Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
  • C08J5/18—Manufacture of films or sheets
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
  • C08F210/02—Ethene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F232/00—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system
  • C08F232/02—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system having no condensed rings
  • C08F232/04—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system having no condensed rings having one carbon-to-carbon double bond
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F232/00—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system
  • C08F232/02—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system having no condensed rings
  • C08F232/06—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system having no condensed rings having two or more carbon-to-carbon double bonds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F232/00—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system
  • C08F232/08—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system having condensed rings
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F2420/00—Metallocene catalysts
  • C08F2420/10—Heteroatom-substituted bridge, i.e. Cp or analog where the bridge linking the two Cps or analogs is substituted by at least one group that contains a heteroatom
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F4/00—Polymerisation catalysts
  • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
  • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
  • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
  • C08F4/62—Refractory metals or compounds thereof
  • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
  • C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
  • C08F4/65908—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised 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
  • C08J2323/04—Homopolymers or copolymers of ethene
  • C08J2323/08—Copolymers of ethene

Definitions

• TITLE BLENDS OF CYCLIC OLEFIN COPOLYMERS AND FILMS PREPARED
• the present disclosure provides blends of ethylene polymer(s) and two or more copolymers comprising a cyclic olefin content and films comprising the blends.
• PE Polyethylene
• compositions containing polyethylene are useful in many applications, such as in films.
• the blown film technique is a useful way to manufacture PE films.
• One use of such films is in making bags, where the films can be formed as continuous cylinders then crimped to close one end.
• the process to blow polyethylenes into such films involves a balance between processability (e.g., flowability and melt strength) of the polymer on the one hand and mechanical properties (e.g., tensile strength, modulus) of the polymer on the other. Improvements in both the polymer materials used to make such films, and the process itself, can synergistically make more blown films commercially attractive.
• LLDPE linear, low density polyethylenes
• LLDPE resins are synthesized by copolymerizing ethylene with an alpha-olefin (olefin) comonomer such as 1 -butene, 1 -hexene or 1-octene.
• olefin alpha-olefin
• This copolymerization results in an ethylene-based copolymer with many short chain branches (SCB) along the polymer backbone.
• SCB short chain branches
• the incorporation of 1 -butene, 1 -hexene or 1-octene comonomers results in ethyl (2 carbons), butyl (4 carbons), or hexyl (6 carbons) branches, respectively, along the polymer backbone. Chain length of the short chain branches has effects on the end use properties and processability.
• Short chain branches (SCB), of less than approximately 40 carbon atoms, interfere with the formation of crystal structures. Short branches mainly influence the mechanical, thermal and optical properties. It has been observed that differences in comonomer type have effects on the blown film properties. In general, film performance properties such as impact strength (toughness) and tear strength increase with an increase in the comonomer length. Blown film performance is also influenced by the comonomer composition distribution (CCD) (also often referred to as the short chain branch distribution (SCBD)) across the molecular weight distribution (MWD). LLDPE's have a high impact resistance but are difficult to process, thus LLDPE can benefit from the addition of longer- chain comonomers.
• CCD comonomer composition distribution
• MWD molecular weight distribution
• COC cyclic olefin copolymers
• these cyclic olefin copolymers usually require high comonomer content (e.g., 35 wt% or greater) included in the copolymer, thus becoming a limiting factor for manufacturing, and compromising cost effectiveness and high throughput productivity.
• high comonomer content e.g. 35 wt% or greater
• conventional COCs have poor optical properties.
• references of interest include: US 6,559,253; US 6,528,670; Hong, M. et al. (2012) “Synthesis of Novel Cyclic Olefin Copolymer (COC) with High Performance via Effective Copolymerization of Ethylene with Bulky Cyclic Olefin,” Macromolecules, v.45(13), pp. 5397-5402; U.S. 5,942,587; JP 2016/190449; JP 2016/049775; CN 104527189; JP 2014/031218; US 8,945,702; US 8,329,276; JP 2005/199514; US 7,052,750; JP 6271724; JP 5051501; Walcher, T.
• blends comprising:
• first COC semi crystalline cyclic olefin copolymer
• first COC semi crystalline cyclic olefin copolymer
• C2-C40 linear and/or branched olefin monomer(s) such as linear or branched alpha olefin monomers
• density of about 0.92 g/cm 3 to about 0.94 g/cm 3
• modulus less than 20-80 kpsi, an elongation at break of 150-500%, and glass transition temperatures less than 38 °C
• second COC an amorphous cyclic olefin copolymer
• second COC amorphous cyclic olefin copolymer
• C2-C40 linear and/or branched olefin monomer(s) such as linear and/or branched alpha olefin monomers
• density greater than 0.97 g/cm 3
• modulus 260-380 kpsi
• glass transition temperature 54 to 138°C (130-280 °F)
• a semicrystalline olefin copolymer comprising C2-C40 monomer(s) having a density of about 0.90 g/cm 3 to about 0.96 g/cm 3 , a modulus less than 150 kpsi, an elongation at break of greater than 400%, and a glass transition temperatures less than -32 °C (-90 °F).
• the blend has a melt index of up to 2 g/10 min.
• This invention also relates to use of said blends in film applications, and the properties of those films.
• FIG. 1A is a graph illustrating extensional viscosity plot of pull-off force (melt strength) as a function of draw ratio of copolymers, according to one embodiment.
• FIG. IB is a graph illustrating extensional viscosity plot of pull-off force (melt strength) as a function of draw ratio of a comparative Exceed 1018, according to one embodiment.
• FIG. 2A is a graph illustrating elongational viscosity of films having a cyclic olefin copolymer, according to one embodiment.
• FIG. 2B is a graph illustrating elongational viscosity of a comparative ExceedTM 1018 polyethylene, according to one embodiment.
• FIG. 3A is a graph illustrating heat seal performance of films prepared with cyclic olefin copolymers and comparative copolymers, according to one embodiment.
• FIG. 3B is a graph illustrating heat seal performance of films prepared with cyclic olefin copolymers and comparative copolymers, according to one embodiment.
• FIG. 4A is a graph illustrating hot tack performance of films prepared with cyclic olefin copolymers and comparative copolymers, according to one embodiment.
• FIG. 4B is a graph illustrating hot tack performance of films prepared with cyclic olefin copolymers and comparative copolymers, according to one embodiment.
• FIG. 5 is a graph illustrating the 1% secant modulus of films prepared from a blend of EnableTM2010HA and TOP AS® 8007 at 50:50 ratio to which was added from 1 wt% up to 50 wt% of LCOC resin (Example 2, Table 2).
• FIG. 6A is a graph illustrating the puncture energy break of films from a blend of EnableTM2010HA and TOP AS® 8007 at 50:50 ratio to which was added from 1 wt% up to 50 wt% of LCOC resin (Example 2, Table 2).
• FIG. 6B is a graph illustrating the puncture peak force of films prepared from a blend of EnableTM2010HA and TOP AS® 8007 at 50:50 ratio to which was added from 1 wt% up to 50 wt% of LCOC resin (Example 2, Table 2).
• FIG. 7 is a graph illustrating the oxygen transmission rate (OTR) of films prepared from a blend of EnableTM2010HA and TOP AS® 8007 at 50:50 ratio to which was added from 1 wt% up to 50 wt% of LCOC resin (Example 2, Table 2).
• FIG. 8 is a graph illustrating the water vapor transmission rate of films prepared from a blend of EnableTM2010HA and TOP AS® 8007 at 50:50 ratio to which was added from 1 wt% up to 50 wt% of LCOC resin (Example 2, Table 2).
• FIG. 9 is a graph illustrating 30mhi AFM scans of the blends prepared from a blend of EnableTM2010HA and TOP AS® 8007 at 50:50 ratio to which was added from 1 wt% up to 50 wt% of LCOC resin (Example 2, Table 2).
• the present disclosure provides blends comprising 1) a semicrystalline cyclic olefin copolymer (first COC) comprising less than 15 wt% of C5-C40 cyclic olefin comonomer(s) and greater than 85 wt% of C2-C40 monomer(s) content, 2) an amorphous cyclic olefin copolymer (second COC) comprising more than 25 wt% of a C5-C40 cyclic olefin comonomer and less than 75 wt% of C2-C40 monomer(s), and 3) a semicrystalline olefin copolymer comprising C2-C40 monomer(s) and formed parts, such as films, comprising the blends, preferably where the wt% cyclic olefin comonomer in the semicrystalline cyclic olefin copolymer and the amorphous cyclic olefin copolymer differ by at
• Films of the present disclosure have advantageous mechanical properties (such as melt strength), barrier properties (oxygen and water vapor transmission rate) and optical properties (such as haze).
• Cyclic olefin copolymers such as ethylene- norbomene copolymers, methods for making cyclic olefin copolymers and films therefrom.
• Cyclic olefin copolymers can be synthesized using group 4 based catalyst(s), such as hafnium- based catalysts, and can include the product of one or more monomers, such as linear alpha- olefin monomers (e.g., ethylene), a cyclic olefin content of more than 25 wt% (for the amorphous cyclic olefin copolymer) and from about 0.5 wt% to 15 wt% (for the semicrystalline cyclic olefin copolymer), based on the weight of the copolymer.
• group 4 based catalyst(s) such as hafnium- based catalysts
• the semicrystalline cyclic olefin copolymer (first COC) of the present disclosure can have one or more of: a melt index (ASTM 1238) (MI) from about 0.2 g/lOmin to about 5 g/lOmin; a high load melt index (HLMI) from about 1 g/lOmin to about 130 g/lOmin; a density of about 0.92 g/cm 3 to about 0.94 g/cm 3 ; a melt strength of about 1 cN or greater; an elongation stress Sigma Z of 0 MPa to 0.6 MPa; an ethylene content of about 80 wt% to about 99.5 wt%; a crystallization temperature“Tc” of about 75°C to about 115°C, a melting temperature“Tm” of about 90°C to about 125°C, a melt index ratio (MIR) value greater than 25, a modulus less than 20-80 kpsi, an elongation at break of 150-500%
• MI
• films made from the blends described herein demonstrate excellent physical properties such as excellent stiffness, barrier and tensile properties.
• a film (e.g., compression molded film) of the present disclosure can have one or more of: a melt index from about 0.05 g/lOmin to about 2 g/lOmin; a melt index ratio (MIR) of about 25 to 70; a cyclic olefin content of from about 0.5 wt% to about 15 wt%; a 1% Secant Modulus of 60,000 psi to about 130,000 psi; a Tensile Strength of about 3,500 psi to about 5,000 psi, an Elongation at Break (Ultimate Elongation) of about 80% to 320%, a Normalized Peak Puncture Force of 5,000 g/mm to 10,000 g/mm, a Puncture Break Energy of 7,000 mm-g/mm to 17,000 mm- g/mm, an average Water Vapor Transmission rate
• a“group 4 metal” is an element from group 4 of the periodic table, e.g., Hf, Ti, or Zr.
• wt% is weight percent
• mol% is mole percent
• vol% is volume percent
• Me is methyl
• Ph is phenyl
• Et is ethyl
• Pr is propyl
• iPr is isopropyl
• n-Pr is normal propyl
• Bu is butyl
• tBu is tertiary butyl
• Ph is phenyl
• Bn is benzyl (i.e., CFhPh)
• MWD molecular weight distribution
• PDI polydispersity index
• MAO is methylalumoxane
• THF also referred to as thf
• RT is room temperature (and is 23°C unless otherwise indicated)
• SLPM is standard liter per minute
• tol is toluene
• NB is norbomene
• MD is machine direction
• TD transversal direction
• an“olefin,” alternatively referred to as“alkene,” is a linear, branched, or cyclic compound of carbon and hydrogen having at least one double bond.
• an“olefin” is a linear, branched, or cyclic compound of carbon and hydrogen having at least one double bond.
• the olefin present in such polymer or copolymer is the polymerized form of the olefin.
• a copolymer when a copolymer is said to have an“ethylene” content of 35 wt% to 55 wt%, it is understood that the monomer (“mer”) unit in the copolymer is derived from ethylene in the polymerization reaction and said derived units are present at 35 wt% to 55 wt%, based upon the weight of the copolymer.
• A“polymer” has two or more of the same or different monomer (“mer”) units.
• a “homopolymer” is a polymer having mer units that are the same.
• A“copolymer” is a polymer having two or more mer units that are different from each other.
• A“terpolymer” is a polymer having three mer units that are different from each other. “Different” as used to refer to mer units indicates that the mer units differ from each other by at least one atom or are different isomerically. Accordingly, the definition of copolymer, as used herein, includes terpolymers.
• An ethylene polymer is a polymer comprising at least 50 mol% ethylene and less than 0.5 mol% cyclic olefin, preferably 0 wt% cyclic olefin.
• An ethylene copolymer is a polymer comprising at least 50 mol% ethylene, at least 0.1 mol% of a C3 to C40 linear or branched olefin, and less than 0.5 mol% cyclic olefin, preferably 0 wt% cyclic olefin.
• Linear polymer means that the polymer has few, if any, long chain branches and has a branching index (g' v is) value of about 0.979 or greater, such as about 0.98 or greater.
• the branching index is determined by using a high temperature gel permeation chromatography equipped with three in-line detectors: a differential refractive index detector (DRI), a light scattering (LS) detector, and a viscometer (GPC-3D), as described below.
• DRI differential refractive index detector
• LS light scattering
• GPS-3D viscometer
• “low comonomer content” is defined as a polyolefin having less than 8 wt% of comonomer based upon the total weight of the polyolefin, except for cyclic olefin copolymers, where 25 wt% or less cyclic olefin is defined to be "low”.
• “high comonomer content” is defined as a polyolefin having greater than or equal to 8 wt% of comonomer based upon the total weight of the polyolefin, except for cyclic olefin copolymers, where more than 25 wt% is defined to be "high”.
• ethylene shall be considered an a-olefin.
• a“catalyst” includes a single catalyst, or multiple catalysts with each catalyst being conformational isomers or configurational isomers.
• Conformational isomers include, for example, conformers and rotamers.
• Configurational isomers include, for example, stereoisomers.
• a“catalyst system” includes at least one catalyst compound and an activator and an optional co-activator.
• a catalyst when a catalyst is described as including neutral stable forms of its components, it is well understood by one of ordinary skill in the art, that the ionic form of the component is the form that reacts with the monomers to produce polymers.
• catalysts of the present disclosure represented by a formula are intended to embrace ionic forms thereof of the compounds in addition to the neutral stable forms of the compounds.
• activators of the present disclosure are intended to embrace ionic and or reaction product forms thereof of the activator in addition to ionic or neutral form.
• complex may also be referred to as catalyst precursor, precatalyst, catalyst, catalyst compound, transition metal compound, or transition metal complex. These words are used interchangeably. Activator and cocatalyst are also used interchangeably.
• substituted generally means that a hydrogen of the substituted species has been replaced with a different atom or group of atoms.
• methyl-cyclopentadiene is cyclopentadiene that has been substituted with a methyl group.
