WO2009073274A1 - Moisture curable propylene-alpha-olefin copolymers - Google Patents

Moisture curable propylene-alpha-olefin copolymers Download PDF

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WO2009073274A1
WO2009073274A1 PCT/US2008/079149 US2008079149W WO2009073274A1 WO 2009073274 A1 WO2009073274 A1 WO 2009073274A1 US 2008079149 W US2008079149 W US 2008079149W WO 2009073274 A1 WO2009073274 A1 WO 2009073274A1
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copolymer
propylene
graft
olefm
graft copolymer
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PCT/US2008/079149
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French (fr)
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Trazollah Ouhadi
Jean-Roch H. Schauder
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Advanced Elastomer Systems, L.P.
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Publication of WO2009073274A1 publication Critical patent/WO2009073274A1/en

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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/42Introducing metal atoms or metal-containing groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F255/00Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
    • C08F255/02Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms
    • C08F255/04Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms on to ethene-propene copolymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F255/00Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
    • C08F255/02Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms
    • C08F255/06Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms on to ethene-propene-diene terpolymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/24Crosslinking, e.g. vulcanising, of macromolecules
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J151/00Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
    • C09J151/06Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/10Materials in mouldable or extrudable form for sealing or packing joints or covers
    • C09K3/1006Materials in mouldable or extrudable form for sealing or packing joints or covers characterised by the chemical nature of one of its constituents
    • C09K3/1018Macromolecular compounds having one or more carbon-to-silicon linkages
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/24Materials not provided for elsewhere for simulating ice or snow
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2300/00Characterised by the use of unspecified polymers
    • C08J2300/10Polymers characterised by the presence of specified groups, e.g. terminal or pendant functional groups
    • C08J2300/108Polymers characterised by the presence of specified groups, e.g. terminal or pendant functional groups containing hydrolysable silane groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/10Homopolymers or copolymers of propene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2666/00Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
    • C08L2666/02Organic macromolecular compounds, natural resins, waxes or and bituminous materials
    • C08L2666/14Macromolecular compounds according to C08L59/00 - C08L87/00; Derivatives thereof

