# Patent

## Title
Olefin functionalization by metathesis reaction

## Abstract

This invention relates to a process to functionalize propylene co-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene a co-oligomer having an Mn of 300 to 30,000 g/mol comprising 10 to 90 mol % propylene and 10 to 90 mol % of ethylene, wherein the oligomer has at least X % allyl chain ends, where: 1) X=(−0.94 (mol % ethylene incorporated)+100), when 10 to 60 mol % ethylene is present in the co-oligomer, and 2) X=45, when greater than 60 and less than 70 mol % ethylene is present in the co-oligomer, and 3) X=(1.83*(mol % ethylene incorporated)−83), when 70 to 90 mol % ethylene is present in the co-oligomer. This invention also relates to a process to functionalize propylene homo-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene homo-oligomer, comprising propylene, wherein the oligomer has: at least 93% allyl chain ends, an Mn of about 500 to about 20,000 g/mol, an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.2:1.0, and less than 100 ppm aluminum.

## Background
PRIORITY CLAIM
This application is a continuation in part of U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008, which is incorporated by reference herein.
STATEMENT OF RELATED CASES
This application is also related to U.S. Ser. No. 12/487,739, filed Jun. 19, 2009.


FIELD OF THE INVENTION
This invention relates to functionalization of vinyl terminated polyolefins by metathesis reactions.
BACKGROUND OF THE INVENTION
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. These reactions, however, have had limited success with the metathesis of functionalized olefins.
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.
R. T. Mathers and G. W. Coates Chem. Commun. 2004, 422-423 disclose examples of using cross-metathesis to functionalize polyolefins containing pendant vinyl groups to form polar-functionalized products with a graft-type structure.
D. Astruc et al. J. Am. Chem. Soc. 2008, 130, 1495-1506, and D. Astruc et al. Angew. Chem. Int. Ed. 2005, 44, 7399-7404 disclose examples of using cross metathesis to functionalize non-polymeric molecules containing vinyl groups.
For reviews of methods to form end-functionalized polyolefins, see: (a) S. B. Amin and T. J. Marks Angew. Chem. Int. Ed. 2008, 47, 2006-2025; (b) T. C. Chung Prog. Polym. Sci. 2002, 27, 39-85; (c) R. G. Lopez, F. D'Agosto, C. Boisson Prog. Polym. Sci. 2007, 32, 419-454.
U.S. Ser. No. 12/487,739, filed Jun. 19, 2009 discloses certain vinyl terminated oligomers and polymers that are functionalized for use in lubricant applications.
U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008 discloses certain vinyl terminated oligomers and polymers that are functionalized in U.S. Ser. No. 12/487,739, filed Jun. 19, 2009.
Additional references of interest include: U.S. Pat. No. 4,988,764.
Thus, there is a need to develop a means to provide functionalized polyolefins (particularly end-functionalized) by metathesis reactions, particularly reactions with good conversion, preferably under mild reaction conditions is a minimal number of steps. There is also a need for a single reaction type that allows for a variety of functional groups to be added to polyolefins in an economical manner. The instant invention's use of olefin alkene metathesis to introduce functional groups is both a commercially economical and an “atom-economical” route to end functionalized polyolefins.
This invention further provides vinyl-terminated polyolefins that react with functionalized alkenes in the presence of a metathesis catalyst to form polar end-functionalized polyolefins.
End-functionalized polyolefins that feature a chemically reactive or polar end group are of interest for use in a broad range of applications as compatibilizers, tie-layer modifiers, surfactants, and surface modifiers. Herein is described a novel method for their production by the metathesis of vinyl-terminated polyolefins with functionalized alkenes. This method is useful in a range of polyolefins, including isotactic polypropylene (iPP), atactic polypropylene (aPP), ethylene propylene copolymer (EP), and polyethylene (PE).
SUMMARY OF THE INVENTION
This invention relates to a process to functionalize polyolefins (as used herein polyolefin is defined to include both polymers and oligomers) comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and one or more vinyl terminated polyolefins, preferably the vinyl terminated polyolefin comprise one or more of:

    a) a propylene co-oligomer having an Mn of 300 to 30,000 g/mol (as measured by 1H NMR) comprising 10 to 90 mol % propylene and 10 to 90 mol % of ethylene, wherein the oligomer has at least X % allyl chain ends (relative to total unsaturations), where: 1) X=(−0.94 (mol % ethylene incorporated)+100), when 10 to 60 mol % ethylene is present in the co-oligomer, and 2) X=45, when greater than 60 and less than 70 mol % ethylene is present in the co-oligomer, and 3) X=(1.83*(mol % ethylene incorporated)−83), when 70 to 90 mol % ethylene is present in the co-oligomer; and/or
    b) a propylene oligomer, comprising more than 90 mol % propylene and less than 10 mol % ethylene, wherein the oligomer has: at least 93% allyl chain ends, an Mn of about 500 to about 20,000 g/mol (as measured by 1H NMR), an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0, and less than 1400 ppm aluminum; and/or c) a propylene oligomer, comprising at least 50 mol % propylene and from 10 to 50 mol % ethylene, wherein the oligomer has: at least 90% allyl chain ends, Mn of about 150 to about 10,000 g/mol (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.3:1.0, wherein monomers having four or more carbon atoms are present at from 0 to 3 mol %; and/or
    d) a propylene oligomer, comprising at least 50 mol % propylene, from 0.1 to 45 mol % ethylene, and from 0.1 to 5 mol % C4 to C12 olefin, wherein the oligomer has: at least 87% allyl chain ends (alternately at least 90%), an Mn of about 150 to about 10,000 g/mol, (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0; and/or
    e) a propylene oligomer, comprising at least 50 mol % propylene, from 0.1 to 45 wt% ethylene, and from 0.1 to 5 mol % diene, wherein the oligomer has: at least 90% allyl chain ends, an Mn of about 150 to about 10,000 g/mol (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.7:1 to 1.35:1.0; and/or
    f) a homooligomer, comprising propylene, wherein the oligomer has: at least 93% allyl chain ends, an Mn of about 500 to about 20,000 g/mol (as measured by 1H NMR), an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.2:1.0, and less than 1400 ppm aluminum.




DETAILED DESCRIPTION
This invention relates to a process to functionalize vinyl terminated polyolefin comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and one or more vinyl terminated oligomers or polymers, preferably comprising one or more of the vinyl terminated oligomers described herein.
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).
Typically, 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 the heteroatom containing alkene reactant are charged to the reactor per mole of polyolefin charged.
Typically, 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 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 C4-10 alkanes, chlorobenzene, and aromatic and alkylsubstituted aromatic compounds such as benzene, toluene, mesitylene, and xylene. In a preferred embodiment, 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. As used herein, the term continuous means a system that operates without interruption or cessation. For example, 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.
In a preferred embodiment, the productivity of the process is at least 200 g of polar end-functionalized 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.
This invention further relates to a process, preferably an in-line process, preferably a continuous process, to produce functionalized polyolefin, comprising introducing monomer and catalyst system into a reactor, obtaining a reactor effluent containing vinyl terminated polyolefin, optionally removing (such as flashing off) solvent, unused monomer and/or other volatiles, obtaining vinyl terminated polyolefin (such as those described herein), introducing vinyl terminated polyolefin, alkene metathesis catalyst and heteroatom containing alkene (as described herein) into a reaction zone (such as a reactor, an extruder, a pipe and/or a pump) and obtaining functionalized polyolefin (such as those described herein).
Alkene Metathesis Catalysts
An alkene metathesis catalyst is a compound that catalyzes the reaction between a vinyl terminated oligomer (or polymer) with a heteroatom containing alkene to produce a heteroatom functionalized oligomer (or polymer), typically with the elimination of ethylene.
In a preferred embodiment, the alkene metathesis catalyst is represented by the Formula (I):




where:

    M is a Group 8 metal, preferably Ru or Os, preferably Ru;
    X and X1 are, independently, any anionic ligand, preferably a halogen (preferably Cl), an alkoxide or a triflate, or X and X1 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 L1 are, independently, a neutral two electron donor, preferably a phosphine or a N-heterocyclic carbene, L and L1 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;
    L1 and X1 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 R1 are, independently, hydrogen or C1 to C30 substituted or unsubstituted hydrocarbyl (preferably a C1 to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl);
    R1 and L1 or X1 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.


For purposes of this invention and claims thereto a substituted hydrocarbyl is a radical made of carbon and hydrogen where at least one hydrogen is replaced by a heteroatom. For purposes of this invention and claims thereto a substituted alkyl or aryl group is a radical made of carbon and hydrogen where at least one hydrogen is replaced by a heteroatom or a linear, branched, or cyclic substituted or unsubstituted hydrocarbyl group having 1 to 30 carbon 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 C1 to C12 hydrocarbyl groups) or a C1 to C10 hydrocarbyl, preferably a C1 to C10 alkyl group, preferably methyl, ethyl, propyl, butyl, or phenyl.
Preferred triflates are represented by the Formula (II):




where R2 is hydrogen or a C1 to C30 hydrocarbyl group, preferably a C1 to C12 alkyl group, preferably methyl, ethyl, propyl, butyl, or phenyl.

Preferred N-heterocyclic carbenes are represented by the Formula (III) or the Formula (IV):




where

    each R4 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 CH2C(CH3)3; and
    each R5 is hydrogen, a halogen, or a C1 to C12 hydrocarbyl group, preferably hydrogen, bromine, chlorine, methyl, ethyl, propyl, butyl, or phenyl.


In other useful embodiments, one of the N groups bound to the carbene in formula (III) or (IV) is replaced with an S, O or P atom, preferably an S atom.
Other useful N-heterocyclic carbenes include the compounds described in Hermann, W. A. Chem. Eur. J. 1996, 2, 772 and 1627; Enders, D. et al. Angew. Chem. Int. Ed. 1995, 34, 1021; Alder R. W., Angew. Chem. Int. Ed. 1996, 35, 1121; and Bertrand, G. et al. Chem. Rev. 2000, 100, 39.
In a preferred embodiment, the alkene metathesis catalyst is one or more of tricyclohexylphosphine[1,3-bis(2,4,6-trimethylphenyl)imidazol-2-ylidene][3-phenyl-1H-inden-1-ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[3-phenyl-1H-inden-1-ylidene][1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydro-imidazol-2-ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2-ylidene][(phenylthio)methylene]ruthenium(II) dichloride, bis(tricyclohexylphosphine)-3-phenyl-1H-inden-1-ylideneruthenium(II) dichloride, 1,3-Bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2-ylidene[2-(i-propoxy)-5-(N,N-dimethylaminosulfonyl)phenyl]methyleneruthenium(II) dichloride, and [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]-[2-[[(4-methylphenyl)imino]methyl]-4-nitrophenolyl]-[3-phenyl-1H-inden-1-ylidene]ruthenium(II) chloride.
In another embodiment, the alkene metathesis catalyst is represented in Formula (I) above, where: M is Os or Ru; R1 is hydrogen; X and X1 may be different or the same and are any anionic ligand; L and L1 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, C1-C20 alkyl, or aryl. The C1-C20 alkyl may optionally be substituted with one or more aryl, halide, hydroxy, C1-C20 alkoxy, or C2-C20 alkoxycarbonyl groups. The aryl may optionally be substituted with one or more C1-C20 alkyl, aryl, hydroxyl, C1-C5 alkoxy, amino, nitro, or halide groups. L and L1 are preferably phosphines of the formula PR3′ R4′ R5′, where R3′ is a secondary alkyl or cycloalkyl, and R4′ and R5′ are aryl, C1-C10 primary alkyl, secondary alkyl, or cycloalkyl. R4′ and R5′ may be the same or different. L and L1 preferably the same and are -P(cyclohexyl)3, -P(cyclopentyl)3, or-P(isopropyl)3. X and X1 are most preferably the same and are chlorine.
In another embodiment of the present invention, the ruthenium and osmium carbene compounds have the Formula (V):




where M is Os or Ru, preferably Ru; X, X1, L and L1 are as described above; and R9 and R10 may be different or the same and may be hydrogen, substituted or unsubstituted alkyl, or substituted or unsubstituted aryl. The R9 and R10 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. Pat. No. 6,111,121.

