  • Preferred activators typically include alumoxane compounds, modified alumoxane compounds, and ionizing anion precursor compounds that abstract one reactive, ⁇ -bound, metal ligand making the metal complex cationic and providing a charge-balancing noncoordinating or weakly coordinating anion.
  • alumoxane activators are utilized as an activator in the catalyst composition.
  • Alumoxanes are generally polymeric compounds containing -Al(Ri)- O- sub-units, where R 1 is an alkyl group.
  • Examples of alumoxanes include methylalumoxane (MAO), modified methylalumoxane (MMAO), ethylalumoxane and isobutylalumoxane.
  • Alkylalumoxanes and modified alkylalumoxanes are suitable as catalyst activators, particularly when the abstractable ligand is an alkyl, halide, alkoxide, or amide.
  • alumoxanes Mixtures of different alumoxanes and modified alumoxanes may also be used. It may be preferable to use a visually clear methylalumoxane.
  • a cloudy or gelled alumoxane can be filtered to produce a clear solution or clear alumoxane can be decanted from the cloudy solution.
  • Another alumoxane is a modified methyl alumoxane (MMAO) cocatalyst type 3A (commercially available from Akzo Chemicals, Inc. under the trade name Modified Methylalumoxane type 3A, covered under patent number U.S. Patent No. 5,041,584).
  • MMAO modified methyl alumoxane
  • the activator is an alumoxane (modified or unmodified)
  • some embodiments select the maximum amount of activator at a 5000-fold molar excess Al/M over the catalyst precursor (per metal catalytic site).
  • the minimum activator-to-catalyst-precursor is a 1 : 1 molar ratio. Alternate preferred ranges include up to 500: 1, alternately up to 200: 1, alternately up to 100: 1 alternately from 1 : 1 to 50: 1.
  • alumoxane is present at zero mol%, alternately the alumoxane is present at a molar ratio of aluminum to transition metal less than 500: 1, preferably less than 300: 1, preferably less than 100: 1, preferably less than 1 : 1.
  • the alumoxane has been treated to remove free alkyl aluminum compounds, particularly trimethyl aluminum.
  • the activator used herein to produce the vinyl terminated polyolefin is bulky as defined herein and is discrete.
  • Aluminum alkyl or organoaluminum compounds which may be utilized as co- activators (or scavengers) include trimethylaluminum, triethylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, and the like.
  • an ionizing or stoichiometric activator neutral or ionic non-coordinating anion (as defined in USSN 12/143,663, filed on June 20, 2008), such as tri (n-butyl) ammonium tetrakis (pentafluorophenyl) borate, a tris perfluorophenyl boron metalloid precursor or a tris perfluoronapthyl boron metalloid precursor, polyhalogenated heteroborane anions (WO 98/43983), boric acid (U.S. Patent No. 5,942,459), or combination thereof.
  • an ionizing or stoichiometric activator neutral or ionic non-coordinating anion (as defined in USSN 12/143,663, filed on June 20, 2008), such as tri (n-butyl) ammonium tetrakis (pentafluorophenyl) borate, a tris perfluorophenyl boron metalloid precursor or a tris
  • the activator is N,N-dimethylanilinium tetrakis(perfluoronapthyl)borate, ⁇ , ⁇ -dimethylanilinium tetrakis(perfluorobiphenyl)borate, ⁇ , ⁇ -dimethylanilinium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triphenylcarbenium tetrakis(perfluoronaphthyl)borate, triphenylcarbenium tetrakis(perfluorobiphenyl)borate, triphenylcarbenium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, or triphenylcarbenium tetrakis(perfluorophenyl)borate.