• picric acid can be described as phenol that has been substituted with three nitro groups, or, alternatively, as benzene that has been substituted with one hydroxy and three nitro groups.
• An“anionic ligand” is a negatively charged ligand that donates one or more pairs of electrons to a metal ion.
• A“neutral donor ligand” is a neutrally charged ligand which donates one or more pairs of electrons to a metal ion.
• a scavenger is a compound that can be added to a reactor to facilitate polymerization by scavenging impurities. Some scavengers may also act as chain transfer agents. Some scavengers may also act as activators and may be referred to as co-activators. A co-activator, that is not a scavenger, may also be used in conjunction with an activator in order to form an active catalyst. In at least one embodiment, a co-activator is pre-mixed with the transition metal compound to form an alkylated transition metal compound.
• scavengers may include, but are not limited to, trialkylaluminums, methylalumoxanes, modified methylalumoxanes, MMAO-3A (Akzo Nobel), bis(diisobutylaluminum)oxide (Akzo Nobel), tri(n-octyl)aluminum, triisobutylaluminum, and diisobutylaluminum hydride.
• alkoxy or“alkoxide” means an alkyl ether radical wherein the term alkyl is as defined herein.
• suitable alkyl ether radicals include methoxy, ethoxy, n- propoxy, iso-propoxy, n-butoxy, iso-butoxy, sec-butoxy, and tert-butoxy.
• alkoxides include those where the alkyl group is a Ci to Cio hydrocarbyl.
• the alkyl group may be straight chain, branched, or cyclic.
• the alkyl group may be saturated or unsaturated. In at least one embodiment, the alkyl group may include at least one aromatic group.
• aryrloxy or“ayrloxide” means an aryl ether radical wherein the term aryl is as defined herein.
• suitable aryl ether radicals include phenoxy.
• hydrocarbyl radical refers to Ci-Cioo radicals, that may be linear, branched, or cyclic, and when cyclic, aromatic or non-aromatic.
• radicals include methyl, ethyl, n- propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, pentyl, iso-amyl, hexyl, octyl, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cyclooctyl, and their substituted analogues.
• Substituted hydrocarbyl radicals are radicals in which at least one hydrogen atom of the hydrocarbyl radical has been substituted with at least one halogen (such as Br, Cl, F or I) or at least one functional group such as C(0)R*, C(0)NR*2, C(0)OR*, NR*2, OR*, SeR*, TeR*, PR*2, ASR*2, SbR*2, SR*, BR*2, SiR*3, GeR*3, SnR*3, and PbR*3 (where R* is independently a hydrogen or hydrocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure), or where at least one heteroatom has been inserted within a hydrocarbyl ring.
• at least one hydrogen atom of the hydrocarbyl radical has been substituted with at least one halogen (such as Br, Cl, F or I) or at least one functional group such as C(0)R
• alkenyl means a straight-chain, branched-chain, or cyclic hydrocarbon radical having one or more double bonds.
• suitable alkenyl radicals include ethenyl, propenyl, allyl, 1,4-butadienyl cyclopropenyl, cyclobutenyl, cyclopentenyl, cyclohexenyl, cyclooctenyl.
• alkyl means a straight-chain, branched-chain, or cyclic hydrocarbon radical having no double bonds.
• suitable alkenyl radicals include methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, nonyl, decyl, undecyl, dodecyl, or isomers thereof, such as iso-, tert-, n-, sec-.
• aryl or“aryl group” includes a C4-C20 aromatic ring, such as a six carbon aromatic ring, and the substituted variants thereof, including phenyl, 2-methyl-phenyl, xylyl, 4-bromo-xylyl.
• heteroaryl means an aryl group where a ring carbon atom (or two or three ring carbon atoms) has been replaced with a heteroatom, such as N, O, or S.
• aromatic also refers to pseudoaromatic heterocycles which are heterocyclic substituents that have similar properties and structures (nearly planar) to aromatic heterocyclic ligands, but are not by definition aromatic; likewise the term aromatic also refers to substituted aromatics.
• isomers of a named alkyl, alkenyl, alkoxide, or aryl group exist (e.g., n-butyl, iso-butyl, iso-butyl, and tert-butyl) reference to one member of the group (e.g., n-butyl) shall expressly disclose the remaining isomers (e.g., iso-butyl, sec-butyl, and tert-butyl) in the family.
• alkyl, alkenyl, alkoxide, or aryl group without specifying a particular isomer (e.g., butyl) expressly discloses all isomers (e.g., n-butyl, iso-butyl, sec-butyl, and tert-butyl).
• ring atom means an atom that is part of a cyclic ring structure.
• a benzyl group has six ring atoms and tetrahydrofuran has 5 ring atoms.
• a heterocyclic ring is a ring having a heteroatom in the ring structure as opposed to a heteroatom-substituted ring where a hydrogen on a ring atom is replaced with a heteroatom.
• tetrahydrofuran is a heterocyclic ring and 4-AA-di methyl amino-phenyl is a heteroatom-substituted ring.
• aromatic also refers to pseudoaromatic heterocycles which are heterocyclic substituents that have similar properties and structures (nearly planar) to aromatic heterocyclic ligands, but are not by definition aromatic; likewise, the term aromatic also refers to substituted aromatics.
• A“composition” of the present disclosure can include components (e.g., oil, polymer, etc.) and or reaction product(s) of two or more of the components.
• mixing refers to combining solid polyolefin such as cyclic olefin copolymer(s) and another reagent (e.g., additives, organic reagent, inorganic reagent, solvent, etc.), which may be solid.
• ahomogenizer is used for such mixing.
• homogenizers are mechanical devices that combine two or more distinct materials, such as one or all in solid form, by physical methods such as mixing, spinning, agitation, vibration, or some combination thereof.
• Suitable homogenizers can be generally divided between horizontal conveyors, in which a screw or screw-like mechanism conveys polymer granules and or pellets and additive mixtures down the length of the homogenizer, and vertical or horizontal blenders which homogenizes polymer granules and or pellets and additive mixtures by agitation or some other non-conveying means.
• the homogenizer maintains the materials being mixed in solid and or liquid form and does not create a molten material such as by heating a polymer to its melting point temperature.
• “melt strength” refers to the resistance of a polymer melt to stretching.
• melt strength refers to the force required to draw a molten polymer extrudate at an extrusion temperature of 190°C until breakage of the extrudate whereby the force is applied by take up rollers.
• Melt index is determined herein using an extensional rheometer at 190°C, and the test is conducted by placing a 2 Kg weight at the top of a plunger for a simple capillary die.
• MI Melt Index
• MIR Melt Index Ratio
• Hot Tack Initiation Temperature is the temperature at which seal strength is 1 N/25.4 mm.
• a Hot Tack test measures the temperature at which the film sticks to itself while the seal is still hot.
• Heat Seal Strength is the temperature as which the cooled seal undergoes a break type of failure.
• the term“elongation stress Sigma Z” refers to a force per unit cross sectional area of the strand, which is taken from a Rheotens analysis, i.e., a viscosity measurement. The force is measured and the width of the strand is measured.
• continuous means a system that operates without interruption or cessation.
• a continuous process to produce a polymer would be one where the reactants are continually introduced into one or more reactors and polymer product is continually withdrawn during a polymerization process.
• a solution polymerization means a polymerization process in which the polymer is dissolved in a liquid polymerization medium, such as an inert solvent or monomer(s) or their blends.
• a solution polymerization can be homogeneous.
• a homogeneous polymerization is one where the polymer product is dissolved in the polymerization medium.
• a bulk polymerization means a polymerization process in which the monomers and or comonomers being polymerized are used as a solvent or diluent with little or no inert hydrocarbons as a solvent or diluent.
• a small fraction of inert solvent might be used as a carrier for catalyst and scavenger.
• a bulk polymerization system contains less than about 25 wt% of inert solvent or diluent, such as less than about 10 wt%, such as less than about 1 wt%, such as about 0 wt%.
• Conversion is the amount of monomer that is converted to polymer product, and is calculated based on the polymer yield and the amount of monomer fed into the reactor.
• Amorphous materials have molecules randomly arranged, which is typically reflected in a Tg over 40°C, such as over 50°C.
• Crystalline materials are considered to have molecules orderly arranged.
• Semicrystalline materials are considered to have molecules arranged both with packing order (crystalline) and without packing uniformity (amorphous), which is typically reflected in a Tg under 40°C, such as under 0°C.
• the cyclic olefin copolymers of the present disclosure can be formed by contacting ethylene and one or more Cri to C40 (such as C7 to C40) cyclic olefins with a catalyst system including an activator and at least one or more catalyst compound(s).
• Suitable catalysts are those capable of polymerizing a C2 to C20 olefin and incorporating cyclic olefins to form the ethylene copolymers.
• Suitable catalysts may include metallocene, post metallocene or other single site catalyst, and Ziegler-Natta catalysts.
• post-metallocene catalyst also known as“non-metallocene catalyst” describes transition metal complexes that do not feature any pi-coordinated cyclopentadienyl anion donors.
• Post-metallocene catalyst can be used for the polymerization of olefins when combined with common activators. See Baier, M. C.; Zuideveld, M. A.; Mecking, S. Angew. Chem. Int. Ed. 2014, 53, 2-25; Gibson, V. C., Spitzmesser, S. K. Chem. Rev. 2003, 103, 283-315; Britovsek, G. J. P., Gibson, V. C., Wass, D. F. Angew.
• a catalyst compound of the present disclosure can be a bridged biscyclopentadienyl transition metal compound comprising:
• a transition metal bound to both cyclopentadienyl ligands iii) a transition metal bound to both cyclopentadienyl ligands; and iv) a bridge group connecting the two cyclopentadienyl ligands, said bridge having one or more carbon or silicon atoms.
• Suitable catalysts can be, but are not limited to, those described in U.S. Patent No. 6,528,670 Bl.
• the bridged metallocene compounds can be bridged biscyclopentadienyl hafnium or zirconium compounds.
• bridged biscyclopentadienyl hafnium or zirconium compounds of the present disclosure include those compounds having one substituted or unsubstituted carbon or substituted silicon atom bridging two cyclopentadienyl (Cp) ligands of the metal centers, the aromatic fused-ring substituted cyclopentadienyl ligand or ligands optionally containing substituents on the non-cyclopentadienyl aromatic rings selected from C1-C20 hydrocarbyl or hydrocarbylsilyl substituents.
• Substituents typically include one or more
• Ci to C30 hydrocarbon or hydrocarbylsilyl groups that can be linear, branched, cyclic, aliphatic, aromatic or combined groups, whether in a fused-ring or pendant configuration. Examples include methyl, isopropyl, n-propyl, n-butyl, isobutyl, tertiary butyl, neopentyl, phenyl, and benzyl.
• “Hydrocarbylsilyl” is exemplified by, but not limited to, CH2-SiR*3, (where R* is Ci to C10 alkyl, such as methyl), trimethylsilyl and triethylsilyl.
• heteroatom containing cyclopentadienyl rings or fused ring where a non-carbon Group 14 or 15 atom replaces one of the ring carbons in the Cp ring or in a fused ring, is considered for this specification to be within the terms“cyclopentadienyl”,“indenyl”, and“fluorenyl”
• bridged biscyclopentadienyl compounds can be represented by the formula:
• M is zirconium or hafnium, such as hafnium
• each of Cp 1 and Cp 2 is independently a substituted or unsubstituted cyclopentadienyl-containing group
• T is a Group 14 element containing bridging group, such as comprising one or more carbon or silicon atoms;
• each of Y 1 and Y 2 is independently an anionic leaving group
• each of Q 1 and Q 2 is independently a substituted or unsubstituted hydrocarbyl group; and each of Ar 1 and Ar 2 is independently a substituted or unsubstituted aryl group.
• Ar 1 and Ar 2 may be independently:
• each of R 30 , R 31 , R 32 , R 33 , and R 34 may be independently hydrogen, linear or branched C1-C40 hydrocarbyl, linear or branched substituted C1-C40 hydrocarbyl, silylcarbyl, substituted silylcarbyl, C6-C10 aryl, substituted C6-C10 aryl, -NR'2, -SR', -OR', -OSiR'3, -PR'2, where each R' is hydrogen, halogen, C1-C 10 alkyl, or phenyl.
• Q 1 and Q 2 may be independently hydrogen, linear or branched C1-C40 hydrocarbyl, linear or branched substituted C1-C40 hydrocarbyl, silylcarbyl, substituted silylcarbyl, C6-C10 aryl, substituted C6-C 10 aryl, -NR’2, -SR’, -OR’, -OSiR’3, -PR’2, where each R’ is hydrogen, halogen, C1-C 10 alkyl, or phenyl.
• each of Cp 1 and Cp 2 may be independently unsubstituted cyclopentadienyl, substituted cyclopentadienyl, unsubstituted indenyl, substituted indenyl, unsubstituted fluorenyl, or substituted fluorenyl.
• Y 1 and Y 2 may be independently hydrogen, halide, hydroxyl, or C 1-C50 substituted or unsubstituted hydrocarbyl, amide, alkoxide, sulfide, phosphide, halide, or a combination thereof, or Y 1 and Y 2 are joined together to form a metallocycle ring, or Y 1 and Y 2 are joined to form a chelating ligand, or an alkylidene, (such as each of Y 1 and Y 2 is independently a Ci to C12 alkyl (such as methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, nonyl, decyl, undecyl, dodecyl, or isomers thereof, such as iso-, tert-, n-, sec-), hydrido, benzyl, neopen
• T is a bridging group comprising Si, Ge, or C, such as T is dialkyl silicon or dialkyl germanium, such as T is dimethyl silicon.
• T is CH 2 , CH 2 CH 2 , C(CH 3 ) 2 , SiMe 2 , SiPh 2 , SiMePh, silylcyclobutyl (Si(CH 2 ) 3 ), (Ph) 2 C, (p-(Et) 3 SiPh) 2 C, cyclopentasilylene (Si(CH 2 ) 4 ), or Si(CH 2 ) 5 .
• Specific bridged biscyclopentadienyl compounds include those derived from: (1) indenyl-based complexes such as the rac- or meso-isomer, or mixtures, of dimethylsilyl bis(indenyl)hafnium dimethyl, dimethylsilyl bis(2-methyl-indenyl)hafnium dimethyl, dimethylsilyl bis(2-propyl-indenyl)hafhium dimethyl, dimethylsilyl bis(4-methyl, 2-phenyl- indenyljhafnium dimethyl, or methylene(indenyl)(2,7-di-tertbutyl-fluorenyl)haihium dimethyl, and diphenylmethylene(indenyl)(2,7-bis tert-butylfluorenyl)haihium dibenzyl; (2) fluorenyl-based complexes such as dibutylsilyl(fluorenyl)(cyclopentadie
• the bridged biscyclopentadienyl compound is (p-triethylsilylphenyl)carbyl(cyclopentadienyl)(2,7-di-t-butylfluorenyl)hafnium dimethyl, which is represented by the structure:
• a catalyst system of the present disclosure may include a support material (with or without activator).
• the supported material is a porous support material, for example, talc, and inorganic oxides.