In another embodiment, the alkene metathesis catalyst useful herein may be any of the catalysts described in U.S. Pat. No. 6,111,121, U.S. Pat. No. 5,312,940, U.S. Pat. No. 5,342,909, US 7,329,758, U.S. Pat. No. 5,831,108, U.S. Pat. No. 5,969,170, U.S. Pat. No. 6,759,537, U.S. Pat. No. 6,921,735, US 2005-0261451 A1, including but not limited to, benzylidene-bis(tricyclohexylphosphine)dichlororuthenium, benzylidene[1,3-bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(tricyclohexylphosphine)ruthenium, dichloro(o-isopropoxyphenylmethylene)(tricyclohexylphosphine)ruthenium(II), (1,3-Bis-(2,4,6-trimethylphenyl)-2-imidazolidinylidene)dichloro(o-isopropoxyphenylmethylene)ruthenium, 1,3-Bis(2-methylphenyl)-2-imidazolidinylidene]dichloro(2-isopropoxyphenylmethylene)ruthenium(II), [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro[3-(2-pyridinyl)propylidene]ruthenium(II), [1,3-Bis(2-methylphenyl)-2-imidazolidinylidene]dichloro(phenylmethylene) (tricyclohexylphosphine)ruthenium(II), [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(3-methyl-2-butenylidene)(tricyclohexylphosphine)ruthenium(II), and [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(benzylidene)bis(3-bromopyridine)ruthenium(II).
In another embodiment, the Schrock type metathesis catalysts may be used herein as alkene metathesis catalysts. In another embodiment, the alkene metathesis catalyst useful herein may be any of the catalysts described in U.S. Pat. No. 6,346,652, U.S. Pat. No. 6,121,473, U.S. Pat. No. 5,142,073, U.S. Pat. No. 5,146,033, U.S. Pat. No. 5,087,710, WO 2008/066754, US 2008/0119678, US 2005/0154221, EP 1 056 756 B1, EP 1 501 784 A1, EP 0 509 034 A1, WO 2000/002834; WO 1999/042469, WO 1992/019631, WO1991/009825. Preferred examples include 2,6-Diisopropylphenylimidoneophylidene molybdenum(VI) bis(t-butoxide), 2,6-Diisopropylphenylimidoneophylidene molybdenum(VI) bis(hexafluoro-t-butoxide), 2,6-Diisopropylphenylimido neophylidenemolybdenum(VI) bis(trifluoromethanesulfonate)dimethoxyethane adduct, and 2,6-Diisopropylphenylimidoneophylidene[racemic-BIPHEN]molybdenum(VI).
The above named catalysts are generally available for Sigma-Aldrich Corp. (St. Louis, Mo.) or Strem Chemicals, Inc. (Newburyport, Mass.).
Heteroatom Containing Alkenes
Heteroatom containing alkenes useful in the process described herein include those represented by the formula: H2C═CH—R or R*—HC═CH—R, where R* and R are, independently, a heteroatom containing group, preferably containing from 1 to 30 carbon atoms and at least one heteroatom (preferably the heteroatom(s) are selected from the group consisting of Si, P, O, S, N, Cl, F, I and Br (preferably N, O, Cl and Br, preferably N and O). R and R* may contain 1, 2, 3, or 4 heteroatoms. In another embodiment, both R and R* contain at least one heteroatom. Heteroatom containing alkenes may include, one, two, three, four, five or six heteroatoms. Heteroatom containing alkenes may also include more than one unsaturation, preferably two, three, four, or five unsaturations, preferably as vinyl chain ends. For purposes of this invention and the claims thereto, a heteroatom is defined to be any non-carbon, non-hydrogen atom, preferably any group 13 to 17 element, excluding carbon.
Preferred R groups are selected from the group consisting of alcohols, amides, nitriles, imines, haloalkyls, acids, esters, anhydrides, acid-esters, oxycarbonyls, carbonyls, formyls, formylcarbonyls, hydroxyls, and acetyl halides.
Particularly preferred heteroatom containing alkenes include those represented by the formula: —C(O)—X, where the O is double bonded to the C and the X is hydrogen, nitrogen, hydroxy, oxyhydrocarbyl (e.g. ester), oxygen, the salt moiety -OM wherein M is a metal, e.g. alkali, alkaline earth, transition metal, copper, zinc and the like, oxyhetero, e.g. -O-Z wherein Z represents a heteroatom such as silicon, phosphorus, boron, sulfur, which heteroatom may be substituted with hydrocarbyl or oxyhydrocarbyl groups, or two acyl groups may be joined through (X).
Preferred R groups include alkyl amine groups, such as those represented by the formula: -D-N where D is a hydrocarbyl group having 1 to 12 carbon atoms, preferably ethyl, propyl, butyl, pentyl, hexyl, octyl, decy, dodeccyl.
Preferred R groups include alkyl nitrile groups, such as those represented by the formula: -D-C≡N where D is a hydrocarbyl group having 1 to 12 carbon atoms, preferably ethyl, propyl, butyl, pentyl, hexyl, octyl, decy, dodeccyl, and C is triple bonded to N.
Other preferred R groups include those represented by the formula: D-Y, where D is a hydrocarbyl group having 1 to 12 carbon atoms, preferably ethyl, propyl, butyl, pentyl, hexyl, octyl, decy, dodeccyl, and Y is N or O.
Preferred R groups include acyl groups derived from monounsaturated mono-or dicarboxylic acids and their derivatives, e.g. esters and salts.
In another embodiment, the R group is selected from the group consisting of (i) monounsaturated C4 to C10 dicarboxylic acid (preferably wherein (a) the carboxyl groups are vicinyl, (i.e. located on adjacent carbon atoms) and (b) at least one, preferably both, of said adjacent carbon atoms are part of said monounsaturation); (ii) derivatives of (i) such as anhydrides or C1 to C5 alcohol derived mono-or diesters of (i); (iii) monounsaturated C3 to C10 monocarboxylic acid wherein the carbon-carbon double bond is conjugated to the carboxyl group, i.e., of the structure —C═C—C(O)— (where O is double bonded to C), and (iv) derivatives of (iii) such as C1 to C5 alcohol derived monoesters of (iii).
Particularly preferred heteroatom containing alkenes include acrylonitrile, acrylamide, allyl amine, acrylic acid, crotonic acid, methacrylic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, itaconic anhydride, citraconic acid, citraconic anhydride, mesaconic acid, glutaconic acid, chloromaleic acid, aconitic acid, crotonic acid, methylcrotonic acid, sorbic acid, 3-hexenoic acid, 10-decenoic acid, 2-pentene-1,3,5-tricarboxylic acid, cinnamic acid, and lower alkyl (e.g. C1 to C4 alkyl) acid esters of the foregoing, e.g. methyl maleate, ethyl fumarate, methyl fumarate, etc. Particularly preferred heteroatom containing alkenes include methyl acrylate, acrylic acid, and 5-hexen-1-ol.
The functionalized vinyl terminated oligomers described herein may be further derivatized as described in U.S. Pat. No. 6,022,929.
Vinyl Terminated Olefin Oligomers and Polymers
Vinyl terminated olefin oligomers and polymers useful in this invention include propylene homo-oligomers, comprising propylene and less than 0.5 wt % comonomer, preferably 0 wt % comonomer, wherein the oligomer has:

    
    
        i) at least 93% allyl chain ends (preferably at least 95%, preferably at least 97%, preferably at least 98%);
        ii) a number average molecular weight (Mn) of about 500 to about 20,000 g/mol, as measured by 1H 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);
        iii) an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.3:1.0; and
    
    


iv) less than 1400 ppm aluminum, (preferably less than 1200 ppm, preferably less than 1000 ppm, preferably less than 500 ppm, preferably less than 100 ppm).
Vinyl terminated olefin oligomers and polymers useful in this invention also include propylene co-oligomers having an Mn of 300 to 30,000 g/mol as measured by 1H NMR (preferably 400 to 20,000, preferably 500 to 15,000, preferably 600 to 12,000, preferably 800 to 10,000, preferably 900 to 8,000, preferably 900 to 7,000 g/mol), comprising 10 to 90 mol % propylene (preferably 15 to 85 mol %, preferably 20 to 80 mol %, preferably 30 to 75 mol %, preferably 50 to 90 mol %) and 10 to 90 mol % (preferably 85 to 15 mol %, preferably 20 to 80 mol %, preferably 25 to 70 mol %, preferably 10 to 50 mol %) of one or more alpha-olefin comonomers (preferably ethylene, butene, hexene, or octene, preferably ethylene), wherein the oligomer has at least X % allyl chain ends (relative to total unsaturations), where: 1) X=(−0.94 (mol % ethylene incorporated)+100{alternately 1.20 (−0.94 (mol % ethylene incorporated)+100), alternately 1.50 (−0.94 (mol % ethylene incorporated)+100)}), when 10 to 60 mol % ethylene is present in the co-oligomer, and 2) X=45 (alternately 50, alternately 60), when greater than 60 and less than 70 mol % ethylene is present in the co-oligomer, and 3) X=(1.83*(mol % ethylene incorporated)−83, {alternately 1.20 [1.83* (mol % ethylene incorporated)−83], alternately 1.50 [1.83*(mol % ethylene incorporated)−83]}), when 70 to 90 mol % ethylene is present in the co-oligomer. Alternately X is 80% or more, preferably 85% or more, preferably 90% or more, preferably 95% or more. In an alternate embodiment the oligomer 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. Alternately, the oligomer 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 oligomers and polymers useful in this invention also include propylene oligomers, 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 oligomer has:

    
    
        i) at least 93% allyl chain ends (preferably at least 95%, preferably at least 97%, preferably at least 98%);
        ii) a number average molecular weight (Mn) of about 400 to about 30,000 g/mol, as measured by 1H 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);
        iii) an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1. 35:1.0, and
        iv) less than 1400 ppm aluminum, (preferably less than 1200 ppm, preferably less than 1000 ppm, preferably less than 500 ppm, preferably less than 100 ppm).
    
    


Vinyl terminated olefin oligomers and polymers useful in this invention also include propylene oligomers, 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 oligomer has:

    
    
        i) at least 90% allyl chain ends (preferably at least 91%, preferably at least 93%, preferably at least 95%, preferably at least 98%);
        ii) an Mn of about 150 to about 20,000 g/mol, as measured by 1H NMR (preferably 200 to 15,000, preferably 250 to 15,000, preferably 300 to 10,000, preferably 400 to 9,500, preferably 500 to 9,000, preferably 750 to 9,000); and
        iii) an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.3:1.0, wherein monomers having four or more carbon atoms are present at from 0 to 3 mol % (preferably at less than 1 mol %, preferably less than 0.5 mol %, preferably at 0 mol %).
    
    


Vinyl terminated olefin oligomers and polymers useful in this invention also include propylene oligomers, comprising:
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 % C4 to C12 olefin (such as butene, hexene or octene, preferably butene), wherein the oligomer has:

    
    
        i) at least 90% allyl chain ends (preferably at least 91%, preferably at least 93%, preferably at least 95%, preferably at least 98%);
        ii) a number average molecular weight (Mn) of about 150 to about 15,000 g/mol, as measured by 1H 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 9,000); and
        iii) an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0.
    
    


Vinyl terminated olefin oligomers and polymers useful in this invention also include propylene oligomers, comprising:
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 C4 to C12 alpha-omega dienes (such as butadiene, hexadiene, octadiene), norbornene, ethylidene norbornene, vinylnorbornene, norbornadiene, and dicyclopentadiene), wherein the oligomer has:

    
    
        i) at least 90% allyl chain ends (preferably at least 91%, preferably at least 93%, preferably at least 95%, preferably at least 98%);
        ii) a number average molecular weight (Mn) of about 150 to about 20,000 g/mol, as measured by 1H NMR (preferably 200 to 15,000, preferably 250 to 12,000, preferably 300 to 10,000, preferably 400 to 9,500, preferably 500 to 9,000, preferably 750 to 9,000); and
        iii) an isobutyl chain end to allylic vinyl group ratio of 0.7:1 to 1.35:1.0.
    
