Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
  • C08L23/12—Polypropene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
  • C08L23/14—Copolymers of propene
  • C08L23/142—Copolymers of propene at least partially crystalline copolymers of propene with other olefins
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
  • C08L23/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2205/00—Polymer mixtures characterised by other features
  • C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group

Definitions

• the present invention relates to films made from blends of thermoplastic polymer materials which have improved properties. More particularly, the present invention relates to films made from blends of a propylene polymer, a butylene polymer with a low melt index and a butylene polymer with a high melt index which are heat shrinkable and which have good clarity and good processability.
• Thermoplastic blends for films are used as packaging material, and in the area of shrink packaging, for objects that are packaged in thermoplastic shrink film.
• Shrink film is used in many applications, for example, for many types of packaging and wrapping articles such as toys, sporting goods, stationary, greeting cards, hardware, household products, office supplies and forms, phonograph records, industrial parts, computer floppy diskettes, and photo albums, etc. Heat is applied to the film and the film shrinks to conform to the shape of the article packaged therein.
• thermoplastic films shrink to some extent if they are subjected to elevated temperatures. Use is made of this characteristic by subjecting objects packaged in such films for a short time to elevated temperatures, e.g. exposing them to a blast of heated air, or by immersing in boiling water so that the film shrinks, thereby tightly enclosing the objects packaged therein.
• films fabricated from polyolefins or irradiated polyolefins are examples.
• a film should exhibit a high shrink energy or contractile force when exposed to elevated temperatures.
• the film should not only be heat shrinkable but have good clarity and be easily processed.
• a shrink film should possess the following specific properties:
• the shrink force should be between 100 and 400 grams per inch at 100° C. depending on the objects to be encased.
• the percent shrinkage should be between 10 and 50% at 121° C. depending on the objects to be encased.
• the modulus should be between 60,000 and 350,000 psi depending upon the objects to been encased.
• machinability the coefficient of friction should be less than 0.5.
• tear strength should be as high as possible; typical is 3 to 15 grams per mil of film thickness and per inch of width.
• elongation should be between 50 and 150% depending on the objects to be encased.
• Films may be oriented or unoriented. Oriented films may be obtained by stretching processes in which tensions capable of stretching the film are applied to the film, the directions of which form an angle of about 90° utilizing well known prior art techniques. These film stretching tensions may be applied sequentially, as in the case of the film, after forming, is subjected to stretching in a longitudinal direction and thereafter tension is applied in a transverse direction to stretch the film transversely, or simultaneously, whereby longitudinal and transverse tensions are applied to the film at the same time resulting in a simultaneous longitudinal and transverse stretching of the film.
• U.S. Pat. No. 3,900,534 discloses a biaxially oriented thermoplastic film structure formed from a blend comprising polypropylene and polybutene homopolymers where the polybutene is present in a small amount of more than 10% but less than 20% by weight.
• U.S. Pat. No. 3,634,553 discloses a heat shrinkable oriented thermoplastic film which comprises a blend of polypropylene and an ethylene/butene-1 copolymer.
• European Patent Applications 145,014A discloses a blend of a random copolymer of propylene and an alpha olefin with 4 or more carbon atoms (i.e. perhaps butene-1), where the alpha olefin content in the copolymer is 8 to 30 mole % (m %).
• Multilayers may include three layers (propylene-ethylene plus butene-1-ethylene plus ethylene-propylene rubber)/tie layer/linear low density polyethylene (LLDPE) by Union Carbide, U.S. Pat. No. 4,196,240 (1980) for frozen poultry and U.S. Pat. No. 4,207,363 (1980) for primal meat cuts. Three layers of propylene-ethylene/(EVA+butene-1-ethylene)/propylene-ethylene, U.S. Pat. No. 4,194,039 (1980) is known. Also three layers (polyproylene+polybutylene)/EVA/irradiated EVA by Cryovac, U.S. Pat. No. 3,754,063 (1973), U.S. Pat. No. 3,932,274 (1974 ), and U.S. Pat. No. 3891,008 (1975) for turkey bags are known.
• LLDPE linear low density polyethylene
• Polyvinyl chloride has been used to produce good shrink films.
• PVC has been shown to be better in certain applications than the use of polyolefins such as propylene polymers.
• the use of polyolefins in shrink wrap results in a moderate to high shrink force which is undesirable in many applications.
• the use of polyolefins allows the use of high speed automated packaging machinery with lower cost, and less corrosion of equipment.
• PVC may produce a better looking package because of the low shrink force and better optics.
• the seal and shrink of PVC films may take place over a much broader temperature range and tear strength may be better.
• the polybutylene polypropylene polymer blend film of the present invention exhibits low shrink force which is adjustable by the blending ratio, low shrink temperature, low stiffness, better optics, low corrosion, low cost, and can be used on high speed automated packaging machines.
• the new film composition may reduce the scraps generated at the stretching operation during the fabrication of biaxially oriented low shrink force shrink films.
• polypropylene, low melt flow polybutylene and high melt flow polybutylene may be blended producing a heat shrinkable oriented thermoplastic film having good clarity and good processability.
• the blend can be formed into a packaging film, sheet, or laminar structure which is shrinkable and has good clarity and good processability.
• the blend comprises from about 10% by weight to about 90% by weight preferably 30% to 70% and more preferably 40% to 60% of a polypropylene homopolymer or copolymer, from about 10% by weight to about 90% by weight preferably 30% to 70% and more preferably 40% to 60% of a low melt index polybutylene homopolymer or copolymer and from 0.5% by weight to about 10% by weight preferably 2% to 8% and more preferably 4% to 6% of a high melt index polybutylene homopolymer or copolymer.
• the high melt index poly-1-butene referred to herein is a butene-1-polymer containing at least about 90%, preferably at least about 95%, ad more preferably about 97%, by weight of isotactic portions.
• isotactic poly-1-butenes having a low molecular weight, e.g. less than about 280,000 as determined by solution viscosity in "Decalin" (decahydronaphthalene).
• Usable poly-1-butenes have a density of 0.900-0.925, preferably 0.905-0.920 and especially 0.910-0.915.
• Usable poly-1-butenes have melt indices in the range of from 10 to 350, more preferably 20-300, and most preferably 100-200, as determined by ASTM D-1238 Condition E, at 190° C.
• the intrinsic viscosity of the polybutylene may range from about 0.03 to about 0.20 preferably from about .06 to about 0.11 at 130° C.