Definitions

  • the present invention relates in general to moisture-curable propylene copolymers, and more particularly to hydrolizable silane graft propylene-based polymers and thermoplastic compositions thereof.
  • Silane graft polyethylene-based compositions (having at least 50 wt% ethylene derived units) have been disclosed in EP 0 510 559 A2, WO 2005/003199, US 6,472,015, US 6,455,637, US 5,844,009, US 5,883,145, US Patent Publication 2002/0151647 and US Patent Publication 2003/0050401.
  • One problem with using polyethylene-based polymers in forming graft polymers is that the peroxides that are used to initiate the grafting also act as a cross- linker towards polyethylene themselves.
  • One aspect of the present invention is directed to hydrolysable silane graft propylene- ⁇ -olef ⁇ n copolymers (“graft copolymer”) comprising a propylene- ⁇ -olef ⁇ n copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ -olef ⁇ n copolymer, of ethylene-derived units or a C 4 to C 10 ⁇ -olefm-derived unit, and having, in one embodiment, the following features: a density of from 0.850 to 0.920 g/cm 3 ; a MWD of from 1.5 to 20; an H f of less than or equal to 75 J/g; a T m of from 25 to 105 0 C; and a triad tacticity by 13 C NMR of 75% or greater; and a hydrolysable silane component.
  • graft copolymer comprising a propylene- ⁇ -olef ⁇ n copolymer component compris
  • Another aspect of the present invention is directed to a cross-linked propylene- ⁇ - olefin copolymer (“cross-linked copolymer”) comprising the propylene- ⁇ -olef ⁇ n copolymer component and the hydrolysable silane component, the copolymer and silane having been subjected to the presence of water and, in a preferred embodiment, a condensation catalyst.
  • Yet another aspect of the present invention is directed to a composition of the graft copolymer and a polyolefm, an oil, a filler, or any combination thereof, thus forming the graft propylene- ⁇ -olefm copolymer composition ("graft copolymer composition").
  • a further aspect of the invention is direct to a composition of the cross-linked copolymer with a polyolefm, an oil, a filler, or any combination thereof, thus forming a crosslinked propylene- ⁇ -olef ⁇ n copolymer composition ("cross-linked copolymer composition").
  • moisture curable sealant refers to a compound or composition that can be cross-linked as initiated by exposure to liquid or vapor water, and being capable
  • One aspect of the invention is directed to a hydrolizable silane graft propylene- ⁇ - olefin copolymer comprising a propylene- ⁇ -olefm copolymer component comprising propylene-derived units and from 5 to 35 wt% (by weight of the propylene- ⁇ -olefm copolymer) of ethylene-derived units or a C 4 to C 10 ⁇ -olefin-derived unit; and a hydrolysable silane component.
  • hydrolizable silane graft propylene- ⁇ -olefm copolymer may be claimed such that the characteristics of the propylene- ⁇ -olefm copolymer alone — prior to reacting with (grafting to) the hydrolizable silane — are described.
  • the "hydrolizable silane graft propylene- ⁇ -olefin copolymer” may be claimed as the grafting reaction product of the "propylene- ⁇ -olefm copolymer” (having certain features as described herein) and a “hydrolizable silane.”
  • the crosslinking of polymers, in particular polyolefins, by the combined process of chemical grafting of silane molecules onto the polymer to form a silane graft resin, followed by catalyzed hydrolysis and condensation of the silane is known in the art such as is described in US 3,646,155 and US 6,455,637.
  • the preferred polyolefins for use in forming a graft copolymer are so called "propylene- ⁇ -olefm copolymers.”
  • the "propylene- ⁇ -olefm copolymers" described herein are copolymers of propylene-derived units and one or more units derived from ethylene or a C 4 -C 10 ⁇ -olefm and optionally one or more diene-derived units.
  • Preferred ⁇ -olefms are ethylene, 1-butene, 1- hexene and 1-octene.
  • Typical comonomer content of the copolymer is from 5 to 35 wt% in one embodiment.
  • the comonomer content is adjusted so that the copolymer preferably has a MWD (Mw/Mn) of from 1.5 to 20, more preferably from 1.5 to 5, a heat of fusion (H f ) less than or equal to 75 J/g and a T m less than or equal to 105 0 C.
  • MWD MWD
  • H f heat of fusion
  • T m less than or equal to 105 0 C.
  • the amount of a particular comonomer may be less than 5 wt%, but the combined comonomer content is preferably greater than 5 wt%.
  • the total weight percent of the C 2 or C 4 -C 10 ⁇ -olefin-derived units is preferably from 5 to 35 wt%, more preferably from 7 to 32 wt%, more preferably from 8 to 25 wt%, more preferably from 8 to 20 wt%, and more preferably from 8 to 16 wt%.
  • Particular embodiments of copolymers having more than one ⁇ -olefm include propylene- ethylene-octene, propylene-ethylene -hexene and propylene-ethylene-butene polymers. These copolymers may further comprise a diene as described below.
  • the embodiments described below are discussed with reference to ethylene as a preferred comonomer, but such embodiments are equally applicable with 1-butene, 1 -hexene or 1-octene as a comonomer.
  • the propylene-ethylene copolymer described below comprises ethylene, propylene and optionally a diene.
  • the propylene-ethylene copolymer can comprise from 5 to 25 wt% ethylene - derived units, preferably from 5 to 20 wt%, more preferably from 5 to 16 wt%, and more preferably from 6 to 16 wt% ethylene. In a preferred embodiment, the propylene-ethylene copolymer comprises greater than 11 wt% ethylene.
  • the propylene-ethylene copolymer can comprise from 75 to 95 wt% propylene-derived units, more preferably from 84 to 95 wt%, more preferably from 85 to 95 wt%, and more preferably from 85 to 94 wt% by weight of the copolymer.
  • the propylene-ethylene copolymer may optionally comprise less than or equal to 10 wt% diene derived units (or "diene"), preferably less than or equal to 5 wt% diene, more preferably less than or equal to 3 wt% diene, preferably from 0.1 to 3 or 4 or 5 or 6 wt%, more preferably from 0.1 to 2 wt%, and more preferably from 0.1 to 1 wt% diene.
  • diene derived units or "diene”
  • Suitable dienes useful as co-monomers are, for example: 1 ,4-hexadiene, 1 ,6-octadiene, 5-methyl-l,4- hexadiene, 3,7-dimethyl-l,6-octadiene, dicyclopentadiene (DCPD), ethylidiene norbornene (ENB), norbornadiene, 5 -vinyl-2 -norbornene (VNB), and combinations thereof.
  • the diene, if present, is most preferably ENB.
  • the propylene- ⁇ -olefm copolymer can have a triad tacticity of three propylene units, as measured by 13 C NMR, of 75% or greater, 80% or greater, 82% or greater, 85% or greater, or 90% or greater. Preferred ranges include from 50 to 99 %, more preferably from 60 to 99%, more preferably from 75 to 99% and more preferably from 80 to 99%; and in other embodiments from 60 to 97%.
  • Triad tacticity is determined as follows: The tacticity index, expressed herein as "m/r", is determined by 13 C nuclear magnetic resonance (NMR). The tacticity index m/r is calculated as defined by H. N. Cheng in 17 MACROMOLECULES 1950 (1984).
  • m or "r” describes the stereochemistry of pairs of contiguous propylene groups, "m” referring to meso and “r” to racemic.
  • An m/r ratio of 1.0 generally describes a syndiotactic polymer, and an m/r ratio of 2.0 an atactic material.
  • An isotactic material theoretically may have a ratio approaching infinity, and many by-product atactic polymers have sufficient isotactic content to result in ratios of greater than 50.
  • Embodiments of the propylene- ⁇ -olef ⁇ n copolymer have a tacticity index m/r ranging from a lower limit of 4 or 6 to an upper limit of 8 or 10 or 12.
  • the propylene- ⁇ -olefm copolymer has an H f , determined according to the Differential Scanning Calorimetry (DSC) procedure described herein, greater than or equal to 0.5 or 1 or 5 J/g, and is less than or equal to 80 J/g, preferably less than or equal to 70 J/g, more preferably less than or equal to 50 J/g, more preferably less than or equal to 35 J/g.
  • the Hf ranges from a lower limit of 1.0, or 1.5, or 3.0, or 4.0, or 6.0, or 7.0 J/g to an upper limit of 30, or 35, or 40, or 50, or 60 or 70, or 80 J/g.
  • the propylene-ethylene copolymer has a percent crystallinity of from 0.5 to 40%, preferably 1 to 30%, and more preferably 5 to 25% wherein "percent crystallinity" is determined according to the DSC procedure described herein.
  • the thermal energy for the highest order of polypropylene is estimated at 189 J/g (i.e., 100% crystallinity is equal to 189 J/g).
  • the propylene-ethylene copolymer of the present disclosure preferably has a crystallinity of less than 40%, preferably from 0.25 to 25%, more preferably from 0.5 to 22%, and most preferably from 0.5 to 20%.
  • the sample is heated at about 10°C/min to attain a final temperature of about 165°C.
  • the thermal output recorded as the area under the melting peak of the sample, is a measure of the heat of fusion and can be expressed in Joules per gram (J/g) of polymer and is automatically calculated by the Perkin Elmer System.
  • J/g Joules per gram
  • the melting profile shows two (2) maxima, the maxima at the highest temperature is taken as the melting point within the range of melting of the sample relative to a baseline measurement for the increasing heat capacity of the polymer as a function of temperature.
  • the propylene-ethylene copolymer preferably has a single broad melting transition.
  • the "melting point" (T m ) is defined as the temperature of the greatest heat absorption within the range of melting of the sample.
  • T m melting point
  • the propylene-ethylene copolymer may show secondary melting peaks adjacent to the principal peak, but for purposes herein, such secondary melting peaks are considered together as a single melting point, with the highest of these peaks being considered the T m of the propylene-ethylene copolymer.
  • the propylene-ethylene copolymer preferably has a T m of from 25 to 105 0 C, preferably from 25 to 85°C, more preferably from 25 to 75°C, more preferably from 25 to 65°C, more preferably from 30 to 80 0 C, more preferably from 30 to 70 0 C and more preferably from 30 to 60 0 C.
  • the propylene- ⁇ -olefm copolymer can have a density of 0.850 to 0.920 g/cm 3 , more preferably, 0.870 to 0.900 g/cm 3 , more preferably 0.880 to 0.890 g/cm 3 at room temperature as measured per the ASTM D-1505 test method.
  • the propylene- ⁇ -olefm copolymer can have a melt flow rate (MFR, ASTM D1238, 2.16 kg, 23O 0 C), equal to or greater than 0.2 dg/min.
  • MFR melt flow rate
  • ASTM D1238, 2.16 kg, 23O 0 C melt flow rate
  • the MFR is from 0.5 to 5000 dg/min and more preferably from 1 to 2500 dg/min.
  • the propylene- ⁇ -olefm copolymer has an MFR of 0.5 to 1500 dg/min, from 2 to 1000 dg/min in another embodiment, and from 5 to 500 dg/min in yet another embodiment, and from 10 to 250 dg/min in yet another embodiment, and from 10 to 100 dg/min in yet another embodiment, and from 2 to 40 dg/min in yet another embodiment, and from 2 to 30 dg/min in yet another embodiment.
  • Preferred propylene-ethylene copolymers may have a Mooney viscosity [ML (1+4) @ 125 0 C] as determined according to ASTM D 1646, of less than 100, more preferably less than 75, even more preferably less than 60, most preferably less than 30.
  • the propylene- ⁇ -olefm copolymer can have a Mw of 5,000 to 5,000,000 g/mole, more preferably a Mw of 10,000 to 1,000,000, and more preferably a Mw of 50,000 to 400,000.
  • the propylene- ⁇ -olefm copolymer can have a Mn of 2,500 to 2,500,000 g/mole, more preferably a Mn of 10,000 to 250,000, and more preferably a Mn of 25,000 to 200,000.
  • the propylene- ⁇ -olefm copolymer can have a Mz of 10,000 to 7,000,000 g/mole, more preferably a Mz of 80,000 to 700,000, and more preferably a Mz of 100,000 to 500,000.
  • the molecular weight distribution (MWD) of the propylene-ethylene copolymer is from 1.5 to 20 in one embodiment, and from 1.5 to 15 in another embodiment, and more preferably 1.5 to 5, more preferably 1.8 to 5 and most preferably 1.8 to 4 or 3.
  • Techniques for determining the molecular weight (Mn, Mz and Mw) and molecular weight distribution (MWD) are as follows, and as in Verstate et al. in 21 MACROMOLECULES 3360 (1988). Molecular weight and molecular weight distribution are measured using a Waters 150 gel permeation chromatograph equipped with a Chromatix KMX-6 on-line light scattering photometer.
  • the system is used at 135°C with 1,2,4- trichlorobenzene as the mobile phase.
  • Showdex Showa-Denko America, Inc.
  • polystyrene gel columns 802, 803, 804 and 805 are used. This technique is discussed in LIQUID CHROMATOGRAPHY OF POLYMERS AND RELATED MATERIALS III 207 (J. Cazes ed., Marcel Dekker, 1981).
  • No corrections for column spreading are employed; however, data on generally accepted standards, e.g., National Bureau of Standards Polyethylene 1484 and anionically produced hydrogenated polyisoprenes (an alternating ethylenepropylene copolymer) demonstrate that such corrections on Mw/Mn or Mz/Mw are less than 0.05 units.