  • N,N-dimethylanilinium tetrakis(perfluoronapthyl)borate ⁇ , ⁇ -dimethylanilinium tetra
  • each R 1 is, independently, a halide, preferably a fluoride
  • each R2 is, independently, a halide, a to C20 substituted aromatic hydrocarbyl group or a siloxy group of the formula -0-Si-R a , where R a is a Q to C20 hydrocarbyl or hydrocarbylsilyl group (preferably R2 is a fluoride or a perfluorinated phenyl group);
  • each R3 is a halide, to C20 substituted aromatic hydrocarbyl group or a siloxy group of the formula -0-Si-R a , where R a is a to C20 hydrocarbyl or hydrocarbylsilyl group (preferably R3 is a fluoride or a perfluorinated aromatic hydrocarbyl group); wherein R2 and R3 can form one or more saturated or unsaturated, substituted or unsubstituted rings (preferably R2 and R3 form a perfluorinated phenyl ring);
  • L is an neutral Lewis base
  • d is 1, 2, or 3;
  • the anion has a molecular weight of greater than 1020 g/mol
  • Molecular volume is used herein as an approximation of spatial steric bulk of an activator molecule in solution. Comparison of substituents with differing molecular volumes allows the substituent with the smaller molecular volume to be considered “less bulky” in comparison to the substituent with the larger molecular volume. Conversely, a substituent with a larger molecular volume may be considered “more bulky” than a substituent with a smaller molecular volume.
  • Molecular volume may be calculated as reported in "A Simple "Back of the Envelope” Method for Estimating the Densities and Molecular Volumes of Liquids and Solids," Journal of Chemical Education, Vol. 71, No. 11, November 1994, pp. 962-964.
  • V s is the sum of the relative volumes of the constituent atoms, and is calculated from the molecular formula of the substituent using the following table of relative volumes. For fused rings, the V s is decreased by 7.5% per fused ring.
  • Exemplary bulky activators useful in catalyst systems herein include: trimethylammonium tetrakis(perfluoronaphthyl)borate, triethylammonium tetrakis(perfluoronaphthyl)borate, tripropylammonium tetrakis(perfluoronaphthyl)borate, tri(n-butyl)ammonium tetrakis(perfluoronaphthyl)borate, tri(t-butyl)ammonium tetrakis(perfluoronaphthyl)borate, ⁇ , ⁇ -dimethylanilinium tetrakis(perfluoronaphthyl)borate, ⁇ , ⁇ -diethylanilinium tetrakis(perfluoronaphthyl)borate, N,N-dimethyl-(2,4,6- trimethylanilinium) tetrakis
  • the typical activator-to-catalyst-precursor ratio is a 1 : 1 molar ratio for non- alumoxane activators.
  • Alternate preferred ranges include from 0.1 : 1 to 100: 1, alternately from 0.5: 1 to 200: 1, alternately from 1 : 1 to 500: 1 alternately from 1 : 1 to 1000: 1.
  • a particularly useful range is from 0.5: 1 to 10: 1, preferably 1 : 1 to 5: 1.
  • catalyst compounds can be combined with one or more activators or activation methods described above.
  • activators have been described in U.S. Patent Nos. 5, 153, 157; 5,453,410; European publication EP 0 573 120 B l; PCT publications WO 94/07928; and WO 95/14044. These documents all discuss the use of an alumoxane in combination with an ionizing activator.
  • the catalyst system may comprise an inert support material.
  • the supported material is a porous support material, for example, talc, and inorganic oxides.
  • Other support materials include zeolites, clays, organoclays, or any other organic or inorganic support material and the like, or mixtures thereof.
  • the support material is an inorganic oxide in a finely divided form.
  • Suitable inorganic oxide materials for use in metallocene catalyst systems herein include Groups 2, 4, 13, and 14 metal oxides such as silica, alumina and mixtures thereof.
  • Other inorganic oxides that may be employed either alone or in combination with the silica, or alumina are magnesia, titania, zirconia, and the like.
  • Other suitable support materials can be employed, for example, finely divided functionalized polyolefins such as finely divided polyethylene.
  • Particularly useful supports include magnesia, titania, zirconia, montmorillonite, phyllosilicate, zeolites, talc, clays, and the like. Also, combinations of these support materials may be used, for example, silica-chromium, silica-alumina, silica-titania, and the like.
  • Preferred support materials include AI2O3, ⁇ 3 ⁇ 4, S1O2, and combinations thereof, more preferably S1O2, AI2O3, or S1O2/AI2O3 .
  • the support material most preferably an inorganic oxide, has a surface area in the range of from about 10 to about 700 m 2 /g, pore volume in the range of from about 0.1 to about 4.0 cc/g and average particle size in the range of from about 5 to about 500 ⁇ . More preferably, the surface area of the support material is in the range of from about 50 to about 500 m 2 /g, pore volume of from about 0.5 to about 3.5 cc/g and average particle size of from about 10 to about 200 ⁇ .