• Other support materials include zeolites, clays, organo-clays, or any other suitable organic or inorganic support material, or mixtures thereof.
• a support material of the present disclosure can be an inorganic oxide in a finely divided form.
• Suitable inorganic oxide materials for use in catalyst systems include groups 2, 4, 13, and 14 metal oxides, such as silica, alumina, and mixtures thereof.
• Other inorganic oxides that may be employed either alone or in combination with the silica, or alumina are magnesia, titania, or zirconia.
• Other suitable support materials can be employed, for example, finely divided functionalized polyolefins, such as finely divided polyethylene.
• Particularly useful supports include magnesia, titania, zirconia, montmorillonite, phyllosilicate, zeolites, talc, and clays.
• support materials may be used, for example, silica-chromium, silica-alumina, and silica-titania.
• suitable support materials include AI2O3, Zr02, S1O2, and combinations thereof, such as S1O2, AI2O3, or S1O2/AI2O3.
• the support material such as an inorganic oxide, has a surface area in the range of from about 10 m 2 /g to about 700 m 2 /g, pore volume in the range of from about 0.1 cm 3 /g to about 4.0 cm 3 /g and average particle size in the range of from about 5 pm to about 500 pm.
• the surface area of the support material is in the range of from about 50 m 2 /g to about 500 m 2 /g, pore volume of from about 0.5 cm 3 /g to about 3.5 cm 3 /g and average particle size of from about 10 pm to about 200 pm.
• the surface area of the support material can be in the range from about 100 m 2 /g to about 400 m 2 /g, with a pore volume of from about 0.8 cm 3 /g to about 3.0 cm 3 /g and an average particle size of from about 5 pm to about 100 pm.
• the average pore size of the support material useful in the present disclosure can be in the range of from about 10 A to about 1000 A, such as about 50 A to about 500 A, such as about 75 A to about 350 A.
• Suitable silicas are marketed under the tradenames of DAVISON 952 or DAVISON 955 by the Davison Chemical Division of W.R. Grace and Company. In at least one embodiment, DAVISON 948 is used.
• the support material should be dry, that is, free of absorbed water. Drying of the support material can be effected by heating or calcining at about 100°C to about 1,000°C, such as at least about 600°C. When the support material is silica, it is heated to at least about 200°C, such as about 200°C to about 850°C, such as at about 600°C; and for a time of about 1 minute to about 100 hours, from about 12 hours to about 72 hours, or from about 24 hours to about 60 hours.
• the calcined support material must have at least some reactive hydroxyl (OH) groups to produce supported catalyst systems of this disclosure.
• the calcined support material is then contacted with at least one polymerization catalyst system having at least one catalyst compound and an activator.
• the support material having reactive surface groups, such as hydroxyl groups, is slurried in a non-polar solvent and the resulting slurry is contacted with a solution of a catalyst compound and an activator.
• the slurry of the support material is first contacted with the activator for a period of time in the range from about 0.5 hours to about 24 hours, from about 2 hours to about 16 hours, or from about 4 hours to about 8 hours.
• the solution of the catalyst compound is then contacted with the isolated support/activator.
• the supported catalyst system is generated in situ.
• the slurry of the support material is first contacted with the catalyst compound for a period of time in the range of from about 0.5 hours to about 24 hours, from about 2 hours to about 16 hours, or from about 4 hours to about 8 hours.
• the slurry of the supported catalyst compound is then contacted with the activator solution.
• the mixture of the catalyst, activator and support is heated to about 0°C to about 70°C, such as about 23°C to about 60°C, such as at room temperature.
• Suitable contact times can range from about 0.5 hours to about 24 hours, from about 2 hours to about 16 hours, or from about 4 hours to about 8 hours.
• Suitable non-polar solvents are materials in which all of the reactants used herein, e.g., the activator, and or the catalyst compound, are at least partially soluble and which are liquid at reaction temperatures.
• Suitable non-polar solvents are alkanes, such as isopentane, hexane, n-heptane, octane, nonane, and decane, although a variety of other materials including cycloalkanes, such as cyclohexane, aromatics, such as benzene, toluene, and ethylbenzene, may also be employed.
• toluene is used as non-polar solvent for the preparation of the catalyst solutions.
• the catalyst precursor, activator, coactivator, if needed, suitable solvent, and support may be added in any order or simultaneously.
• the complex and activator is combined in solvent to form a solution.
• the support is added, and the mixture is stirred for about 1 minute to about 10 hours.
• the total solution volume may be greater than the pore volume of the support, but some embodiments limit the total solution volume below that needed to form a gel or slurry (about 90% to about 400%, such as about 100% to about 200% of the pore volume).
• the residual solvent is removed under vacuum, such as at about ambient temperature and over about 10 to about 16 hours. But greater or lesser times and temperatures are possible.
• the complex may also be supported absent the activator; in that case, the activator (and co-activator if needed) is added to a polymerization process’s liquid phase. Additionally, two or more different complexes may be placed on the same support. Likewise, two or more activators or an activator and co-activator may be placed on the same support.
• Suitable solid particle supports can be included of polymeric or refractory oxide materials, each being porous for example.
• a support material that has an average particle size greater than about 10 pm is suitable.
• V arious embodiments include a porous support material, such as for example, talc, inorganic oxides, inorganic chlorides, for example, magnesium chloride and resinous support materials such as polystyrene polyolefin or polymeric compounds or another organic support material.
• inorganic oxide materials are support material including group 2, 3, 4, 5, 13, or 14 metal or metalloid oxides.
• the catalyst support materials include silica, alumina, silica-alumina, and their mixtures.
• inorganic oxides may serve either alone or in combination with the silica, alumina, or silica-alumina. These are magnesia, titania, or zirconia.
• Lewis acidic materials such as montmorillonite and similar clays may also serve as a support. In this case, the support can, optionally, double as the activator component; however, an additional activator may also be used.
• the support material may be pretreated by any suitable method.
• inorganic oxides may be calcined, chemically treated with dehydroxylating agents, such as aluminum alkyls, or both.
• polymeric carriers will also be suitable in accordance with the present disclosure, see for example the descriptions in WO 95/15815 and U.S. Patent No. 5,427,991.
• the methods disclosed may be used with the catalyst complexes, activators or catalyst systems of the present disclosure to adsorb or absorb them on the polymeric supports, particularly if made up of porous particles, or may be chemically bound through functional groups bound to or in the polymer chains.
• Suitable supports can have a surface area of from about 10 m 2 /g to about 700 m 2 /g, a pore volume of about 0.1 cm 3 /g to about 4.0 cm 3 /g and an average particle size of about 10 pm to about 500 pm.
• suitable supports include a surface area of about 50 m 2 /g to about 500 m 2 /g, a pore volume of 0.5 cm 3 /g to 3.5 cm 3 /g, or an average particle size of 10 pm-200 pm.
• Suitable supports can have a pore size of about 10 A to about 1000 A, alternatively about 50 A to about 500 A, or about 75 A to about 350 A.
• the catalyst complexes of the present disclosure can be deposited on the support at a loading level of about 10 micromoles to about 100 micromoles of complex per gram of solid support; alternately about 20 micromoles to about 80 micromoles of complex per gram of solid support; or about 40 micromoles to about 60 micromoles of complex per gram of support. But greater or lesser values may be used provided that the total amount of solid complex does not exceed the support’s pore volume.
• cocatalyst and“activator” are used herein interchangeably and are defined to be a compound which can activate one or more of the catalyst compounds described above by converting the neutral catalyst compound to a catalytically active catalyst compound cation.
• catalyst systems may be formed by combining the complexes with activators in any suitable manner including by supporting them for use in slurry or gas phase polymerization.
• the catalyst systems may also be added to or generated in solution polymerization or bulk polymerization (in the monomer).
• Suitable catalyst system may include a complex as described above and an activator such as alumoxane or a non-coordinating anion.
• Non-limiting activators include alumoxanes, aluminum alkyls, ionizing activators, which may be neutral or ionic, and other suitable cocatalysts.
• Suitable activators may include alumoxane compounds, modified alumoxane compounds, and ionizing anion precursor compounds that abstract a reactive, s-bound, metal ligand making the metal complex cationic and providing a charge-balancing non-coordinating or weakly coordinating anion.
• Alumoxane Activators include alumoxanes, aluminum alkyls, ionizing activators, which may be neutral or ionic, and other suitable cocatalysts.
• Suitable activators may include alumoxane compounds, modified alumoxane compounds, and ionizing anion precursor compounds that abstract a reactive, s-bound, metal ligand making the metal complex cationic and providing a charge-balancing non-coordinating or weakly coordinating anion.
• alumoxane activators are utilized as an activator in the catalyst system.
• the alkylalumoxane may be used with another activator.
• Alumoxanes are generally oligomeric compounds containing -A ⁇ R ⁇ -O- sub-units, where R 1 is an alkyl group. Examples of alumoxanes include methylalumoxane (MAO), modified methylalumoxane (MMAO), ethylalumoxane, and isobutylalumoxane.
• Alkylalumoxanes and modified alkylalumoxanes are suitable as catalyst activators, particularly when the abstractable ligand is an alkyl, halide, alkoxide or amide. Mixtures of different alumoxanes and modified alumoxanes may also be used. For example, a visually clear methylalumoxane can be used. A cloudy or gelled alumoxane can be filtered to produce a clear solution or clear alumoxane can be decanted from the cloudy solution. Suitable alumoxane can be a modified methyl alumoxane (MMAO) cocatalyst type 3A (commercially available from Akzo Chemicals, Inc. under the trade name Modified Methylalumoxane type 3 A, covered under U.S. Patent No. 5,041,584).
• MMAO modified methyl alumoxane
• alumoxane is solid polymethylaluminoxane as described in U.S. Patent Nos. 9,340,630; 8,404,880; and 8,975,209.
• embodiments may include the maximum amount of activator such as at up to about a 5000-fold molar excess Al/M over the catalyst compound (per metal catalytic site).
• the minimum activator-to-catalyst- compound is about a 1 : 1 molar ratio.
• suitable ranges include from about 1 : 1 to about 500: 1, alternately from about 1: 1 to about 200: 1, alternately from about 1 : 1 to about 100: 1, or alternately from about 1 : 1 to about 50: 1.
• little or no alumoxane is used in the polymerization processes described herein.
• alumoxane is present at about zero mole%, alternately the alumoxane is present at a molar ratio of aluminum to catalyst compound transition metal less than about 500: 1, such as less than about 300: 1, such as less than about 100: 1, such as less than about 1: 1.
• a non-coordinating anion is defined to mean an anion either that does not coordinate to the catalyst metal cation or that does coordinate to the metal cation, but only weakly.
• NCA is also defined to include multicomponent NCA-containing activators, such as N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate, that contain an acidic cationic group and the non-coordinating anion.
• NCA is also defined to include neutral Lewis acids, such as tris(pentafluorophenyl)boron, that can react with a catalyst to form an activated species by abstraction of an anionic group.
• NCA coordinates weakly enough that a neutral Lewis base, such as an olefmically or acetylenically unsaturated monomer can displace it from the catalyst center.
• a neutral Lewis base such as an olefmically or acetylenically unsaturated monomer can displace it from the catalyst center.
• Any suitable metal or metalloid that can form a compatible, weakly coordinating complex may be used or contained in the non-coordinating anion. Suitable metals include aluminum, gold, and platinum. Suitable metalloids include boron, aluminum, phosphorus, and silicon.
• “Compatible” non-coordinating anions can be those which are not degraded to neutrality when the initially formed complex decomposes, and the anion does not transfer an anionic substituent or fragment to the cation so as to cause it to form a neutral transition metal compound and a neutral by-product from the anion.
• Non-coordinating anions useful in accordance with the present disclosure are those that are compatible, stabilize the transition metal cation in the sense of balancing its ionic charge at +1, and yet retain sufficient lability to permit displacement during polymerization.
• an ionizing activator such as tri(n-butyl) ammonium tetrakis(pentafluorophenyl)borate, a tris perfluorophenyl boron metalloid precursor or a tris perfluoronaphthyl boron metalloid precursor, polyhalogenated heteroborane anions (WO 98/43983), boric acid (U.S. Patent No. 5,942,459), or combination thereof. It is also within the scope of the present disclosure to use neutral or ionic activators alone or in combination with alumoxane or modified alumoxane activators.
• the catalyst systems of the present disclosure can include at least one NCA activator.
• boron containing NCA activators represented by the formula below is used:
• Z is (L-H) or a reducible Lewis acid
• L is a neutral Lewis base
• H is hydrogen
• (L-H) + is a Bronsted acid
• a d is a non-coordinating anion, for example a boron containing non coordinating anion having the charge d-; and d is 1, 2, or 3.
• the cation component, Zd + may include Bronsted acids such as protons or protonated Lewis bases or reducible Lewis acids capable of protonating or abstracting a moiety, such as an alkyl or aryl, from the bulky ligand containing transition metal catalyst precursor, resulting in a cationic transition metal species.
• the activating cation Z d + may also be a moiety such as silver, tropylium, carboniums, ferroceniums and mixtures, such as carboniums and ferroceniums, such as Zd + is triphenyl carbonium.
• Suitable reducible Lewis acids can be a triaryl carbonium (where the aryl can be substituted or unsubstituted, such as those represented by the formula: (AnC + ), where Ar is aryl substituted with a Ci to C40 hydrocarbyl or with a substituted Ci to C40 hydrocarbyl, or a heteroaryl substituted with a Ci to C40 hydrocarbyl, or with a substituted Ci to C40 hydrocarbyl; such as the reducible Lewis acids in“Z” include those represented by the formula: (Ph3C), where Ph is a substituted or unsubstituted phenyl, such as substituted with Ci to C40 hydrocarbyls or substituted a Ci to C40 hydrocarbyls, such as Ci to C20 alkyls or aromatics or substituted Ci to C20 alkyls or aromatics, such as Z is a triphenylcarbonium.
• the aryl can be substituted or unsubstituted, such as those represented by the
• Zd + is the activating cation (L-H)d + , such as a Bronsted acid, capable of donating a proton to the transition metal catalytic precursor resulting in a transition metal cation, including ammoniums, oxoniums, phosphoniums, silyliums, and mixtures thereof, such as ammoniums of methylamine, aniline, dimethylamine, diethylamine, N-methylaniline, diphenylamine, trimethylamine, triethylamine, N,N-dimethylaniline, methyldiphenylamine, pyridine, p-bromo-N,N-dimethylaniline, p-nitro-N,N-dimethylaniline, phosphoniums from triethylphosphine, triphenylphosphine, and diphenylphosphine, oxoniums from ethers such as dimethyl ether diethyl ether, tetrahydro
• each Q is a fluorinated hydrocarbyl group having 1 to 20 carbon atoms, such as each Q is a fluorinated aryl group, such as each Q is a pentafluoryl aryl group.
• suitable A d also include diboron compounds as disclosed in U.S. Patent No. 5,447,895, which is fully incorporated herein by reference.