  • the propylene- ⁇ -olefm copolymers can include copolymers prepared according to the procedures in WO 02/36651, US 6992158, and/or WO 00/01745. Preferred methods for producing the propylene- ⁇ -olefm copolymers are found in US Patent Application Publication 2004/0236042 and US 6,881,800.
  • Preferred propylene- ⁇ -olefm copolymers are available commercially under the trade names VistamaxxTM (ExxonMobil Chemical Company, Houston, TX, USA) and VersifyTM (The Dow Chemical Company, Midland, Michigan, USA), certain grades of TafmerTM XM or NotioTM (Mitsui Company, Japan) or certain grades of SoftelTM (Basell Polyolefms of the Netherlands).
  • the propylene- ⁇ -olefm copolymer as described above is reacted in the molten state with an organic silane having the general formula YSiRR"2, wherein Y is selected from vinyl terminated radicals, each R" is independently selected from hydrolysable organic radicals; and R can be a R" radical, or selected from Ci to Cio alkyl radicals (both R and R" are bound to the silicon atom).
  • Y is selected from a vinyl radical, vinyl terminated Ci to Cio alkyl radicals.
  • the vinyl terminated radical is preferably selected from vinyl, allyl, butenyl, cyclohexenyl, cyclopentadienyl, and cyclohexadienyl radicals.
  • Examples of the most preferred silanes are vinyltriethoxysilane and vinyltrimethoxy silane.
  • alkoxy radical such as methoxy, ethoxy and butoxy radicals
  • an acyloxy radical for example the formyloxy, acetoxy or propionoxy radicals
  • Other end-chain unsaturated silanes commercially available such as glycidoxyalkyl-methyl-diethoxysilane or methacryloxyalkyl-
  • 3-Mercapto-alkyltrialkoxysilane can be grafted onto the backbone of the invention in a mechanism involving radical coupling reactions.
  • the hydrolysable silane graft propylene- ⁇ -olefm is formed by reacting a maleic anhydride (or other suitable anhydride) and a peroxide with the propylene- ⁇ -olefm copolymer to form a maleic anhydride graft propylene- ⁇ -olefm copolymer (as described in US 6,884,850) followed by contacting the maleic anhydride graft propylene- ⁇ -olefm copolymer with an amino-silane to form a silane graft propylene- ⁇ -olefm copolymer.
  • the silane component in this embodiment is derived from an amino silane having the following formula: YHN(CH2) n SiRR"2, wherein N is a nitrogen atom, n is from 1 to 20 and wherein Y radical is either hydrogen or one alkyl radical, Ci to C 2 o alkyl radical terminated by -NH 2 ; R" is selected from hydrolysable organic radicals (as elucidated above), and R can be an alkyl group or a R" radical, or selected from Ci to C 10 alkyl radicals (both R and R" are bound to the silicon atom).
  • a propylene- ⁇ -olefm with an epoxy functionality can be produced by grafting a molecule containing at least one unsaturation double bond and at least one epoxy functionality, such as glycidyl methacrylate (C 7 H 10 O 3 ). A propylene- ⁇ -olefm with such an epoxy functional group will then react with an amino silane. This can then lead to the moisture curable copolymer as described herein.
  • the amount of silane reacted with the propylene- ⁇ -olefm depends in part upon the reaction conditions and the degree of modification desired in the propylene- ⁇ - olefm.
  • the proportion may vary from 0.03 to 50 wt% based on the total weight of the silane graft copolymer, and from 0.03 to 10 wt% in another embodiment, and from 0.05 to 2.5 wt% in yet another embodiment, and from 0.1 to 4 wt% in yet another embodiment, and from 0.5 to 5 wt% in yet another embodiment.
  • a free-radical initiator is also combined with the propylene- ⁇ -olefm and silane to initiate the graft polymerization reaction.
  • the free-radical initiator can be added at the same time as the silane, or after addition of the silane.
  • Most preferred free-radical initiators are organic peroxides such as benzoyl peroxide, dichlorobenzoyl peroxide, dicumyl peroxide, 2,5-Dimethyl-2,5-di-(tert-butyl-peroxy)-hexyne-(3), 2,5-Dimethyl-2,5-di-(tert-butyl-peroxy)- hexane-(3), di-tertiarybutyl peroxide.
  • the most preferred free-radical initiator for use in the compositions of the present invention is dicumyl peroxide. The criteria for choosing an appropriate free-radical initiator are known to persons skilled in the art and are described in US 3,646,155.
  • the organic peroxide free-radical initiator is added in an amount of from 0.1 to 1.0 wt% of the propylene- ⁇ -olefm, more preferably from 0.05 to 0.2 wt%.
  • the silane and free-radical initiator are reacted with the propylene- ⁇ -olefm copolymer and silane above the melting point of the copolymer and/or decomposition temperature of the free-radical initiator under conditions in which the copolymer is subjected to mechanical shearing (melt blending), using processes known to those skilled in the art.
  • melt blending takes place at from 60 to 200 0 C in one embodiment, and from 80 to 18O 0 C in another embodiment, and from 100 to 175 0 C in yet another embodiment, in order to accomplish grafting of the silane onto the propylene- ⁇ -olefm
  • the final hydrolysable silane graft propylene- ⁇ -olefm copolymer possesses from 0.03 to 4 or 5 or 10 wt% of the hydrolysable silane component in one embodiment, and from 0.05 to 3 wt% in a particular embodiment, and from 0.1 to 1 wt% in yet another particular embodiment, the propylene- ⁇ -olefm copolymer component making up the remainder.
  • the silane graft propylene- ⁇ -olefm copolymer is subsequently melt-processed in one embodiment with an amount of one or more silanol condensation catalysts (used to facilitate the cross-linking reaction of the graft copolymer), and optionally with one or more of a number of other additives, such as pigmenting agents, fillers, flame-retardants, antioxidants, stabilizers, processing oils, unmodified thermoplastics, compatibilizers and the like, to form a "composition,” as described further below.
  • silanol condensation catalysts used to facilitate the cross-linking reaction of the graft copolymer
  • additives such as pigmenting agents, fillers, flame-retardants, antioxidants, stabilizers, processing oils, unmodified thermoplastics, compatibilizers and the like
  • the silanol condensation catalyst (or “catalyst”) is typically selected from the group consisting of organic bases, carboxylic acids and organometallic compounds including organic titanates and complexes or carboxylates of lead, cobalt, iron, nickel, zinc and tin.
  • the catalyst is selected from dibutyltin dilaurate, dibutyltin diacetate, dibutyltin octanoate, dioctyltin maleate, dibutyltin oxide and titanium compounds such as titanium-2- ethylhexoxide.
  • the most preferred silanol condensation catalyst is dibutyltin dilaurate, though any material which will catalyze the silane condensation reaction is suitable for the invention.
  • the condensation catalyst is preferably added in an amount of from 0.01 to 5 wt%, and from 0.01 to 3 wt% in another embodiment, more preferably 0.05 to 2 wt%, and most preferably 0.1 to 1 wt% (by weight of the hydro lizable silane graft propylene- ⁇ -olefm copolymer).
  • the condensation catalyst can be added into the propylene- ⁇ -olefm copolymer or its blend in pure form, or in a masterbatch with a polymer, or an organic or inorganic filler/carrier.
  • composition thus produced to moisture, at from 20 to 25 0 C in one embodiment, and preferably at an elevated temperature, will induce crosslinking of the silane groups via a combined hydrolysis and condensation reaction. Atmospheric moisture is usually sufficient to permit the crosslinking to occur, but the rate of crosslinking may be increased by the use of an artificially moistened atmosphere, or by immersion in liquid water. Subjecting the composition to combined heat and moisture will accelerate the crosslinking reaction. Most preferably, crosslinking is effected at a temperature above 50 0 C and most preferably by exposing the composition to a temperature of 85°C and a relative humidity of 90% for approximately 100 hours.
  • the propylene- ⁇ -olefm copolymer, silane, free radical initiator and silanol condensation catalyst may be combined in any number of ways and in any order.
  • the propylene- ⁇ -olefm, silane and free-radical initiator are first combined and melt blended at or above the melting point of all of the components, at from 60 to 25O 0 C in one embodiment, and from 80 to 18O 0 C in another embodiment, and from 90 to 230 0 C in yet another embodiment, and from 100 to 175 0 C in yet another embodiment, in order to accomplish grafting of the silane onto the propylene- ⁇ -olefm and/or blending the components.
  • the silanol condensation catalyst can be combined with the graft copolymer, forming a graft copolymer composition.
  • the propylene- ⁇ -olefm, silane, free-radical initiator and silanol condensation catalyst are melt blended together in order to accomplish both the grafting of the silane onto the propylene- ⁇ -olefm and blending of the components, forming the graft copolymer composition.
  • other "additives" may be combined with the graft copolymer to form compositions.
  • the propylene- ⁇ -olefm, silane, free-radical initiator, silanol condensation catalyst and additives are reacted by melt blending as described above to form the graft copolymer composition.
  • the graft copolymer composition can then be passed through a multi-strand die, cooled, and subsequently chopped into pellets with a strand pelletizer and dried. The material so processed can then be exposed to moisture at any time convenient for its use as, for example, a moisture curable sealant, preferably at an elevated temperature, to effect crosslinking of the material.
  • the end result is the cross-linked propylene- ⁇ -olefm copolymer composition (or "cross-linked copolymer composition").
  • the propylene- ⁇ -olefm, silane and free-radical initiator are first reacted as described above to produce the graft copolymer, which can then be isolated, pelletized, etc.
  • This graft copolymer can then be separately melt processed by combining the silanol condensation catalyst and additives, combined as mentioned above.
  • This graft copolymer composition can then be exposed to moisture at any time convenient for its use as, for example, a moisture curable sealant, preferably at an elevated temperature, to effect crosslinking of the material. The end result is the cross-linked copolymer composition.
  • the graft copolymer may be combined with a thermoplastic, a polyolefin or polyamide in one embodiment.
  • Polyolefin can include any known polymer comprising olefm-derived units, and in particular includes propylene homopolymers, propylene random copolymers, propylene impact copolymers, propylene block copolymers, plastomers, high density polyethylenes, linear low density polyethylenes, low density polyethylenes, and combinations thereof.
  • the hydro lizable silane graft propylene- ⁇ -olefm copolymer may be blended with a processing oil (“oil").
  • the hydrolizable silane graft propylene- ⁇ -olefm copolymer is blended with a filler.
  • the hydrolizable silane graft propylene- ⁇ -olefin copolymer may be blended with any combination of a polyolefin, oil, and filler.
  • the hydrolizable silane graft propylene- ⁇ -olefm copolymer is blended with from 1 to 70 wt% (by weight of the composition) of an oil, and from 5 to 60 wt% in yet another embodiment, and from 10 to 40 wt% in yet another embodiment.
  • the polyolefin is a propylene homopolymer.
  • Oils includes plasticizers, extender oils, synthetic processing oils, or a combination thereof can also be optionally added to the blend.
  • the extender oils can include, but are not limited to, aromatic, naphthenic, and paraffmic extender oils.
  • Exemplary synthetic processing oils are polylinear ⁇ -olefms, polybranched ⁇ -olefms, and hydrogenated polyalphaolefms.
  • the compositions of this invention can include organic esters, alkyl ethers, or combinations thereof. Synthetic polyalphaolefins are also useful in lowering the glass transition temperature (T g ).
  • Commercially available poly- ⁇ -olefms that can be useful include ElevastTM A30, and Elevast L30 (ExxonMobil Chemical, Houston). Oligomeric (e.g., IndopolTM, BP, Great Britain) and polymeric processing additives can also be used.
  • the hydrolizable silane graft propylene- ⁇ -olefm copolymer is blended with from 1 or 2 to 60 wt% (by weight of the composition) of a polyolefin, and from 10 to 50 wt% in yet another embodiment.
  • the polyolefin is a propylene homopolymer or copolymer.
  • the polyolefin is a propylene copolymer comprising from 0.1 to 20 wt% ethylene derived units or a C 4 to Cio ⁇ -olefm derived units, and from 0.1 to 5 wt% in another embodiment.
  • the polypropylene has an MFR (230/2.16) of from 0.1 to 2000 dg/min, and from 0.5 to 200 dg/min in yet another embodiment, and from 1 to 20 dg/min in yet another embodiment, and from 2 to 10 dg/min in yet another embodiment.