  • the surface area of the support material is in the range is from about 100 to about 400 m 2 /g, pore volume from about 0.8 to about 3.0 cc/g and average particle size is from about 5 to about 100 ⁇ .
  • the average pore size of the support material useful in the invention is in the range of from 10 to 1000 A, preferably 50 to about 500 A, and most preferably 75 to about 350 A.
  • the support material should be dry, that is, free of absorbed water. Drying of the support material can be effected by heating or calcining at about 100°C to about 1000°C, preferably at least about 600° C. When the support material is silica, it is heated to at least 200°C, preferably about 200°C to about 850°C, and most preferably at about 600°C; and for a time of about 1 minute to about 100 hours, from about 12 hours to about 72 hours, or from about 24 hours to about 60 hours.
  • the calcined support material must have at least some reactive hydroxyl (OH) groups to produce the catalyst system of this invention.
  • the calcined support material is then contacted with at least one polymerization catalyst comprising at least one metallocene compound and an activator.
  • the support material having reactive surface groups, typically hydroxyl groups, is slurried in a non-polar solvent and the resulting slurry is contacted with a solution of a metallocene compound and an activator.
  • the slurry of the support material in the solvent is prepared by introducing the support material into the solvent, and heating the mixture to about 0 to about 70°C, preferably to about 25 to about 60°C, preferably at room temperature. Contact times typically range from about 0.5 hours to about 24 hours, from about 0.5 hours to about 8 hours, or from about 0.5 hours to about 4 hours.
  • Suitable non-polar solvents are materials in which all of the reactants used herein, i.e., the activator, and the metallocene compound, are at least partially soluble and which are liquid at reaction temperatures.
  • Preferred non-polar solvents are alkanes, such as isopentane, hexane, n-heptane, octane, nonane, and decane, although a variety of other materials including cycloalkanes, such as cyclohexane, aromatics, such as benzene, toluene and ethylbenzene, may also be employed.
  • the support material is contacted with a solution of a metallocene compound and an activator, such that the reactive groups on the support material are titrated, to form a supported polymerization catalyst.
  • the period of time for contact between the metallocene compound, the activator, and the support material is as long as is necessary to titrate the reactive groups on the support material.
  • titrate is meant to react with available reactive groups on the surface of the support material, thereby reducing the surface hydroxyl groups by at least 80%, at least 90%, at least 95%, or at least 98%.
  • the surface reactive group concentration may be determined based on the calcining temperature and the type of support material used.
  • the support material calcining temperature affects the number of surface reactive groups on the support material available to react with the metallocene compound and an activator: the higher the drying temperature, the lower the number of sites.
  • the support material is silica which, prior to the use thereof in the first catalyst system synthesis step, is dehydrated by fluidizing it with nitrogen and heating at about 600°C for about 16 hours, a surface hydroxyl group concentration of about 0.7 millimoles per gram (mmols/gm) is typically achieved.
  • mmols/gm millimoles per gram
  • the exact molar ratio of the activator to the surface reactive groups on the carrier will vary. Preferably, this is determined on a case-by-case basis to assure that only so much of the activator is added to the solution as will be deposited onto the support material without leaving excess of the activator in the solution.
  • the amount of the activator which will be deposited onto the support material without leaving excess in the solution can be determined in any conventional manner, e.g., by adding the activator to the slurry of the carrier in the solvent, while stirring the slurry, until the activator is detected as a solution in the solvent by any technique known in the art, such as by !fi NMR.
  • the amount of the activator added to the slurry is such that the molar ratio of B to the hydroxyl groups (OH) on the silica is about 0.5: 1 to about 4: 1, preferably about 0.8: 1 to about 3 : 1, more preferably about 0.9: 1 to about 2: 1 and most preferably about 1 : 1.
  • the amount of boron on the silica may be determined by using ICPES (Inductively Coupled Plasma Emission Spectrometry), which is described in J. W. Olesik, "Inductively Coupled Plasma- Optical Emission Spectroscopy," in the Encyclopedia of Materials Characterization, C. R. Brundle, C. A. Evans, Jr. and S.
