JP2006052313A - Propylenic polymer and application to shrinkable film - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a shrinkable film which has a large heat shrinking factor, a small natural shrinking factor, and an excellent shrinkage balance, and to provide a propylenic polymer for the shrinkable film. <P>SOLUTION: This propylenic polymer satisfies all of requirements consisting of [1] a MFR (230°C, 2.16 kgf) of 0.05 to 8 (g/10 min), [2] a melting point of ≤140°C determined by DSC, and [3] a n-decane soluble content of ≤3 wt.%. The propylenic polymer is preferably a (co)polymer obtained by polymerizing or copolymerizing propylene or the propylene with a 2 to 20C α-olefin excluding the propylene in the presence of a specific metallocene catalyst. The propylenic polymer (or its composition blended with a petroleum resin) is suitably used for shrinkable films or shrinkable labels. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a propylene-based polymer and a molded product obtained therefrom, and more particularly to a polypropylene-based polymer (or composition) for shrink film and a shrink film or shrink label obtained therefrom.

  As materials widely used for shrink films, polypropylene resins, polyvinyl chloride resins, polystyrene resins, and the like are well known. Polypropylene resins have features such as light weight and good transparency, and polyvinyl chloride resins and polystyrene resins have features such as a high shrinkage rate and a large shrinkage rate. In recent years, environmental issues and recycling issues have become important, so the development of shrink films using polyolefin has attracted attention. Conventional shrink films made of polyolefin resin are inferior to those made of vinyl chloride resin in terms of heat shrinkage, dimensional deformation during storage of the film at room temperature, so-called natural shrinkage, and the like.

  In particular, this film often wraps containers of various shapes such as cup noodle wrapping, stacking wrapping, paper pack wrapping, and shrink labels for beverage PET bottles, and a shrink film having a high shrinkage rate is required. Shrinkage processing is often performed by hot air or steam in a shrink tunnel. Furthermore, it is required that the dimensional deformation during storage of the film at room temperature, that is, the so-called natural shrinkage rate is small.

  For example, JP 11-512756 A and JP 2002-363308 A disclose a polypropylene-based shrink film made of a metallocene catalyst.

However, the thermal shrinkage rate and the natural shrinkage rate are not necessarily sufficient. When trying to achieve a high thermal shrinkage ratio in a shrink film made of polyolefin such as polypropylene, the natural shrinkage ratio (a phenomenon that shrinks with time at room temperature (25 to 40 ° C.)) becomes large, and the film quality is hindered. For this reason, a shrink film having a good balance between heat shrinkage and natural shrinkage is desired.
Japanese Patent Publication No.11-512756 JP 2002-363308 A

  The present invention is based on a polypropylene-based resin for shrink film having a low n-decane soluble content and excellent transparency, and can be stretched at 100 ° C. or lower. The thus obtained film has an 80 ° C. atmosphere. An object of the present invention is to provide a practical shrink film having a lower shrinkage of 25% or more, a shrinkage of 35% or more in a 90 ° C. atmosphere, and a natural shrinkage of 40% or less of 3.0% or less. .

  In the propylene polymer for shrink film of the present invention, [1] MFR (230 ° C., 2.16 kgf) satisfies 0.05 to 8 (g / 10 min), and [2] melting point determined by DSC is 140 ° C. or less. And [3] n-decane soluble content is 3% by weight or less.

  A preferred embodiment of the propylene polymer of the present invention is a propylene polymer having a melting point determined by DSC of 120 ° C. or less, which is defined in the requirement [2]. A further preferred embodiment of the propylene-based polymer of the present invention is characterized in that the molecular weight distribution (Mw / Mn) is 4.0 or less and the Mw / Mn content of n-decane solubles is 4.0 or less. It has been done.

  In a particularly preferred embodiment of the propylene polymer of the present invention, the propylene polymer is obtained by homopolymerizing propylene or copolymerizing propylene and an α-olefin having 2 to 20 carbon atoms excluding propylene in the presence of a metallocene catalyst. (Co) polymer obtained in this way.