• boron compounds which may be used as an activating cocatalyst include the compounds described as (and particularly those specifically listed as) activators in U.S. Patent No. 8,658,556, which is incorporated by reference herein.
• Bulky activators are also useful herein as NCAs. “Bulky activator” as used herein refers to anionic activators represented by the formula:
• each R 1 is, independently, a halide, such as a fluoride
• Ar is a substituted or unsubstituted aryl group (such as a substituted or unsubstituted phenyl), such as substituted with Ci to C40 hydrocarbyls, such as Ci to C20 alkyls or aromatics; each R 2 is, independently, a halide, a G, to C20 substituted aromatic hydrocarbyl group or a siloxy group of the formula -0-Si-R a , where R a is a Ci to C20 hydrocarbyl or hydrocarbylsilyl group (such as R 2 is a fluoride or a perfluorinated phenyl group);
• each R 3 is a halide, G, to C20 substituted aromatic hydrocarbyl group or a siloxy group of the formula -0-Si-R a , where R a is a Ci to C20 hydrocarbyl or hydrocarbylsilyl group (such as R 3 is a fluoride or a G, perfluorinated aromatic hydrocarbyl group); wherein R 2 and R 3 can form one or more saturated or unsaturated, substituted or unsubstituted rings (such as R 2 and R 3 form a perfluorinated phenyl ring);
• L is a neutral Lewis base
• (L-H) + is a Bronsted acid
• d is 1, 2, or 3;
• the anion has a molecular weight of greater than 1020 g/mol
• Suitable (Ar3C)d + is (Ph3C)d + , where Ph is a substituted or unsubstituted phenyl, such as substituted with Ci to C40 hydrocarbyls or substituted Ci to C40 hydrocarbyls, such as Ci to C20 alkyls or aromatics or substituted Ci to C20 alkyls or aromatics.
• Molecular volume is used herein as an approximation of spatial steric bulk of an activator molecule in solution. Comparison of substituents with differing molecular volumes allows the substituent with the smaller molecular volume to be considered“less bulky” in comparison to the substituent with the larger molecular volume. Conversely, a substituent with a larger molecular volume may be considered“more bulky” than a substituent with a smaller molecular volume. [0116] Molecular volume may be calculated as reported in“A Simple‘Back of the Envelope’ Method for Estimating the Densities and Molecular Volumes of Liquids and Solids,” Journal of Chemical Education, Vol. 71, No. 11, November 1994, pp. 962-964.
• MV Molecular volume
• one or more of the NCA activators is chosen from the activators described in U.S. Patent No. 6,211,105.
• Suitable activators include N,N-dimethylanilinium tetrakis(perfluoronaphthyl)borate, N,N-dimethylanilinium tetrakis(perfluorophenyl)borate, triphenylcarbeniumtetrakis(perfluorophenyl)borate,
• the activator includes a triaryl carbonium (such as triphenylcarbenium tetraphenylborate, triphenylcarbenium tetrakis(pentafluorophenyl)borate, triphenylcarbenium tetrakis-(2,3,4,6-tetrafluorophenyl)borate.
• a triaryl carbonium such as triphenylcarbenium tetraphenylborate, triphenylcarbenium tetrakis(pentafluorophenyl)borate, triphenylcarbenium tetrakis-(2,3,4,6-tetrafluorophenyl)borate.
• Suitable activator may include one or more of trialky lammonium tetrakis(pentafluorophenyl)borate, N,N-dialkylanilinium tetrakis(pentafluorophenyl)borate, N,N-dimethyl-(2,4,6-trimethylanilinium) tetrakis(pentafluorophenyl)borate, trialkylammonium tetrakis-(2,3,4,6-tetrafluorophenyl)borate, N,N-dialkylanilinium tetrakis- (2,3,4,6-tetrafluorophenyl)borate, trialkylammonium tetrakis(perfluoronaphthyl)borate, N,N- dialkylanilinium tetrakis(perfluoronaphthyl)borate, trialkylammonium tetrakis(perfluorobiphenyl
• the ionic activator Zd + (A d ) is one or more of N,N- dimethylanilinium tetrakis(perfluorophenyl)borate, N,N-dimethylanilinium tetrakis(perfluoronaphthyl)borate, N,N-dimethylanilinium tetrakis(perfluorobiphenyl)borate, N,N-dimethylanilinium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triphenylcarbenium tetrakis(perfluoronaphthyl)borate, triphenylcarbenium tetrakis(perfluorobiphenyl)borate, triphenylcarbenium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triphenylcarbenium tetra(perfluorophenyl)borate, N,N-d
• Suitable activator-to-catalyst ratio e.g., all NCA activators-to-catalyst ratio is about a ri l molar ratio.
• Alternate suitable ranges include from about 0.1 : 1 to about 100: 1, alternately from about 0.5: 1 to about 200: 1, alternately from about 1: 1 to about 500: 1, alternately from about 1 :1 to about 1000: 1.
• a particularly useful range is from about 0.5: 1 to about 10: 1, such as about 1: 1 to about 5: 1.
• the catalyst compounds can be combined with combinations of alumoxanes and NCA’s (see for example, U.S. Patent Nos. 5,153,157; 5,453,410; EP 0 573 120 Bl; WO 94/07928; and WO 95/14044 which discuss the use of an alumoxane in combination with an ionizing activator).
• a co-activator or chain transfer agent such as a group 1, 2, or 13 organometallic species (e.g., an alkyl aluminum compound such as tri-n-octyl aluminum), may also be used in the catalyst system herein.
• organometallic species e.g., an alkyl aluminum compound such as tri-n-octyl aluminum
• the complex-to-co-activator molar ratio is from 1 : 100 to 100: 1; 1 :75 to 75:1; 1 :50 to 50: 1; 1:25 to 25:1; 1: 15 to 15: 1; ri lO to 10: 1; 1 :5 to 5: 1; 1 :2 to 2: 1; 1 : 100 to 1 : 1; 1 :75 to 1: 1; 1:50 to 1: 1; 1 :25 to 1: 1; 1: 15 to 1 : 1; ri lO to 1: 1; 1:5 to 1: 1; 1 :2 to 1: 1; ri lO to 2: 1.
• the activator is N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate.
• one or more scavengers or co-activators may be used in the catalyst system.
• Aluminum alkyl or organoaluminum compounds which may be utilized as scavengers or co-activators include, for example, trimethylaluminum, triethylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, and diethyl zinc.
• Those scavengers having bulky or Ce to C20 linear hydrocarbyl substituents connected to the metal or metalloid center usually minimize adverse interaction with the active catalyst.
• Examples include triethylaluminum, such as bulky compounds, such as tri-iso-butyl aluminum, tri-iso-prenyl aluminum, and long-chain linear alkyl-substituted aluminum compounds, such as tri-n-hexyl aluminum, tri-n-octyl aluminum, or tri-n-dodecyl aluminum.
• triethylaluminum such as bulky compounds, such as tri-iso-butyl aluminum, tri-iso-prenyl aluminum, and long-chain linear alkyl-substituted aluminum compounds, such as tri-n-hexyl aluminum, tri-n-octyl aluminum, or tri-n-dodecyl aluminum.
• the scavengers are present at less than about 14 wt%, or from about 0.1 wt% to about 10 wt%, or from about 0.5 wt% to about 7 wt%, by weight of the catalyst system.
• Suitable aluminum alkyl or organoaluminum compounds which may be utilized as co-activators include, for example, trimethylaluminum, triethylaluminum, tri-iso- butylaluminum, tri-n-hexylaluminum, or tri-n-octylaluminum.
• the co activators are present at less than about 14 wt%, or from about 0.1 to about 10 wt%, or from about 0.5 to about 7 wt%, by weight of the catalyst system.
• the complex-to-co- activator molar ratio is from about 1: 100 to about 100: 1; about 1 :75 to about 75: 1; about 1 :50 to about 50: 1; about 1:25 to about 25: 1; about 1 :15 to about 15: 1; about 1: 10 to about 10: 1; about 1 :5 to about 5: 1; about 1 :2 to about 2: 1; about 1: 100 to about 1: 1; about 1:75 to about 1 : 1; about 1 :50 to about 1: 1; about 1 :25 to about 1 : 1; about 1 :15 to about 1 : 1; about 1 :10 to about 1: 1; about 1:5 to about 1: 1; about 1 :2 to about 1: 1; about 1: 10 to about 2: 1.
• the present disclosure relates to polymerization processes where monomers (e.g., ethylene), and cyclic olefin comonomers (e.g., norbomene) are contacted with a catalyst system including an activator and at least one catalyst compound, as described above.
• monomers e.g., ethylene
• cyclic olefin comonomers e.g., norbomene
• the catalyst compound and activator may be combined in any order, and are combined prior to contacting with the monomers.
• Monomers include substituted or unsubstituted C2 to C40 alpha olefins, such as C2 to C20 alpha olefins, such as C2 to C 12 alpha olefins, such as ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene and isomers thereof.
• the monomer includes ethylene or C4 to C40 olefins, such as C7to C20 olefins.
• the C4 to C40 olefin monomers may be linear, branched, or cyclic.
• the C4 to C40 olefin monomers may be strained or unstrained, monocyclic or polycyclic, and may optionally include heteroatoms and or one or more functional groups.
• Exemplary C2 to C40 olefin monomers may include ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene.
• Polymers of the present disclosure further include one or more C5 to C40 cyclic olefin comonomers, such as C5 to C20 cyclic olefin comonomers, such as C5 to C10 cyclic olefin comonomers, such as a C7 cyclic olefin comonomer.
• C5 to C40 cyclic olefin comonomers may include linear, branched, or cyclic substituents.
• the C5 to C40 cyclic olefin comonomers may be strained or unstrained, monocyclic or polycyclic, and may optionally include heteroatoms and or one or more functional groups.
• Exemplary C2 to C40 cyclic olefin comonomers can include norbomene, norbomadiene, dicyclopentadiene, cyclopentene, cycloheptene, cyclooctene, cyclooctadiene, cyclododecene, 7-oxanorbomene, 7-oxanorbomadiene, substituted derivatives thereof, and isomers thereof, such as cyclooctene, 1,5-cyclooctadiene, l-hydroxy-4-cyclooctene, l-acetoxy-4-cyclooctene, 5-methylcyclopentene, cyclopentene, dicyclopentadiene, norbomene, norbomadiene, and their respective homologs and derivatives, such as norbomene, norbomadiene, and dicyclopentadiene.
• Polymerization processes of the present disclosure can be carried out in any suitable manner. Any suitable suspension, homogeneous, bulk, solution, slurry, or gas phase polymerization process can be used. Such processes can be run in a batch, semi-batch, or continuous mode. Homogeneous polymerization processes and slurry processes can be used. (A homogeneous polymerization process is a process where at least 90 wt% of the product is soluble in the reaction media.) A bulk homogeneous process can be used.
• a bulk process is a process where monomers being polymerized also serves as solvent or diluent and the monomer concentration in all feeds to the reactor is at least 70 volume % or more.
• no inert hydrocarbon is present or added in the reaction medium as a solvent or diluent, (except for the small amounts used as the carrier for the catalyst system or other additives, or amounts found with the monomer; e.g., propane in propylene).
• the process is a slurry process.
• the term“slurry polymerization process” means a polymerization process where a supported catalyst is employed and monomers are polymerized on the supported catalyst particles. At least 95 wt% of polymer products derived from the supported catalyst can be in granular form as solid particles (not dissolved in the diluent).
• the process is a solution polymerization process.
• a polymer can be recovered from the effluent of any one or more polymerizations by separating the polymer from other constituents of the effluent using conventional separation means.
• polymer can be recovered from a polymerization effluent by coagulation with a non-solvent such as isopropyl alcohol, acetone, or n-butyl alcohol, or the polymer can be recovered by stripping the solvent or other media with heat or steam.
• a non-solvent such as isopropyl alcohol, acetone, or n-butyl alcohol
• One or more conventional additives such as antioxidants can be incorporated in the polymer during the recovery procedure.
• Suitable antioxidants may include phenyl-beta-naphthylamine, di-tert- butylhydroquinone, triphenyl phosphate, heptylated diphenylamine, 2,2'-methylene-bis (4- methyl-6-tert-butyl)phenol, and 2,2,4-trimethyl-6-phenyl-l,2-dihydroquinoline.
• Other methods of recovery such as by the use of lower critical solution temperature (LOST) followed by devolatilization are also envisioned.
• LOST lower critical solution temperature
• the catalyst may be deactivated as part of the separation procedure to reduce or eliminate further uncontrolled polymerization downstream the polymer recovery processes. Deactivation may be effected by the mixing with suitable polar substances such as water, whose residual effect following recycle can be counteracted by suitable sieves or scavenging systems.
• Suitable diluents/solvents for polymerization include non-coordinating, inert liquids.
• examples include straight and branched-chain hydrocarbons, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof, such as can be found commercially (IsoparTM); perhalogenated hydrocarbons, such as perfluorinated C4 to C10 alkanes, chlorobenzene, and aromatic and alkylsubstituted aromatic compounds, such as benzene, toluene, mesitylene, and xylene.
• straight and branched-chain hydrocarbons such as isobut
• Suitable solvents also include liquid olefins which may act as monomers or comonomers including ethylene, propylene, 1 -butene, 1 -hexene, 1- pentene, 3-methyl- 1-pentene, 4-methyl- 1-pentene, 1-octene, 1-decene, and mixtures thereof.
• aliphatic hydrocarbon solvents are used as the solvent, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof.
• the solvent is not aromatic, such as aromatics are present in the solvent at less than 1 wt%, such as less than 0.5 wt%, such as less than 0 wt% based upon the weight of the solvents.
• Polymerizations can be run at any temperature and or pressure suitable to obtain the desired ethylene polymers.
• Suitable temperatures and or pressures may include a temperature in the range of from about 0°C to about 300°C, such as about 20°C to about 200°C, such as about 35°C to about 150°C, such as from about 40°C to about 120°C, such as from about 45°C to about 80°C, such as the temperature of polymerization can be 130°C; and at a pressure in the range of from about 0.35 MPa to about 10 MPa, such as from about 0.45 MPa to about 6 MPa, such as from about 0.5 MPa to about 4 MPa, such as from about 0.55 MPa to about 3 MPa, such as from about 0.60 MPa to about 2 MPa, such as from about 0.65 MPa to about 1 MPa (such as from about 0.95 psig to about 145 psig), such as the polymerization process may be carried out at a pressure of about 2.4 MPa.
• hydrogen is present in the polymerization reactor at a partial pressure of 0.001 psig to 50 psig (0.007 kPa to 345 kPa), such as from 0.01 psig to 25 psig (0.07 kPa to 172 kPa), such as 0.1 psig to 10 psig (0.7 kPa to 70 kPa).
• 500 ppm or less, or 400 ppm or less, or 300 ppm of less of hydrogen can be added into the reactor.
• at least 50 ppm of hydrogen is added, such as 100 ppm or greater, such as 200 ppm or greater.