  • a composition comprising a multiblock polyolefin represented by the formula:
  • Z is the portion of a cyclic monomer having at least one internal double bond that remains after a ring-opening metathesis reaction, preferably Z is a C ⁇ to hydrocarbyl or substituted hydrocarbyl (including olefins and substituted olefins), preferably a Q to C ⁇ hydrocarbyl or substituted hydrocarbyl, preferably a Q to hydrocarbyl or substituted hydrocarbyl (preferably the substituent on the substituted hydrocarbyl is a C [ to C 5 hydrocarbyl or a Cj to C5 substituted hydrocarbyl (such as methyl, ethyl, propyl, butyl, pentyl, or an isomer thereof), a halogen (such as Br, CI, I, or F), an ether or ester (such as an alkyl ether, an alkyl ester,, an aryl ether or an aryl ester, where the alkyl is a Q to C20 alkyl group and the
  • PO and PO* are polyolefins, preferably PO and PO* are each, independently, a substituted or unsubstituted hydrocarbyl group having 9 to 10,000 carbon atoms (preferably 20 to 7500 carbon atoms, preferably 30 to 4000, preferably from 40 to 2000), preferably at least one of PO and PO* has from 20 to 10,000 carbon atoms, preferably 30 to 2000; and
  • n is 1 to about 10,000, in particular from about 10 to about 7500, more particularly from about 50 to about 5000 and in one aspect from about 100 to about 2000.
  • the mixture of I, II, and III comprises about 30% to about 70% of multiblock polyolefin (I), about 1% to about 30% of multiblock polyolefin (II), and about 1% to about 30% multiblock polyolefin (III).
  • the mixture of la, Ila, and Ilia comprises about 30% to about 70% of multiblock polyolefin (la), about 1% to about 30% of multiblock polyolefin (Ila), and about 1% to about 30% multiblock polyolefin (Ilia).
  • composition of any of paragraphs 1 through 6, wherein the multiblock polyolefin has a Mn of 200 to 200,000 g/mol, preferably from 400 to 20,000 g/mol, preferably 300 to
  • composition of any of paragraphs 1 through 17, wherein the PO and the PO* comprise about 15 wt% to about 95 wt% ethylene, preferably about 30 wt% to about 95 wt% ethylene.
  • composition of any of paragraphs 1 through 13, wherein the multiblock polyolefin has a viscosity at 60°C of greater than 1000 cP, greater than 12,000 cP, or greater than 100,000 cP, and less than 200,000 cP, less than 150,000 cP, or less than 100,000 cP.
  • M is a Group 8 metal
  • X and X 1 are, independently, any anionic ligand, or X and X 1 may be joined to form a dianionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • L and L 1 are neutral two electron donors, L and L 1 may be joined to form a single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms; L and X may be joined to form a bidentate monoanionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms; L 1 and X 1 may be joined to form a multidentate monoanionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • R and R 1 are, independently, hydrogen or Q to C30 substituted or unsubstituted hydrocarbyl; R 1 and L 1 or X 1 may be joined to form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms; and
  • R and L or X may be joined to form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms.
  • M is Ru or Os
  • X and X 1 are, independently, a halogen, an alkoxide or a triflate, or X and X 1 may be joined to form a dianionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • L and L 1 are, independently, a phosphine or a N-heterocyclic carbene, L and L 1 may be joined to form a single ring of up to 30 non-hydrogen atoms or a multinuclear ring system, of up to 30 non-hydrogen atoms;
  • L and X may be joined to form a multidentate monoanionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • L 1 and X 1 may be joined to form a multidentate monoanionic group and may form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • R and R 1 are, independently, hydrogen or a Q to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl;
  • R 1 and L 1 or X 1 may be joined to form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms;
  • R and L or X may be joined to form single ring of up to 30 non-hydrogen atoms or a multinuclear ring system of up to 30 non-hydrogen atoms.