  The present invention also includes a polypropylene resin composition for shrink film comprising the propylene-based polymer and petroleum resin.

  The present invention further relates to a shrink film or a shrink label obtained from the propylene polymer or the polypropylene resin composition.

  By using a specific metallocene catalyst, the propylene-based polymer for shrink film of the present invention has a low melting point and a small amount of n-decane soluble component, and also has a small Mw / Mn of n-decane soluble component. Therefore, it is possible to obtain a shrink film excellent in shrinkage balance in which the thermal shrinkage rate is large while the natural shrinkage rate is small. Further, when it has a melting point of 120 ° C. or lower, it became possible to obtain a heat shrinkage ratio (40% or higher at 90 ° C.) that could not be achieved with the existing Ziegler-Natta catalyst.

  Hereinafter, embodiments of the invention will be described in detail from the viewpoint of the polypropylene-based polymer for shrink film and the shrink film (or shrink label) of the present invention.

Propylene Polymer The propylene polymer of the present invention has [1] MFR (230 ° C., 2.16 kgf) in the range of 0.05 to 8 (g / 10 min), and [2] melting point determined by DSC. The temperature is 140 ° C. or lower, and [3] n-decane soluble content is 3% by weight or less.

  The MFR (230 ° C., 2.16 kgf) of the propylene polymer of the present invention is in the range of 0.05 to 8 (g / 10 min), preferably 0.5 to 6, and more preferably 1 to 5. . An MFR of less than 0.05 is not preferred because the extrusion characteristics are poor and molding is difficult, and an MFR of more than 8 is not preferred because the thermal shrinkage rate is reduced.

  The n-decane soluble content of the propylene polymer of the present invention is 3% by weight or less, preferably 2.5% by weight or less, more preferably 2% by weight or less. If the amount of n-decane solubles exceeds 3% by weight, the natural shrinkage rate is increased, and the blocking resistance of the film is insufficient.

  The molecular weight distribution (Mw / Mn) of the n-decane soluble content of the propylene-based polymer and the copolymer in the present invention is 4.0 or less, preferably 3.0 or less. If Mw / Mn is greater than 4.0, the natural shrinkage rate is increased, which is not preferable.

  A preferred embodiment of the propylene-based polymer of the present invention is characterized in that the melting point determined by DSC is 120 ° C. or less, preferably 100 to 118 ° C., as defined in the requirement [2]. When the temperature is lower than 100 ° C., there is a problem that the blocking resistance is deteriorated or the rigidity is lowered, which is not preferable.

  A particularly preferred embodiment of the propylene polymer of the present invention is a propylene polymer (copolymer) obtained by homopolymerization of propylene or copolymerization of propylene and an α-olefin having 2 to 20 carbon atoms excluding propylene in the presence of a metallocene catalyst. ) Polymer.

  The metallocene catalyst used in the present invention includes at least one compound selected from metallocene compounds and compounds capable of reacting with organometallic compounds, organoaluminum oxy compounds and metallocene compounds to form ion pairs. Furthermore, a metallocene catalyst which can be subjected to stereoregular polymerization such as an isotactic or syndiotactic structure, if necessary, is preferably a metallocene catalyst comprising a particulate carrier. Among the metallocene compounds, a crosslinkable metallocene compound that has already been published (WO01 / 27124) by an international application filed by the present applicant is preferably used.