• certain embodiments include hydrogen added to the reactor in amounts ranging from a low of any one of about 50 ppm, 100 ppm, 150 ppm, and 200 ppm to a high of any one of about 250 ppm, 300 ppm, 350 ppm, 400 ppm, 450 ppm, and 500 ppm.
• the activity of the catalyst system is at least 50 g/mmol/hour, such as 500 g/mmol/hour or greater, such as 5,000 g/mmol/hr or greater, such as 50,000 g/mmol/hr or greater, such as 100,000 g/mmol/hr or greater.
• the catalyst efficiency can be 10,000 kg of polymer per kg of catalyst or more, such as 20,000 kg of polymer per kg of catalyst or more, such as 30,000 kg of polymer per kg of catalyst or more, such as 40,000 kg of polymer per kg of catalyst or more, such as 50,000 kg of polymer per kg of catalyst or more, such as the catalyst efficiency can be of from about 10,000 kg of polymer per catalyst to about 60,000 kg of polymer per catalyst.
• the conversion of olefin monomer is at least 10%, based upon polymer yield and the weight of the monomer entering the reaction zone, such as 20% or more, such as 30% or more, such as 50% or more.
• alumoxane is present at zero mol%, alternately the alumoxane is present at a molar ratio of aluminum to transition metal less than 500: 1, such as less than 300: 1, such as less than 100: 1, such as less than 1 : 1.
• scavenger such as tri alkyl aluminum
• the scavenger is present at zero mol%, alternately the scavenger is present at a molar ratio of scavenger metal to transition metal of less than 100: 1, such as less than 50: 1, such as less than 15: 1, such as less than 10: 1.
• the polymerization 1) is conducted at temperatures of 0°C to 300°C (such as 130°C); 2) is conducted at a pressure of atmospheric pressure to 10 MPa (such as 0.35 MPa to 10 MPa, such as from 0.45 MPa to 6 MPa, such as from 0.5 MPa to 4 MPa, such as from 0.65 MPa to 2.5 MPa); 3) is conducted in an aliphatic hydrocarbon solvent (such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof; such as where aromatics are present in the solvent at less than 1 wt%, such as less than 0.5 wt%, such
• the catalyst system used in the polymerization includes no more than one catalyst compound.
• a "reaction zone” also referred to as a "polymerization zone” is a vessel where polymerization takes place, for example, a batch reactor. When multiple reactors are used in either series or parallel configuration, each reactor is considered as a separate polymerization zone. For a multi-stage polymerization in both a batch reactor and a continuous reactor, each polymerization stage is considered as a separate polymerization zone. In at least one embodiment, the polymerization occurs in one reaction zone. Room temperature is 23°C unless otherwise noted.
• additives may also be used in the polymerization, such as one or more scavengers, promoters, modifiers, chain transfer agents (such as diethyl zinc), reducing agents, oxidizing agents, hydrogen, aluminum alkyls, or silanes.
• Chain transfer agents may include alkylalumoxanes, a compound represented by the formula AIR3 or ZnR2 (where each R is, independently, a Ci to Cx aliphatic radical, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl or an isomer thereol), or a combination thereof, such as diethyl zinc, methylalumoxane, trimethylaluminum, triisobutylaluminum, trioctylaluminum, or a combination thereof.
• AIR3 or ZnR2 where each R is, independently, a Ci to Cx aliphatic radical, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl or an isomer thereol
• a combination thereof such as diethyl zinc, methylalumoxane, trimethylaluminum, triis
• This disclosure also relates to compositions of matter produced by methods of the present disclosure.
• the catalyst systems and methods herein produce cyclic olefin copolymers.
• the blends described herein comprise a first polymer, which is a semicrystalline cyclic olefin copolymer comprising less than 15 wt% of a C5-C40 cyclic olefin comonomer and greater than 85 wt% of C2-C40 linear and/or branched olefin monomer(s) (e.g., non-cyclic monomers such as linear or branched olefins, such as linear or branched alpha-olefins), based on the total weight of the copolymer.
• a first polymer which is a semicrystalline cyclic olefin copolymer comprising less than 15 wt% of a C5-C40 cyclic olefin comonomer and greater than 85 wt% of C2-C40 linear and/or branched olefin monomer(s) (e.g., non-cyclic monomers such as linear or branched olef
• the semicrystalline cyclic olefin copolymer may have a C2-C40 olefin (linear or branched) content of about 85 wt% to about 99.5 wt%, such as of about 86 wt% to about 98 wt%, such as of about 87 wt% to about 96 wt%.
• the semicrystalline cyclic olefin copolymer may have from about 0.5 wt% to 15 wt% cyclic olefin-derived units, based on the total weight of the copolymer.
• the semicrystalline cyclic olefin copolymer can have a cyclic olefin content of from about 0.5 wt% to 15 wt%, such as from about 1 wt% to about 10 wt%, such as from about 2 wt% to about 8 wt%, such as from about 3 wt% to about 5 wt%, such as from about 4 wt% to about 8 wt%, alternatively from about 9 wt% to about 15 wt%, based on the total weight of the copolymer.
• the cyclic comonomer in the semicrystalline cyclic olefin copolymer is one or more of dicyclopentadiene, cyclopentene, cycloheptene, cyclooctene, cyclooctadiene, cyclododecene, 7-oxanorbomene, 7-oxanorbomadiene, substituted derivatives thereof, and isomers thereof, such as 1,5-cyclooctadiene, l-hydroxy-4- cyclooctene, l-acetoxy-4-cyclooctene, 5-methylcyclopentene, cyclopentene, dicyclopentadiene, norbomene, norbomadiene, and their respective homologs and derivatives.
• the cyclic olefin in the semicrystalline cyclic olefin copolymer is norbomene.
• the C2-C40 linear and or branched olefin in the semicrystalline cyclic olefin copolymer is selected from C2-C20 linear and or branched olefins, optionally from C2-C 12 linear and or branched olefins, such as ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene and isomers thereof.
• the C2 to C40 olefin in the semicrystalline cyclic olefin copolymer is ethylene.
• the C2 to C40 olefin in the amorphous cyclic olefin copolymer is selected from C2-C20, optionally C2 to C 12, linear and or branched olefins, such as ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene and isomers thereof.
• the C2 to C40 olefin in the amorphous cyclic olefin copolymer is ethylene.
• the C2 to C40 olefin in the semicrystalline and the amorphous cyclic olefin copolymers is ethylene.
• the cyclic olefin in the first and second cyclic olefin copolymers is the same, preferably norbomene. Alternately the cyclic olefin in the first and second cyclic olefin copolymers is different.
• the semicrystalline cyclic olefin copolymer can have a heat of fusion“Hf”, as determined by the Differential Scanning Calorimetry (“DSC”), of 250 J/g or less, such as from 85 J/g to 230 J/g, such as from 90 J/g to 200 J/g, a melting point (T m ) of 130°C or less, such as from about 90°C to about 125°C, such as from about 100°C to about 120°C and a crystallization temperature“Tc” of 120°C or less, such as from about 75°C to about 115°C, such as from about 80°C to about 110°C.
• DSC Differential Scanning Calorimetry
• the semicrystalline cyclic olefin copolymer has a melt index from about 0.02 g/lOmin to about 5 g/lOmin, such as from about 0.03 g/lOmin to about 4.8 g/lOmin, such as from about 0.04 g/lOmin to about 4.6 g/lOmin, such as from about 0.05 g/lOmin to about 4.4 g/lOmin, such as from about 0.06 g/lOmin to about 4.2 g/lOmin, such as from about 0.07 g/lOmin to about 3.8 g/lOmin.
• the semicrystalline cyclic olefin copolymer has a high load melt index (HLMI, ASTM 1238) from about 1 g/lOmin to about 130 g/lOmin; such as from about 2 g/lOmin to about 125 g/lOmin, such as from about 3 g/lOmin to about 120 g/lOmin, such as from about 4 g/lOmin to about 115 g/lOmin.
• HLMI high load melt index
• the semicrystalline cyclic olefin copolymer has a melt index ratio (MIR) value greater than 25, such as from 25 to 70, such as from 26 to 65, such as from 27 to 60, such as from 28 to 55.
• MIR melt index ratio
• the semicrystalline cyclic olefin copolymer can have a density of about 0.92 g/cm 3 to about 0.94 g/cm 3 , such as from about 0.925 g/cm 3 to about 0.935 g/cm 3 , such as from about 0.93 g/cm 3 to about 0.935 g/cm 3 , such as from about 0.92 g/cm 3 to about 0.933 g/cm 3 .
• the semicrystalline cyclic olefin copolymer has a melt strength of about 1 cN or greater, such as about 1 cN to about 16 cN, such as from about 5 cN to about 15 cN, such as from about 7 cN to about 14 cN, such as from about 10 cN to about 14 cN.
• the semicrystalline cyclic olefin copolymer has an number averaged molecular weight of from about 20,000 g/mol to about 200,000 g/mol, such as form about 30,000 g/mol to about 150,000 g/mol, such as from about 50,000 g/mol to about 120,000 g/mol; a weight averaged molecular weight of from about 50,000 g/mol to about 400,000 g/mol, such as from about 75,000 g/mol to about 300,000 g/mol, such as from about 100,000 g/mol to about 250,000 g/mol; and a polydispersity (PDI defined as Mw/Mn) of about 1.5 to about 7.5, such as from about 2.0 to 7, such as from about 2.5 to about 6.5.
• Molecular weight is determined by Gel Permeation Chromatography (GPC).
• the semicrystalline cyclic olefin copolymer has a unimodal or multimodal molecular weight distribution as determined by Gel Permeation Chromatography (GPC).
• the blends described herein also comprise a second polymer which is an amorphous cyclic olefin copolymer comprising more than 25 wt% of a C5-C40 cyclic olefin comonomer and less than 75 wt% of a C2-C40 monomer (linear or branched, such as linear alpha olefin) based on the total weight of the copolymer.
• a second polymer which is an amorphous cyclic olefin copolymer comprising more than 25 wt% of a C5-C40 cyclic olefin comonomer and less than 75 wt% of a C2-C40 monomer (linear or branched, such as linear alpha olefin) based on the total weight of the copolymer.
• the copolymer may have a C2-C40 olefin content of about less than 75 wt% to about 0.5 wt%, such as of about 70 wt% to about 5 wt%, such as of about 65 wt% to about 10 wt%, such as of about 60 wt% to about 15 wt%, such as of about 55 wt% to about 20 wt% and such as of about 50 wt% to about 25 wt%.
• the cyclic olefin copolymer 25 wt% or more of cyclic olefin-derived units, based on the total weight of the copolymer.
• the cyclic olefin copolymer can have a cyclic olefin content of more than 25 wt% to 99.5 wt%, such as from about 30 wt% to about 95 wt%, such as from about 35 wt% to about 90 wt%, such as from about 40 wt% to about 85 wt%, such as from about 45 wt% to about 80 wt% and such as from about 50 wt% to about 75 wt% based on the total weight of the copolymer.
• the cyclic comonomer in the amorphous cyclic olefin copolymer is one or more of dicyclopentadiene, cyclopentene, cycloheptene, cyclooctene, cyclooctadiene, cyclododecene, 7-oxanorbomene, 7-oxanorbomadiene, substituted derivatives thereof, and isomers thereof, such as 1,5-cyclooctadiene, l-hydroxy-4-cyclooctene, 1-acetoxy- 4-cyclooctene, 5-methylcyclopentene, cyclopentene, dicyclopentadiene, norbomene, norbomadiene, and their respective homologs and derivatives.
• the cyclic olefin comonomer in the amorphous cyclic olefin copolymer is norbomene.
• the C2-C40 olefin in the amorphous cyclic olefin copolymer is selected from ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene and isomers thereof.
• the C2 to C40 alpha- olefin in the amorphous cyclic olefin copolymer is ethylene.
• the amorphous cyclic olefin copolymer has a melt index from about 0.02 g/lOmin to about 5 g/lOmin, such as from about 0.03 g/lOmin to about 4.8 g/lOmin, such as from about 0.04 g/lOmin to about 4.6 g/lOmin, such as from about 0.05 g/lOmin to about 4.4 g/lOmin, such as from about 0.06 g/lOmin to about 4.2 g/lOmin, such as from about 0.07 g/lOmin to about 3.8 g/lOmin.
• the amorphous cyclic olefin copolymer has a high load melt index (HLMI, ASTM 1238) from about 1 g/lOmin to about 130 g/lOmin; such as from about 2 g/lOmin to about 125 g/lOmin, such as from about 3 g/lOmin to about 120 g/lOmin, such as from about 4 g/lOmin to about 115 g/lOmin.
• HLMI high load melt index
• the amorphous cyclic olefin copolymer has a melt index ratio (MIR) value greater than 25, such as from 25 to 70, such as from 26 to 65, such as from 27 to 60, such as from 28 to 55.
• MIR melt index ratio
• the amorphous cyclic olefin copolymer can have a density of about 0.97 g/cm 3 to about 1.05 g/cm 3 , such as from about 0.98 g/cm 3 to about 1.04g/cm 3 , such as from about 0.99 g/cm 3 to about 1.03 g/cm 3 , such as from about 1.0 g/cm 3 to about 1.02 g/cm 3 .
• the amorphous cyclic olefin copolymer has an number averaged molecular weight of from about 20,000 g/mol to about 200,000 g/mol, such as form about 30,000 g/mol to about 150,000 g/mol, such as from about 50,000 g/mol to about 120,000 g/mol; a weight averaged molecular weight of from about 50,000 g/mol to about 400,000 g/mol, such as from about 75,000 g/mol to about 300,000 g/mol, such as from about 100,000 g/mol to about 250,000 g/mol; and a polydispersity (PDI defined as Mw/Mn) of about 1.5 to about 7.5, such as from about 2.0 to 7, such as from about 2.5 to about 6.5.
• Molecular weight is determined by Gel Permeation Chromatography (GPC), unless otherwise indicated.
• the amorphous cyclic olefin copolymer has a unimodal or multimodal molecular weight distribution as determined by Gel Permeation Chromatography (GPC).
• GPC Gel Permeation Chromatography
• unimodal is meant that the GPC trace has one peak or inflection point.
• multimodal is meant that the GPC trace has at least two peaks or inflection points.
• An inflection point is that point where the second derivative of the curve changes in sign (e.g., from negative to positive or vice versus).
• the blends described herein also comprise a third polymer which is a semicrystalline olefin copolymer comprising C2-C40 monomers having a density of about 0.90 g/cm 3 to about 0.96 g/cm 3 .
• the third polymer is an ethylene polymer having a density of about 0.90 g/cm 3 to about 0.96 g/cm 3 .
• Ethylene polymers useful herein are selected from ethylene homopolymers and ethylene copolymers.
• the methods of making semicrystalline olefin polymer include slurry, solution, gas phase, high pressure, or other suitable processes, and by using catalyst systems appropriate for the polymerization of polyethylenes, such as Ziegler-Natta-type catalysts, chromium catalysts, metallocene-type catalysts, other appropriate catalyst systems, or combinations thereof, or by free-radical polymerization.