  • the alkene metathesis catalyst is one or more of: tricyclohexylphosphine[l,3-bis(2,4,6-trimethylphenyl)imidazol-2-ylidene][3- phenyl- lH-inden- 1 -ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[3-phenyl- 1H- inden- 1 -yliden] [ 1 ,3 -bis(2,4,6-trimethylphenyl)-4,5-dihydro-imidazol-2-ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[l,3-bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2- ylidene][(phenylthio)methylene]ruthenium(II) dichloride, bis(tricyclohexylphosphine[l,3-bis
  • cyclic hydrocarbyl monomer comprising at least one internal double bond comprises one or more of cyclopropene, cyclobutene, cyclopentene, cyclohexene, methylcyclohexene, cycloheptene, cyclooctadiene, cyclooctene, norbornadiene, norbornene, cyclobutadiene, cyclohexadiene, cycloheptadiene, cyclooctatetraene, 1,5-cyclooctadiene, l,5-dimethyl-l,5-cyclooctadiene, dicyclopentadiene, and isomers thereof.
  • 13 C NMR data was collected at either room temperature or 120°C in a 10 mm probe using a Varian spectrometer with a 1 Hydrogen frequency of at least 400 MHz.
  • the spectra were acquired using time averaging to provide a signal to noise level adequate to measure the signals of interest.
  • Samples were dissolved in tetrachloroethane-d2 at concentrations between 10 wt% to 15 wt% prior to being inserted into the spectrometer magnet.
  • Polypropylene microstructure is determined by 13 C NMR spectroscopy, including the concentration of isotactic and syndiotactic diads ([m] and [r]), triads ([mm] and [rr]), and pentads ([mmmm] and [rrrr]).
  • the designation "m” or “r” describes the stereochemistry of pairs of contiguous propylene groups, "m” referring to meso and "r” to racemic. Samples are dissolved in d2-l, l,2,2-tetrachloroethane, and spectra recorded at 125°C using a 100 MHz (or higher) NMR spectrometer.
  • the "propylene tacticity index”, expressed herein as [m/r], is calculated as defined in H.N. Cheng, Macromolecules, 17, pg. 1950 (1984).
  • [m/r] is 0 to less than 1.0, the polymer is generally described as syndiotactic, when [m/r] is 1.0 the polymer is atactic, and when [m/r] is greater than 1.0 the polymer is generally described as isotactic.
  • the system was operated at an eluent flow rate of 2.0 mL/min and an oven temperature of 165°C. 1,2,4- trichlorobenzene was used as the eluent.
  • the polymer samples were dissolved in 1,2,4- trichlorobenzene at a concentration of 0.1 - 0.9 mg/mL. 250 uL of a polymer solution was injected into the system. The concentration of the polymer in the eluent was monitored using an evaporative light scattering detector. The molecular weights presented are relative to linear polystyrene standards.
  • DSC Differential Scanning Calorimetry
  • Weight percent 1-octene was obtained from the ratio of peak heights at 1378 and 4322 cm -1 . This method was calibrated using a set of ethylene/ 1-octene copolymers with a range of known wt% 1-octene content.
  • Catalyst Zhan IB is l,3-Bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2-ylidene[2-(i- propoxy)-5-(N,N-dimethylaminosulfonyl)phenyl]methyleneruthenium(II) dichloride (Strem Chemicals, catalog #44-0082) and Catalyst Neolyst M2 is tricyclohexylphosphine[3-phenyl- lH-inden- 1 -ylidene] [1 ,3-bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2- ylidene]ruthenium(II) dichloride (Strem Chemicals, catalog # 44-7777), aPP is atactic polypropylene, iPP is isotactic polypropylene, EP is ethylene-propylene copolymer, TCE is 1, 1,2,2-tetrach
  • 1,5-cyclooctadiene (1,5-COD) or l,5-dimethyl-l,5-cyclooctadiene (1,5-Me 2 -1,5- COD) were purchased from Sigma Aldrich.
  • the vinyl-terminated iPP, vinyl-terminated EP, and vinyl-terminated aPP were prepared as described in WO 2009/155471.
  • test tubes outfitted with stir bars were charged with 1,5- cyclooctadiene (1,5-COD) or l,5-dimethyl-l,5-cyclooctadiene (1,5-Me 2 -1,5-C0D)
  • Various amounts of the vinyl-terminated polymer dimers from Examples 1 -4 and toluene were added as indicated in Table 1.