  • the hydrolizable silane graft propylene- ⁇ -olefin copolymer is blended with from 1 to 40 wt% of a filler, and from 2 to 30 wt% in another embodiment, and from 3 to 20 wt% in yet another embodiment.
  • Fillers that can be included in the hydrolizable silane graft propylene- ⁇ -olefin copolymer composition include those reinforcing and non-reinforcing fillers or extenders that are conventionally employed in the compounding of polymeric materials.
  • Useful fillers include carbon black, calcium carbonate, clays, silica, talc, and titanium dioxide.
  • one embodiment of the present invention is a graft copolymer composition — a moisture curable sealant in a particular embodiment — comprising from 5 or 10 or 15 or 20 or 30 or 40 wt% to an upper limit of 75 or 80 or 85 or 90 or 95 wt% (by weight of the composition) of the graft copolymer; and a thermoplastic from a lower limit of 2 or 5 or 6 or 10 or 15 wt% to an upper limit of from 30 or 35 or 40 or 45 or 50 or 50 wt%, where the thermoplastic is preferably a polyolefin, and most preferably a polypropylene; and an oil from a lower limit of 5 or 10 or 15 wt% to an upper limit of from 25 or 30 or 40 or 50 or 60 wt% of the composition.
  • the graft copolymer composition also includes from 0.1 or 0.5 or 0.8 or 1.0 or 1.5 wt% to an upper limit of from 3.5 or 4.0 or 4.5 or 5.0 wt% of a silanol condensation catalyst by weight of the composition.
  • the graft copolymer composition also includes from 1 or 5 or 10 or 15 wt% to an upper limit of from 20 or 25 or 30 or 40 or 50 or 60 wt% of one or more f ⁇ ller(s). Any one of the ranges above may also be a 0.9 or 0.5 or 0.2 fraction thereof in order to make the entire composition comprise a total of 100%.
  • hydrolizable silane graft propylene- ⁇ -olefm copolymer such as antioxidants, antiozonates, UV stabilizers, slip agents, and other minor additives known in the art.
  • the graft copolymer compositions may be produced by any number of methods as described herein.
  • One method of forming a silane graft propylene- ⁇ -olefm copolymer comprises (a) providing a propylene- ⁇ -olefm copolymer comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ -olefin, of ethylene-derived units or a C 4 to C20 ⁇ -olefm-derived unit; (b) reacting a hydrolysable vinyl silane and a free-radical initiator with the propylene- ⁇ -olefin copolymer to form a silane graft propylene- ⁇ -olefm copolymer; or (c) reacting a maleic anhydride and a free-radical initiator with the propylene- ⁇ -olefin copolymer to form a maleic anhydride graft propylene- ⁇ -olef
  • the graft copolymer is further blended with from 0.01 to 5 wt%, based on total weight of final blend, of one or more silanol condensation catalyst(s).
  • the "reacting" steps of (b) or (c) take place from any temperature at or above the melting point of the graft copolymer, or from 80 or 90 or 95 or 100 to an upper limit of from 150 or 170 or 200 or 23O 0 C.
  • the "reacting" steps occur during melt blending of the components, the melt blending taking place by any suitable means known in the art.
  • the free-radical initiator, silane and copolymer can be combined with one another in any order.
  • the reacting steps of (b) or (c) occur during melt-blending of the components.
  • the silane graft propylene- ⁇ -olefm copolymer is contacted with a silanol condensation catalyst and water/moisture to form a cross-linked silane graft propylene- ⁇ -olefm copolymer.
  • the "contacting" step occurs at from 20 or 25 to an upper limit of from 40 or 50 or 60 or 70 or 85 0 C.
  • the graft copolymer has a Shore A hardness (ISO 868) of from greater than 40, and from greater than 50 in another embodiment, and greater than 60 in another embodiment, and from 40 to 90 in yet another embodiment, and from 50 to 70 in yet another embodiment.
  • the graft copolymer has an Elongation at Break (ISO 37) of from 100 to 1100%, and from 400 to 1100% in another embodiment, and from 500 to 1000% in another embodiment, and greater than 200 in yet another embodiment, and greater than 400 in yet another embodiment, and greater than 500 in yet another embodiment.
  • ISO 37 Elongation at Break
  • the graft copolymer has a Tensile Strength (ISO 37) of from greater than 1 MPa, and from greater than 3 MPa in another embodiment, and from greater than 5 MPa in another embodiment, and greater than 7 MPa in another embodiment, and greater than 10 MPa in yet another embodiment, and from and from 3 to 15 MPa in yet another embodiment, and from 5 to 15 MPa in yet another embodiment, and from 7 to 13 MPa in yet another embodiment.
  • ISO 37 Tensile Strength
  • the graft copolymer has a haze (ASTM D 1003) value of from less than 15% in one embodiment, and less than 20% in another embodiment, and less than 25% in yet another embodiment, and from 1 to 25 wt% in yet another embodiment, and from 2 to 20% in yet another embodiment, and from 5 to 20% in yet another embodiment.
  • the cross-linked copolymer composition has a Shore A hardness (ISO 868) of from less than 90, and from less than 80 in another embodiment, and from less than 70 in yet another embodiment, and a range of from 20 to 90 in yet another embodiment, and from 40 to 90 in yet another embodiment, and from 30 to 80 in yet another embodiment, and from 45 to 70 in yet another embodiment, and from 40 to 60 in yet another embodiment.
  • ISO 868 Shore A hardness
  • the cross-linked copolymer composition has an Elongation at Break (ISO 37) of from 100 to 900%, and from 400 to 900% in another embodiment, and from 500 to 800% in yet another embodiment, and from greater than 200% in yet another embodiment, and from greater than 400 % in yet another embodiment.
  • ISO 37 Elongation at Break
  • the cross-linked copolymer composition has a Tensile Strength (ISO 37) of from less than 22 MPa, and less than 20 MPa in another embodiment, and less than 18 MPa in yet another embodiment, and greater than 5 MPa in yet another embodiment, and from greater than 7 MPa in yet another embodiment, and from 3 to 20 MPa in yet another embodiment, and from 5 to 20 MPa in yet another embodiment, and from 7 to 15 MPa in yet another embodiment.
  • ISO 37 Tensile Strength
  • the cross-linked copolymer composition has a Compression Set (23 0 C, 22 hours, 25% compression, ISO 815) of from less than 35, and from 40 in another embodiment, and less than 35 in another embodiment, and less than 30 in yet another embodiment, and from 10 to 40 in yet another embodiment, and from 10 to 35 in yet another embodiment, and from 12 to 32 in yet another embodiment.
  • Compression Set 23 0 C, 22 hours, 25% compression, ISO 815) of from less than 35, and from 40 in another embodiment, and less than 35 in another embodiment, and less than 30 in yet another embodiment, and from 10 to 40 in yet another embodiment, and from 10 to 35 in yet another embodiment, and from 12 to 32 in yet another embodiment.
  • the graft copolymer or graft copolymer composition is useful as a moisture curable sealant in one embodiment.
  • the graft copolymer or graft copolymer composition (optionally including the silanol condensation catalyst) is stored in the absence of moisture until it is ready to be used. It can then be applied, preferably in a paste, gel or liquid form, to a surface or surfaces to be bonded or filled, thus allowing atmospheric moisture to cure the composition and bonding the surfaces and/or sealing the surfaces.
  • the invention is further illustrated by the following examples: EXAMPLES
  • the vinyl silane is vinyltrimethoxy silane, which includes dicumyl peroxide (DynaSylanTM 13 VTMO, Evonic Industries [formerly Degussa]).
  • DynaSylan 13 is a 91.5/8.5 (wt/wt) blend of dicumyl peroxide and vinyl trimethoxy silane. Note that the I 2 (measured according to ASTM D1238, 2.16 kg, 19O 0 C) advantageously increases (viscosity goes down) as more vinyl-silane and peroxide is added.
  • silane grafted propylene- ⁇ -olefm blends the mixer type was a Brabender 50 ml, run at a chamber temperature of 150 0 C for a mixing time of 5 min; the chamber loading was 49.5 g. After blends are dumped, they are compressed in a cold press (room temperature) to 2 mm for 2 min.
  • Cross-Linked Graft Copolymer Cross-linking experiments of silane grafted propylene- ⁇ -olefm copolymer samples A-G are illustrated as summarized in Table 2 and sample V in Table 3.
  • the W and X samples demonstrate that the silane graft propylene- ⁇ -olefm can be used as the rubber phase in a thermoplastic vulcanizate-type composition and cross-linked by exposure to moisture. With good tensile strength and low CS. Due to the ability of the silane graft propylene- ⁇ -olefm to absorb and maintain the process oil, product with low hardness (33 Sh A) was obtained using cPP-g (3) and process oil. Test methods are as described above. [0068] Transparency of the graft copolymer. Table 4 presents data indicating the transparency of the graft copolymer and compositions. This is indicated by the level of haze.
  • Haze was measured by the following method: ASTM D 1003 on 2 mm ISO plaque (injection molded). VistamaxxTM and ExactTM were obtained from ExxonMobil Chemical Company, Houston TX. Exact is an example of an ethylene -based polymer (also referred to as a "plastomer” in the art), comprising from 50 to 99 wt% ethylene derived units and from 1 to 50 wt% of a copolymer (preferably a C 3 to Cio ⁇ -olefm) and having a density of from 0.850 to 0.910 g/cm 3 .
  • a copolymer preferably a C 3 to Cio ⁇ -olefm
  • a hydrolizable silane graft propylene- ⁇ -olefm copolymer comprising: (a) a propylene- ⁇ -olefm copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ -olefm copolymer, of ethylene-derived units or a C 4 to C 10 ⁇ -olefm-derived unit, and having: (i) a density of from 0.850 to 0.920 g/cm 3 ; (ii) a MWD of from 1.5 to 20; (iii) an Hf of less than or equal to 75 J/g;
  • graft copolymer of any of the preceding numbered embodiments, wherein the graft copolymer comprises from 95.0 to 99.97 wt% (by weight of the of the graft copolymer) of propylene- ⁇ -olefm copolymer component and from 0.03 to 5 wt% (by weight of the of the graft copolymer) of the hydrolysable silane component.
  • YSiRR"2 wherein Y is selected from vinyl terminated radicals, each R" is independently selected from hydrolysable organic radicals; and R can be a R" radical, or selected from Ci to C 10 alkyl radicals (both R and R" are bound to the silicon atom). 7.
  • the graft copolymer has a MWD of from 1.8 to 5.
  • the propylene - ⁇ -olefm copolymer has a triad tacticity by 13 C NMR of 80% or greater.
  • graft copolymer of any of the preceding numbered embodiments wherein the graft copolymer is a component of a composition including from 0.01 to 5 wt%, based on total weight of final blend, of a silanol condensation catalyst.
  • the graft copolymer of embodiments 14 and 20, wherein the cross-linked copolymer composition has an Elongation at Break (ISO 37) of from 100 to 900.
  • the graft copolymer of embodiments 14 and 20-21, wherein the cross-linked copolymer composition has a Tensile Strength (ISO 37) of from less than 22 MPa.
  • a method of forming a silane graft propylene- ⁇ -olefm copolymer of any of the preceding embodiments 1-24 comprising: (a) providing the propylene- ⁇ -olef ⁇ n; and
  • Another aspect of the invention is directed to the use of a hydro lizable silane graft propylene- ⁇ -olef ⁇ n copolymer comprising a propylene- ⁇ -olefm copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ - olefin copolymer, of ethylene-derived units or a C4 to ClO ⁇ -olefm-derived unit; and a hydrolysable silane component.
  • Yet another aspect of the invention is directed to the use of a moisture curable sealant comprising a hydrolizable silane graft propylene- ⁇ -olef ⁇ n copolymer, the copolymer comprising a propylene- ⁇ -olef ⁇ n copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ -olef ⁇ n copolymer, of ethylene-derived units or a C4 to ClO ⁇ -olefm-derived unit; and a hydro lysable silane component.
  • a moisture curable sealant comprising a hydrolizable silane graft propylene- ⁇ -olef ⁇ n copolymer, the copolymer comprising a propylene- ⁇ -olef ⁇ n copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ -olef ⁇ n copolymer, of ethylene-derived units or
  • Yet another aspect of the invention is directed to the graft copolymer reaction product, in the presence of a free-radical initiator, of a propylene- ⁇ -olefm copolymer comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ - olefin copolymer, of ethylene-derived units or a C4 to ClO ⁇ -olefin-derived unit; and a hydro lysable silane.
  • Yet another aspect of the invention is directed to the graft copolymer reaction product, in the presence of a free-radical initiator, and an oil, of a propylene- ⁇ -olefm copolymer comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene- ⁇ -olef ⁇ n copolymer, of ethylene-derived units or a C4 to ClO ⁇ -olefm-derived unit; and a hydrolysable silane.
  • the graft copolymer may comprise from