    


Any of the oligomers 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.
As used herein, the term “oligomer” is defined to have an Mn of from 100 to 25,000 g/mol as measured by 1H NMR. A polymer has an Mn of more than 25,000 g/mol. When an oligomer is referred to as comprising an olefin, the olefin present in the oligomer is the oligomerized form of the olefin. A propylene oligomer is an oligomer having at least 50 mol % of propylene. A co-oligomer is an oligomer comprising at least two different monomer units (such as propylene and ethylene). A homo-oligomer is an oligomer comprising units of the same monomer (such as propylene). As used herein, Mn is number average molecular weight (measured by 1H NMR unless stated otherwise), Mw is weight average molecular weight (measured by Gel Permeation Chromatography), and Mz is z average molecular weight (measured by Gel Permeation Chromatography), wt % is weight percent, and mol % is mole percent. Molecular weight distribution (MWD) is defined to be Mw (measured by Gel Permeation Chromatography) divided by Mn (measured by 1H 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” or “vinyl content”) is defined to be an oligomer (polymer) having at least one terminus represented by formula IL




where the ‘’ represents the oligomer or polymer chain. In a preferred embodiment the allyl chain end is represented by the formula II:





The amount of allyl chain ends is determined using 1H NMR at 120° C. using deuterated tetrachloroethane as the solvent on a 500 MHz machine, and in selected cases confirmed by 13C 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 114 1992, 1025-1032 that are useful herein.

“Isobutyl chain end” is defined to be an oligomer or polymer having at least one terminus represented by the formula:




where M represents the oligomer or polymer chain. In a preferred embodiment, the isobutyl chain end is represented by one of the following formulae:





where M represents the oligomer or polymer chain.

The percentage of isobutyl end groups is determined using 13C NMR (as described in the example section) and the chemical shift assignments in Resconi et al, J Am. Chem. Soc. 1992, 114, 1025-1032 for 100% propylene oligomers (and polymers) and set forth in FIG. 2 for E-P oligomers (and polymers).
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.
In a preferred embodiment, the propylene oligomer 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.
The oligomer preferably has an Mn as determined by 1H 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. Further, a desirable molecular weight range can be any combination of any upper molecular weight limit with any lower molecular weight limit described above. Mn is determined according to the methods described below in the examples section.
The oligomer 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.
The oligomer preferably contains less than 80 wt % of C4 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 C4 olefin(s) based upon the weight of the oligomer.
Alternately, the oligomer preferably contains less than 20 wt % of C4 or more olefin(s), (such as C4 to C30 olefins, typically such as C4 to C12 olefins, typically such as C4, C6, C8, C12, olefins, etc.), 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 C4 olefin(s) based upon the weight of the oligomer, as determined by 13C NMR.
In another embodiment, the oligomer composition produced 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 1H NMR assuming one unsaturation per chain.
In another embodiment, the oligomer composition produced 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 GC.
In another embodiment, the oligomer produced 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.
In another embodiment, the oligomers described herein may have a melting point (DSC first melt) of from 60 to 130° C., alternately 50 to 100° C. In another embodiment, the oligomers described herein have no detectable melting point by DSC following storage at ambient temperature (23° C.) for at least 48 hours.
Melting temperature (Tm) and glass transition temperature (Tg) are measured using Differential Scanning Calorimetry (DSC) using commercially available equipment such as a TA Instruments 2920 DSC. Typically, 6 to 10 mg of the sample, that has been stored at room temperature for at least 48 hours, is sealed in an aluminum pan and loaded into the instrument at room temperature. 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. Alternatively, 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. For samples displaying multiple peaks, the melting point (or melting temperature) 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.
In another embodiment, the oligomers described herein are a liquid at 25° C.
In another embodiment, the oligomers 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 and Mz are measured by using a High Temperature Size Exclusion Chromatograph (either from Waters Corporation or Polymer Laboratories), equipped with a differential refractive index detector (DRI), Experimental details, are described in: T. Sun, P. Brant, R. R. Chance, and W. W. Graessley, Macromolecules, Volume 34, Number 19, 6812-6820, (2001) and references therein. Three Polymer Laboratories PLgel 10 mm Mixed-B columns are used. The nominal flow rate is 0.5 cm3/min, and the nominal injection volume is 300 μL. The various transfer lines, columns and differential refractometer (the DRI detector) are contained in an oven maintained at 135° C. Solvent for the SEC 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 μm glass pre-filter and subsequently through a 0.1 μm Teflon filter. The TCB is then degassed with an online degasser before entering the SEC. 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 135° C. The injection concentration is from 1.0 to 2.0 mg/ml, with lower concentrations being used for higher molecular weight samples. 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 concentration, c, at each point in the chromatogram is calculated from the baseline-subtracted DRI signal, IDRI, using the following equation:

c=KDRIIDRI/(dn/dc)

where KDRI is a constant determined by calibrating the DRI, and (dn/dc) is the refractive index increment for the system. The refractive index, n=1.500 for TCB at 135° C. and λ=690 nm. For purposes of this invention and the claims thereto (dn/dc)=0.104 for propylene polymers and 0.1 otherwise. Units on parameters throughout this description of the SEC method are such that concentration is expressed in g/cm3, molecular weight is expressed in g/mole, and intrinsic viscosity is expressed in dL/g.

Molecular weight distribution (Mw/Mn—by GPC-DRI) is determined by the method above. In some embodiments, the oligomers of this invention have an Mw/Mn (by GPC-DRI) of 1.5 to 20, alternately 1.7 to 10.
In another embodiment, 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)). Many of these materials are known in the art and can be functionalized using the processes described herein, e.g. contacting an alkene metathesis catalyst (as described herein) with a heteroatom containing alkene (as described herein) and one or more vinyl containing materials. Vinyl terminated polymers include homo-and co-polymers of heteroatom containing monomers, as well as polymers of olefin monomers only. (The term 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).
Process to Make Vinyl Terminated Oligomers
The oligomers described above are typically prepared in a homogeneous process, preferably a bulk process as described in U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008, which is incorporated by reference herein. In a preferred embodiment, propylene and optional comonomers (such as ethylene) can be oligomerized by reacting a catalyst system (comprising metallocene compound(s), and one or more activators) with the olefins. 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. Such processes and modes are well known in the art. 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.) 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 system or other additives, or amounts typically found with the monomer; e.g. propane in propylene).
Suitable diluents/solvents for oligomerization 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 C4-10 alkanes, chlorobenzene, and aromatic and alkylsubstituted aromatic compounds such as benzene, toluene, mesitylene, and xylene. Suitable solvents also include liquid olefins which may act as monomers or comonomers including ethylene, propylene, 1-butene, 1-hexene, 1-pentene, 3-methyl-1-pentene, 4-methyl-1-pentene, 1-octene, and 1-decene. Mixtures of the foregoing are also suitable.
In a preferred embodiment, the feed concentration for the oligomerization is 60 volume % solvent or less, preferably 40 volume % or less, preferably 20 volume % or less. Preferably the oligomerization is run in a bulk process.
Suitable additives to the oligomerization process can include one or more scavengers, promoters, modifiers, reducing agents, oxidizing agents, hydrogen, aluminum alkyls, or silanes.
In a preferred embodiment hydrogen is present in the oligomerization reactor at a partial pressure of 0.001 to 50 psig, preferably from 0.01 to 25 psig, more preferably 0.1 to 10 psig. 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. Preferably 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.
In an alternate embodiment, 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.
In an alternate embodiment, 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.
Preferred oligomerizations 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.
In a typical oligomerization, the residence time of the reaction is up to 60 minutes, preferably between 5 to 50 minutes, preferably 10 to 40 minutes.
Catalyst Compound to Make Vinyl Terminated Oligomers
Catalyst compounds useful herein to produce the vinyl terminated oligomers include one or more metallocene compound(s) represented by the formulae:




where

    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 R1 is, independently, hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, R1 may the same or different as R2;
    each R2 is, independently, hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, provided that at least one of R1 or R2 is not hydrogen, preferably both of R1 and R2 are not hydrogen, preferably R1 and/or R2 are not branched;
    each R3 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 C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, provided however that at least three R3 groups are not hydrogen (alternately four R3 groups are not hydrogen, alternately five R3 groups are not hydrogen);
    {Alternately, when the catalyst compound is to used to make the homo-oligomer then each R3 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 C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, provided however that: 1) all five R3 groups are methyl, or 2) four R3 groups are not hydrogen and at least one R3 group is a C2 to C8 substituted or unsubstituted hydrocarbyl (preferably at least two, three, four or five R3 groups are a C2 to C8 substituted or unsubstituted hydrocarbyl)};
    each R4 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 C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, substituted phenyl (such as propyl phenyl), phenyl, silyl, substituted silyl, (such as CH2SiR′, where R′ is a C1 to C12 hydrocarbyl, such as methyl, ethyl, propyl, butyl, phenyl);
    R5 is hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl;
    R6 is hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl;
    each R7 is, independently, hydrogen, or a C1 to C8 alkyl group, preferably a C1 to C8 linear Alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, provided however that at least seven R7 groups are not hydrogen, alternately at least eight R7 groups are not hydrogen, alternately all R7 groups are not hydrogen, (preferably the R7 groups at the 3 and 4 positions on each Cp ring of Formula III are not hydrogen);
    N is nitrogen;
    T is a bridge, preferably, Si or Ge, preferably Si;
    each Ra, is independently, hydrogen, halogen or a C1 to C20 hydrocarbyl, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, phenyl, benzyl, substituted phenyl, and two Ra 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.


The term “substituted” means that a hydrogen group has been replaced with a hydrocarbyl group, a heteroatom or a heteroatom containing group. For example methyl cyclopentadiene (Cp) is a Cp group substituted with a methyl group and ethyl alcohol is an ethyl group substituted with an —OH group.
In an alternate embodiment, at least one R4 group is not hydrogen, alternately at least two R4 groups are not hydrogen, alternately at least three R4 groups are not hydrogen, alternately at least four R4 groups are not hydrogen, alternately all R4 groups are not hydrogen.
Catalyst compounds that are particularly useful in this invention include one or more of:

    (1,3-Dimethylindenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (1,3,4,7-Tetramethylindenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (1,3-Dimethylindenyl)(tetramethylcyclopentadienyl)hafniumdimethyl,
    (1,3-Diethylindenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (1,3-Dipropylindenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (1-Methyl,3-propyllindenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (1,3-Dimethylindenyl)(tetramethylpropylcyclopentadienyl)hafniumdimethyl,
    (1,2,3-Trimethylindenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (1,3-Dimethylbenzindenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (2,7-Bis t-butylfluorenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (9-Methylfluorenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    (2,7,9-Trimethylfluorenyl)(pentamethylcyclopentadienyl)hafniumdimethyl,
    μ-Dihydrosilyl(bis tetramethylcyclopentadienyl)hafniumdimethyl,
    μ-Dihydrosilyl(bis tetramethylcyclopentadienyl)hafniumdimethyl,
    μ-Dimethylsilyl(tetramethylcyclopentadienyl)(3-propyltrimethylcyclopentadienyl)hafniumdimethyl, and
    μ-Dicyclopropylsilyl(bis tetramethylcyclopentadienyl)hafniumdimethyl.