  • the test tubes were transferred to a metal block, which was heated to 55°C. Stirring was initiated, and the Zhan IB catalyst (25 ⁇ ⁇ of a 0.04 M toluene solution) was added. Heating and stirring were continued for 18 h, during which some solvent loss occurred. Ethyl vinyl ether (0.1 mL) was added to quench any remaining active catalyst.
  • the samples were dried in vacuo and then analyzed by GPC. Results are tabulated in Table 1.
  • the product was fractionated into two components using preparative temperature rising elution fractionation (Prep-TREF).
  • the component that eluted below 30°C (34 area%) was shown to contain both polypropylene and polyethylene by NMR spectroscopy.
  • a second component with a peak elution temperature of 98°C (66 area%) was shown by 3 ⁇ 4 NMR spectroscopy to contain only polyethylene.
  • the polyethylene is presumed to be derived from ROMP of cyclooctadiene.
  • compositions, an element or a group of elements are preceded with the transitional phrase "comprising,” it is understood that we also contemplate the same composition or group of elements with transitional phrases “consisting essentially of,” “consisting of,” “selected from the group of consisting of,” or “is” preceding the recitation of the composition, element, or elements and vice versa.

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  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
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Abstract

La présente invention concerne une composition contenant une polyoléfine multiséquencée représentée par la formule : PO-(-C=C-Z-)n-C=C-PO* (I) ou PO-(-C-C-Z-)n-C-C-PO* (Ia), où Z est la partie d'un monomère cyclique contenant au moins une double liaison interne qui reste après la réaction d'ouverture de cycle par métathèse; PO et PO* sont chacun indépendamment des polyoléfines; et n est compris entre 1 et 10 000. L'invention concerne également un procédé de production de cette polyoléfine, le procédé comprenant le contact d'un catalyseur de métathèse d'alcène avec un dimère de polyoléfines à terminaison vinylique et un monomère d'hydrocarbyle cyclique contenant au moins une double liaison interne.
EP12764275.9A 2011-03-25 2012-03-05 Polymères triséquencés à base d'oléfines obtenus par polymérisation par ouverture de cycle par métathèse Withdrawn EP2688954A4 (fr)

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US13/072,432 US8669330B2 (en) 2011-03-25 2011-03-25 Olefin triblock polymers via ring-opening metathesis polymerization
EP11167037 2011-05-23
PCT/US2012/027670 WO2012134713A2 (fr) 2011-03-25 2012-03-05 Polymères triséquencés à base d'oléfines obtenus par polymérisation par ouverture de cycle par métathèse
EP12764275.9A EP2688954A4 (fr) 2011-03-25 2012-03-05 Polymères triséquencés à base d'oléfines obtenus par polymérisation par ouverture de cycle par métathèse

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WO2000055218A1 (fr) * 1999-03-18 2000-09-21 California Institute Of Technology Nouveaux copolymeres a trois sequences et a deux sequences aba, et procedes de preparation correspondant
EP1862491A1 (fr) * 2005-03-22 2007-12-05 Zeon Corporation Résine thermoplastique, procédé servant à produire celle-ci et matière de moulage
WO2008141941A1 (fr) * 2007-05-23 2008-11-27 Basf Se Poylstyrol isotactique à groupes réactifs

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BR9808578A (pt) * 1997-02-07 2000-05-30 Exxon Chemical Patents Inc Polìmeros de propileno incorporando macrÈmeros de polietileno
GB0428172D0 (en) * 2004-12-23 2005-01-26 Ici Plc Olefin metathesis polymerisation
US8283419B2 (en) * 2008-06-20 2012-10-09 Exxonmobil Chemical Patents Inc. Olefin functionalization by metathesis reaction

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WO2000055218A1 (fr) * 1999-03-18 2000-09-21 California Institute Of Technology Nouveaux copolymeres a trois sequences et a deux sequences aba, et procedes de preparation correspondant
EP1862491A1 (fr) * 2005-03-22 2007-12-05 Zeon Corporation Résine thermoplastique, procédé servant à produire celle-ci et matière de moulage
WO2008141941A1 (fr) * 2007-05-23 2008-11-27 Basf Se Poylstyrol isotactique à groupes réactifs

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WO2012134713A2 (fr) 2012-10-04
EP2688954A4 (fr) 2014-10-01

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