• the polymers are made by the catalysts, activators, and processes described in U.S. Patent Nos. 6,342,566; 6,384,142; 5,741,563; PCT publications WO 03/040201; and WO 97/19991.
• Such catalysts are well known in the art, and are described in, for example, ZIEGLER CATALYSTS (Gerhard Fink, Rolf Mrilhaupt and Hans H. Brintzinger, eds., Springer-Verlag 1995); Resconi et al; and I, II METALLOCENE-BASED POLYOLEFINS (Wiley & Sons 2000).
• a "metallocene” catalyst compound is a transition metal catalyst compound having one, two or three, typically one or two, substituted or unsubstituted cyclopentadienyl ligands bound to the transition metal, typically a metallocene catalyst is an organometallic compound containing at least one p-bound cyclopentadienyl moiety (or substituted cyclopentadienyl moiety).
• Substituted or unsubstituted cyclopentadienyl ligands include substituted or unsubstituted indenyl, fluorenyl, tetrahydro-v-indacenyl. tetrahydro- v-indacenyl.
• a metallocene polymer is a polymer made using a metallocene catalyst.
• a metallocene polyethylene is an ethylene polymer made using a metallocene catalyst.
• the ethylene polymers useful herein are metallocene polyethylenes (mPEs).
• the ethylene copolymer comprises one or more mPEs, such as those described in U.S. Patent Publication No. 2007/0260016, U.S. Patent No. 6,476,171, and U.S. Patent No. 6,255,426).
• the ethylene polymer comprises a Ziegler-Natta polyethylene.
• the ethylene polymer is produced using chrome based catalysts, such as, for example, in U.S. Patent No. 7,491,776, including that fluorocarbon does not have to be used in the production.
• chrome based catalysts such as, for example, in U.S. Patent No. 7,491,776, including that fluorocarbon does not have to be used in the production.
• Commercial examples of polymers produced by chromium include the PaxonTM grades of polyethylene produced by ExxonMobil Chemical Company, Houston Texas.
• the ethylene polymer comprises substantially linear and linear ethylene polymers (SLEPs).
• SEPs substantially linear and linear ethylene polymers
• Substantially linear ethylene polymers and linear ethylene polymers and their method of preparation are fully described in U.S. Patent Nos. 5,272,236; 5,278,272; 3,645,992; 4,937,299; 4,701,432; 4,937,301; 4,935,397; 5,055,438; EP 129,368; EP 260,999; and WO 90/07526, which are fully incorporated herein by reference.
• a linear or substantially linear ethylene polymer means a homopolymer of ethylene or a copolymer of ethylene and one or more alpha-olefin comonomers having a linear backbone (i.e. no cross linking), a specific and limited amount of long-chain branching or no long-chain branching, a narrow molecular weight distribution, a narrow composition distribution (e.g., for alpha-olefin copolymers) or a combination thereof. More explanation of such polymers is discussed in U.S. Patent No. 6,403,692, which is incorporated herein by reference for all purposes.
• the ethylene polymers is produced by gas-phase polymerization of ethylene and, optionally, a C3 to C20 alpha-olefin using transition metal catalyst(s), such as traditional Ziegler-Natta catalysts or metallocene catalysts, useful examples include bis(n-C3-4 alkyl cyclopentadienyl) halhiumX2, or(cyclopentadienyl)(propyl,tetramethyl- cyclopentadienyl)hafniumX2, where X is a leaving group, such as halogen or Ci to C20 alkyl.
• transition metal catalyst(s) such as traditional Ziegler-Natta catalysts or metallocene catalysts
• useful examples include bis(n-C3-4 alkyl cyclopentadienyl) halhiumX2, or(cyclopentadienyl)(propyl,tetramethyl- cyclopentadienyl)hafniumX2, where X is a leaving group,
• Preferred ethylene polymers and copolymers that are useful in this invention include those sold by ExxonMobil Chemical Company in Houston Texas, including those sold as ExxonMobilTM HDPE, ExxonMobilTM LLDPE, and ExxonMobilTM LDPE; and those sold under the ENABLETM, EXACTTM, EXCEEDTM, ESCORENETM, EXXCOTM, ESCORTM, PAXONTM, and OPTEMATM tradenames.
• Particularly useful grades include ExceedTM 1018 LLDPE, EnableTM 2010 polyethylene (such as ENABLETM 2010HA polyethylene), and the LDPETM 103 series.
• the PE and the first semicrystalline cyclic olefin copolymer have similar density(e.g., + 20%, preferably ⁇ 5%) , thermal profile (similar (e.g., + 30%, preferably +10%) Tm and Tc) and/or similar (e.g., + 30%, preferably +10%) crystallinity.
• the PE and the first semicrystalline cyclic olefin copolymer have similar (e.g., + 20%, preferably ⁇ 5%) density.
• the PE and the first semicrystalline cyclic olefin copolymer have similar (e.g., + 30%, preferably +10%) Tm.
• the PE and the first semicrystalline cyclic olefin copolymer have similar (e.g., + 30%, preferably +10%) Tc.
• the PE and the first semicrystalline cyclic olefin copolymer have similar (e.g., + 30%, preferably +10%) difference between Tm and Tc.
• the PE and the first semicrystalline cyclic olefin copolymer have similar (e.g., + 30%, preferably +10%) crystallinity.
• the 1% Secant Modulus, Tensile Strength, Total Haze, Elongation at Break, Normalized Peak Puncture Force, Puncture Break Energy, Water Vapor Transmission Rate and Oxygen Transmission Rate of the semicrystalline olefin (linear or branched) polymer should be different (independently greater than + 10%, preferably greater than + 25%, preferably greater than +30%, preferably greater than +50%) than the semicrystalline cyclic olefin copolymer.
• the 1% Secant Modulus, Tensile Strength, Total Haze, Elongation at Break, Normalized Peak Puncture Force, Puncture Break Energy, Water Vapor Transmission Rate and Oxygen Transmission Rate of the semicrystalline olefin (linear or branched) polymer should be different (independently greater than + 10%, preferably greater than + 25%, preferably greater than +30%, preferably greater than +50%) than the amorphous cyclic olefin copolymer.
• the 1% Secant Modulus, Tensile Strength, Total Haze, Elongation at Break, Normalized Peak Puncture Force, Puncture Break Energy, Water Vapor Transmission Rate and Oxygen Transmission Rate of the semicrystalline olefin (linear or branched) polymer should be different (independently greater than + 10%, preferably greater than + 25%, preferably greater than +30%, preferably greater than +50%) than the semicrystalline cyclic olefin copolymer and the amorphous cyclic olefin copolymer.
• the 1% Secant Modulus, Tensile Strength, Total Haze, Elongation at Break, Normalized Peak Puncture Force, Puncture Break Energy, Water Vapor Transmission Rate and Oxygen Transmission Rate of the semicrystalline olefin (linear or branched) polymer should be different (as indicated below for the individual properties) than the semicrystalline cyclic olefin copolymer and/or the amorphous cyclic olefin copolymer.
• the 1% secant modulus of the ethylene polymer should be different (e.g., more than 25% different, preferably greater than 50% preferably greater than 100%) than the semicrystalline cyclic olefin copolymer.
• the Tensile Strength of the ethylene polymer should be different (e.g., more than 10% different, preferably greater than 25%) than the semicrystalline cyclic olefin copolymer.
• the Elongation at Break of the ethylene polymer should be different (e.g., more than 10% different, preferably greater than 25%) than the semicrystalline cyclic olefin copolymer.
• the Normalized Peak Puncture Force of the ethylene polymer should be different (e.g., more than 10% different, preferably greater than 25%) than the semicrystalline cyclic olefin copolymer.
• the Puncture Break Energy of the ethylene polymer should be different (e.g., more than 10% different, preferably greater than 25%) than the semicrystalline cyclic olefin copolymer.
• the Total Haze of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50% preferably greater than 100%) than the semicrystalline cyclic olefin copolymer.
• the Water Vapor Transmission Rate of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50% preferably greater than 100%) than the semicrystalline cyclic olefin copolymer.
• the Oxygen Transmission Rate of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50% preferably greater than 100%) than the semicrystalline cyclic olefin copolymer.
• the 1% secant modulus of the ethylene polymer should be different (e.g., greater than 50% different, preferably greater than 100% preferably greater than 200%) than the amorphous cyclic olefin copolymer.
• the Elongation at Break of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50%, preferably greater than 100%) than the amorphous cyclic olefin copolymer.
• the Tensile Strength of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50%) than the amorphous cyclic olefin copolymer.
• the Normalized Peak Puncture Force of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50%, preferably greater than 100%) than the amorphous cyclic olefin copolymer.
• the Puncture Break Energy of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50%, preferably greater than 100%) than the amorphous cyclic olefin copolymer.
• the Total Haze of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50% preferably greater than 100%) than the amorphous cyclic olefin copolymer.
• the Water Vapor Transmission Rate of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50%, preferably greater than 100%) than the amorphous cyclic olefin copolymer.
• the Oxygen Transmission Rate of the ethylene polymer should be different (e.g., greater than 25% different, preferably greater than 50%, preferably greater than 100%) than the amorphous cyclic olefin copolymer.
• Selection of the semicrystalline cyclic olefin copolymer, the amorphous cyclic olefin copolymer and the semicrystalline olefin copolymer (ethylene polymer) is based on the ability of the semicrystalline cyclic olefin copolymer to increase the stability of immiscible blends of the amorphous cyclic olefin copolymer and the semicrystalline olefin copolymer (ethylene polymer), and to control the phase morphology of the blend.
• the semicrystalline cyclic olefin copolymer is used to improve the balance of mechanical and barrier properties of films made using blends of the amorphous cyclic olefin and the semicrystalline olefin copolymer.
• the semicrystalline cyclic olefin copolymer acts as a compatibilizing agent between the amorphous cyclic olefin copolymer, (such as ethylene-norbomene copolymers with low (25 wt% or less) percentages of norbomene,)and the semicrystalline olefin copolymer (ethylene copolymer).
• a“blend” may refer to a dry or extruder blend of three or more different polymers, and in-reactor blends, including blends arising from the use of multi or mixed catalyst systems in a single reactor zone, and blends that result from the use of one or more catalyst(s) in one or more reactor(s) under the same or different conditions (e.g., a blend resulting from in series reactors (the same or different) each running under different conditions and or with different catalysts).
• This invention relates to blends comprising:
• the semicrystalbne cyclic olefin copolymer has a density about 0.92 g/cm 3 to about 0.94 g/cm 3 .
• any of the blends described herein can be combined with optional additives (see, for example, US 2016/0060430, paragraphs [0082]-[0093]).
• the blends herein can include additives such as pigments, antioxidants, fillers, etc.
• the semicrystalbne cyclic olefin copolymer or 1 ST COC, amorphous cyclic olefin copolymer or 2 ND COC and the semicrystalbne olefin (linear or branched) copolymer or PE, and/or blends of the present disclosure can have an additive content of from about 0.1 wt% to about 15 wt%, such as from about 1 wt% to about 5 wt%.
• films of the blends described herein can have an additive content of from about 0.1 wt% to about 15 wt%, such as from about 1 wt% to about 5 wt%.
• a useful additive combination includes: IRGANOXTM 1076, IRGAFOS® 168, and DYNAMARTM FX-5929 (a free-flowing fluropolymer based processing additive, available from 3M), such as for example: 300 ppm IRGANOXTM 1076, 1500 ppm IRGAFOSTM 168, and 400 ppm DYNAMARTM FX-5929.
• Another useful additive combination includes: IRGANOXTM 1076 and IRGAFOSTM 168, and, such as for example: 50% IRGANOXTM 1076, and 50% IRGAFOSTM 168.
• Blends of the present disclosure including semicrystalbne cyclic olefin copolymer, amorphous cyclic olefin copolymer and semicrystalbne olefin (linear or branched) copolymer (such as ethylene copolymer, a semi-crystalline cyclic olefin copolymer and amorphous cyclic olefin copolymer) are optionally combined with one or more additional polymer(s) prior to being formed into a film, molded part, or other article.
• semicrystalbne cyclic olefin copolymer such as ethylene copolymer, a semi-crystalline cyclic olefin copolymer and amorphous cyclic olefin copolymer
• Useful additional polymers include, but are not limited to, other polyethylenes, isotactic polypropylene, syndiotactic polypropylene, random copolymer of propylene and ethylene, and or butene, and or hexene, polybutene, ethylene vinyl acetate, LDPE, LLDPE, HDPE, ethylene vinyl acetate, ethylene methyl acrylate, copolymers of acrylic acid, polymethylmethacrylate or any other polymers polymerizable by a high-pressure free radical process, polyvinylchloride, polybutene-1, isotactic polybutene, ABS resins, ethylene- propylene rubber (EPR), vulcanized EPR, EPDM, block copolymer, styrenic block copolymers, polyamides, polycarbonates, PET resins, cross linked polyethylene, copolymers of ethylene and vinyl alcohol (EVOH), polymers of aromatic monomers such as polystyrene,
• the present disclosure also relates to films including the blends described herein.
• the blends disclosed herein may be utilized to prepare monolayer films or multilayer films. These films may be formed by any extrusion or coextrusion techniques discussed below. Films may be unoriented, uniaxially oriented or biaxially oriented to the same or different extents. Physical properties of the film may vary depending on the film forming techniques used.
• films containing blend monolayer or multilayer may be formed by using casting techniques, such as a chill roll casting process.
• a chill roll casting process Exemplary of such chill roll casting processes and apparatus can be described in The Wiley-Encyclopedia of Packaging Technology, Second Edition, A. L. Brody and K. S. Marsh, Ed., John Wiley and Sons, Inc., New York (1997).
• chill roll casting is one example, other forms of casting may be employed.
• blends can be made using a BRABENDER® 3 Zone Electric Mixer (dry) (such as at 200°C for 5 min at a mixer speed of 80 rpm). After mixing, the polymer blend is then molded into films by compression molding (such as at 177°C) to obtain the target value, such as 3 mil).
• dry such as at 200°C for 5 min at a mixer speed of 80 rpm.
• the polymer blend is then molded into films by compression molding (such as at 177°C) to obtain the target value, such as 3 mil).
• the films can be of any desirable thickness or composition.
• films are within a range of from about 0.5 mil to about 20 mils, such as from about 1 mils to about 15 mils, such as from about 2 mils to about 10 mils, for example about 6 mils.
• the films can include other additives such as pigments, antioxidants, fillers, etc.
• the films of the present disclosure have a combination of unique and useful properties as described in more detail below.
• the present disclosure relates to a film including, for example, at least 5 wt% of the cyclic olefin copolymers (e.g., both 1 ST COC and 2 ND COC) based on the total weight of the film.
• a film can have a cyclic olefin copolymer content of from about 5 wt% to about 99.9 wt%, such as from about 10 wt% to about 30 wt%, alternatively from about 90 wt% to about 99.9 wt%.