In an alternate embodiment, 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.
Activators and Activation Methods for Catalyst Compounds to Make Vinyl Terminated Oligomers
The terms “cocatalyst” and “activator” are 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, for example, 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, σ-bound, metal ligand making the metal complex cationic and providing a charge-balancing noncoordinating or weakly coordinating anion.
In one embodiment, alumoxane activators are utilized as an activator in the catalyst composition. Alumoxanes are generally oligomeric compounds containing —Al(R1)—O— sub-units, where R1 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. 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. Pat. No. 5,041,584).
When 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.
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.
Ionizing Activators
It is within the scope of this invention to use an ionizing or stoichiometric activator, neutral or ionic non-coordinating anion (as defined in U.S. Ser. No. 12/143,663, filed on Jun. 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. Pat. No. 5,942,459) or combination thereof. It is also within the scope of this invention to use neutral or ionic activators alone or in combination with alumoxane or modified alumoxane activators. Preferably the activator is N,N-dimethylanilinium tetrakis(perfluoronapthyl)borate, N,N-dimethylanilinium tetrakis(perfluorobiphenyl)borate, N,N-dimethylanilinium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triphenylcarbenium tetrakis(perfluoronapthyl)borate, triphenylcarbenium tetrakis(perfluorobiphenyl)borate, triphenylcarbenium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, or triphenylcarbenium tetrakis(perfluorophenyl)borate. For additional activators useful herein, please see U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008.
The typical NCA activator-to-catalyst-precursor ratio is a 1:1 molar ratio. 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.
Properties of Functionalized Oligomers
In another embodiment the functionalized (and optionally derivatized) propylene oligomers and propylene-ethylene co-oligomers (“functionalized co(oligomers)”) described herein have less than 10 wt % allyl chain ends, preferably less than 8%, preferably less than 6%, preferably less than 5%, preferably less than 4%, preferably less than 3%, preferably less than 2%, preferably less than 1% (relative to total unsaturations as measured by 1H NMR, using the protocol described in U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008).
In another embodiment the functionalized co(oligomers) described herein have less than 10% allyl chain ends, preferably less than 5%, preferably less than 1%, (relative to total unsaturations as measured by 1H NMR, using the protocol described in U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008); and less than 10 wt % vinylidene unsaturations, preferably less than 5%, preferably less than 1%, (relative to total unsaturations as measured by 1H NMR); and/or less than 10% vinylene unsaturations, preferably less than 5%, preferably less than 1%, (relative to total unsaturations as measured by 1H NMR, using the protocol described in U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008). No hydrogen or chain transfer/termination agent should be used during functionalization, derivitization or stripping (of unreacted monomer) for measurement of unsaturations.
In another embodiment, the functionalized co(oligomers) consist essentially of propylene, functional group and optionally ethylene. Alternately C4 olefins (such as isobutylene, butadiene, n-butene) are substantially absent from the functionalized co(oligomers). Alternately C4-20 olefins are substantially absent from the functionalized co(oligomers). Alternately isobutylene is substantially absent from the functionalized co(oligomers). By substantially absent is meant that the monomer is present in the oligomer/co-oligomer at 1 wt % or less, preferably at 0.5 wt % or less, preferably at 0 wt %.
In another embodiment, the number of functional groups is present at 0.60 to 1.2, alternately 0.75 to 1.1 functional groups per chain (preferably assuming that Mn has not altered by more than 15% as compared to the Mn of the oligomer or co-oligomer prior to functionalization and optional derivatization). Number of functional groups per chain=F/Mn, as determined by 1H NMR as follows: The instrument used is a 400 MHz Varian pulsed fourier transform NMR spectrometer equipped with a variable temperature proton detection probe operating at 120° C. The sample is dissolved in 1,1,2,2-tetrachloroethane-d2 (TCE-d2) or CDCl3 and transferred into a 5 mm glass NMR tube. (The solvent has less than 10,000 ppm water and is free of other contaminants that could change the chemical shifts in the NMR spectrum). Acquisition parameters are pulse width=450, acquisition delay=8 s and number of scans=120. Chemical shifts are determined relative to the residual TCE-d1 signal which is set to 5.98 ppm and residual CHCl3, which is set at 7.24 ppm. VRA is the normalized integrated signal intensity for the vinyls with shifts between from about 4.9 to 5.1 ppm. VRDA is the normalized integrated signal intensity for the vinylidene resonances between from about 4.65 to 4.85 ppm and the vinylene resonances at from about 5.15 to 5.6 ppm. IA is the normalized integrated signal intensities for the aliphatic region of interest between from about 0 to 2.1 ppm (IA). The number of vinyl groups/1000 Carbons (VI) is determined from the formula: (VRA*1000)/(IA+VRA+VDRA). Likewise, the number of vinylidene & vinylene groups/1000 carbons (VE) is determined from the formula: (VDRA*1000)/(IA+VRA+VDRA). VRA, VDRA and IA are the normalized integrated signal intensities in the chemical shift regions defined above. Mn is calculated assuming one unsaturated end-group per oligomer chain. Mn=(14,000 g/mol)/(VI+VE).
After the oligomer in question is functionalized it is necessary to determine the resonances/chemical shift regions of the functional group to determine % functionalization. To do so, repeat the above 1H NMR procedure on a clean sample of the functionalized oligomer (e.g. washed to remove unreacted materials, contaminants, etc.). Refer to “The Sadtler Guide to NMR Spectra”, ed. William Walter Simons, published by the Sadtler Research Laboratories, 1972 for assistance in determining the shift regions for specific functional groups. The number of functional groups/1000 C's (F)=(FA*1000)/(FA+IA+VRA+VDRA), where FA=normalized integrated signal intensities in the chemical shift region of the functional group, and IA, VRA, VDRA are as defined above.
Percent functionalization of the oligomer=(F*100)/(F+VI+VE). The number of vinyl groups/1000 carbons (VI*) and number of vinylidene groups/1000 carbons (VE*) for the functionalized oligomer are determined from the 1HNMR spectra of the functionalized oligomer in the same manner as VI and VE for the unfunctionalized oligomer. Preferably the percent functionalization of the oligomer is 75% or more, preferably 80% or more, preferably 90% or more, preferably 95% or more.
In a preferred embodiment, F+VI*+VE*≧(0.50(VI+VE)), preferably F+VI*+VE*≧(0.60(VI+VE)), preferably F+VI*+VE*≧(0.70(VI+VE)), preferably F+VI*+VE*≧(0.75(VI+VE)), preferably F+VI*+VE*≧(0.80(VI+VE)), preferably F+VI*+VE*≧(0.85(VI+VE)), preferably F+VI*+VE*>(0.90(VI+VE)), preferably F+VI*+VE*≧(0.95(VI+VE)), preferably F+VI*+VE*≧(0.98(VI+VE)), preferably F+VI*+VE*≧(0.99(VI+VE)).
In another embodiment, the functionalized co(oligomers) are represented by the formula:




where  represents oligomer or co-oligmer

X is H or a functional group, provided at least one X is a functional group. Useful functional groups include any of the functional groups described above. Preferred functional groups include heteroatom containing groups where the heteroatom comprises Si, P, O, S, N, Br, Cl, F, I and or Br (preferably N, O, Cl and or Br, preferably N and or O). Particularly preferred functional groups are selected from the group consisting of acids, esters, anhydrides, acid-esters, oxycarbonyls, carbonyls, formyls, formylcarbonyls, hydroxyls, and acetyl halides. Particularly preferred functional groups include those represented by the formula: —C(O)—X*, where the O is double bonded to the C and the X* is hydrogen, nitrogen, hydroxy, oxyhydrocarbyl (e.g. ester), oxygen, the salt moiety -OM wherein M is a metal, e.g. alkali, alkaline earth, transition metal, copper, zinc and the like, oxyhetero, e.g. -O-Z wherein Z represents a heteroatom such as phosphorus boron, sulfur, which heteroatom may be substituted with hydrocarbyl or oxyhydrocarbyl groups, or two acyl groups may be joined through (X*).

Preferred functional groups include acyl groups derived from monounsaturated mono-or dicarboxylic acids and their derivatives, e.g. esters and salts.
More specifically, oligomer functionalized with mono-or dicarboxylic acid material, i.e., acid, anhydride, salt or acid ester are preferred, including the reaction product of the oligomer with a monounsaturated carboxylic reactant comprising at least one member selected from the group consisting of (i) monounsaturated C4 to C10 dicarboxylic acid (preferably wherein (a) the carboxyl groups are vicinyl, (i.e. located on adjacent carbon atoms) and (b) at least one, preferably both, of said adjacent carbon atoms are part of said monounsaturation); (ii) derivatives of (i) such as anhydrides or C1 to C5 alcohol derived mono-or diesters of (i); (iii) monounsaturated C3 to C10 monocarboxylic acid wherein the carbon-carbon double bond is conjugated to the carboxyl group, i.e., of the structure —C═C—C(O)— (where O is double bonded to C), and (iv) derivatives of (iii) such as C1 to C5 alcohol derived monoesters of (iii).
Suitable unsaturated acid materials thereof which are useful functional groups, include acrylic acid, crotonic acid, methacrylic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, itaconic anhydride, citraconic acid, citraconic anhydride, mesaconic acid, glutaconic acid, chloromaleic acid, aconitic acid, crotonic acid, methylcrotonic acid, sorbic acid, 3-hexenoic acid, 10-decenoic acid, 2-pentene-1,3,5-tricarboxylic acid, cinnamic acid, and lower alkyl (e.g. C1 to C4 alkyl) acid esters of the foregoing, e.g. methyl maleate, ethyl fumarate, methyl fumarate, etc. Particularly preferred are the unsaturated dicarboxylic acids and their derivatives, especially maleic acid, fumaric acid and maleic anhydride.
Preferably at least 90 wt % of the functionalized or derivatized propylene oligomers or propylene-ethylene co-oligomers are represented by one or both of the above formulae, alternately at least 95 wt %, alternately at least 98 wt %, based upon the weight of the functionalized or derivatized propylene oligomers or propylene-ethylene co-oligomers.
In another embodiment this invention relates to:

    1. A process to functionalize propylene co-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene and a propylene co-oligomer having an Mn of 300 to 30,000 g/mol (as measured by 1H NMR) comprising 10 to 90 mol % propylene and 10 to 90 mol % of ethylene, wherein the oligomer has at least X % allyl chain ends (relative to total unsaturations), where: 1) X=(−0.94 (mol % ethylene incorporated)+100), when 10 to 60 mol % ethylene is present in the co-oligomer, and 2) X=45, when greater than 60 and less than 70 mol % ethylene is present in the co-oligomer, and 3) X=(1.83*(mol % ethylene incorporated)−83), when 70 to 90 mol % ethylene is present in the co-oligomer.
    2. The process of paragraph 1 wherein the oligomer has more than 90% allyl chain ends (relative to total unsaturations).
    3. The process of paragraph 1 wherein the oligomer comprises 15 to 95 wt % ethylene and has more than 80% allyl chain ends (relative to total unsaturations).
    4. The process of paragraph 1 wherein the oligomer comprises at 30 to 95 wt % ethylene and has more than 70% allyl chain ends (relative to total unsaturations).
    5. The process of paragraph 1 wherein the oligomer comprises at 30 to 95 wt % ethylene and has more than 90% allyl chain ends (relative to total unsaturations).
    6. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene and a propylene oligomer comprising more than 90 mol % propylene and less than 10 mol % ethylene, wherein the oligomer has: at least 93% allyl chain ends, an Mn of about 500 to about 20,000 g/mol (as measured by 1H NMR), an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0, and less than 1400 ppm aluminum.
    7. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene and a propylene oligomer comprising at least 50 mol % propylene and from 10 to 50 mol % ethylene, wherein the oligomer has: at least 90% allyl chain ends, Mn of about 150 to about 10,000 g/mol (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.3:1.0, wherein monomers having four or more carbon atoms are present at from 0 to 3 mol %.
    8. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene and a propylene oligomer comprising at least 50 mol % propylene, from 0.1 to 45 mol % ethylene, and from 0.1 to 5 mol % C4 to C12 olefin, wherein the oligomer has: at least 87% allyl chain ends (alternately at least 90%), an Mn of about 150 to about 10,000 g/mol, (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0.
    9. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene and a propylene oligomer comprising at least 50 mol % propylene, from 0.1 to 45 wt % ethylene, and from 0.1 to 5 mol % diene, wherein the oligomer has: at least 90% allyl chain ends, an Mn of about 150 to about 10,000 g/mol (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.7:1 to 1.35:1.0.
    10. A process to functionalize propylene homooligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene and a homooligomer comprising propylene, wherein the oligomer has: at least 93% allyl chain ends, an Mn of about 500 to about 20,000 g/mol (as measured by 1H NMR), an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.2:1.0, and less than 1400 ppm aluminum.
    11. The process of any of paragraphs 1 to 10, wherein the oligomer is a liquid at 25° C.
    12. The process of any of paragraphs 1 to 11, wherein the Mn is about 500 to about 7,500 g/mol, the Mw is 1,000 to about 20,000 g/mol, and the Mz is about 1400 (alternately 1700) to about 150,000 g/mol.
    13. The process of any of paragraphsl to 12 wherein the alkene metathesis catalyst is represented by the Formula (I):






where:

    M is a Group 8 metal;
    X and X1 are, independently, any anionic ligand, or X and X1 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 L1 are neutral two electron donors, L and L1 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;
    L1 and X1 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 R1 are, independently, hydrogen or C1 to C30 substituted or unsubstituted hydrocarbyl; R1 and L1 or X1 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.
    14. The process of paragraph 13 wherein M is Ru or Os;
    X and X1 are, independently, a halogen, an alkoxide or a triflate, or X and X1 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 L1 are, independently, a phosphine or a N-heterocyclic carbene, L and L1 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;
    L1 and X1 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 R1 are, independently, hydrogen or a C1 to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl;
    R1 and L1 or X1 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.
    15. The process of any of paragraphs 1 to 14 wherein the alkene metathesis catalyst is one or more of: 2,6-Diisopropylphenylimidoneophylidene molybdenum(VI) bis(t-butoxide), 2,6-Diisopropylphenylimidoneophylidene molybdenum(VI) bis(hexafluoro-t-butoxide), 2,6-Diisopropylphenylimido neophylidenemolybdenum(VI) bis(trifluoromethanesulfonate)dimethoxyethane adduct, 2,6-Diisopropylphenylimidoneophylidene[racemic-BIPHEN]molybdenum(VI), tricyclohexylphosphine[1,3-bis(2,4,6-trimethylphenyl)imidazol-2-ylidene][3-phenyl-1H-inden-1-ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[3-phenyl-1H-inden-1-ylidene][1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydro-imidazol-2-ylidene]ruthenium(II) dichloride, tricyclohexylphosphine[1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2-ylidene][(phenylthio)methylene]ruthenium(II) dichloride, bis(tricyclohexylphosphine)-3-phenyl-1H-inden-1-ylideneruthenium(II) dichloride, 1,3-Bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2-ylidene[2-(i-propoxy)-5-(N,N-dimethylaminosulfonyl)phenyl]methyleneruthenium(II) dichloride, and [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]-[2-[[(4-methylphenyl)imino]methyl]-4-nitrophenolyl]-[3-phenyl-1H-inden-1-ylidene]ruthenium(II) chloride, benzylidene-bis(tricyclohexylphosphine)dichlororuthenium, benzylidene[1,3-bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(tricyclohexylphosphine)ruthenium, dichloro(o-isopropoxyphenylmethylene)(tricyclohexylphosphine)ruthenium(II), (1,3-Bis-(2,4,6-trimethylphenyl)-2-imidazolidinylidene)dichloro(o-isopropoxyphenylmethylene)ruthenium, 1,3-Bis(2-methylphenyl)-2-imidazolidinylidene]dichloro(2-isopropoxyphenylmethylene)ruthenium(II), [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro[3-(2-pyridinyl)propylidene]ruthenium(II), [1,3-Bis(2-methylphenyl)-2-imidazolidinylidene]dichloro(phenylmethylene) (tricyclohexylphosphine)ruthenium(II), [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(3-methyl-2-butenylidene)(tricyclohexylphosphine)ruthenium(II), and [1,3-Bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(benzylidene)bis(3-bromopyridine)ruthenium(II).
    16. The process of any of paragraphsl to 15 wherein the heteroatom containing alkene is represented by the formula: H2C═CH—R or R*—HC═CH—R, where R* and R are, independently, a heteroatom containing group containing 1 to 30 carbon atoms and at least one heteroatom.
    17. The process of paragraph 16 where R* and R are, independently, a heteroatom containing group containing 1 to 30 carbon atoms and at least one heteroatom selected from the group consisting of Si, P, O, S, N, Cl, F, I and Br.
    18. The process of paragraph 16 where R* and R are selected from the group consisting of alcohols, amides, nitriles, imines, haloalkyls, acids, esters, anhydrides, acid-esters, oxycarbonyls, carbonyls, formyls, formylcarbonyls, hydroxyls, and acetyl halides.
    19. The process of paragraph 16 where R* and R are represented by the formula -D-Y, where D is a hydrocarbyl group having 1 to 12 carbon atoms and Y is nitrogen or oxygen.
    20. The process of any of paragraphs 1 to 15 wherein the heteroatom containing alkene comprises one or more of acrylonitrile, acrylamide, allyl amine, acrylic acid, crotonic acid, methacrylic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, itaconic anhydride, citraconic acid, citraconic anhydride, mesaconic acid, glutaconic acid, chloromaleic acid, aconitic acid, crotonic acid, methylcrotonic acid, sorbic acid, 3-hexenoic acid, 10-decenoic acid, 2-pentene-1,3,5-tricarboxylic acid, cinnamic acid, and lower alkyl (e.g. C1 to C4 alkyl) acid esters of the foregoing, e.g. methyl maleate, ethyl fumarate, methyl fumarate, 5-hexen-1-ol.
    21. The process of paragraphs 1 to 20 wherein the propylene co-oligomer is prepared by a process having productivity of at least 4.5×103 g/mmol/hr, comprising:


contacting, at a temperature of from 35° C. to 150° C., propylene, 0.1 to 70 mol % ethylene and from 0 to about 5 wt % hydrogen in the presence of a catalyst system comprising an activator and at least one metallocene compound represented by the formulae:




where

    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 R1 is, independently, a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, R1 may the same or different as R2;
    each R2 is, independently, a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, preferably R1 and/or R2 are not branched;
    each R3 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 C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, provided however that at least three R3 groups are not hydrogen (alternately four R3 groups are not hydrogen, alternately five R3 groups are not hydrogen);
    each R4 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 C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, substituted phenyl (such as propyl phenyl), phenyl, silyl, substituted silyl, (such as CH2SiR′, where R′ is a C1 to C12 hydrocarbyl, such as methyl, ethyl, propyl, butyl, phenyl);
    R5is hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl;
    R6 is hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl;
    each R7 is, independently, hydrogen, or a C1 to C8 alkyl group, preferably a C1 to C8 linear Alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, provided however that at least seven R7 groups are not hydrogen, alternately at least eight R7 groups are not hydrogen, alternately all R7 groups are not hydrogen, (preferably the R7 groups at the 3 and 4 positions on each Cp ring of Formula III are not hydrogen);
    N is nitrogen;
    T is a bridge, preferably, Si or Ge, preferably Si;
    each Ra, is independently, hydrogen, halogen or a C1 to C20 hydrocarbyl, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, phenyl, benzyl, substituted phenyl, and two Ra 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.
    22. The process of paragraphs 1 to 20 wherein the propylene homo-oligomer is prepared by a homogeneous process having productivity of at least 4.5×106 g/mmol/hr, comprising:


contacting, at a temperature of from 30° C. to 120° C., propylene, 0 mol % comonomer And from 0 to about 5 wt % hydrogen in the presence of a catalyst system comprising an activator and at least one metallocene compound represented by the formulae:




where

    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 R1 is, independently, a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, R1 may the same or different as R2;
    each R2 is, independently, a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, preferably R1 and/or R2 are not branched;
    each R3 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 C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, provided however that: 1) all five R3 groups are methyl, or 2) four R3 groups are not hydrogen and at least one R3 group is a C2 to C8 substituted or unsubstituted hydrocarbyl (preferably at least two, three, four or five R3 groups are a C2 to C8 substituted or unsubstituted hydrocarbyl);
    each R4 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 C1 to C8 linear alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, substituted phenyl (such as propyl phenyl), phenyl, silyl, substituted silyl, (such as CH2SiR′, where R′ is a C1 to C12 hydrocarbyl, such as methyl, ethyl, propyl, butyl, phenyl);
    R5 is hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl;
    R6 is hydrogen or a C1 to C8 alkyl group, preferably a C1 to C8 linear alkyl group, preferably methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl;
    each R7 is, independently, hydrogen, or a C1 to C8 alkyl group, preferably a C1 to C8 linear Alkyl group, preferably methyl ethyl, propyl, butyl, pentyl, hexyl, heptyl or octyl, provided however that at least seven R7 groups are not hydrogen, alternately at least eight R7 groups are not hydrogen, alternately all R7 groups are not hydrogen, (preferably the R7 groups at the 3 and 4 positions on each Cp ring of Formula III are not hydrogen);
    N is nitrogen;
    T is a bridge, preferably, Si or Ge, preferably Si;
    each Ra, is independently, hydrogen, halogen or a C1 to C20 hydrocarbyl, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, phenyl, benzyl, substituted phenyl, and two Ra 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.
    23. The process of paragraph 21 or 22, wherein the activator comprises one or more non-coordinating anions.
    24. The process of any of the above paragraphs where the process is a continuous process comprising introducing monomer and catalyst system into a reactor, obtaining a reactor effluent containing vinyl terminated propylene co-oligomer or propylene homo-oligomer, optionally removing solvent, unused monomer and/or other volatiles, obtaining vinyl terminated polyolefin (such as those described herein), introducing vinyl terminated propylene co-oligomer or propylene homo-oligomer and further combining the propylene co-oligomer or propylene homo-oligomer with an alkene metathesis catalyst and heteroatom containing alkene in a reaction zone and obtaining functionalized propylene co-oligomer or propylene homo-oligomer.
    25. The process of any of the above paragraphs where the co-oligomer contains less than 80 wt % of C4 olefin(s).
    26. A process to functionalize a vinyl containing material, comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene and one or more vinyl containing materials, preferably vinyl containing polymers, preferably vinyl containing polyolefins.
    27. The process of paragraph 26 wherein the alkene metathesis catalyst is as described in paragraph 13, 14 or 15.
    28. The process of paragraph 26 wherein the heteroatom containing alkene is as described in paragraph 16, 17, 18, 19 or 20.


EXAMPLES
Tests and Materials.
Products were characterized by 1H NMR and DSC as follows:
1H NMR
1H NMR data was collected at either room temperature or 120° C. (for purposes of the claims, 120° C. shall be used) in a 5 mm probe using a Varian spectrometer with a 1Hydrogen frequency of at least 400 MHz. Data was recorded using a maximum pulse width of 45°, 8 seconds between pulses and signal averaging 120 transients. Spectral signals were integrated and the number of unsaturation types per 1000 carbons was calculated by multiplying the different groups by 1000 and dividing the result by the total number of carbons.
DSC
Melting temperature (Tm) and glass transition temperature (Tg) are measured using Differential Scanning Calorimetry (DSC) using commercially available equipment such as a TA Instruments 2920 DSC. Typically, 6 to 10 mg of the sample, that has been stored at room temperature for at least 48 hours, is sealed in an aluminum pan and loaded into the instrument at room temperature. 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. Alternatively, 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. For samples displaying multiple peaks, the melting point (or melting temperature) 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.
All molecular weights are number average unless otherwise noted. All molecular weights are reported in g/mol.
The following abbreviations are used in the Examples: Catalyst A is tricyclohexylphosphine[1,3-bis(2,4,6-trimethylphenyl)imidazol-2-ylidene][3-phenyl-1H-inden-1-ylidene]ruthenium(II) dichloride (CAS#[254972-49-1]), Catalyst B is tricyclohexylphosphine[3-phenyl-1H-inden-1-ylidene][1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydro-imidazol-2-ylidene]ruthenium(II) dichloride (CAS# [536724-67-1]), MA is methyl acrylate, aPP is atactic polypropylene, iPP is isotactic polypropylene, EP is ethylene-propylene copolymer, TCE is 1,1,2,2-tetrachloroethane, h is hours, min is minutes, Mn is the number average molecular weight as determined by 1H NMR spectroscopy by comparison of integrals of the aliphatic region to the olefin region as determined using the protocol described in the Experimental section of U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008.
Each of the specific examples described below uses a vinyl-containing reactant. These reactants are summarized in Table 1. PE1 was purchased from Fluka and is 1-octadecene (≧95.0% unsaturation). The other vinyl-terminated polyolefins were prepared according to procedures described in U.S. Ser. No. 12/143,663, filed on Jun. 20, 2008.