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Abstract

An aspect of the description is directed to hydrolysable silane graft propylene-α-olefm copolymers useful for moisture curable sealants, the copolymers comprising a propylene-α- olefin copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α-olefm copolymer, of ethylene-derived units or a C4 to C10 α-olefm- derived unit, and having, in one embodiment, the following features: a density of from 0.850 to 0.920 g/cm3; a MWD of from 1.5 to 20; an Hf of less than or equal to 75 J/g; a Tm of from 25 to 105°C; and a triad tacticity by 13C NMR of 75% or greater; and a hydrolysable silane component. The graft copolymer can be combined with oil and/or a thermoplastic to form a graft copolymer composition capable of being cross-linked by exposure to moisture.

Description

MOISTURE CURABLE PROPYLENE- ALPHA-OLEFIN COPOLYMERS
FIELD OF THE INVENTION
[0001] The present invention relates in general to moisture-curable propylene copolymers, and more particularly to hydrolizable silane graft propylene-based polymers and thermoplastic compositions thereof. BACKGROUND
[0002] Clear, moisture curable sealants are useful in many applications. The most widely used clear moisture curable sealants are silicon moisture curable sealants. However, such moisture curable sealants are expensive. Transparent polyurethane sealants exist, but have poor weathering resistance so would not be practical for outdoor use. It would be desirable to make a lower cost moisture curable sealant that is clear and weatherable. Polyolefms offer such a promise, in particular, hydrolizable silane graft polyolefms, as these could potentially be made into compositions that are easily moisture curable and would give very good adhesion to polar substrates including glass.
[0003] Silane graft polyethylene-based compositions (having at least 50 wt% ethylene derived units) have been disclosed in EP 0 510 559 A2, WO 2005/003199, US 6,472,015, US 6,455,637, US 5,844,009, US 5,883,145, US Patent Publication 2002/0151647 and US Patent Publication 2003/0050401. One problem with using polyethylene-based polymers in forming graft polymers is that the peroxides that are used to initiate the grafting also act as a cross- linker towards polyethylene themselves. Thus, what results from contacting peroxides with polyethylene-based polymers is a highly cross-linked polymer with higher molecular weight, and thus very high viscosity, specifically in the case where a high silane level (which necessitates the use of high levels of peroxides) is required to get higher performance. Such compositions are not suitable for moisture curable sealants. Further, the cross-linked polyethylene tends to lack clarity due to its crystalline nature.
[0004] On the other hand, peroxides tend to act as chain-breaking agents towards polypropylenes. S. Yang et al, "Mechanism of a One-Step Method for Preparing Silane Grafting and Cross-linking Polypropylene" in 47 POLYMER ENGINEERING AND SCIENCE 1004 (2007) teaches the grafting of silane to polypropylene, thus forming moisture cross-linkable propylene homopolymer. However, this article teaches grafting and cross-linking in one step. To be useful as a moisture curable sealant, the graft polymer itself is preferably stable and fluid, or of low viscosity, prior to its application to a surface as a sealant. [0005] The grafting of maleic anhydride to propylene copolymers having high clarity has been disclosed in US 6,884,850 and United States Serial Number 11/810,030, where it is taught to graft a propylene-ethylene copolymer with ethylenically unsaturated carboxylic acids or acid derivatives or epoxides (e.g., maleic anhydride) by the reaction of the moiety and a peroxide with the polymer. However, such a composition is not moisture cross- linkable, hence, not suitable as a curable sealant.
[0006] What would be desirable is a clear, moisture curable sealant (being stable and having a low viscosity prior to curing) comprised mostly of polyolefinic material, thus reducing cost. The inventors have discovered a solution to this problem. SUMMARY
[0007] One aspect of the present invention is directed to hydrolysable silane graft propylene-α-olefϊn copolymers ("graft copolymer") comprising a propylene-α-olefϊn copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α-olefϊn copolymer, of ethylene-derived units or a C4 to C10 α-olefm-derived unit, and having, in one embodiment, the following features: a density of from 0.850 to 0.920 g/cm3; a MWD of from 1.5 to 20; an Hf of less than or equal to 75 J/g; a Tm of from 25 to 1050C; and a triad tacticity by 13C NMR of 75% or greater; and a hydrolysable silane component. [0008] Another aspect of the present invention is directed to a cross-linked propylene-α- olefin copolymer ("cross-linked copolymer") comprising the propylene-α-olefϊn copolymer component and the hydrolysable silane component, the copolymer and silane having been subjected to the presence of water and, in a preferred embodiment, a condensation catalyst. [0009] Yet another aspect of the present invention is directed to a composition of the graft copolymer and a polyolefm, an oil, a filler, or any combination thereof, thus forming the graft propylene-α-olefm copolymer composition ("graft copolymer composition"). A further aspect of the invention is direct to a composition of the cross-linked copolymer with a polyolefm, an oil, a filler, or any combination thereof, thus forming a crosslinked propylene- α-olefϊn copolymer composition ("cross-linked copolymer composition"). [0010] Insofar as certain numerical ranges of the features of the invention(s) are described, it is understood that any desirable upper limit of that range can be combined with any desirable lower limit of that range, as disclosed herein, to achieve a preferred range. DETAILED DESCRIPTION
[0011] As used herein, "moisture curable sealant" refers to a compound or composition that can be cross-linked as initiated by exposure to liquid or vapor water, and being capable
-7- of bonding other surfaces together by surface attachment; and includes compounds or compositions that are used to bond different surfaces (e.g., to bond them together), as well as bond to a surface or surfaces for the purpose of filling a hole or gap in such surface(s). [0012] One aspect of the invention is directed to a hydrolizable silane graft propylene-α- olefin copolymer comprising a propylene-α-olefm copolymer component comprising propylene-derived units and from 5 to 35 wt% (by weight of the propylene-α-olefm copolymer) of ethylene-derived units or a C4 to C10 α-olefin-derived unit; and a hydrolysable silane component. It is understood that the "hydrolizable silane graft propylene-α-olefm copolymer" may be claimed such that the characteristics of the propylene-α-olefm copolymer alone — prior to reacting with (grafting to) the hydrolizable silane — are described. In some embodiments, the "hydrolizable silane graft propylene-α-olefin copolymer" may be claimed as the grafting reaction product of the "propylene-α-olefm copolymer" (having certain features as described herein) and a "hydrolizable silane." [0013] The crosslinking of polymers, in particular polyolefins, by the combined process of chemical grafting of silane molecules onto the polymer to form a silane graft resin, followed by catalyzed hydrolysis and condensation of the silane, is known in the art such as is described in US 3,646,155 and US 6,455,637. The preferred polyolefins for use in forming a graft copolymer are so called "propylene-α-olefm copolymers." [0014] The "propylene-α-olefm copolymers" described herein are copolymers of propylene-derived units and one or more units derived from ethylene or a C4-C10 α-olefm and optionally one or more diene-derived units. Preferred α-olefms are ethylene, 1-butene, 1- hexene and 1-octene.
[0015] Typical comonomer content of the copolymer is from 5 to 35 wt% in one embodiment. In general, the comonomer content is adjusted so that the copolymer preferably has a MWD (Mw/Mn) of from 1.5 to 20, more preferably from 1.5 to 5, a heat of fusion (Hf) less than or equal to 75 J/g and a Tm less than or equal to 1050C. In some embodiments, where more than one comonomer is present, the amount of a particular comonomer may be less than 5 wt%, but the combined comonomer content is preferably greater than 5 wt%. [0016] In such an embodiment, when there is more than one α-olefin-derived unit in the copolymer, the total weight percent of the C2 or C4-C10 α-olefin-derived units (or "α-olefm") is preferably from 5 to 35 wt%, more preferably from 7 to 32 wt%, more preferably from 8 to 25 wt%, more preferably from 8 to 20 wt%, and more preferably from 8 to 16 wt%. Particular embodiments of copolymers having more than one α-olefm include propylene- ethylene-octene, propylene-ethylene -hexene and propylene-ethylene-butene polymers. These copolymers may further comprise a diene as described below.
[0017] The embodiments described below are discussed with reference to ethylene as a preferred comonomer, but such embodiments are equally applicable with 1-butene, 1 -hexene or 1-octene as a comonomer. The propylene-ethylene copolymer described below comprises ethylene, propylene and optionally a diene.
[0018] The propylene-ethylene copolymer can comprise from 5 to 25 wt% ethylene - derived units, preferably from 5 to 20 wt%, more preferably from 5 to 16 wt%, and more preferably from 6 to 16 wt% ethylene. In a preferred embodiment, the propylene-ethylene copolymer comprises greater than 11 wt% ethylene. The propylene-ethylene copolymer can comprise from 75 to 95 wt% propylene-derived units, more preferably from 84 to 95 wt%, more preferably from 85 to 95 wt%, and more preferably from 85 to 94 wt% by weight of the copolymer. [0019] The propylene-ethylene copolymer may optionally comprise less than or equal to 10 wt% diene derived units (or "diene"), preferably less than or equal to 5 wt% diene, more preferably less than or equal to 3 wt% diene, preferably from 0.1 to 3 or 4 or 5 or 6 wt%, more preferably from 0.1 to 2 wt%, and more preferably from 0.1 to 1 wt% diene. Suitable dienes useful as co-monomers are, for example: 1 ,4-hexadiene, 1 ,6-octadiene, 5-methyl-l,4- hexadiene, 3,7-dimethyl-l,6-octadiene, dicyclopentadiene (DCPD), ethylidiene norbornene (ENB), norbornadiene, 5 -vinyl-2 -norbornene (VNB), and combinations thereof. The diene, if present, is most preferably ENB.
[0020] The propylene-α-olefm copolymer can have a triad tacticity of three propylene units, as measured by 13C NMR, of 75% or greater, 80% or greater, 82% or greater, 85% or greater, or 90% or greater. Preferred ranges include from 50 to 99 %, more preferably from 60 to 99%, more preferably from 75 to 99% and more preferably from 80 to 99%; and in other embodiments from 60 to 97%. Triad tacticity is determined as follows: The tacticity index, expressed herein as "m/r", is determined by 13C nuclear magnetic resonance (NMR). The tacticity index m/r is calculated as defined by H. N. Cheng in 17 MACROMOLECULES 1950 (1984). The designation "m" or "r" describes the stereochemistry of pairs of contiguous propylene groups, "m" referring to meso and "r" to racemic. An m/r ratio of 1.0 generally describes a syndiotactic polymer, and an m/r ratio of 2.0 an atactic material. An isotactic material theoretically may have a ratio approaching infinity, and many by-product atactic polymers have sufficient isotactic content to result in ratios of greater than 50. Embodiments of the propylene-α-olefϊn copolymer have a tacticity index m/r ranging from a lower limit of 4 or 6 to an upper limit of 8 or 10 or 12.
[0021] In a preferred embodiment the propylene-α-olefm copolymer has an Hf, determined according to the Differential Scanning Calorimetry (DSC) procedure described herein, greater than or equal to 0.5 or 1 or 5 J/g, and is less than or equal to 80 J/g, preferably less than or equal to 70 J/g, more preferably less than or equal to 50 J/g, more preferably less than or equal to 35 J/g. Stated another way, in one or more embodiments the Hf ranges from a lower limit of 1.0, or 1.5, or 3.0, or 4.0, or 6.0, or 7.0 J/g to an upper limit of 30, or 35, or 40, or 50, or 60 or 70, or 80 J/g. [0022] In a preferred embodiment, the propylene-ethylene copolymer has a percent crystallinity of from 0.5 to 40%, preferably 1 to 30%, and more preferably 5 to 25% wherein "percent crystallinity" is determined according to the DSC procedure described herein. The thermal energy for the highest order of polypropylene is estimated at 189 J/g (i.e., 100% crystallinity is equal to 189 J/g). In another embodiment, the propylene-ethylene copolymer of the present disclosure preferably has a crystallinity of less than 40%, preferably from 0.25 to 25%, more preferably from 0.5 to 22%, and most preferably from 0.5 to 20%. [0023] The procedure for DSC determinations is as follows. About 0.5 grams of polymer is weighed out and pressed to a thickness of about 15-20 mils (about 381-508 microns) at about 140°C-150°C, using a "DSC mold" and Mylar as a backing sheet. The pressed pad is allowed to cool to ambient temperature by hanging in air (the Mylar is not removed). The pressed pad is annealed at room temperature (about 23-250C) for about 8 days. At the end of this period, an about 15-20 mg disc is removed from the pressed pad using a punch die and is placed in a 10 microliter aluminum sample pan. The sample is placed in a differential scanning calorimeter (Perkin Elmer Pyris 1 Thermal Analysis System) and is cooled to about -1000C. The sample is heated at about 10°C/min to attain a final temperature of about 165°C. The thermal output, recorded as the area under the melting peak of the sample, is a measure of the heat of fusion and can be expressed in Joules per gram (J/g) of polymer and is automatically calculated by the Perkin Elmer System. Under these conditions, the melting profile shows two (2) maxima, the maxima at the highest temperature is taken as the melting point within the range of melting of the sample relative to a baseline measurement for the increasing heat capacity of the polymer as a function of temperature.
[0024] In addition to this level of crystallinity, the propylene-ethylene copolymer preferably has a single broad melting transition. The "melting point" (Tm) is defined as the temperature of the greatest heat absorption within the range of melting of the sample. However, the propylene-ethylene copolymer may show secondary melting peaks adjacent to the principal peak, but for purposes herein, such secondary melting peaks are considered together as a single melting point, with the highest of these peaks being considered the Tm of the propylene-ethylene copolymer. The propylene-ethylene copolymer preferably has a Tm of from 25 to 1050C, preferably from 25 to 85°C, more preferably from 25 to 75°C, more preferably from 25 to 65°C, more preferably from 30 to 800C, more preferably from 30 to 700C and more preferably from 30 to 600C.
[0025] In a preferred embodiment, the propylene-α-olefm copolymer can have a density of 0.850 to 0.920 g/cm3, more preferably, 0.870 to 0.900 g/cm3, more preferably 0.880 to 0.890 g/cm3 at room temperature as measured per the ASTM D-1505 test method.
[0026] In a preferred embodiment, the propylene-α-olefm copolymer can have a melt flow rate (MFR, ASTM D1238, 2.16 kg, 23O0C), equal to or greater than 0.2 dg/min. Preferably, the MFR is from 0.5 to 5000 dg/min and more preferably from 1 to 2500 dg/min. In one embodiment, the propylene-α-olefm copolymer has an MFR of 0.5 to 1500 dg/min, from 2 to 1000 dg/min in another embodiment, and from 5 to 500 dg/min in yet another embodiment, and from 10 to 250 dg/min in yet another embodiment, and from 10 to 100 dg/min in yet another embodiment, and from 2 to 40 dg/min in yet another embodiment, and from 2 to 30 dg/min in yet another embodiment. [0027] Preferred propylene-ethylene copolymers may have a Mooney viscosity [ML (1+4) @ 125 0C] as determined according to ASTM D 1646, of less than 100, more preferably less than 75, even more preferably less than 60, most preferably less than 30. [0028] In one embodiment, the propylene-α-olefm copolymer can have a Mw of 5,000 to 5,000,000 g/mole, more preferably a Mw of 10,000 to 1,000,000, and more preferably a Mw of 50,000 to 400,000. In another embodiment, the propylene-α-olefm copolymer can have a Mn of 2,500 to 2,500,000 g/mole, more preferably a Mn of 10,000 to 250,000, and more preferably a Mn of 25,000 to 200,000. In yet another embodiment, the propylene-α-olefm copolymer can have a Mz of 10,000 to 7,000,000 g/mole, more preferably a Mz of 80,000 to 700,000, and more preferably a Mz of 100,000 to 500,000. [0029] The molecular weight distribution (MWD) of the propylene-ethylene copolymer is from 1.5 to 20 in one embodiment, and from 1.5 to 15 in another embodiment, and more preferably 1.5 to 5, more preferably 1.8 to 5 and most preferably 1.8 to 4 or 3. [0030] Techniques for determining the molecular weight (Mn, Mz and Mw) and molecular weight distribution (MWD) are as follows, and as in Verstate et al. in 21 MACROMOLECULES 3360 (1988). Molecular weight and molecular weight distribution are measured using a Waters 150 gel permeation chromatograph equipped with a Chromatix KMX-6 on-line light scattering photometer. The system is used at 135°C with 1,2,4- trichlorobenzene as the mobile phase. Showdex (Showa-Denko America, Inc.) polystyrene gel columns 802, 803, 804 and 805 are used. This technique is discussed in LIQUID CHROMATOGRAPHY OF POLYMERS AND RELATED MATERIALS III 207 (J. Cazes ed., Marcel Dekker, 1981). No corrections for column spreading are employed; however, data on generally accepted standards, e.g., National Bureau of Standards Polyethylene 1484 and anionically produced hydrogenated polyisoprenes (an alternating ethylenepropylene copolymer) demonstrate that such corrections on Mw/Mn or Mz/Mw are less than 0.05 units. Mw/Mn is calculated from an elution time-molecular weight relationship whereas Mz/Mw is evaluated using the light scattering photometer. The numerical analyses can be performed using the commercially available computer software GPC2, MOLWT2 available from LDC/Milton Roy-Riviera Beach, FIa. [0031] The propylene-α-olefm copolymers can include copolymers prepared according to the procedures in WO 02/36651, US 6992158, and/or WO 00/01745. Preferred methods for producing the propylene-α-olefm copolymers are found in US Patent Application Publication 2004/0236042 and US 6,881,800. Preferred propylene-α-olefm copolymers are available commercially under the trade names Vistamaxx™ (ExxonMobil Chemical Company, Houston, TX, USA) and Versify™ (The Dow Chemical Company, Midland, Michigan, USA), certain grades of Tafmer™ XM or Notio™ (Mitsui Company, Japan) or certain grades of Softel™ (Basell Polyolefms of the Netherlands).