• the present disclosure relates to films comprising semicrystalbne cyclic olefin copolymer, amorphous cyclic olefin copolymer and semicrystalbne olefin (linear or branched) copolymer having:
• melt index from about 0.05 g/lOmin to about 2.5 g/lOmin
• melt index ratio of about 25 to 70;
• a 1% Secant Modulus of from about 60,000 psi or greater, such as from about 60,000 psi to about 130,000 psi;
• a Tensile strength of from about 3,500 psi or greater, such as from about 3,500 psi to about 130,000 psi;
• an Elongation at Break of from about 80% or greater, such as from about 80% to about 320%;
• an average Water Vapor Transmission rate of from about 1 gm/[m 2 -day] or greater, such as from about 1 gm/[m 2 -day] to about 3 gm/[m 2 -day];
• a Normalized Peak Puncture Force of from about 5,000 g/mm or greater, such as from about 5,000 g/mm to about 10,000 g/mm;
• a Puncture Break Energy of from about 7,000 mm-g/mm or greater, such as from about 7,000 mm-g/mm to about 17,000 mm-g/mm.
• films of the present disclosure can have excellent heat sealing and hot tack performance.
• a film can have a hot tack strength of from 2 (N/25.4 mm) to 18 (N/25.4 mm) at a temperature of 125°C, such as from about 10 (N/25.4 mm) to about 13 (N/25.4 mm).
• Hot tack is the strength of a heat seal immediately after sealing, while still in a hot condition, that is, before it has cooled down to ambient temperature and achieved its final strength.
• the package In production lines, the package is often filled by dropping the product into the package from a certain height, or by horizontally filling, both of which will exert a force on the package bottom. If the package bottom cannot resist the disruptive force of filling, the seal on the bottom of the package will fail.
• the interval between heat-sealing the film to make the package and filling the package with product is very short, and it is usually not possible for seal completely cool before filling. Accordingly, hot tack strength becomes important.
• Films of the present disclosure can have a heat seal strength of from about 2 lbs to 16 lbs at a seal bar temperature of 130°C, such as from about 4 lbs to about 12 lbs, such as from about 6 lbs to about 9 lbs.
• the films may have a seal initiation temperature so that it is suitable for packaging applications, such as food packaging.
• Suitable seal initiation temperature (“SIT") may depend on the end use application of the film, for example, for chocolate bars the SIT may be the temperature at which the seal strength is 200 g/inch, for potato chips in the United States the desired SIT may be the temperature at which the seal strength is 500 g/inch, and for potato chips in Asia the SIT may be the temperature at which the seal strength is 1,000 g/inch).
• the SIT may also depend on the type of seal used, for example, a fin seal as compared to a crimp seal.
• the films prepared from the semicrystalline cyclic olefin copolymer, amorphous the cyclic olefin copolymer and the semicrystalline olefin (linear or branched) copolymer have a good balance of stiffness versus toughness as indicated by machine direction tear strength (MD Elmendorf Tear), 1% Secant Modulus (MD), and dart drop impact strength performance (Dart Impact), as well as good shrink performance and excellent optical properties. Furthermore, films prepared from the cyclic olefin copolymers display high clarity property and superior melt strength.
• the films have a 1% Secant Modulus in the machine direction (1% Secant Modulus MD), reported in pounds per square inch (psi), measured according to ASTM D882-95a, of 20,000 psi or greater, such as from about 20,000 psi to about 75,000 psi, such as from about 20,500 psi to about 70,000 psi, such as from 20,000 psi to 40,000 psi, alternatively from about 40,000 psi to about 55,000 psi, such as from about 22,000 psi to about 50,000 psi.
• 1% Secant Modulus MD reported in pounds per square inch (psi), measured according to ASTM D882-95a, of 20,000 psi or greater, such as from about 20,000 psi to about 75,000 psi, such as from about 20,500 psi to about 70,000 psi, such as from 20,000 psi to 40,000 psi, alternatively from about 40,000
• the films may have an MD Elmendorf Tear, as measured by ASTM D 1922-94, of 15 g/mil or greater.
• the films have an MD Elmendorf Tear of from about 15 g/mil to about 350 g/mil, such as from about 17 g/mil to about 300 g/mil, such as from about 20 g/mil to about 150 g/mil, alternatively from about 150 g/mil to about 225 g/mil.
• the films may have a Dart Impact, as measured according to ASTM D 1709-91 (Method A), of from about 75 g/mil to about 750 g/mil, such as from about 80 g/mil to 250 g/mil, alternatively from about 250 g/mil to about 450 g/mil.
• a Dart Impact as measured according to ASTM D 1709-91 (Method A)
• ASTM D 1709-91 Method A
• the film has a total haze, as measured according to ASTM D1003, of from about 1% to about 25%, such as from about 3% to about 20%, such as from about 3% to about 15%, such as from about 3% to about 12%, such as from about 3% to about 10%.
• the films may have an internal haze, as measured according to ASTM D1003, of from about 1% to about 10%, such as from about 1% to about 8%, such as about 1% to about 6%. Internal haze is the haze excluding any film surface contribution.
• the film surfaces are coated with ASTM approved inert liquids to eliminate any haze contribution from the film surface topology.
• the films have a Gloss 45° MD, as measured according to ASTM D2457-90, of from about 3 to about 30, such as from about 5 to about 28, such as from about 6 to about 15, alternatively from about 15 to about 24.
• the films described can be used as shrink films, and in a particular embodiment, shrink films in which the transverse direction (“TD”) of the film heat-shrinks to a greater extent than in the machine direction (“MD”) of the films. Also, the films described undergo TD shrinkage of greater than 40%, such as 50% at desirably low temperatures; at less than 130°C in one embodiment, and at less than 125°C in another embodiment, and at less than 120°C in yet another embodiment, and at less than 110°C in yet another embodiment.
• TD shrinkage of greater than 40%, such as 50% at desirably low temperatures; at less than 130°C in one embodiment, and at less than 125°C in another embodiment, and at less than 120°C in yet another embodiment, and at less than 110°C in yet another embodiment.
• the TD shrinkage is greater than 40%, such as 50% at a given temperature of from 110°C to 115°C, or 120°C, or 125°C, while the MD shrinkage is less than 10% or 15% at a given temperature at the same temperature ranges. In another embodiment, the TD shrinkage is greater than 40%, such as 50% at 121°C, while the MD shrinkage is less than 10% or 15% at the same temperature.
• the thermal shrinkage is determined according to ASTM D2732.
• the films may have an MD shrink of from about 25% to about 75%, such as from about 30% to about 55%, such as from about 30% to about 40%; and a puncture at break energy, as measured according to ASTM D5748, of from about 5 in-lbs/mil to about 25 in-lbs/mil, such as from about 11 in-lbs/mil to 22 in-lbs/mil, such as from about 12 in-lbs/mil to about 17 in-lbs/mil.
• the films of the present disclosure can have an excellent "drawability", which is the melt strength of the polymer used to make the blown film and is the ratio of the die gap to film gauge after the polymer is drawn out into a film.
• the films can be made with gauges of 0.5 mil, 0.75 mil, 1 mil, or 3 mil from a melt extruded using a 60 mil die gap. A higher drawability or "Draw" is desirable. In at least one embodiment, the total draw of the films prepared from the cyclic olefin copolymers is 20 or greater, such as 60 or greater, such as 80 or greater, such as 120 or greater.
• the films of the present disclosure can possess an excellent balance of mechanical properties, toughness, sealability and cling/ adhesive properties.
• the films can be used in hot fill applications or packaging materials heated at temperatures up to 260°F (126°C) during packaging, such as cement, sand, salt, and retort bag applications such as pouches, bags and sacks containing consumer products including food.
• the films can also be used for shrink films and form fill and seal applications requiring abuse resistance.
• the films also possess good softness/feel and exceptional optical/clarity properties useful for food packaging at any temperature.
• copolymers described herein will find utility in other applications like, but not limited to: extrusion coating, injection molding, rotomolding, and blow molding applications.
• films of the present disclosure may vary in thickness depending on the intended application; however, films of a thickness from 10 pm to 50 pm can be suitable for use as, for example, packaging and or as a sealing layer. There may be a sealing layer on both the inner and outer surfaces of the film or the sealing layer may be present on only the inner or the outer surface.
• One or more layers can be modified by corona treatment, electron beam irradiation, gamma irradiation, flame treatment, or microwave.
• one or both of the surface layers is modified by corona treatment.
• End uses include polymer products and products having specific end-uses.
• Exemplary end uses are films, film-based products, diaper back sheets, house wrap, wire and cable coating compositions, articles formed by molding techniques, e.g., injection or blow molding, extrusion coating, foaming, casting, and combinations thereof.
• End uses also include products made from films, e.g., bags, packaging, and personal care films, pouches, medical products, such as for example, medical films and intravenous (IV) bags.
• This invention further relates to:
• a blend comprising:
• an amorphous cyclic olefin copolymer comprising more than 25 wt% of a C5-C40 cyclic olefin comonomer and less than 75 wt% of a C2-C40 linear and/or branched olefin monomer having a density greater than L0 g/cm 3 , a modulus of 260-380 kpsi, an elongation at break of ⁇ 4%, and a glass transition temperature of 54 to 138°C; and
• a semicrystalline olefin copolymer comprising C2-C40 monomers having a density of about 0.90 g/cm 3 to about 0.96 g/cm 3 , a modulus less than 150 kpsi, an elongation at break of greater than 400%, and a glass transition temperatures less than -32°C.
• a film comprising the copolymer of any of paragraphs 1 to 10.
• MI Melt Index
• I21 High Load Melt Index
• Melt index ratio is defined as the ratio of HLMI to MI.
• Density was measured as specified by ASTM D-1505 using chips cut from plaques compression molded in accordance with ASTM D-4703-07, aged for 40 hrs at 23°C plus or minus 2°C, unless specifically stated otherwise.
• Melt Strength is defined as the force required to draw a molten polymer extrudate at a rate of 12 mm/s 2 and at an extrusion temperature of 190°C until breakage of the extrudate whereby the force is applied by take up rollers.
• the polymer was extruded at a velocity of 0.33 mm/s through an annular die of 2 mm diameter and 30 mm length.
• Melt strength values reported herein were determined using a Gottfert Rheotens tester and were reported in centi- Newtons (cN). Additional experimental parameters for determining the melt strength are listed in the table below. For the measurements of melt strength, the resins were stabilized with 500 ppm of Irganox TM 1076 and 1500 ppm of Irgafos TM 168.
• Peak melting point, Tm, (also referred to as melting point or melting temperature), peak crystallization temperature, Tc, (also referred to as crystallization temperature), glass transition temperature (Tg), heat of fusion (DHG or Hi), and percent crystallinity were determined using the following DSC procedure according to ASTM D3418-03.
• Differential scanning calorimetric (DSC) data were obtained using a TA Instruments model Q200 machine. Samples weighing approximately 5mg to 10 mg were sealed in an aluminum hermetic sample pan. The DSC data were recorded by first gradually heating the sample to 200°C at a rate of 10°C/minute.
• the sample was kept at 200°C for 2 minutes, then cooled to -90°C at a rate of 10°C/minute, followed by an isothermal for 2 minutes and heating to 200°C at 10°C/minute. Both the first and second cycle thermal events were recorded. Areas under the endothermic peaks were measured and used to determine the heat of fusion and the percent of crystallinity. The percent crystallinity was calculated using the formula, [area under the melting peak (Joules/gram) / B (Joules/gram)] * 100, where B is the heat of fusion for the 100% crystalline homopolymer of the major monomer component.
• the DSC was performed with TA Instruments’ Discovery 2500 using the following
• the 13 C-NMR was performed on a 10 mm broadband probe using a field of at least 400 MHz in tetrachloroethane-d2 solvent at 120°C with a flip angle of 90° and full NOE with decoupling.
• Sample preparation (polymer dissolution) was performed at 140°C where 0.20 grams of polymer was dissolved in an appropriate amount of solvent to give a final polymer solution volume of 3 ml.
• Chemical shifts were referenced by setting the ethylene backbone (-CH2-)n (where n>6) signal to 29.98 ppm.
• Carbon 13 NMR spectroscopy was used to measure the composition of the reactor products as submitted.
• E-NB ethylene-norbomene copolymer
• Copolymer samples were dissolved at a concentration of 66mg/mL in 1, 1,2,2- tetrachloroethane-d213C NMR spectra were obtained on a Bruker Avance IIIHD 600 NMR spectrometer operating at 600MHz and 150MHz, respectively. Spectra were recorded using a 13C optimized 10mm high temperature cryoprobe at 120°C. 13C ⁇ 1H ⁇ gated composite pulse decoupling was used with a biwaltz65-256 decoupling scheme, a 90° pulse, with a 10 second recycle delay, and 512 transients.
• Mw, Mn and Mw/Mn are determined by using a High Temperature Gel Permeation Chromatography (Agilent PL-220), equipped with three in-line detectors, a differential refractive index detector (DRI), a light scattering (LS) detector, and a viscometer. Experimental details, including detector calibration, are described in: T. Sun, P. Brant, R. R. Chance, and W. W. Graessley, Macromolecules, Volume 34, Number 19, pp. 6812-6820, (2001) and references therein. Three Agilent PLgel 10pm Mixed-B LS columns are used.
• the nominal flow rate is 0.5 mL/min, and the nominal injection volume is 300 pL.
• the various transfer lines, columns, viscometer and differential refractometer (the DRI detector) are contained in an oven maintained at 145°C.
• Solvent for the experiment is prepared by dissolving 6 grams of butylated hydroxy toluene as an antioxidant in 4 liters of Aldrich reagent grade 1,2,4- trichlorobenzene (TCB). The TCB mixture is then filtered through a 0.1 pm Teflon filter. The TCB is then degassed with an online degasser before entering the GPC-3D.
• Polymer solutions are prepared by placing dry polymer in a glass container, adding the desired amount of TCB, then heating the mixture at 160°C with continuous shaking for about 2 hours. All quantities are measured gravimetrically.
• the TCB densities used to express the polymer concentration in mass/volume units are 1.463 g/ml at room temperature and 1.284 g/ml at 145°C.
• the injection concentration is from 0.5 to 2.0 mg/ml, with lower concentrations being used for higher molecular weight samples.
• Prior to running each sample the DRI detector and the viscometer are purged. Flow rate in the apparatus is then increased to 0.5 ml/minute, and the DRI is allowed to stabilize for 8 hours before injecting the first sample.
• the LS laser is turned on at least 1 to 1.5 hours before running the samples.
• the concentration, c, at each point in the chromatogram is calculated from the baseline-subtracted DRI signal, I DR[ . using the following equation:
• K DRI is a constant determined by calibrating the DRI
• (dn/dc) is the refractive index increment for the system.
• Units on parameters throughout this description of the GPC-3D method are such that concentration is expressed in g/cm 3 , molecular weight is expressed in g/mole, and intrinsic viscosity is expressed in dL/g.
• the LS detector is a Wyatt Technology High Temperature DAWN HELEOS.