TABLE 1







% vinyls
Tm*



Mw/



NMR-Mn
(NMR)
(° C.)
Mn1
Mw1
Mz1
Mn1






















PE1
(252)
≧95.0
—
—
—
—
—


a-PP1
261
98
—
98
198
431
2.0


a-PP2
945
97
—
468
1736
4143
3.7


a-PP3
3571 
95
—
2623
9865
20228
3.8


EP1
490
95
—
294
1292
9395
4.4


EP2
2205 
94
—
1379
6200
64135
4.5


i-PP1
3789 
88
 78
3422
8563
14792
2.5


i-PP2
21906 
73
122
25120
52654
97467
2.1





Tm* is DSC second melt;


1determined by GPC - units g/mol.






Example 1
Cross Metathesis Reaction of 1-octadecene and methyl acrylate
1-Octadecene (2.00 mL, 6.24 mmol) and MA (1.13 mL, 12.5 mmol) were combined with hexane (14 mL) and benzene (2 mL). The homogeneous mixture was heated to gentle reflux on a heating plate kept at 73° C. Then a benzene solution of catalyst B (1.31 mL, 0.0312 mmol) was added. Vigorous gas evolution was observed within minutes. After 2 h the volatiles were removed by evaporation under a stream of nitrogen. The resulting brownish suspension was mixed with pentane (12 mL), and the mixture was passed through a short column of neutral alumina that had been slurried with pentane. The column was washed with additional pentane (30 mL). The combined organics were evaporated and dried under reduced pressure at 75° C. for 2 h to yield the ester-capped product as a low-melting, colorless solid. Yield: 1.67 g, 86.2%. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected ester-capped product as a mixture of E and Z isomers (94:6 ratio).
Example 2
Cross Metathesis Reaction of polypropylene and methyl acrylate
Atactic polypropylene aPPI (2.03 g, ca. 7.78 mmol vinyls), MA (1.40 mL, 15.6 mmol) and hexane (12 mL) were combined and heated to a gentle reflux on a heating block kept at 73° C. A benzene solution of catalyst B (1.63 mL, 0.0389 mmol) was then added. Vigorous gas evolution was observed. After 2 h the volatiles were removed by evaporation under a stream of nitrogen. The resulting brownish suspension was mixed with pentane (15 mL), and the mixture was passed through a short column of neutral alumina that had been slurried with pentane. The column was washed with additional pentane (30 mL). The combined organics were evaporated and dried under reduced pressure at 75° C. for 1 h to yield the ester-capped product as a pale yellow oil. Yield: 1.55 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected ester-capped product as a mixture of E and Z isomers (94:6 ratio).
Example 3
Cross Metathesis Reaction of polypropylene and methyl acrylate
Atactic polypropylene aPP2 (2.27 g, ca. 2.40 mmol vinyls), MA (0.433 mL, 4.80 mmol) and hexane (12 mL) were combined and heated to a gentle reflux on a heating block kept at 73° C. A benzene solution of catalyst B (0.673 mL, 0.0160 mmol) was then added. Gas evolution was observed. After 2.75 h the volatiles were removed by evaporation under a stream of nitrogen. The resulting brownish suspension was mixed with pentane (15 mL), and the mixture was passed through a short column of neutral alumina that had been slurried with pentane. The column was washed with additional pentane (30 mL). The combined organics were evaporated and dried under reduced pressure at 75° C. overnight to yield the ester-capped product as a very pale yellow oil. Yield: 2.13 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected ester-capped product as a mixture of E and Z isomers (94:6 ratio).
Example 4
Cross Metathesis Reaction of polypropylene and methyl acrylate
Atactic polypropylene aPP3 (2.48 g, ca. 0.694 mmol vinyls), MA (0.250 mL, 2.78 mmol) and hexane (12 mL) were combined and heated to a gentle reflux on a heating block kept at 73° C. A benzene solution of catalyst B (0.292 mL, 0.00694 mmol) was then added. After 3.5 h the volatiles were removed by evaporation under a stream of nitrogen. The resulting brownish suspension was mixed with pentane (15 mL), and the mixture was passed through a short column of neutral alumina that had been slurried with pentane. The column was washed with additional pentane (30 mL). The combined organics were evaporated and dried under reduced pressure at 75° C. overnight to yield the ester-capped product as a very pale yellow oil. Yield: 2.32 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected ester-capped product as a mixture of E and Z isomers (93:7 ratio).
Example 5
Cross Metathesis Reaction of ethylene-propylene copolymer with methyl acrylate
Ethylene propylene copolymer EP1 (2.44 g, ca. 4.98 mmol vinyls), MA (0.898 mL, 9.96 mmol) and hexane (10 mL) were combined and heated to a gentle reflux on a heating block kept at 73° C. A 0.0238 M solution of catalyst B (1.05 ML, 0.0249 mmol) in benzene was then added. Gas evolution was observed almost immediately. After 16 h the volatiles were removed by evaporation under a stream of nitrogen. The resulting brownish suspension was mixed with pentane (10 mL), and the mixture was passed through a short column of neutral alumina that had been slurried with pentane. The column was washed with additional pentane (20 mL). The combined organics were evaporated and dried under reduced pressure at 75° C. for 2 h to yield the ester-capped product as a very pale yellow oil. Yield: 2.36 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected ester-capped product as a mixture of E and Z isomers (93:7 ratio). Data are summarized in Table 2.
Example 6
Cross Metathesis reaction of ethylene-propylene copolymer with methyl acrylate
Ethylene propylene copolymer EP2 (2.26 g, ca. 1.02 mmol vinyls) and toluene (8 mL) were combined and heated to reflux for 10 min to form a homogeneous solution. The mixture was cooled slightly and hexane (3 mL) was added. The solution became cloudy. The mixture was placed on a heating block kept at 73° C. Methyl acrylate (0.185 mL, 2.05 mmol) was then added followed by a 6.42 mM solution of catalyst B (1.60 mL, 0.0102 mmol) in toluene. Gas evolution was observed. After 3.5 h the mixture was poured into methanol (70 mL) that was rapidly stirred. A white precipitate formed that was isolated on a fritted disk and washed with methanol (2×30 mL). The product was dried under reduced pressure overnight. Yield: 2.13 g. 1H NMR spectroscopic data indicated that most of the starting EP2 had been converted (13% vinyl present) to the expected ester-capped product as a mixture of E and Z isomers. Data are summarized in Table 2.
Example 7
Cross Metathesis Reaction of polypropylene with methyl acrylate
Isotactic polypropylene iPPI (1.26 g, ca. 0.325 mmol vinyls) and toluene (8 mL) were combined and heated to reflux for 10 min to form a homogeneous solution. The mixture was cooled slightly and hexane (3 mL) was added. The mixture was placed on a heating block kept at 73° C. Methyl acrylate (0.100 mL, 1.11 mmol) was then added followed by a 6.42 mM solution of catalyst B (0.506 mL, 0.00325 mmol) in toluene was then added. After 3.5 h the mixture was poured into methanol (70 mL) that was rapidly stirred. A white precipitate formed that was isolated on a fritted disk and washed with methanol (2×30 mL). The product was dried under reduced pressure overnight. Yield: 1.17 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected ester-capped product as a mixture of E and Z isomers. Some vinylidene-containing starting material remained unreacted. This was found by 1H NMR to be 12.9% of the isolated product. Data are summarized in Table 2.
Example 8
Cross Metathesis Reaction of polypropylene with methyl acrylate
Isotactic polypropylene iPP2 (0.738 g, ca. 0.0337 mmol vinyls) and toluene (8 mL) were combined and heated to reflux for 10 min to form a homogeneous solution. The mixture was cooled slightly and hexane (3 mL) was added. The mixture was placed on a heating block kept at 73° C. Methyl acrylate (0. 100 mL, 1.11 mmol) was then added followed by a 6.42 mM solution of catalyst B (0.250 mL, 0.00161 mmol) in toluene was then added. After 3.5 h the mixture was poured into methanol (70 mL) that was rapidly stirred. A fibrous white precipitate formed that was isolated and washed with methanol (2×30 mL). The product was dried under reduced pressure overnight. Yield: 0.72 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected ester-capped product as a mixture of E and Z isomers. Data are summarized in Table 2.
Example 9
Cross Metathesis Reaction of ethylene-propylene copolymer with 5-hexen-1-ol
Ethylene propylene copolymer EP2 (1.65 g, ca. 0.748 mmol vinyls) and toluene (10 mL) were combined and heated to reflux for 10 min to form a homogeneous solution. The mixture was cooled to 60° C., and it became cloudy. Then 5-hexen-1-ol (0.900 mL, 8.99 mmol) and a toluene solution (2 mL) of catalyst A (0.0288 g, 0.0304 mmol) were added. After 18 h the mixture was poured into methanol (50 mL) that was rapidly stirred. A white precipitate formed that was isolated on a fritted disk and washed with methanol (2×15 mL). The product was dried under reduced pressure overnight. Yield: 1.54 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected product. Data are summarized in Table 2.
Example 10
Cross metathesis reaction of 1-octadecene and acrylic acid
1-Octadecene (3.26 g, 12.9 mmol) and acrylic acid (1.12 g, 15.5 mmol) were combined with CH2Cl2 (6 mL). The mixture was heated to 40° C. Then catalyst A (0.0611 g, 0.0645 mmol) in CH2Cl2 (2 mL) was added. Gas evolution was observed after several minutes. After 21 h the mixture was mixed with methanol (80 mL) and stirred well. The mixture was cooled to −15° C. for 2 h then the crystalline product was isolated on a fritted disk and washed with methanol (2×15 mL). The white solid was dried under reduced pressure. Yield: 3.30 g, 86.3%. 1H NMR spectroscopic data indicated that the isolated product was the expected acid-capped product as a single observed isomer, presumably the E isomer.
Example 11
Cross Metathesis Reaction of polypropylene with acrylic acid
Atactic polypropylene aPP2 (1.82 g, ca. 1.93 mmol vinyls) and acrylic acid (0.194 g, 2.70 mmol) were combined with CH2Cl2 (8 mL). The mixture was heated to 40° C. Then catalyst A (0.0166 g, 0.0175 mmol) in CH2Cl2 (2 mL) was added. After about 16 h a thick red oil remained. This was mixed with pentane (20 mL) and stirred well. The resulting orange-red suspension was passed through a short column of silica gel, then neutral alumina. The combined organics were filtered and evaporated to yield a nearly colorless oil. The oil was further dried under reduced pressure. Yield: 0.71 g. 1H NMR spectroscopic data indicated the nearly complete (<5% vinyl present) conversion to the expected acid-capped product and a small amount (ca. 5%) of a vinylene byproduct likely the result of iPP2 homocoupling.








TABLE 2







1H NMR



















Ha
Hb
GPC
DSC
















Ex.
(Ca)
(Cb)
Y
Mn **
Mn1
Mw1
Mz1
Mw/Mn1
Tm* (° C.)



