In the above general formula [I], R ¹ , R ² , R ³ , R ⁴ , R ⁵ , R ⁶ , R ⁷ , R ⁸ , R ⁹ , R ¹⁰ , R ¹¹ , R ¹² , R ¹³ , R ¹⁴ are It is selected from hydrogen, a hydrocarbon group, and a silicon-containing group, and each may be the same or different. Such hydrocarbon groups include methyl, ethyl, n-propyl, allyl, n-butyl, n-pentyl, n-hexyl, n-heptyl, n-octyl, n- Linear hydrocarbon groups such as nonyl group and n-decanyl group; isopropyl group, tert-butyl group, amyl group, 3-methylpentyl group, 1,1-diethylpropyl group, 1,1-dimethylbutyl group, 1 -Branched hydrocarbon groups such as methyl-1-propylbutyl group, 1,1-propylbutyl group, 1,1-dimethyl-2-methylpropyl group, 1-methyl-1-isopropyl-2-methylpropyl group; Cyclic saturated hydrocarbon groups such as cyclopentyl group, cyclohexyl group, cycloheptyl group, cyclooctyl group, norbornyl group and adamantyl group; cyclic unsaturated carbonized groups such as phenyl group, tolyl group, naphthyl group, biphenyl group, phenanthryl group and anthracenyl group A hydrogen group; Saturated hydrocarbon group substituted with cyclic unsaturated hydrocarbon group such as benzyl group, cumyl group, 1,1-diphenylethyl group, triphenylmethyl group; methoxy group, ethoxy group, phenoxy group, furyl group, N-methylamino A heteroatom-containing hydrocarbon group such as a group, N, N-dimethylamino group, N-phenylamino group, pyryl group and thienyl group. Examples of the silicon-containing group include a trimethylsilyl group, a triethylsilyl group, a dimethylphenylsilyl group, a diphenylmethylsilyl group, and a triphenylsilyl group. Further, the adjacent substituents of R ⁵ to R ¹² may be bonded to each other to form a ring. Examples of such substituted fluorenyl groups include benzofluorenyl group, dibenzofluorenyl group, octahydrodibenzofluorenyl group, octamethyloctahydrodibenzofluorenyl group, octamethyltetrahydrodicyclopentafluorenyl group, etc. Can be mentioned.

In the general formula [I], R ¹ , R ² , R ³ and R ⁴ substituted on the cyclopentadienyl ring are preferably hydrogen or a hydrocarbon group having 1 to 20 carbon atoms. Examples of the hydrocarbon group having 1 to 20 carbon atoms include the hydrocarbon groups described above. More preferably, R ³ is a hydrocarbon group having 1 to 20 carbon atoms.

In the general formula [I], R ⁵ to R ¹² substituted on the fluorene ring are preferably hydrocarbon groups having 1 to 20 carbon atoms. Examples of the hydrocarbon group having 1 to 20 carbon atoms include the hydrocarbon groups described above. The adjacent substituents of R ⁵ to R ¹² may be bonded to each other to form a ring.

In the general formula [I], Y that bridges the cyclopentadienyl ring and the fluorenyl ring is preferably a group 14 element, more preferably carbon, silicon, or germanium, and further preferably a carbon atom. R ¹³ and R ¹⁴ substituted for Y are preferably hydrocarbon groups having 1 to 20 carbon atoms. These may be the same or different from each other, and may be bonded to each other to form a ring. Examples of the hydrocarbon group having 1 to 20 carbon atoms include the hydrocarbon groups described above. More preferably, R ¹⁴ is an aryl group having 6 to 20 carbon atoms. Examples of the aryl group include the above-mentioned cyclic unsaturated hydrocarbon group, a saturated hydrocarbon group substituted with a cyclic unsaturated hydrocarbon group, and a heteroatom-containing cyclic unsaturated hydrocarbon group. R ¹³ and R ¹⁴ may be the same or different, and may be bonded to each other to form a ring. As such a substituent, a fluorenylidene group, a 10-hydroanthracenylidene group, a dibenzocycloheptadienylidene group, and the like are preferable.