• the Brookfield melt viscosity is greater than 20,000 CPS at 200° C., preferably greater than 25,000 CPS at 200° C., most preferably greater than 35,000 CPS at 200° C.
• the low melt index butene-1 polymers referred to herein are substantially polybutene-1 containing at least 95%, preferably 97%, and most preferably 98% by weight of isotactic portions.
• Suitable polybutenes have a density of 0.914-0.919 and a melt index of less than 20 g/10 min. at 190° C.
• Suitable polybutenes can be obtained, for example, according to Ziegler-Natta low pressure polymerization of butene-1 as disclosed in German Published Application No. 1,570,353.
• the butene-1 polymers (PB) usable herein are either butene-1 homopolymers or copolymers. If butene-1 copolymers are used, the non-butene comonomer content is preferably 1-30 mole % of either ethylene, propylene, or an alpha olefin having from 5 to 8 carbon atoms.
• Suitable poly-1-butenes can be obtained, for example, in accordance with Ziegler-Natta low-pressure polymerization of butene-1, e.g. by polymerizing butene-1 with catalysts of TiCl 3 or TiCl 3 ⁇ AlCl 3 and Al(C 2 H 5 ) 2 Cl at temperatures of 10°-50° C., preferably 20°-40° C., e.g. according to the process of German Published Application No. 1,570,353. High melt indices are then obtained by further processing the polymer by peroxide cracking.
• the polybutylene may be modified to increase surface activity by reaction with, for example, maleic anhydride or other functional group.
• Duraflex® PB8240 is a particularly suitable low melt index polybutylene having a melt index of 2.0 g/10 min. at 190° C. which is useful in the present blends and is available from Shell Chemical Company.
• Duraflex® DP0800 a developmental poly-1- butene polymer produced by Shell Chemical Company, of Houston, Tex. is a particularly suitable high melt index butene-1 polymer for use in the novel blend.
• This novel polymer is a homopolymer with a melt index of 200 and a molecular weight of 108,000.
• Duraflex® PB0400 a commerically available poly-1-butene polymer produced by Shell Chemical Company, is another high melt index polymer suitable for use in this invention.
• the polymer is a homopolymer with a melt index of 20 g/10 min. at 190° C. and 45 g/10 min. at 210° C. and a molecular weight of 202,000.
• the polypropylene used in the present invention is any crystallizable polypropylene.
• Said polypropylene can be prepared by homopolymerizing propylene irrespective of the method used so long as crystallizable polypropylene is formed.
• the preferred polypropylenes are the substantially isotactic polypropylenes prepared by the Ziegler/Natta or MgCl 2 -supported catalyst polymerization process.
• the propylene polymers usable herein can be either propylene homopolymers or copolymers. If propylene copolymers are used, they can be random or block copolymers with the comomoner content preferably 1-30 mole % of either ethylene, butene, or an alpha olefin having from 5 to 8 carbon atoms.
• Propylene polymers useful in the invention preferably have a melt index of less than 60, more preferably from about 1-15, as measured by ASTM D-1238, Condition L at 230° C.
• a particularly suitable propylene has a melt index of 3.2 and is available from Shell Chemical Company, of Houston, Tex. as PP5CO8.
• a preferred blend contains 5% by weight of a high melt index butene-1-homopolymer having a melt index of about 200 g/10 min., 47.5% by weight of a propylene homopolymer having a melt index of about 3.2 and 47.5% by weight of a low melt index butene-1 homopolymer having a melt index of less than 10.
• the blends may also contain additives and fillers, e.g. mold release agents, UV or thermal stabilizers, slip agents, antiblock agents, nucleating agents, pigments, antioxidants, or flame retardants.
• additives and fillers e.g. mold release agents, UV or thermal stabilizers, slip agents, antiblock agents, nucleating agents, pigments, antioxidants, or flame retardants.
• Blending of the components can occur by one of several methods, such as, dry tumble blending, masterbatch, or melt compounding techniques.
• the method of combining the ingredients of the formulation is important. For example, in most cases, it is desirable to use the least amount of energy to merge the components into an effective blend. Therefore, the preferred method of blending is dry blending the components in a powder form.
• the polymer and copolymer components of the film composition of the present invention are blended together to form a substantially homogeneous resin mixture. This may be accomplished, for example, by tumbling the mixture in a fiber drum. The tumble mixture is then melt compounded by an extruder having good mixing and pelletized thereafter. The blend is then extruded into a film utilizing a standard extruder and tubular on flat film die and is subsequently oriented utilizing any one of a number of prior art film orientation techniques.
• Various thicknesses of shrink film may be manufactured through utilizing a novel resin composition of the present invention.
• the thickness may generally vary from about 0.10 mil to about 5 mils and preferably from about 0.5 mil to about 2.0 mils.
• Blends were prepared from PP5C08, a polypropylene homopolymer having a melt index of 3.2, available from Shell Chemical Co. of Houston, Tex., Duraflex® PB8240 polybutylene, Duraflex® DP0800 polybutylene, and Duraflex® PB0400 polybutylene.
• Formulations 1-6 were prepared in the proportions given in Table II for testing.
• the formulations were prepared by drying tumbling the ingredients for about 1 control hour in a drum at room temperature.
• the dry tumbled blend was placed in a 11/4" single stage screw Brabender extruder, with the screw equipped with a mixing head.
• the compounding was run at a temperature between 420° F. and 450° F. and the mixture was given a residence time of about 5 control minutes in the extruder.
• the mixture was extruded into a strand, cooled and chopped into pellets using conventional techniques. Sheets were then prepared by the casting process using a sheet processing line using a Killion extruder.
• Sheet samples were drain using the conditions given in Table III below.
• the stretching conditions on the sheet were, Draw Speed--30 mm/sec, preheat time--3 minutes, and grip force--125-150 psi.
• Table IV shows the results of the stretching of the formulations on the T. M. Long Stretcher.
• the high melt index butene-1 polymer flows better than the low melt index material creating a film or article with good optical properties.
• the high melt flow material flows better to the surface of the film creating a higher value of glass than a low melt index polybutylene.
• the high melt index material fills the microvoids better than low melt index polybutylene with improved gloss and reduction of microvoids.
• the clarity and haze of the blends containing the high melt index material is improved when compared with those containing only the low melt flow polybutylene material.
• the high melt flow material usually acts as a better lubricant than a low melt flow polybutylene and consequently improves the processability of the material into film, thus reducing film breakage when compared with low melt flow polybutylene material.
• the present invention includes laminar structures, wherein the novel blend is disposed on a substrate, such as nylon or polyester or polycarbonate with or without an additional tie layer adhesive forming a laminate or laminar structure.