1
6.94
5.79
 3.69
312
—
—
—
—



2
6.92
5.79
 3.69
362
223
339
570
1.52


3
6.94
5.80
 3.71
1354
1001
2103
4120
2.1


4
6.95
5.81
 3.72
5710
3934
10686
20701
2.72


5
6.93
5.79
 3.70
691
281
993
6311
3.53


6
6.99
5.86
 3.75
2722
1841
6937
44852
3.77


7
6.98
5.86
 3.76
4277
4446
8926
14863
2.01


8
7.0
5.9
 3.8
18690
22512
21987
106931
2.31


9
5.4-5.5
5.4-5.5

3325
2011
7386
62846
3.67


10
7.07
5.80
10.90 
295
—
—
—
—





(—OH)


11
7.05
5.81
not
2892
756
1898
4389
2.51





obsvd.





For examples 1-5, 10 and 11 solvent of CDCl3 at room temperature was used.


For examples 6-9 solvent of D2-TCE at 120° C. was used.


Tm* is DSC second melt.


1determined by GPC-units g/mol.


** by 1H NMR






All documents described herein are incorporated by reference herein, including any priority documents and/or testing procedures to the extent they are not inconsistent with this text. As is apparent from the foregoing general description and the specific embodiments, while forms of the invention have been illustrated and described, various modifications can be made without departing from the spirit and scope of the invention. Accordingly, it is not intended that the invention be limited thereby. Likewise, the term “comprising” is considered synonymous with the term “including” for purposes of Australian law.

## Claims

1. A process to functionalize propylene co-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene co-oligomer having an Mn of 300 to 30,000 g/mol (as measured by 1H NMR) comprising 50 to 90 mol % propylene and 10 to 50 mol % of ethylene, wherein the co-oligomer has at least X % allyl chain ends (relative to total unsaturations), where X=(−0.94*(mol % ethylene incorporated) +100).

2. The process of claim 1 wherein the co-oligomer has more than 90% allyl chain ends (relative to total unsaturations).

3. The process of claim 1 wherein the co-oligomer comprises 15 to 95 wt % ethylene and has more than 80% allyl chain ends (relative to total unsaturations).

4. The process of claim 1 wherein the co-oligomer comprises at 30 to 95 wt % ethylene and has more than 70% allyl chain ends (relative to total unsaturations).

5. The process of claim 1 wherein the co-oligomer comprises at 30 to 95 wt % ethylene and has more than 90% allyl chain ends (relative to total unsaturations).

6. The process of claim 1, wherein the co-oligomer is a liquid at 25° C.

7. The process of claim 1, wherein the co-oligomer has a Mn of about 500 to about 7,500 g/mole, a Mw of 1,000 to about 20,000 g/mol, and a Mz of about 1400 (alternately 1700) to about 150,000 g/mol.

8. The process of claim 1 wherein the alkene metathesis catalyst is represented by the Formula (I):



where:
M is a Group 8 metal;
X and X1 are, independently, any anionic ligand, or X and X1 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 L1 are neutral two electron donors, L and L1 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;
L1 and X1 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 R1 are, independently, hydrogen or C1 to C30 substituted or unsubstituted hydrocarbyl;
R1 and L1 or X1 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.

9. The process of claim 8 wherein M is Ru or Os;
X and X1 are, independently, a halogen, an alkoxide or a triflate, or X and X1 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 L1 are, independently, a phosphine or a N-heterocyclic carbene, L and L1 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;
L1 and X1 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 R1 are, independently, hydrogen or a C1 to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl;
R1 and L1 or X1 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.

10. The process of claim 1 wherein the alkene metathesis catalyst is one or more of:
2,6-diisopropylphenylimidoneophylidene molybdenum(VI) bis(t-butoxide),
2,6-diisopropylphenylimidoneophylidene molybdenum(VI) bis(hexafluoro-t-butoxide),
2,6-diisopropylphenylimido neophylidenemolybdenum(VI) bis(trifluoromethanesulfonate) dimethoxyethane adduct,
2,6-diisopropylphenylimidoneophylidene[racemic-BIPHEN]molybdenum(VI),
tricyclohexylphosphine[1,3-bis(2,4,6-trimethylphenyl)imidazol-2-ylidene][3-phenyl-1H-inden-1-ylidene]ruthenium(II) dichloride,
tricyclohexylphosphine[3-phenyl-1H-inden-1-ylidene][1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydro-imidazol-2-ylidene]ruthenium(II) dichloride,
tricyclohexylphosphine[1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2-ylidene][(phenylthio)methylene]ruthenium(II) dichloride,
bis(tricyclohexylphosphine)-3-phenyl-1H-inden-1-ylideneruthenium(II) dichloride,
1,3-bis(2,4,6-trimethylphenyl)-4,5-dihydroimidazol-2-ylidene[2-(i-propoxy)-5-(N,N-dimethylaminosulfonyl)phenyl]methyleneruthenium(II) dichloride,
[1,3-bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]-[2-[[(4-methylphenyl)imino]methyl]-4-nitrophenolyl]-[3-phenyl-1H-inden-1-ylidene]ruthenium(II) chloride,
benzylidene-bis(tricyclohexylphosphine)dichlororuthenium,
benzylidene [1,3- bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(tricyclohexylphosphine)ruthenium,
dichloro(o-isopropoxyphenylmethylene)(tricyclohexylphosphine)ruthenium(II),
(1,3-bis-(2,4,6-trimethylphenyl)-2-imidazolidinylidene)dichloro(o-isopropoxyphenylmethylene)ruthenium,
1,3-bis(2-methylphenyl)-2-imidazolidinylidene]dichloro(2-isopropoxyphenylmethylene) ruthenium(II),
[1,3-bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro[3-(2-pyridinyl)propylidene]ruthenium(II),
[1,3-bis(2-methylphenyl)-2-imidazolidinylidene]dichloro(phenylmethylene) (tricyclohexylphosphine)ruthenium(II),
[1,3 -bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(3 -methyl-2-butenylidene) (tricyclohexylphosphine)ruthenium(II), and
[1,3-bis(2,4,6-trimethylphenyl)-2-imidazolidinylidene]dichloro(benzylidene)bis(3-bromopyridine)ruthenium(II).

11. The process of claim 1 wherein the heteroatom containing alkene is represented by the formula: H2C═CH—R or R*—HC═CH—R, where R* and R are, independently, a heteroatom containing group containing 1 to 30 carbon atoms and at least one heteroatom.

12. The process of claim 11 where R* and R are, independently, a heteroatom containing group containing 1 to 30 carbon atoms and at least one heteroatom selected from the group consisting of Si, P, O, S, N, Cl, F, I and Br.

13. The process of claim 11 where R* and R are selected from the group consisting of alcohols, amides, nitriles, imines, haloalkyls, acids, esters, anhydrides, acid-esters, oxycarbonyls, carbonyls, formyls, formylcarbonyls, hydroxyls, and acetyl halides.

14. The process of claim 11 where R* and R are represented by the formula -D-Y, where D is a hydrocarbyl group having 1 to 12 carbon atoms and Y is nitrogen or oxygen.

15. The process of claim 1 wherein the heteroatom containing alkene comprises one or more of acrylonitrile, acrylamide, allyl amine, acrylic acid, crotonic acid, methacrylic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, itaconic anhydride, citraconic acid, citraconic anhydride, mesaconic acid, glutaconic acid, chloromaleic acid, aconitic acid, crotonic acid, methylcrotonic acid, sorbic acid, 3-hexenoic acid, 10-decenoic acid, 2-pentene-1,3,5-tricarboxylic acid, cinnamic acid, and C1 to C4 alkyl acid esters of the foregoing, methyl maleate, ethyl fumarate, methyl fumarate, and 5-hexen-1 -ol.

16. The process of claim 1 wherein the propylene co-oligomer is prepared by a process having productivity of at least 4.5×103 g/mmol/hr, comprising:
contacting, at a temperature of from 35° C. to 150° C., propylene, 0.1 to 70 mol % ethylene and from 0 to about 5 wt % hydrogen in the presence of a catalyst system comprising an activator and at least one metallocene compound represented by the formulae:




where
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, (alternately two X's may form a part of a fused ring or a ring system);
each Q is, independently carbon or a heteroatom
each R1 is, independently, a C1 to C8 alkyl group, R1 may the same or different as R2;
each R2 is, independently, a C1 to C8 alkyl group;
each R3 is, independently, hydrogen, or a substituted or unsubstituted hydrocarbyl group having from 1 to 8 carbon atoms, provided that at least three R3 groups are not hydrogen;
each R4 is, independently, hydrogen or a substituted or unsubstituted hydrocarbyl group, a heteroatom or heteroatom containing group,
R5 is hydrogen or a C1 to C8 alkyl group;
R6 is hydrogen or a C1 to C8 alkyl group;
each R7 is, independently, hydrogen, or a C1 to C8 alkyl group provided that at least seven R7 groups are not hydrogen;
N is nitrogen;
T is a bridge;
each Ra, is independently, hydrogen, halogen or a C1 to C20 hydrocarbyl, and two Ra can form an 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.

17. The process of claim 16, wherein the activator comprises one or more non-coordinating anions.

18. The process of claim 1 where the process is a continuous process comprising introducing monomer and catalyst system into a reactor, obtaining a reactor effluent containing vinyl terminated propylene co-oligomer, optionally removing solvent, unused monomer and/or other volatiles, obtaining vinyl terminated propylene co-oligomer, introducing vinyl terminated propylene co-oligomer and further combining the propylene co-oligomer with an alkene metathesis catalyst and heteroatom containing alkene in a reaction zone and obtaining functionalized propylene co-oligomer.

19. The process of claim 1 where the co-oligomer contains less than 80 wt % of C4 olefin(s).

20. The process of claim 1 wherein the co-oligomer has an Mw/Mn by GPC-DRI of 1.5 to 10.

21. The process of claim 1 where C4 olefins are substantially absent from the functionalized co-oligomers.

22. The process of claim 1 wherein the co-oligomer has a Tg of 0° C. or less.

23. The process of claim 1 wherein the co-oligomer has a melting point of from 60 to 130° C.

24. The process of claim 1 wherein the co-oligomer has no detectable melting point by DSC following storage at 23° C. for 48 hours.

25. The process of claim 1 where C4-20 olefins are substantially absent from the functionalized co-oligomer.

26. The process of claim 1 where the number of functional groups present on the functionalized co-oligomer is 0.60 to 1.2 functional groups per chain, assuming that Mn has not altered by more than 15% as compared to the Mn of the co-oligomer prior to functionalization.

27. The process of claim 1 where the percent functionalization of the functionalized co-oligomer is 75% or more.

28. A process to functionalize propylene co-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene co-oligomer having an Mn of 300 to 30,000 g/mol (as measured by 1H NMR) comprising 10 to 90 mol % propylene and 10 to 90 mol % of ethylene, wherein the co-oligomer has at least X % allyl chain ends (relative to total unsaturations), where: 1) X=(−0.94*(mol % ethylene incorporated)+100), when 10 to 60 mol % ethylene is present in the co-oligomer, and 2) X=45, when greater than 60 and less than 70 mol % ethylene is present in the co-oligomer, and 3) X=(1.83* (mol % ethylene incorporated) −83), when 70 to 90 mol % ethylene is present in the co-oligomer, and wherein the co-oligomer has an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0.

29. The process of claim 28 wherein the co-oligomer has a Tg of 0° C. or less.

30. The process of claim 28 wherein the co-oligomer has a melting point of from 60 to 130° C.

31. A process to functionalize propylene co-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene co-oligomer comprising 95 to 99 mol % propylene and 1 to 4 mol % ethylene wherein the propylene co-oligomer has: at least 97% allyl chain ends, a number average molecular weight (Mn) of about 400 to about 30,000 g/mol, an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0, and less than 1400 ppm aluminum.

32. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene oligomer comprising more than 90 mol % propylene and less than 10 mol % ethylene, wherein the oligomer has: at least 93% allyl chain ends, an Mn of about 500 to about 20,000 g/mol (as measured by 1H NMR), an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0, and less than 1400 ppm aluminum.