[0032] To form the graft copolymer, in one embodiment the propylene-α-olefm copolymer as described above is reacted in the molten state with an organic silane having the general formula YSiRR"2, wherein Y is selected from vinyl terminated radicals, each R" is independently selected from hydrolysable organic radicals; and R can be a R" radical, or selected from Ci to Cio alkyl radicals (both R and R" are bound to the silicon atom). In a particular embodiment, Y is selected from a vinyl radical, vinyl terminated Ci to Cio alkyl radicals. The vinyl terminated radical is preferably selected from vinyl, allyl, butenyl, cyclohexenyl, cyclopentadienyl, and cyclohexadienyl radicals. Examples of the most preferred silanes are vinyltriethoxysilane and vinyltrimethoxy silane.
[0033] More particularly, the group R" represents any hydrolysable organic radical, for example an alkoxy radical such as methoxy, ethoxy and butoxy radicals; an acyloxy radical, for example the formyloxy, acetoxy or propionoxy radicals; oximo radicals such as — ON=C(CHs)2, -ON=CCH3(C2H5) and — ON=C(C6H5)2. Other end-chain unsaturated silanes commercially available such as glycidoxyalkyl-methyl-diethoxysilane or methacryloxyalkyl-trimethoxysilane can be used. Also, 3-Mercapto-alkyltrialkoxysilane can be grafted onto the backbone of the invention in a mechanism involving radical coupling reactions. [0034] In another embodiment, the hydrolysable silane graft propylene-α-olefm is formed by reacting a maleic anhydride (or other suitable anhydride) and a peroxide with the propylene-α-olefm copolymer to form a maleic anhydride graft propylene-α-olefm copolymer (as described in US 6,884,850) followed by contacting the maleic anhydride graft propylene- α-olefm copolymer with an amino-silane to form a silane graft propylene-α-olefm copolymer. The silane component in this embodiment is derived from an amino silane having the following formula: YHN(CH2)nSiRR"2, wherein N is a nitrogen atom, n is from 1 to 20 and wherein Y radical is either hydrogen or one alkyl radical, Ci to C2o alkyl radical terminated by -NH2; R" is selected from hydrolysable organic radicals (as elucidated above), and R can be an alkyl group or a R" radical, or selected from Ci to C10 alkyl radicals (both R and R" are bound to the silicon atom).
[0035] In another embodiment, a propylene-α-olefm with an epoxy functionality can be produced by grafting a molecule containing at least one unsaturation double bond and at least one epoxy functionality, such as glycidyl methacrylate (C7H10O3). A propylene-α-olefm with such an epoxy functional group will then react with an amino silane. This can then lead to the moisture curable copolymer as described herein.
[0036] In any case, the amount of silane reacted with the propylene-α-olefm depends in part upon the reaction conditions and the degree of modification desired in the propylene-α- olefm. The proportion may vary from 0.03 to 50 wt% based on the total weight of the silane graft copolymer, and from 0.03 to 10 wt% in another embodiment, and from 0.05 to 2.5 wt% in yet another embodiment, and from 0.1 to 4 wt% in yet another embodiment, and from 0.5 to 5 wt% in yet another embodiment.
[0037] A free-radical initiator is also combined with the propylene-α-olefm and silane to initiate the graft polymerization reaction. The free-radical initiator can be added at the same time as the silane, or after addition of the silane. Most preferred free-radical initiators are organic peroxides such as benzoyl peroxide, dichlorobenzoyl peroxide, dicumyl peroxide, 2,5-Dimethyl-2,5-di-(tert-butyl-peroxy)-hexyne-(3), 2,5-Dimethyl-2,5-di-(tert-butyl-peroxy)- hexane-(3), di-tertiarybutyl peroxide. The most preferred free-radical initiator for use in the compositions of the present invention is dicumyl peroxide. The criteria for choosing an appropriate free-radical initiator are known to persons skilled in the art and are described in US 3,646,155.
[0038] Preferably, the organic peroxide free-radical initiator is added in an amount of from 0.1 to 1.0 wt% of the propylene-α-olefm, more preferably from 0.05 to 0.2 wt%. [0039] The silane and free-radical initiator are reacted with the propylene-α-olefm copolymer and silane above the melting point of the copolymer and/or decomposition temperature of the free-radical initiator under conditions in which the copolymer is subjected to mechanical shearing (melt blending), using processes known to those skilled in the art. In another embodiment, melt blending takes place at from 60 to 2000C in one embodiment, and from 80 to 18O0C in another embodiment, and from 100 to 1750C in yet another embodiment, in order to accomplish grafting of the silane onto the propylene-α-olefm [0040] The final hydrolysable silane graft propylene-α-olefm copolymer possesses from 0.03 to 4 or 5 or 10 wt% of the hydrolysable silane component in one embodiment, and from 0.05 to 3 wt% in a particular embodiment, and from 0.1 to 1 wt% in yet another particular embodiment, the propylene-α-olefm copolymer component making up the remainder.
[0041] The silane graft propylene-α-olefm copolymer is subsequently melt-processed in one embodiment with an amount of one or more silanol condensation catalysts (used to facilitate the cross-linking reaction of the graft copolymer), and optionally with one or more of a number of other additives, such as pigmenting agents, fillers, flame-retardants, antioxidants, stabilizers, processing oils, unmodified thermoplastics, compatibilizers and the like, to form a "composition," as described further below.
[0042] The silanol condensation catalyst (or "catalyst") is typically selected from the group consisting of organic bases, carboxylic acids and organometallic compounds including organic titanates and complexes or carboxylates of lead, cobalt, iron, nickel, zinc and tin. Preferably, the catalyst is selected from dibutyltin dilaurate, dibutyltin diacetate, dibutyltin octanoate, dioctyltin maleate, dibutyltin oxide and titanium compounds such as titanium-2- ethylhexoxide. The most preferred silanol condensation catalyst is dibutyltin dilaurate, though any material which will catalyze the silane condensation reaction is suitable for the invention. The condensation catalyst is preferably added in an amount of from 0.01 to 5 wt%, and from 0.01 to 3 wt% in another embodiment, more preferably 0.05 to 2 wt%, and most preferably 0.1 to 1 wt% (by weight of the hydro lizable silane graft propylene-α-olefm copolymer). The condensation catalyst can be added into the propylene-α-olefm copolymer or its blend in pure form, or in a masterbatch with a polymer, or an organic or inorganic filler/carrier. [0043] Subjecting the composition thus produced to moisture, at from 20 to 250C in one embodiment, and preferably at an elevated temperature, will induce crosslinking of the silane groups via a combined hydrolysis and condensation reaction. Atmospheric moisture is usually sufficient to permit the crosslinking to occur, but the rate of crosslinking may be increased by the use of an artificially moistened atmosphere, or by immersion in liquid water. Subjecting the composition to combined heat and moisture will accelerate the crosslinking reaction. Most preferably, crosslinking is effected at a temperature above 500C and most preferably by exposing the composition to a temperature of 85°C and a relative humidity of 90% for approximately 100 hours. [0044] The propylene-α-olefm copolymer, silane, free radical initiator and silanol condensation catalyst may be combined in any number of ways and in any order. In one embodiment, the propylene-α-olefm, silane and free-radical initiator are first combined and melt blended at or above the melting point of all of the components, at from 60 to 25O0C in one embodiment, and from 80 to 18O0C in another embodiment, and from 90 to 230 0C in yet another embodiment, and from 100 to 1750C in yet another embodiment, in order to accomplish grafting of the silane onto the propylene-α-olefm and/or blending the components. Next, the silanol condensation catalyst can be combined with the graft copolymer, forming a graft copolymer composition. In another embodiment, the propylene- α-olefm, silane, free-radical initiator and silanol condensation catalyst are melt blended together in order to accomplish both the grafting of the silane onto the propylene-α-olefm and blending of the components, forming the graft copolymer composition. [0045] As mentioned above, other "additives" (oils, thermoplastics, etc.) may be combined with the graft copolymer to form compositions. In a particular embodiment, the propylene-α-olefm, silane, free-radical initiator, silanol condensation catalyst and additives are reacted by melt blending as described above to form the graft copolymer composition. In one embodiment, the graft copolymer composition can then be passed through a multi-strand die, cooled, and subsequently chopped into pellets with a strand pelletizer and dried. The material so processed can then be exposed to moisture at any time convenient for its use as, for example, a moisture curable sealant, preferably at an elevated temperature, to effect crosslinking of the material. The end result is the cross-linked propylene-α-olefm copolymer composition (or "cross-linked copolymer composition").
[0046] In yet another embodiment, the propylene-α-olefm, silane and free-radical initiator are first reacted as described above to produce the graft copolymer, which can then be isolated, pelletized, etc. This graft copolymer can then be separately melt processed by combining the silanol condensation catalyst and additives, combined as mentioned above. This graft copolymer composition can then be exposed to moisture at any time convenient for its use as, for example, a moisture curable sealant, preferably at an elevated temperature, to effect crosslinking of the material. The end result is the cross-linked copolymer composition. [0047] As mentioned above, the graft copolymer may be combined with a thermoplastic, a polyolefin or polyamide in one embodiment. "Polyolefin" can include any known polymer comprising olefm-derived units, and in particular includes propylene homopolymers, propylene random copolymers, propylene impact copolymers, propylene block copolymers, plastomers, high density polyethylenes, linear low density polyethylenes, low density polyethylenes, and combinations thereof. In a further embodiment, the hydro lizable silane graft propylene-α-olefm copolymer may be blended with a processing oil ("oil"). In yet another embodiment, the hydrolizable silane graft propylene-α-olefm copolymer is blended with a filler. In yet another embodiment, the hydrolizable silane graft propylene-α-olefin copolymer may be blended with any combination of a polyolefin, oil, and filler. [0048] In one embodiment, the hydrolizable silane graft propylene-α-olefm copolymer is blended with from 1 to 70 wt% (by weight of the composition) of an oil, and from 5 to 60 wt% in yet another embodiment, and from 10 to 40 wt% in yet another embodiment. In one embodiment, the polyolefin is a propylene homopolymer. "Oils" includes plasticizers, extender oils, synthetic processing oils, or a combination thereof can also be optionally added to the blend. The extender oils can include, but are not limited to, aromatic, naphthenic, and paraffmic extender oils. Exemplary synthetic processing oils are polylinear α-olefms, polybranched α-olefms, and hydrogenated polyalphaolefms. The compositions of this invention can include organic esters, alkyl ethers, or combinations thereof. Synthetic polyalphaolefins are also useful in lowering the glass transition temperature (Tg). Commercially available poly-α-olefms that can be useful include Elevast™ A30, and Elevast L30 (ExxonMobil Chemical, Houston). Oligomeric (e.g., Indopol™, BP, Great Britain) and polymeric processing additives can also be used.
[0049] In another embodiment, the hydrolizable silane graft propylene-α-olefm copolymer is blended with from 1 or 2 to 60 wt% (by weight of the composition) of a polyolefin, and from 10 to 50 wt% in yet another embodiment. In a preferred embodiment, the polyolefin is a propylene homopolymer or copolymer. In yet another embodiment, the polyolefin is a propylene copolymer comprising from 0.1 to 20 wt% ethylene derived units or a C4 to Cio α-olefm derived units, and from 0.1 to 5 wt% in another embodiment. In yet another embodiment, the polypropylene has an MFR (230/2.16) of from 0.1 to 2000 dg/min, and from 0.5 to 200 dg/min in yet another embodiment, and from 1 to 20 dg/min in yet another embodiment, and from 2 to 10 dg/min in yet another embodiment. [0050] In yet another embodiment, the hydrolizable silane graft propylene-α-olefin copolymer is blended with from 1 to 40 wt% of a filler, and from 2 to 30 wt% in another embodiment, and from 3 to 20 wt% in yet another embodiment. Fillers that can be included in the hydrolizable silane graft propylene-α-olefin copolymer composition include those reinforcing and non-reinforcing fillers or extenders that are conventionally employed in the compounding of polymeric materials. Useful fillers include carbon black, calcium carbonate, clays, silica, talc, and titanium dioxide. [0051] Thus, one embodiment of the present invention is a graft copolymer composition — a moisture curable sealant in a particular embodiment — comprising from 5 or 10 or 15 or 20 or 30 or 40 wt% to an upper limit of 75 or 80 or 85 or 90 or 95 wt% (by weight of the composition) of the graft copolymer; and a thermoplastic from a lower limit of 2 or 5 or 6 or 10 or 15 wt% to an upper limit of from 30 or 35 or 40 or 45 or 50 or 50 wt%, where the thermoplastic is preferably a polyolefin, and most preferably a polypropylene; and an oil from a lower limit of 5 or 10 or 15 wt% to an upper limit of from 25 or 30 or 40 or 50 or 60 wt% of the composition. In another embodiment the graft copolymer composition also includes from 0.1 or 0.5 or 0.8 or 1.0 or 1.5 wt% to an upper limit of from 3.5 or 4.0 or 4.5 or 5.0 wt% of a silanol condensation catalyst by weight of the composition. In yet another embodiment, the graft copolymer composition also includes from 1 or 5 or 10 or 15 wt% to an upper limit of from 20 or 25 or 30 or 40 or 50 or 60 wt% of one or more fϊller(s). Any one of the ranges above may also be a 0.9 or 0.5 or 0.2 fraction thereof in order to make the entire composition comprise a total of 100%. [0052] It is possible to also blend minor components into the hydrolizable silane graft propylene-α-olefm copolymer such as antioxidants, antiozonates, UV stabilizers, slip agents, and other minor additives known in the art.