  In the general formula [I], M is preferably a Group 4 transition metal, more preferably Ti, Zr, Hf and the like. Q is selected from the same or different combinations from halogen, a hydrocarbon group, an anionic ligand, or a neutral ligand capable of coordinating with a lone pair of electrons. j is an integer of 1 to 4, and when j is 2 or more, Qs may be the same or different from each other. Specific examples of the halogen include fluorine, chlorine, bromine and iodine, and specific examples of the hydrocarbon group include those described above. Specific examples of the anionic ligand include alkoxy groups such as methoxy, tert-butoxy and phenoxy, carboxylate groups such as acetate and benzoate, and sulfonate groups such as mesylate and tosylate. Specific examples of neutral ligands that can be coordinated by a lone pair include organophosphorus compounds such as trimethylphosphine, triethylphosphine, triphenylphosphine, diphenylmethylphosphine, tetrahydrofuran, diethyl ether, dioxane, 1,2-dimethoxy And ethers such as ethane. At least one Q is preferably a halogen or an alkyl group.

  Examples of such bridged metallocene compounds include isopropylidene (3-tert-butyl-5-methyl-cyclopentadienyl) (fluorenyl) zirconium dichloride, isopropylidene (3-tert-butyl-5-methyl-cyclopentadienyl). ) (3,6-ditert-butylfluorenyl) zirconium dichloride, diphenylmethylene (3-tert-butyl-5-methyl-cyclopentadienyl) (fluorenyl) zirconium dichloride, diphenylmethylene (3-tert-butyl- 5-methyl-cyclopentadienyl) (2,7-ditert-butylfluorenyl) zirconium dichloride, diphenylmethylene (3-tert-butyl-5-methyl-cyclopentadienyl) (3,6-ditert -Butyl fluoreni ) Zirconium dichloride are preferably used.

  In the metallocene catalyst according to the present invention, ions react with the organometallic compound, organoaluminum oxy compound, and transition metal compound (A) used together with the Group 4 transition metal compound represented by the general formula [I]. At least one compound selected from compounds forming a pair, and a particulate carrier used as necessary are disclosed in the above-mentioned publications (WO01 / 27124) and JP-A-11-315109 by the present applicant. The used compounds can be used without limitation.

  Preferable specific examples of the α-olefin used together with propylene in the copolymerization according to the present invention include ethylene, 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene, 1-octene and the like. These can be used at the same time, and among them, ethylene and 1-butene are preferably used.

  This invention also includes the polypropylene resin composition for shrink films which consists of said propylene-type polymer for shrink films, and petroleum resin. As the petroleum resin, a hydrocarbon resin composed of an aliphatic hydrocarbon, an alicyclic hydrocarbon, a hydrogenated hydrocarbon, or the like, or a terpene resin can be arbitrarily used. About the usage-amount of petroleum resin, petroleum resin is 0-45 weight part with respect to propylene polymer 100-55 weight part normally, Preferably petroleum resin is 10-40 weight with respect to propylene polymer 90-60 weight part. The polypropylene resin composition containing part is suitably used in the stretched film field such as shrink film or shrink label.

  In the present invention, addition of an antioxidant, a heat stabilizer, a weather stabilizer, a slip agent, an antiblocking agent, a crystal nucleating agent, etc., as necessary, within a range not impairing the performance as the propylene polymer of the present invention It may contain things.

  Moreover, you may add polyethylene or an elastomer to the polypropylene resin composition of this invention. The polyethylene may be an ethylene homopolymer or an ethylene / α-olefin copolymer, which is a random copolymer comprising ethylene and one or more α-olefins selected from α-olefins having 3 to 10 carbon atoms. It may be a polymer.

  Elastomers include ethylene / α-olefin random copolymers, ethylene / α-olefin / non-conjugated polyene random copolymers, propylene / α-olefin random copolymers, hydrogenated block copolymers, other elastic polymers, And mixtures thereof.

  After blending the above-mentioned components and various additives as required, for example, with a mixer such as a Henschel mixer, a Banbury mixer, a tumbler mixer, etc., it is formed into a pellet using a uniaxial or biaxial extruder to form a film as described below. Although it is possible to use it, it is also possible to use it for the film forming machine in the state which blended the said component.