Landscapes

• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Crystallography & Structural Chemistry (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Manufacture Of Macromolecular Shaped Articles (AREA)
• Laminated Bodies (AREA)

Priority Applications (8)

Applications Claiming Priority (2)

Related Parent Applications (1)

Publications (1)

Family

ID=27061556

Family Applications (1)

Country Status (8)

Cited By (3)

Families Citing this family (4)

Citations (12)

Family Cites Families (4)

• 1991
  • 1991-02-25 US US07/659,814 patent/USH1213H/en not_active Abandoned
  • 1991-05-15 DE DE69104899T patent/DE69104899T2/de not_active Expired - Fee Related
  • 1991-05-15 EP EP91304358A patent/EP0457568B1/fr not_active Expired - Lifetime
  • 1991-05-15 AT AT91304358T patent/ATE113527T1/de not_active IP Right Cessation
  • 1991-05-16 CA CA002042809A patent/CA2042809C/fr not_active Expired - Fee Related
  • 1991-05-17 AU AU77168/91A patent/AU642017B2/en not_active Ceased
  • 1991-05-17 NZ NZ238182A patent/NZ238182A/en not_active IP Right Cessation
  • 1991-05-17 JP JP3113427A patent/JP3068882B2/ja not_active Expired - Lifetime

Patent Citations (13)

Also Published As

Similar Documents

Legal Events