[0053] The graft copolymer compositions may be produced by any number of methods as described herein. One method of forming a silane graft propylene-α-olefm copolymer comprises (a) providing a propylene-α-olefm copolymer comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α-olefin, of ethylene-derived units or a C4 to C20 α-olefm-derived unit; (b) reacting a hydrolysable vinyl silane and a free-radical initiator with the propylene-α-olefin copolymer to form a silane graft propylene-α-olefm copolymer; or (c) reacting a maleic anhydride and a free-radical initiator with the propylene- α-olefin copolymer to form a maleic anhydride graft propylene-α-olefin copolymer, followed by contacting the maleic anhydride graft propylene-α-olefm copolymer with an amino-silane or a epoxy-silane to form a silane graft propylene-α-olefm copolymer. In one embodiment, the graft copolymer is further blended with from 0.01 to 5 wt%, based on total weight of final blend, of one or more silanol condensation catalyst(s). In another embodiment, the "reacting" steps of (b) or (c) take place from any temperature at or above the melting point of the graft copolymer, or from 80 or 90 or 95 or 100 to an upper limit of from 150 or 170 or 200 or 23O0C. Preferably, the "reacting" steps occur during melt blending of the components, the melt blending taking place by any suitable means known in the art. The free-radical initiator, silane and copolymer can be combined with one another in any order. In one embodiment, the reacting steps of (b) or (c) occur during melt-blending of the components.
[0054] To form the cross-linked graft copolymer, the silane graft propylene-α-olefm copolymer is contacted with a silanol condensation catalyst and water/moisture to form a cross-linked silane graft propylene-α-olefm copolymer. In one embodiment, the "contacting" step occurs at from 20 or 25 to an upper limit of from 40 or 50 or 60 or 70 or 850C. [0055] In certain embodiments, the graft copolymer has a Shore A hardness (ISO 868) of from greater than 40, and from greater than 50 in another embodiment, and greater than 60 in another embodiment, and from 40 to 90 in yet another embodiment, and from 50 to 70 in yet another embodiment. [0056] In another embodiment, the graft copolymer has an Elongation at Break (ISO 37) of from 100 to 1100%, and from 400 to 1100% in another embodiment, and from 500 to 1000% in another embodiment, and greater than 200 in yet another embodiment, and greater than 400 in yet another embodiment, and greater than 500 in yet another embodiment. [0057] In yet another embodiment, the graft copolymer has a Tensile Strength (ISO 37) of from greater than 1 MPa, and from greater than 3 MPa in another embodiment, and from greater than 5 MPa in another embodiment, and greater than 7 MPa in another embodiment, and greater than 10 MPa in yet another embodiment, and from and from 3 to 15 MPa in yet another embodiment, and from 5 to 15 MPa in yet another embodiment, and from 7 to 13 MPa in yet another embodiment. [0058] In yet another embodiment, the graft copolymer has a haze (ASTM D 1003) value of from less than 15% in one embodiment, and less than 20% in another embodiment, and less than 25% in yet another embodiment, and from 1 to 25 wt% in yet another embodiment, and from 2 to 20% in yet another embodiment, and from 5 to 20% in yet another embodiment. [0059] In certain embodiments, the cross-linked copolymer composition has a Shore A hardness (ISO 868) of from less than 90, and from less than 80 in another embodiment, and from less than 70 in yet another embodiment, and a range of from 20 to 90 in yet another embodiment, and from 40 to 90 in yet another embodiment, and from 30 to 80 in yet another embodiment, and from 45 to 70 in yet another embodiment, and from 40 to 60 in yet another embodiment.
[0060] In another embodiment, the cross-linked copolymer composition has an Elongation at Break (ISO 37) of from 100 to 900%, and from 400 to 900% in another embodiment, and from 500 to 800% in yet another embodiment, and from greater than 200% in yet another embodiment, and from greater than 400 % in yet another embodiment.
[0061] In another embodiment, the cross-linked copolymer composition has a Tensile Strength (ISO 37) of from less than 22 MPa, and less than 20 MPa in another embodiment, and less than 18 MPa in yet another embodiment, and greater than 5 MPa in yet another embodiment, and from greater than 7 MPa in yet another embodiment, and from 3 to 20 MPa in yet another embodiment, and from 5 to 20 MPa in yet another embodiment, and from 7 to 15 MPa in yet another embodiment.
[0062] In yet another embodiment, the cross-linked copolymer composition has a Compression Set (230C, 22 hours, 25% compression, ISO 815) of from less than 35, and from 40 in another embodiment, and less than 35 in another embodiment, and less than 30 in yet another embodiment, and from 10 to 40 in yet another embodiment, and from 10 to 35 in yet another embodiment, and from 12 to 32 in yet another embodiment.
[0063] As mentioned, the graft copolymer or graft copolymer composition is useful as a moisture curable sealant in one embodiment. Typically, the graft copolymer or graft copolymer composition (optionally including the silanol condensation catalyst) is stored in the absence of moisture until it is ready to be used. It can then be applied, preferably in a paste, gel or liquid form, to a surface or surfaces to be bonded or filled, thus allowing atmospheric moisture to cure the composition and bonding the surfaces and/or sealing the surfaces. [0064] The invention is further illustrated by the following examples: EXAMPLES
[0065] Graft Copolymer. Data for silane graft propylene-α-olefin copolymer samples 1-6 are illustrated as summarized in Table 1. The first sample shows silane grafting of a propylene-α-olefm copolymer (cPP 1) having an MFR (230/2.16) of 3.0 dg/min, 16 wt% ethylene derived units. The second sample shows the silane grafting of a propylene-α-olefm (cPP 2) having MFR 4.1 dg/min, 10.3 wt% ethylene derived units and 2.1 wt% ENB derived units. The vinyl silane is vinyltrimethoxy silane, which includes dicumyl peroxide (DynaSylan™ 13 VTMO, Evonic Industries [formerly Degussa]). DynaSylan 13 is a 91.5/8.5 (wt/wt) blend of dicumyl peroxide and vinyl trimethoxy silane. Note that the I2 (measured according to ASTM D1238, 2.16 kg, 19O0C) advantageously increases (viscosity goes down) as more vinyl-silane and peroxide is added. Mixing conditions for silane grafted propylene-α-olefm blends: the mixer type was a Brabender 50 ml, run at a chamber temperature of 1500C for a mixing time of 5 min; the chamber loading was 49.5 g. After blends are dumped, they are compressed in a cold press (room temperature) to 2 mm for 2 min.
[0066] Cross-Linked Graft Copolymer. Cross-linking experiments of silane grafted propylene-α-olefm copolymer samples A-G are illustrated as summarized in Table 2 and sample V in Table 3. A masterbatch of dibutyltindilaurate (catalyst) was made using 3.465 grams of the dibutyltindilaurate in 51.535 grams Vistamaxx 6102. This catalyst masterbatch was added to a portion of the Sample 3 from the grafting sample (cPP-g (3), containing 1.43 wt% vinyl silane) and Sample 6 from the grafting sample (cPP-g(6) containing 1.33 wt % vinyl silane). This was followed by a cross-linking reaction after an aging of 24 hours in water at 230C or at 500C. These properties, compared with samples without catalysts, show a significant increase of hardness, tensile strength and decrease of compression set (CS). All compositions were mixed in a Brabender (50 ml) at 15O0C chamber temperature. The curing is done by immersing the samples in water at a given temperature and for a given time. Test methods are as follows:
• Hardness (230C), ISO 868, 15 sec. delay, 2mm/30mm (thickness/diameter disk, cold pressed plaque). Measurement was done on stack of 3 disks of 2 mm thickness and 30 mm diameter.
• Tensile Strength, (230C), ISO 37 (500 mm/min), type 2 dumbbell, 2 mm cold pressed plaque.
• Elongation at Break, (230C), ISO 37 (500 mm/min), type 2 dumbbell, 2 mm cold pressed plaque. • Modulus at 100% strain, (230C), ISO 37 (500 mm/min), type 2 dumbbell, 2 mm cold pressed plaque.
• Compression Set ("CS") (on cold pressed plaque; 25% compression; 230C and 7O0C), ISO 815, stack of 3 disks 2mm/12mm, (thickness/diameter disk). [0067] Cross-Linked Copolymer Compositions. Blends (samples W-X) of polypropylene (Borsoft™ SD233CF, MFR of 7.0 dg/min; Borealis) and process oil (Paralux™ 6001 R, ChevronTexaco Global Lubricants) with grafted propylene-α-olefm Samples 3 and 6 (cPP-g (3) and cPP-g (6)) are illustrated as summarized in Table 3. The W and X samples demonstrate that the silane graft propylene-α-olefm can be used as the rubber phase in a thermoplastic vulcanizate-type composition and cross-linked by exposure to moisture. With good tensile strength and low CS. Due to the ability of the silane graft propylene-α-olefm to absorb and maintain the process oil, product with low hardness (33 Sh A) was obtained using cPP-g (3) and process oil. Test methods are as described above. [0068] Transparency of the graft copolymer. Table 4 presents data indicating the transparency of the graft copolymer and compositions. This is indicated by the level of haze. Haze was measured by the following method: ASTM D 1003 on 2 mm ISO plaque (injection molded). Vistamaxx™ and Exact™ were obtained from ExxonMobil Chemical Company, Houston TX. Exact is an example of an ethylene -based polymer (also referred to as a "plastomer" in the art), comprising from 50 to 99 wt% ethylene derived units and from 1 to 50 wt% of a copolymer (preferably a C3 to Cio α-olefm) and having a density of from 0.850 to 0.910 g/cm3.
Figure imgf000018_0001
Table 2. Cross-linked Graft Propylene-α-olefϊn Examples
Figure imgf000019_0001
Figure imgf000020_0001
Table 4. Haze Values
Figure imgf000020_0002
1. Having described the various aspects of the invention and demonstrated certain of its features, the invention(s) can be described by the numbered embodiments, wherein in a first embodiment, a hydrolizable silane graft propylene-α-olefm copolymer is provided, comprising: (a) a propylene-α-olefm copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α-olefm copolymer, of ethylene-derived units or a C4 to C10 α-olefm-derived unit, and having: (i) a density of from 0.850 to 0.920 g/cm3; (ii) a MWD of from 1.5 to 20; (iii) an Hf of less than or equal to 75 J/g;
(iv) a Tm of from 25 to l05°C;
(v) a triad tacticity by 13C NMR of 75% or greater; and (b) a hydrolysable silane component.
2. The graft copolymer of the first embodiment, wherein the propylene-α-olefm copolymer comprises from 5 to 25 wt% ethylene-derived units.
3. The graft copolymer of the first and second embodiment, wherein the Hf is less than or equal to 60 J/g.
4. The graft copolymer of any of the preceding numbered embodiments, wherein the graft copolymer comprises from 95.0 to 99.97 wt% (by weight of the of the graft copolymer) of propylene-α-olefm copolymer component and from 0.03 to 5 wt% (by weight of the of the graft copolymer) of the hydrolysable silane component.
5. The graft copolymer of any of the preceding numbered embodiments, wherein the propylene-α-olefm copolymer also comprises from 0.1 to 6 wt% diene-derived units.
6. The graft copolymer of any of the preceding numbered embodiments, wherein the silane component is derived from a vinyl silane having the following formula:
YSiRR"2, wherein Y is selected from vinyl terminated radicals, each R" is independently selected from hydrolysable organic radicals; and R can be a R" radical, or selected from Ci to C10 alkyl radicals (both R and R" are bound to the silicon atom). 7. The graft copolymer of any of the preceding numbered embodiments, wherein the silane component is derived from an amino silane having the following formula: YHN(CH2)nSiRR"2, wherein N is a nitrogen atom, n is from 1 to 20 and wherein Y radical is either hydrogen or one alkyl radical Ci to C2o alkyl radical terminated by - NH2; R" is selected from hydrolysable organic radicals, and R can be an alkyl group or a R" radical, or selected from Ci to C10 alkyl radicals. 8. The graft copolymer of any of the preceding numbered embodiments, wherein the graft copolymer has a MWD of from 1.8 to 5. 9. The graft copolymer of any of the preceding numbered embodiments, wherein the graft copolymer has a haze value of from less than 25%.
10. The graft copolymer of any of the preceding numbered embodiments, the propylene - α-olefm copolymer has a triad tacticity by 13C NMR of 80% or greater.
11. The graft copolymer of any of the preceding numbered embodiments, wherein the graft copolymer is a component of a composition including from 0.01 to 5 wt%, based on total weight of final blend, of a silanol condensation catalyst.
12. The graft copolymer of embodiment 11, wherein the graft copolymer is cross-linked to form a cross-linked propylene-α-olefm copolymer.
13. The graft copolymer of embodiment 12, wherein the graft copolymer is a component of a composition including from 2 to 50 wt% polypropylene to form a cross-linked copolymer composition.
14. The graft copolymer of embodiment 13, wherein the graft copolymer is a component of a composition including from 5 to 60 wt% oil to form a cross-linked copolymer composition. 15. The graft copolymer of embodiment 12, wherein the cross-linked copolymer has a Shore A hardness (ISO 868) of from greater than 40.
16. The graft copolymer of embodiments 12 and 15, wherein the cross-linked copolymer has a Shore A hardness (ISO 868) of from 40 to 90.
17. The graft copolymer of embodiments 12 and 15-16, wherein the cross-linked copolymer has an Elongation at Break (ISO 37) of from 100 to 1100.
18. The graft copolymer of embodiments 12 and 15-17, wherein the cross-linked copolymer has a Tensile Strength (ISO 37) of from greater than 3 MPa.
19. The graft copolymer of embodiments 12 and 15-18, wherein the cross-linked copolymer has a Compression Set (230C, 22 hours, 25% compression, ISO 815) of from less than 50.
20. The graft copolymer of embodiment 14, wherein the cross-linked copolymer composition has a Shore A hardness (ISO 868) of from less than 90.
21. The graft copolymer of embodiments 14 and 20, wherein the cross-linked copolymer composition has an Elongation at Break (ISO 37) of from 100 to 900. 22. The graft copolymer of embodiments 14 and 20-21, wherein the cross-linked copolymer composition has a Tensile Strength (ISO 37) of from less than 22 MPa.
23. The graft copolymer of embodiments 14 and 20-22, wherein the cross-linked copolymer composition has a Compression Set (230C, 22 hours, 25% compression, ISO 815) of from less than 35.
24. A moisture curable sealant formed from the silane graft propylene-α-olefϊn copolymer any of the preceding numbered embodiments.
25. A method of forming a silane graft propylene-α-olefm copolymer of any of the preceding embodiments 1-24 comprising: (a) providing the propylene-α-olefϊn; and
(b) reacting a hydrolysable vinyl silane and a free-radical initiator with the propylene-α-olefm copolymer to form a silane graft propylene-α-olefm; or
(c) reacting a maleic anhydride and a free-radical initiator with the propylene-α- olefm copolymer to form a maleic anhydride graft propylene-α-olefm copolymer, followed by contacting the maleic anhydride graft propylene-α- olefm copolymer with an amino-silane to form a silane graft propylene-α- olefm copolymer.
26. The method of embodiment 25, wherein the reacting steps of (b) or (c) take place at from 90 to 23O0C. 27. The method of any of embodiments 25 and 26, wherein the reacting steps of (b) or (c) occur during melt-blending of the components.
28. The method of any of embodiments 25-27, wherein the silane graft propylene-α-olefm copolymer is contacted with water and a silanol condensation catalyst to form a cross- linked silane graft propylene-α-olefm copolymer. 29. The method of any of embodiment 28, wherein the contacting step occurs at from 20 to 850C.
[0069] Another aspect of the invention is directed to the use of a hydro lizable silane graft propylene-α-olefϊn copolymer comprising a propylene-α-olefm copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α- olefin copolymer, of ethylene-derived units or a C4 to ClO α-olefm-derived unit; and a hydrolysable silane component.
[0070] Yet another aspect of the invention is directed to the use of a moisture curable sealant comprising a hydrolizable silane graft propylene-α-olefϊn copolymer, the copolymer comprising a propylene-α-olefϊn copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α-olefϊn copolymer, of ethylene-derived units or a C4 to ClO α-olefm-derived unit; and a hydro lysable silane component.
[0071] Yet another aspect of the invention is directed to the graft copolymer reaction product, in the presence of a free-radical initiator, of a propylene-α-olefm copolymer comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α- olefin copolymer, of ethylene-derived units or a C4 to ClO α-olefin-derived unit; and a hydro lysable silane.
[0072] Yet another aspect of the invention is directed to the graft copolymer reaction product, in the presence of a free-radical initiator, and an oil, of a propylene-α-olefm copolymer comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α-olefϊn copolymer, of ethylene-derived units or a C4 to ClO α-olefm-derived unit; and a hydrolysable silane.
[0073] In any of the preceding embodiments, the graft copolymer may comprise from
95.0 to 99.97 wt% (by weight of the of the graft copolymer) of propylene-α-olefm copolymer component and from 0.03 to 5 wt% (by weight of the of the graft copolymer) of the hydrolysable silane component.