Shrink film (shrink label)
By forming a film of the propylene-based polymer of the present invention or a polypropylene resin composition comprising the polymer and a petroleum resin, the film can be stretched at 100 ° C. or less. A practical shrink film having a shrinkage ratio of 25% or more at 90 ° C., a shrinkage ratio of 35% or more in a 90 ° C. atmosphere, and a natural shrinkage ratio of 40% or less at 40 ° C. is provided. The manufacturing method of the shrink film thru | or shrink label of this invention is demonstrated. The film is produced by a known coextrusion technique or stretching technique. For example, the propylene-based polymer or polypropylene resin composition of the present invention is extruded from a flat sheet from a T-die, cooled and drawn, and stretched 1.0 to 6.0 times in the machine direction and 3 to 3 in the transverse direction. The film of the present invention is obtained by tenter stretching, annealing while relaxing in the width direction by 0 to 12%, and then winding. In addition to uniaxial or biaxial stretching by the tenter as described above, the tubular sheet may be extruded from a round die and stretched in a tubular shape, that is, the tubular method simultaneous biaxial stretching may be used.

EXAMPLES Next, although this invention is demonstrated in detail based on an Example, this invention is not limited to this Example. The measuring method of the physical property in an Example is as follows.
1) n-decane soluble amount A sample was completely dissolved by adding 200 ml of n-decane to 5 g of the sample and heating with stirring. It was cooled to 20 ° C. over about 3 hours and left for 30 minutes. Thereafter, the precipitate was filtered off. The filtrate was put in 1000 ml of acetone to precipitate the components dissolved in n-decane. The precipitate and acetone were filtered off and the precipitate was dried. Even when the filtrate side was concentrated to dryness, no residue was observed. The amount of soluble n-decane was determined by the following formula.
n-decane soluble content (wt%) = [precipitate weight / sample weight] × 100

2) Mw / Mn measurement [weight average molecular weight (Mw), number average molecular weight (Mn)]
It measured as follows using GPC-150C Plus made from Waters. The separation columns were TSKgel GMH6-HT and TSKgel GMH6-HTL, the column size was 7.5 mm in inner diameter and 600 mm in length, the column temperature was 140 ° C., and o-dichlorobenzene (Wako Pure Chemical Industries) was used as the mobile phase. Industry) and BHT (Wako Pure Chemical Industries) 0.025% by weight as an antioxidant, moved at 1.0 ml / min, the sample concentration was 0.1% by weight, the sample injection volume was 500 microliters, A differential refractometer was used as a detector. Standard polystyrene used was manufactured by Tosoh Corporation for molecular weights of Mw <1000 and Mw> 4 × 10 ⁶ , and used by Pressure Chemical Co. for 1000 ≦ Mw ≦ 4 × 10 ⁶ .

3) Melting point (Tm)
Using Perkin Elmer DSC-7, 7 mg of the sample was heated to 230 ° C. at 10 ° C./min, held at 230 ° C. for 10 minutes, cooled to 50 ° C. at 10 ° C./min, and again at 10 ° C./min. It was determined from the endothermic curve when the temperature was raised.

4) Melt flow rate (MFR)
Measurement was performed at 230 ° C. and a load of 2.16 kg by the method of ASTM D-1238. Without introducing nitrogen into the cylinder, the pellets were directly charged into the cylinder and melted.

5) Shrinkage rate The stretched film was cut into a size of 1 cm in width and 15 cm in length, and contracted by applying it to warm water at a predetermined temperature for 10 seconds. The shrinkage rate was determined from the original length and the contracted length.

6) The natural shrinkage ratio The stretched film was cut into a size of 1 cm in width and 15 cm in length and stored in an oven at 40 ° C. for 7 days for shrinkage. The shrinkage rate was determined from the original length and the contracted length.