• M molecular weight at each point in the chromatogram is determined by analyzing the LS output using the Zimm model for static light scattering (M.B. Huglin, LIGHT SCATTERING FROM POLYMER SOLUTIONS, Academic Press, 1971):
• AR(0) is the measured excess Rayleigh scattering intensity at scattering angle Q
• c is the polymer concentration determined from the DRI analysis
• a 2 is the second virial coefficient
• R(q) is the form factor for a monodisperse random coil
• K 0 is the optical constant for the system:
• N A is Avogadro’s number
• (dn/dc) is the refractive index increment for the system, which take the same value as the one obtained from DRI method.
• a high temperature Viscotek Corporation viscometer which has four capillaries arranged in a Wheatstone bridge configuration with two pressure transducers, is used to determine specific viscosity.
• One transducer measures the total pressure drop across the detector, and the other, positioned between the two sides of the bridge, measures a differential pressure.
• the specific viscosity, p s for the solution flowing through the viscometer is calculated from their outputs.
• the intrinsic viscosity, [h] at each point in the chromatogram is calculated from the following equation:
• s C[T
• the branching index (g' v is) is calculated using the output of the GPC-DRI-LS-VIS method as follows.
• the average intrinsic viscosity, [p] avg , of the sample is calculated by:
• the branching index g' vjs is defined as: g vis
• Gauge reported in mils, was measured using a Measuretech Series 200 instrument. The instrument measures film thickness using a capacitance gauge. For each film sample, ten film thickness data points were measured per inch of film as the film was passed through the gauge in a transverse direction. From these measurements, an average gauge measurement was determined and reported.
• Tensile properties including tensile strength, at 100% (200%, 300%, 400%, 500%, 600%, 700%, 800%, etc.) elongation, stress and strain at the primary yield point, stress and strain at the secondary yield point, 1% Secant modulus, tensile strength at yield, tensile strength at break, ultimate tensile strength, elongation at yield, elongation at break, yield stress, and strain hardening were measured as specified by ASTM D-882.
• Dart Impact also known as Dart F50, or Dart Drop Impact or Dart Drop Impact Strength
• ASTM D-1709 Method A
• Haze both internal and total reported as a percentage (%), was measured as specified by ASTM D1003.
• Gloss a dimensionless number, was measured as specified by ASTM D-2457 at 45°.
• 1% secant modulus and tensile properties were determined by ASTM D882-10, with the following modifications: a jaw separation of 5 inches and a sample width of 1-inch is used.
• the index of stiffness of thin films is determined by manually loading the samples with slack and pulling the specimen at a rate of jaw separation (crosshead speed) of 0.5 inches per minute to a designated strain of 1%. Added manually loading samples with slack due to ASTM requiring an automated program. The calculation procedures are determined as following:
• Yield point is the first point in which there is an increase in strain (elongation) and none in stress (force). The yield is determined by a 2% off-set method.
• 1% secant modulus is measured of the material stiffness and is calculated as a function of the total force at 1% extension, divided by the cross-sectional area times 100 and reported in PSI units.
• 1% Secant Modulus Load at 1% Elongation / (Average Thickness (Inches) x Width) x 100.
• the puncture tests were performed on all the samples with a 1mm micro-puncture test probe at a rate of 20 mm/min instead of a rate of lOin/min with the traditional puncture probe.
• the micro-puncture test was needed mainly because the pure component of LCOC and the blends at 25 wt% and 50 wt% caused the clamp strength to fail when the traditional puncture probe at a rate of 10 in/min was used. This resulted in slipping from the clamp, compromising the test area and preventing the probe from breaking through the film.
• the use of the micro puncture test probe allowed to have a film area of 0.79cm2 versus a traditional area of 50.24cm2.
• WVTR Water vapor transmission rate
• Oxygen transmission rate was performed on a MOCON Ox-Tran 2/21 from MOCON, Inc. using ASTM D3985 at 23°C ⁇ 0.5°C where samples are also loaded without specific orientation.
• WAXS wide-angle X-ray scattering
• SAXS small-angle X-ray scattering
• Samples were mounted flat on a multi-sample stage with their machine direction vertical. The system was calibrated with LaB6 for sample-detector distance and instrumental broadening in WAXS and AgBeh for sample-detector distance in SAXS. Sample thickness was also measured and the scattered intensity was scaled to absolute units (cm-1). Scattering patterns were collected on a DECTRIS Pilatus 300K area detector under vacuum.
• the imaging on both AFMs was performed with free air amplitudes and set-points so as to maintain a net repulsive tip-sample interaction.
• the data channels monitored were “Phase” and“Amplitude” at the first eigenmode and“Phase” and“Amplitude” at the second eigenmode and also“Height” for bimodal imaging and“Phase” and“Height” at the first eigenmode for TappingModeTM.
• the samples were cut to fit into AFM holders and then cyro- microtomed in the bulk area prior to scanning at -120°C. All samples were purged under N2 in a desiccator before AFM imaging.
• Phase data is a measure of the hardness of a surface where darker (purple) portions are harder and lighter (yellow) portions are softer. Without being limited by theory, it is believed that the harder portions of the“Phase” data are the COC and softer (yellow) areas are PE structures.
• ExceedTM 1018 resin is an ethylene and 1 -hexene copolymer available from ExxonMobil Chemical Company having: a density of 0.918 g/cm 3 (ASTM D1505); a melt index of 1 g/10 min (ASTM D1238; 190°C, 2.16 kg); and a Peak Melting Temperature of 119°C.
• EnableTM2010HA resin is an ethylene and 1-hexene copolymer available from ExxonMobil Chemical Company having: a density of 0.921 g/cm 3 (ASTM D1505); a melt index of 1 g/10 min (ASTM D1238; 190°C, 2.16 kg); and a Peak Melting Temperature of 114°C.
• EXP-605TM polyethylene is an ethylene and 1 -hexene copolymer available from
• ExxonMobil Chemical Company having: a density of 0.940 g/cm 3 ; a tensile strength at yield (MD) of 19.3 MPa and (TD) of 22.8 MPa; a tensile strength at break (MD) of 64.8 MPa and (TD) of 44.1 MPa; and elongation at break (MD) of 504% and (TD) of 44.1 MPa; a 1% secant modulus (MD) of 572 MPa and (TD) of 800 MPa; a Haze of 23% and Gloss (45°) of 25; a melt index (MI) of 0.2 g/10 min; a melt index ratio (HLMI/MI) of 75.
• EXP-605TM polyethylene is also referred to“example 13” herein.
• IrganoxTM 1076 is an antioxidant available from Ciba Specialty Chemicals Corporation, Tarrytown, NY.
• Irgafos 168TM is an antioxidant available from Ciba Specialty Chemicals Corporation, Tarrytown, NY.
• TOP AS 8007 is an ethylene-norbomene copolymer having 65 wt% norbomene content available from Topas Advanced Polymers/Polyplastics. Ethylene-norbomene Copolymerization.
• the ethylene-norbomene copolymers were produced in a continuous stirred tank reactor system.
• a 1 -liter autoclave reactor was equipped with a stirrer, a pressure controller, and a water cooling/steam heating element with a temperature controller.
• the reactor was operated in liquid fill condition at a reactor pressure in excess of the bubbling point pressure of the reactant mixture, keeping the reactants in liquid phase.
• Isohexane was pumped into the reactors by Pulsa feed pumps.
• Norbomene was dissolved in toluene at a concentration of about 85 wt% and the solution was then fed into reactor using a metering pump. All flow rates of liquid were controlled using Coriolis mass flow controller (Quantim series from Brooks).
• Ethylene and Eh flowed as a gas under its own pressure through a Brooks flow controller.
• Monomers e.g., ethylene and norbomene
• Eh feeds were combined into one stream and then mixed with isohexane stream. The mixture was then fed to the reactor through a single line.
• Scavenger solution was also added to the combined solvent and monomer stream just before it entered the reactor to further reduce any catalyst poisons.
• Catalyst solution was fed to the reactor using an ISCO syringe pump through a separated line.
• Isohexane used as solvent
• monomers e.g., ethylene and norbomene
• Toluene used for the preparation of the catalyst solutions was purified by the same technique.
• the polymer produced in the reactor exited through a back pressure control valve that reduced the pressure to atmospheric. This caused the unconverted monomers in the solution to flash into a vapor phase which was vented from the top of a vapor liquid separator.
• the liquid phase including mainly polymer and solvent, was collected for polymer recovery.
• the collected samples were first air-dried in a hood to evaporate most of the solvent, and then dried in a vacuum oven at a temperature of about 90°C for about 12 hours. The vacuum oven dried samples were weighed to obtain yields.
• the detailed polymerization process conditions and some characteristic properties are listed in Table 2.
• the scavenger feed rate was adjusted to adjust the catalyst efficiency, and the feed rate varied from 0 (no scavenger) to 15 pmol/min.
• the catalyst feed rates were also adjusted according to the level of impurities in the system to reach the targeted conversions listed. All the reactions were carried out at a pressure of about 2.4 MPa/g unless otherwise mentioned.
• Table 1 illustrates the norebomene content evaluated by 13 C NMR, as well as the MI and HLMI for six ethylene-norbomene copolymers (Examples 1-6) produced using the polymerization procedure as explained above.
• Examples 5 and 6 had the lowest content of NB (1.7 mol%), whereas Example 2 contained no more than 4.0 mol% (12.1 wt%) of NB.
• Example 2 had the lowest MI value of 0.2 g/lOmin, whereas Example 1 (3.7 mol% of NB) holds the highest MI (1.7 g/lOmin) and HLMI (41.9 g/min).
• the films made from the ethylene-norbomene copolymers had desirable processability superior to that of ExceedTM 1018 and EXP-605 (Example 13).
• the films also demonstrated superior bubble stability, superior MD tear resistance, and superior impact resistance when compared to ExceedTM 1018 and EXP-605 (Example 13).
• Table 4
• Table 5 illustrates some films properties.
• the blown films were found to be anisotropic.
• the blown films were compression molded in order to relax the stress in the film, thus forming a stress free sample.
• the stress free samples were then evaluated accordingly and illustrated in Table 6. Table 5
• FIG. 1A is a graph illustrating an extensional viscosity plot of pull-off force (melt strength) as a function of draw ratio of the cyclic olefin copolymer compositions.
• FIG. 2A is a graph illustrating a comparison of the elongational viscosity of the cyclic olefin copolymer compositions.
• FIGS. 1 A and 2A show that the ethylene-norbomene copolymers of Example 2 (4 mol% NB) has a melt strength and elongational viscosity greater than those of Examples 6A, 6B, 3, 5 and 1, but less than that of Example 4 (3 mol% NB).
• FIG. IB is a graph illustrating an extensional viscosity plot of pull-off force (melt strength) as a function of draw ratio of Exceed 1018
• FIG. 2B is a graph illustrating the elongational viscosity of Exceed 1018.
• FIGS. IB and 2B show that Examples 1 and 5 present comparable melt strengths and elongational viscosity as compared to the melt strength and elongational viscosity of Exceed 1018.
• the films exhibited improved heat seal performance and hot tack performance when compared with films made from 100 wt% ExceedTM 1018 and EXP-605 (FIGS. 3A, 3B, 4A, and 4B).
• Cyclic olefin copolymers produced heat-seal films having similar or lower seal initiation temperatures and improved hot-tack performance when compared to
• Example 3 exhibits similar heat seal performance and improved hot tack performance as compared to films made from 100 wt% of ExceedTM 1018 (FIGS. 3A and 4A; Table 6).
• FIGS. 4A and 4B are graphs illustrating a comparison of the hot tack performance of cyclic olefin copolymers to comparative commercial polymer, ExceedTM 1018. All data points are reported in Table 7 with seal conditions as follows:
• the films were evaluated for their uniformity and clarity using standard photographic techniques.
• a 3 mil ExceedTM 1018 film with a Haze of 20.1 % was compared to a 3 mil ethylene-norbomene copolymer-based film (Example 5) with a Haze of 7.8% via Full Field Birefringence Image Analysis. Images showed the exceptional clarity of the ethylene- norbomene copolymer-based film (Example 5a) containing only 1.7 mol% of NB.
• the semi crystalline cyclic olefin copolymer (1 ST COC) used in Experiment Set II is Example 2 from Tables 1 and 2 above.
• the amorphous cyclic olefin copolymer (2 ND COC) used in Experiment Set II is TOP ASTM 8007.
• the semicrystalline olefin copolymer (PE) used in Experiment Set II is EnableTM2010HA.
• the blends were compression molded into thin films ( ⁇ 3mil) and the films were evaluated for their mechanical, optical and barrier properties (puncture, tensile and elongation, optics, OTR and WVTR tests). The samples were also investigated for their microstructure by microscopy and X-ray (phase morphology, miscibility, crystallite size and long period length).
• the blends were made using a BRABENDER® 3 Zone Electric Mixer (dry) at 200°C for 5 min at a mixer speed of 80 rpm. After mixing, the polymer blend was molded into films by compression molding at 177°C. Samples were pressed for 3 min with a low pressure -3,500 tons and followed by 30 min at a higher pressure of -25,000 tons. The heat was removed at 15C°/min under pressure of -25,000 tons. Films with a thickness greater than 3 mil were compression molded a second time under identical conditions to obtain the target value of 3 mil. For comparison purposes, compression molded films of the pure resins were similarly prepared and evaluated.
• the blends’ long period value decreases with an increase in the l ST COC content up to about 25 wt%.
• the blends’ long period is constant at l ST COC content of 25 wt% and 50 wt%. This is likely related to the phase inversion that occurs near this loading, as also evidenced in AFM analysis. While the 2nd COC is entirely amorphous, is does show a small low-q scattering peak most likely due to a small amount of PE.
• WAXS wide angle X-ray scattering
• the particle diameter of the PE in the COC matrix is on the range of 2-3 pm with a rather broad particle diameter distribution for blends containing up to 10 wt% loading of the l ST COC resin.
• the blend morphology changes. Further, the COC particles seem to stratify indicating the l ST COC improved the miscibility of the PE and 2 ND COC resins.
• the AFM analysis supports the X-ray data where at high loadings of l ST COC the miscibility is improved and the crystal size decreases as shown by the average long period length and crystallite size values.
• Table C Film performance of all the samples
• Table D Melting temperature, heat fusion and degree of crystallinity of the pure components and blends
• Table F WAXS 110 and 200 crystallite size
• ranges from any lower limit may be combined with any upper limit to recite a range not explicitly recited, as well as, ranges from any lower limit may be combined with any other lower limit to recite a range not explicitly recited, in the same way, ranges from any upper limit may be combined with any other upper limit to recite a range not explicitly recited.
• ranges from any upper limit may be combined with any other upper limit to recite a range not explicitly recited.
• within a range includes every point or individual value between its end points even though not explicitly recited. Thus, every point or individual value may serve as its own lower or upper limit combined with any other point or individual value or any other lower or upper limit, to recite a range not explicitly recited.
• compositions, an element or a group of elements are preceded with the transitional phrase “comprising,” it is understood that we also contemplate the same composition or group of elements with transitional phrases“consisting essentially of,”“consisting of,”“selected from the group of consisting of,” or“is” preceding the recitation of the composition, element, or elements and vice versa.

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