Claims

1. A hydro lizable silane graft propylene-α-olefϊn copolymer is provided, comprising:
(a) a propylene-α-olefm copolymer component comprising propylene-derived units and from 5 to 35 wt%, by weight of the propylene-α-olefm copolymer, of ethylene-derived units or a C4 to C10 α-olefm-derived unit, and having:
(i) a density of from 0.850 to 0.920 g/cm3;
(ii) a MWD of from 1.5 to 20;
(iii) an Hf of less than or equal to 75 J/g;
(iv) a Tm of from 25 to l05°C; (v) a triad tacticity by 13C NMR of 75% or greater; and
(b) a hydrolysable silane component.
2. The graft copolymer of claim 1, wherein the propylene-α-olefm copolymer comprises from 5 to 25 wt% ethylene-derived units.
3. The graft copolymer of any of any of the preceding claims, wherein the Hf is less than or equal to 60 J/g.
4. The graft copolymer of any of any of the preceding claims, wherein the graft copolymer comprises from 95.0 to 99.97 wt% (by weight of the of the graft copolymer) of propylene-α-olefm copolymer component and from 0.03 to 5 wt% (by weight of the of the graft copolymer) of the hydrolysable silane component.
5. The graft copolymer of any of any of the preceding claims, wherein the propylene-α- olefm copolymer also comprises from 0.1 to 6 wt% diene-derived units.
6. The graft copolymer of any of any of the preceding claims, wherein the silane component is derived from a vinyl silane having the following formula: YSiRR"2, wherein Y is selected from vinyl terminated radicals, each R" is independently selected from hydrolysable organic radicals; and R can be a R" radical, or selected from Ci to Cio alkyl radicals (both R and R" are bound to the silicon atom).
7. The graft copolymer of any of any of the preceding claims, wherein the silane component is derived from an amino silane having the following formula: YHN(CH2)nSiRR"2, wherein N is a nitrogen atom, n is from 1 to 20 and wherein Y radical is either hydrogen or one alkyl radical Ci to C20 alkyl radical terminated by - NH2; R" is selected from hydrolysable organic radicals, and R can be an alkyl group or a R" radical, or selected from Ci to C10 alkyl radicals.
8. The graft copolymer of any of any of the preceding claims, wherein the graft copolymer has a MWD of from 1.8 to 5.
9. The graft copolymer of any of any of the preceding claims, wherein the graft copolymer has a haze value of from less than 25%.
10. The graft copolymer of any of any of the preceding claims, the propylene-α-olefm copolymer has a triad tacticity by 13C NMR of 80% or greater.
11. The graft copolymer of any of any of the preceding claims, wherein the graft copolymer is a component of a composition including from 0.01 to 5 wt%, based on total weight of final blend, of a silanol condensation catalyst.
12. The graft copolymer of claim 11, wherein the graft copolymer is cross-linked to form a cross-linked propylene-α-olefm copolymer.
13. The graft copolymer of claim 12, wherein the graft copolymer is a component of a composition including from 2 to 50 wt% polypropylene to form a cross-linked copolymer composition.
14. The graft copolymer of claim 13, wherein the graft copolymer is a component of a composition including from 5 to 60 wt% oil to form a cross-linked copolymer composition.
15. The graft copolymer of claim 12, wherein the cross-linked copolymer has a Shore A hardness (ISO 868) of from greater than 40.
16. The graft copolymer of claim 12 or 15, wherein the cross-linked copolymer has a Shore A hardness (ISO 868) of from 40 to 90.
17. The graft copolymer of claims 12, 15 or 16, wherein the cross-linked copolymer has an Elongation at Break (ISO 37) of from 100 to 1100.
18. The graft copolymer of claims 12 or 15 to 17, wherein the cross-linked copolymer has a Tensile Strength (ISO 37) of from greater than 3 MPa.
19. The graft copolymer of claims 12 or 15 to 18, wherein the cross-linked copolymer has a Compression Set (23oC, 22 hours, 25% compression, ISO 815) of from less than 50.
20. The graft copolymer of claim 14, wherein the cross-linked copolymer composition has a Shore A hardness (ISO 868) of from less than 90.
21. The graft copolymer of claims 14 or 20, wherein the cross-linked copolymer composition has an Elongation at Break (ISO 37) of from 100 to 900.
22. The graft copolymer of claims 14 and 20-21, wherein the cross-linked copolymer composition has a Tensile Strength (ISO 37) of from less than 22 MPa.
23. The graft copolymer of claims 14 or 20 to 22, wherein the cross-linked copolymer composition has a Compression Set (23oC, 22 hours, 25% compression, ISO 815) of from less than 35.
24. A moisture curable sealant formed from the silane graft propylene-α-olefm copolymer any of the preceding claims.
25. A method of forming a silane graft propylene-α-olefm copolymer of any of the preceding claims comprising:
(a) providing the propylene-α-olefm; and
(b) reacting a hydrolysable vinyl silane and a free-radical initiator with the propylene-α-olefm copolymer to form a silane graft propylene-α-olefm; or
(c) reacting a maleic anhydride and a free-radical initiator with the propylene-α- olefin copolymer to form a maleic anhydride graft propylene-α-olefm copolymer, followed by contacting the maleic anhydride graft propylene-α- olefm copolymer with an amino-silane to form a silane graft propylene-α- olefm copolymer.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011083043A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Polyolefins modified by silicones
WO2011083044A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Organopolysiloxanes containing an unsaturated group
WO2011083045A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Modified polyolefins
WO2011083047A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Modified polyolefins
WO2011083050A3 (en) * 2010-01-06 2011-09-29 Dow Corning Corporation Modified diene elastomers
US8476375B2 (en) 2008-07-03 2013-07-02 Dow Corning Corporation Polymers modified by silanes
US8569417B2 (en) 2008-07-03 2013-10-29 Dow Corning Corporation Modified polyolefins
US9045578B2 (en) 2010-01-06 2015-06-02 Dow Corning Corporation Process for forming crosslinked and branched polymers
WO2020261258A1 (en) * 2019-06-27 2020-12-30 Carmel Olefins Ltd. Polyolefin based compositions modified by silanes

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7994253B2 (en) * 2008-04-15 2011-08-09 Exxonmobil Chemical Patents Inc. Translucent propylene-based elastomeric compositions
GB0812187D0 (en) * 2008-07-03 2008-08-13 Dow Corning Modified polyethylene
DE102008041279A1 (en) * 2008-08-15 2010-02-18 Evonik Degussa Gmbh Silane-modified polyolefins with a high degree of functionalization
US8975334B2 (en) * 2009-07-23 2015-03-10 Exxonmobil Chemical Patents Inc. Crosslinkable propylene-based copolymers, methods for preparing the same, and articles made therefrom
KR20110100018A (en) * 2010-03-03 2011-09-09 엘에스전선 주식회사 Insulation resin composition resistant to thermal deformation and the cable using the same
CN103221470B (en) 2010-09-30 2014-09-03 联合碳化化学及塑料技术有限责任公司 Polymeric compositions with voltage stabilizer additive
EP2635446A1 (en) * 2010-11-03 2013-09-11 Dow Corning Corporation Epoxidised elastomer compositions modified by silanes
FR2972193B1 (en) * 2011-03-04 2014-07-04 Setup Performance MODIFIED POLYOLEFINS, CROSS-LINKABLE AFTER PROCESSING, AND PROCESS FOR THE PRODUCTION OF SAID POLYOLEFINS
US10626229B2 (en) * 2013-03-29 2020-04-21 Furukawa Electric Co., Ltd. Silane-crosslinkable ethylene-propylene copolymer and crosslinked body of the same
US10040888B1 (en) * 2013-06-14 2018-08-07 Cooper-Standard Automotive Inc. Composition including silane-grafted polyolefin
US10100139B2 (en) 2013-08-01 2018-10-16 Cooper-Standard Automotive Inc. Hose, composition including silane-grafted polyolefin, and process of making a hose
EP3164633B1 (en) 2014-07-02 2020-01-29 Cooper-Standard Automotive, Inc. Hose, abrasion resistant composition, and process of making a hose
WO2017109073A1 (en) * 2015-12-22 2017-06-29 Solvay Specialty Polymers Italy S.P.A. Multilayer assembly including a composite material
JP6792646B2 (en) 2016-12-10 2020-11-25 クーパー−スタンダード・オートモーティブ・インコーポレーテッド Micro high density seals, compositions, and methods of making them
WO2018107073A1 (en) 2016-12-10 2018-06-14 Cooper-Standard Automotive Inc. Shoe soles, compositions, and methods of making the same
JP6800081B2 (en) * 2017-04-19 2020-12-16 古河電気工業株式会社 Kit for preparing silane crosslinked resin molded article and method for manufacturing silane crosslinked resin molded article
EP3409701A1 (en) 2017-05-31 2018-12-05 Borealis AG A crosslinkable propylene polymer composition

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004055083A1 (en) * 2001-12-13 2004-07-01 Exxonmobil Chemical Patents, Inc. Process for making a thermoplastic vulcanizates
WO2007008765A2 (en) * 2005-07-11 2007-01-18 Dow Global Technologies Inc. Silane-grafted olefin polymers, compositions and articles prepared therefrom, and methods for making the same
WO2007116708A1 (en) * 2006-03-31 2007-10-18 Mitsui Chemicals, Inc. Thermoplastic polymer composition, method for producing thermoplastic polymer composition, molded body obtained from thermoplastic polymer composition and electric wire

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4113063A1 (en) 1991-04-22 1992-10-29 Continental Ag Thermoplastic elastomers and process for their preparation
DE69406637T2 (en) * 1993-12-22 1998-03-19 Sumitomo Chemical Co Layered polypropylene film
US5461110A (en) * 1994-05-04 1995-10-24 Du Pont Canada Inc. Cross-linkable adhesive polymers
JP4057657B2 (en) * 1994-09-19 2008-03-05 センチネル・プロダクツ・コープ Crosslinked foam structure of linear polyolefin and method for producing the same
CA2203595A1 (en) * 1996-04-26 1997-10-26 Robert F. Hurley Cross-linked polyolefin tape
US5844009A (en) * 1996-04-26 1998-12-01 Sentinel Products Corp. Cross-linked low-density polymer foam
KR20000057214A (en) * 1996-11-25 2000-09-15 진 엠.보스 Polymer blends with controlled morphologies
JPH10265588A (en) * 1997-01-24 1998-10-06 Mitsui Chem Inc Shrinkable film made of olefinic copolymer
US6211300B1 (en) * 1998-04-10 2001-04-03 Chisso Corporation Propylene-ethylene block copolymer compositions and processes for production thereof
EP1021486B1 (en) * 1998-06-22 2004-09-22 General Electric Company Silane vulcanized thermoplastic elastomers
US6143818A (en) * 1999-08-04 2000-11-07 Ato Findley, Inc. Hot melt adhesive based on ethylene-propylene rubber (EPR) and semicrystalline olefinic polymers
CA2290318C (en) * 1999-11-24 2009-02-03 Shaw Industries Limited Crosslinked compositions containing silane-grafted polyolefins and polypropylene
DE60142573D1 (en) * 2000-10-30 2010-08-26 Exxon Mobil Chem Patents Inc EN-ETHYLENE COPOLYMERS
US7282541B2 (en) * 2000-10-30 2007-10-16 Exxonmobil Chemical Patents Inc. Functionalized polypropylene-based polymers
US6794453B2 (en) * 2000-11-06 2004-09-21 Shawcor Ltd. Crosslinked, predominantly polypropylene-based compositions
GB0227003D0 (en) * 2002-11-19 2002-12-24 Solvay Crosslinking retarders for crosslinkable polyolefins
BRPI0411775A (en) 2003-06-25 2006-08-08 Union Carbide Chem Plastic moisture crosslinkable polymeric composition, wire or cable construction using the same and method for its preparation
CN101248133B (en) * 2005-06-24 2012-11-21 埃克森美孚化学专利公司 Functionalized propylene copolymer adhesive composition
WO2007084219A1 (en) * 2006-01-17 2007-07-26 Exxonmobil Chemical Patents Inc. Process for making dynamically-loaded articles comprising propylene-based elastomers, composition for use in such processes, and article made using such processes

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004055083A1 (en) * 2001-12-13 2004-07-01 Exxonmobil Chemical Patents, Inc. Process for making a thermoplastic vulcanizates
WO2007008765A2 (en) * 2005-07-11 2007-01-18 Dow Global Technologies Inc. Silane-grafted olefin polymers, compositions and articles prepared therefrom, and methods for making the same
WO2007116708A1 (en) * 2006-03-31 2007-10-18 Mitsui Chemicals, Inc. Thermoplastic polymer composition, method for producing thermoplastic polymer composition, molded body obtained from thermoplastic polymer composition and electric wire
EP2006327A1 (en) * 2006-03-31 2008-12-24 Mitsui Chemicals, Inc. Thermoplastic polymer composition, method for producing thermoplastic polymer composition, molded body obtained from thermoplastic polymer composition and electric wire

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8476375B2 (en) 2008-07-03 2013-07-02 Dow Corning Corporation Polymers modified by silanes
US8569417B2 (en) 2008-07-03 2013-10-29 Dow Corning Corporation Modified polyolefins
WO2011083043A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Polyolefins modified by silicones
WO2011083044A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Organopolysiloxanes containing an unsaturated group
WO2011083045A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Modified polyolefins
WO2011083047A1 (en) 2010-01-06 2011-07-14 Dow Corning Corporation Modified polyolefins
WO2011083050A3 (en) * 2010-01-06 2011-09-29 Dow Corning Corporation Modified diene elastomers
US9045578B2 (en) 2010-01-06 2015-06-02 Dow Corning Corporation Process for forming crosslinked and branched polymers
US9181379B2 (en) 2010-01-06 2015-11-10 Dow Corning Corporation Modified polyolefins
US9493615B2 (en) 2010-01-06 2016-11-15 Dow Corning Corporation Organopolysiloxanes containing an unsaturated group
WO2020261258A1 (en) * 2019-06-27 2020-12-30 Carmel Olefins Ltd. Polyolefin based compositions modified by silanes
US11649344B2 (en) 2019-06-27 2023-05-16 Carmel Olefins Ltd. Polyolefin based compositions modified by silanes

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