33. The process of claim 32 wherein the oligomer has an Mw/Mn by GPC-DRI of 1.5 to 10.

34. The process of claim 32 wherein the oligomer is a liquid at 25° C.

35. The process of claim 32 where C4 olefins are substantially absent from the functionalized oligomer.

36. The process of claim 32 wherein the oligomer comprises 95 to 99 mol % propylene.

37. The process of claim 32 wherein the oligomer has at least 95% allyl chain ends.

38. The process of claim 32 wherein the oligomer has a number average molecular weight (Mn) of about 600 to about 15,000 g/mol.

39. The process of claim 32 wherein the oligomer has a Tg of 0° C. or less.

40. The process of claim 32 wherein the oligomer has a melting point of from 60 to 130° C.

41. The process of claim 32 wherein the oligomer has no detectable melting point by DSC following storage at 23° C. for 48 hours.

42. The process of claim 32 wherein F+VI*+VE*≧(0.80(VI+VE)), wherein VI is the number of vinyl groups/1000 carbons and VE is number of vinylidene groups/1000 carbons for the unfunctionalized oligomer, VI* is the number of vinyl groups/1000 carbons and VE* is the number of vinylidene groups/1000 carbons for the functionalized oligomer, and F is the number of functional groups per 1000 carbons.

43. The process of claim 32 where C4-20 olefins are substantially absent from the functionalized co-oligomer.

44. The process of claim 32 where the number of functional groups present on the functionalized oligomer is 0.75 to 1.1 functional groups per chain, assuming that Mn has not altered by more than 15% as compared to the Mn of the oligomer prior to functionalization.

45. The process of claim 32 where the percent functionalization of the functionalized oligomer is 80% or more.

46. The process of claim 32 wherein the alkene metathesis catalyst is represented by the Formula (I):



where:
M is a Group 8 metal;
X and X1 are, independently, any anionic ligand, or X and X1 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 L1 are neutral two electron donors, L and L1 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;
L1 and X1 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 R1 are, independently, hydrogen or C1 to C30 substituted or unsubstituted hydrocarbyl;
R1 and L1 or X1 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.

47. The process of claim 46 wherein M is Ru or Os;
X and X1 are, independently, a halogen, an alkoxide or a triflate, or X and X1 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 L1 are, independently, a phosphine or a N-heterocyclic carbene, L and L1 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;
L1 and X1 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 R1 are, independently, hydrogen or a C1 to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl;
R1 and L1 or X1 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.

48. The process of claim 32 wherein the heteroatom containing alkene is represented by the formula: H2C═CH—R or R*—HC═CH—R, where R* and R are, independently, a heteroatom containing group containing 1 to 30 carbon atoms and at least one heteroatom selected from the group consisting of Si, P, O, S, N, Cl, F, I and Br.

49. The process of claim 32 wherein the propylene oligomer is prepared by a process having productivity of at least 4.5×103 g/mmol/hr, comprising:
contacting, at a temperature of from 35° C. to 150° C., propylene, 0.1 to 70 mol % ethylene and from 0 to about 5 wt % hydrogen in the presence of a catalyst system comprising an activator and at least one metallocene compound represented by the formulae:




where
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, (alternately two X's may form a part of a fused ring or a ring system);
each Q is, independently carbon or a heteroatom
each R1 is, independently, a C1 to C8 alkyl group, R1 may the same or different as R2;
each R2 is, independently, a C1 to C8 alkyl group;
each R3 is, independently, hydrogen, or a substituted or unsubstituted hydrocarbyl group having from 1 to 8 carbon atoms, provided that at least three R3 groups are not hydrogen;
each R4 is, independently, hydrogen or a substituted or unsubstituted hydrocarbyl group, a heteroatom or heteroatom containing group;
R5 is hydrogen or a C1 to C8 alkyl group;
R6 is hydrogen or a C1 to C8 alkyl group;
each R7 is, independently, hydrogen, or a C1 to C8 alkyl group, provided that at least seven R7 groups are not hydrogen;
N is nitrogen;
T is a bridge;
each Ra, is independently, hydrogen, halogen or a C1 to C20 hydrocarbyl, and two Ra can form an 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.

50. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene oligomer comprising at least 50 mol % propylene and from 10 to 50 mol % ethylene, wherein the oligomer has: at least 90% allyl chain ends, Mn of about 150 to about 10,000 g/mol (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.3:1.0, wherein monomers having four or more carbon atoms are present at from 0 to 3 mol %.

51. The process of claim 50 wherein F+VI*+VE*≧(0.80(VI+VE)), wherein VI is the number of vinyl groups/1000 carbons and VE is number of vinylidene groups/1000 carbons for the unfunctionalized oligomer, VI* is the number of vinyl groups/1000 carbons and VE* is the number of vinylidene groups/1000 carbons for the functionalized oligomer, and F is the number of functional groups per 1000 carbons.

52. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene oligomer comprising at least 50 mol % propylene, from 0.1 to 45 mol % ethylene, and from 0.1 to 5 mol % C4 to C12 olefin, wherein the oligomer has: at least 87% allyl chain ends (alternately at least 90%), an Mn of about 150 to about 10,000 g/mol, (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.35:1.0.

53. The process of claim 52 wherein the oligomer comprises at least 60 mol % propylene, from 0.1 to 10 mol % ethylene, and from 0.1 to 5 mol % C4 to C12 olefin.

54. The process of claim 52 wherein the oligomer has at least 93% allyl chain ends and an Mn of about 750 to about 10,000 g/mol.

55. The process of claim 52 wherein F+VI*+VE*≧(0.80(VI+VE)), wherein VI is the number of vinyl groups/1000 carbons and VE is number of vinylidene groups/1000 carbons for the unfunctionalized oligomer, VI* is the number of vinyl groups/1000 carbons and VE* is the number of vinylidene groups/1000 carbons for the functionalized oligomer, and F is the number of functional groups per 1000 carbons.

56. A process to functionalize propylene oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a propylene oligomer comprising at least 50 mol % propylene, from 0.1 to 45 wt % ethylene, and from 0.1 to 5 mol % diene, wherein the oligomer has: at least 90% allyl chain ends, an Mn of about 150 to about 10,000 g/mol (as measured by 1H NMR), and an isobutyl chain end to allylic vinyl group ratio of 0.7:1 to 1.35:1.0.

57. The process of claim 56 wherein the oligomer has at least 93% allyl chain ends and an Mn of about 750 to about 10,000 g/mol.

58. The process of claim 56 wherein the diene is selected from the group consisting of C4 to C12 alpha-omega dienes, norbornene, ethylidene norbornene, vinylnorbornene, norbornadiene, and dicyclopentadiene.

59. The process of claim 56 wherein F+VI*+VE*≧(0.80(VI+VE)), wherein VI is the number of vinyl groups/1000 carbons and VE is number of vinylidene groups/1000 carbons for the unfunctionalized oligomer, VI* is the number of vinyl groups/1000 carbons and VE* is the number of vinylidene groups/1000 carbons for the functionalized oligomer, and F is the number of functional groups per 1000 carbons.

60. A process to functionalize propylene homo-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a homo-oligomer comprising propylene, wherein the homo-oligomer has: at least 93% allyl chain ends, an Mn of about 500 to about 20,000 g/mol (as measured by 1H NMR), an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.2:1.0, and less than 1400 ppm aluminum.

61. The process of claim 60 wherein the propylene homo-oligomer is prepared by a homogeneous process having productivity of at least 4.5×106 g/mmol/hr, comprising:
contacting, at a temperature of from 30° C. to 120° C., propylene, 0 mol % comonomer and from 0 to about 5 wt % hydrogen in the presence of a catalyst system comprising an activator and at least one metallocene compound represented by the formulae:




where
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, (alternately two X's may form a part of a fused ring or a ring system);
each Q is, independently carbon or a heteroatom;
each R1 is, independently, a C1 to C8 alkyl group R1 may the same or different as R2;
each R2 is, independently, a C1 to C8 alkyl group;
each R3 is, independently, hydrogen, or a substituted or unsubstituted hydrocarbyl group having from 1 to 8 carbon atoms provided that: 1) all five R3 groups are methyl, or 2) four R3 groups are not hydrogen and at least one R3 group is a C2 to C8 substituted or unsubstituted hydrocarbyl;
each R4 is, independently, hydrogen or a substituted or unsubstituted hydrocarbyl group, a heteroatom or heteroatom containing group
R5 is hydrogen or a C1 to C8 alkyl group;
R6 is hydrogen or a C1 to C8 alkyl group;
each R7 is, independently, hydrogen, or a C1 to C8 alkyl group, provided that at least seven R7 groups are not hydrogen;
N is nitrogen;
T is a bridge;
each Ra, is independently, hydrogen, halogen or a C1 to C20 hydrocarbyl, and two Ra can form an 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.

62. The process of claim 60 wherein the homo-oligomer has an Mw/Mn by GPC-DRI of 1.5 to 10.

63. The process of claim 60 wherein the homo-oligomer is a liquid at 25° C.

64. The process of claim 60 wherein the homo-oligomer has at least 98% allyl chain ends.

65. The process of claim 60 wherein the homo-oligomer has a Tg of 0° C. or less.

66. The process of claim 60 wherein the homo-oligomer has a melting point of from 60 to 130° C.

67. The process of claim 60 wherein the homo-oligomer has no detectable melting point by DSC following storage at 23° C. for 48 hours.

68. The process of claim 60 wherein F+VI*+VE*≧(0.80(VI+VE)), wherein VI is the number of vinyl groups/1000 carbons and VE is number of vinylidene groups/1000 carbons for the unfunctionalized oligomer, VI* is the number of vinyl groups/1000 carbons and VE* is the number of vinylidene groups/1000 carbons for the functionalized oligomer, and F is the number of functional groups per 1000 carbons.

69. The process of claim 60 where the process is a continuous process comprising introducing monomer and catalyst system into a reactor, obtaining a reactor effluent containing vinyl terminated propylene homo-oligomer, optionally removing solvent, unused monomer and/or other volatiles, obtaining vinyl terminated propylene homo-oligomer, introducing vinyl terminated propylene homo-oligomer and further combining the propylene homo-oligomer with an alkene metathesis catalyst and heteroatom containing alkene in a reaction zone and obtaining functionalized propylene homo-oligomer.

70. The process of claim 60 where the number of functional groups present on the functionalized oligomer is 0.75 to 1.1 functional groups per chain, assuming that Mn has not altered by more than 15% as compared to the Mn of the homo-oligomer prior to functionalization.

71. The process of claim 60 where the percent functionalization of the functionalized homo-oligomer is 90% or more.

72. The process of claim 60 wherein the alkene metathesis catalyst is represented by the Formula (I):



where:
M is a Group 8 metal;
X and X1 are, independently, any anionic ligand, or X and X1 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 L1 are neutral two electron donors, L and L1 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;
L1 and X1 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 R1 are, independently, hydrogen or C1 to C30 substituted or unsubstituted hydrocarbyl;
R1 and L1 or X1 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.

73. The process of claim 72 wherein M is Ru or Os;
X and X1 are, independently, a halogen, an alkoxide or a triflate, or X and X1 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 L1 are, independently, a phosphine or a N-heterocyclic carbene, L and L1 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;
L1 and X1 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 R1 are, independently, hydrogen or a C1 to C30 substituted or unsubstituted alkyl or a substituted or unsubstituted C4 to C30 aryl;
R1 and L1 or X1 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.

74. The process of claim 60 wherein the heteroatom containing alkene is represented by the formula: H2C═CH—R or R*—HC═CH—R, where R* and R are, independently, a heteroatom containing group containing 1 to 30 carbon atoms and at least one heteroatom selected from the group consisting of Si, P, O, S, N, Cl, F, I and Br.

75. A process to functionalize propylene homo-oligomer comprising contacting an alkene metathesis catalyst with a heteroatom containing alkene, and a homo-oligomer comprising: propylene and 0 wt % comonomer, wherein the homo-oligomer has: at least 95% allyl chain ends, an Mn of about 700 to about 10,000 g/mol, an isobutyl chain end to allylic vinyl group ratio of 0.8:1 to 1.2:1.0, and less than 1400 ppm aluminum.