  In the presence of a metallocene catalyst combining diphenylmethylene (3-t-butyl-5-methylcyclopentadienyl) (2,7-di-t-butylfluorenyl) zirconium dichloride and methylaluminoxane, propylene and ethylene are By copolymerizing, a propylene polymer having an ethylene content of 5.1% by weight and a melting point of 115 ° C. was obtained. To 100 parts by weight of this polymer, 0.1 parts by weight of tetrakis [methylene-3 (3,5-di-t-butyl-4-hydroxyphenyl) propionate] methane as an antioxidant, 2,4-bis 0.1 parts by weight of (1,1-dimethyl) -phosphate phenol, 0.1 parts by weight of calcium stearate as a neutralizing agent, 0.2 parts by weight of synthetic silica, 0.05 parts by weight of erucic acid amide Then, using a KTX-30 twin screw extruder, the propylene polymer was pelletized by melt kneading at a resin temperature of 250 ° C. Table 1 summarizes the measured physical properties of the obtained pellets.

  A sheet having a thickness of 0.4 mm was prepared from the obtained pellets by press molding. As pressing conditions, preheating was performed at 230 ° C. for 6 minutes to apply pressure to prepare a molten sheet, and cooling was performed at 30 ° C. for 2 minutes. The sheet was cut into a predetermined size and uniaxially stretched using Bruckner KAROIV. The stretching conditions were preheating at 90 ° C. for 30 seconds and uniaxial stretching at a speed of 0.6 m / min. The draw ratio was 5 times. Table 1 shows the shrinkage results for the obtained stretched film.

  Except that 70 parts by weight of the propylene polymer used in Example 1 was blended with 30 parts by weight of a petroleum resin (Alcon P-140) and kneaded with a KTX-30 twin screw extruder. The same operation as in Example 1 was performed. Table 1 summarizes the physical properties measured for the obtained pellets and the results of the shrinkage of the stretched film.

[Comparative Example 1]
Dimethylmethylenebis- (2-methyl-4-phenylindenyl) instead of diphenylmethylene (3-t-butyl-5-methylcyclopentadienyl) (2,7-di-t-butylfluorenyl) zirconium dichloride ) Using zirconium dichloride, a propylene polymer having an ethylene content of 5.2% by weight and a melting point of 115 ° C. was obtained. About this propylene polymer, it carried out similarly to Example 1, and obtained the pellet and the stretched film. The physical properties measured for the pellets and stretched film are summarized in Table 1.

[Comparative Example 2]
A comparison was made except that 70 parts by weight of the propylene polymer used in Comparative Example 1 was blended with 30 parts by weight of a petroleum resin (Alcon P-140) and kneaded with a KTX-30 twin screw extruder. Performed as in Example 1. The physical properties measured for the obtained pellets and stretched film are summarized in Table 1.

[Comparative Example 3]
Pellets polymerized using MgCl ₂ -supported TiCl ₄ catalyst and triethylaluminum, except that a propylene polymer having an ethylene content of 4% by weight and a melting point of 139 ° C. was used in the same manner as in Example 1. Got. The physical properties measured for the obtained pellets and stretched film are summarized in Table 1.

[Comparative Example 4]
A comparison was made except that 70 parts by weight of the propylene polymer used in Comparative Example 3 was blended with 30 parts by weight of a petroleum resin (Alcon P-140) and kneaded with a KTX-30 twin screw extruder. Performed as in Example 3. The physical properties measured for the obtained pellets and stretched film are summarized in Table 1.

Claims (7)

A propylene-based polymer for shrink film that simultaneously satisfies the following requirements [1] to [3].
[1] MFR (230 ° C., 2.16 kgf) satisfies 0.05 to 8 (g / 10 min).
[2] The melting point determined by DSC is 140 ° C. or lower
[3] The n-decane soluble content is 3% by weight or less.   The propylene-based polymer for shrink film according to claim 1, wherein the melting point determined by DSC is 120 ° C or lower.   The propylene for shrink film according to claim 1 or 2, wherein the molecular weight distribution (Mw / Mn) is 4.0 or less and the Mw / Mn of the n-decane soluble component is 4.0 or less. Polymer.   The propylene-based polymer for shrink film is a (co) polymer obtained by homopolymerization of propylene or copolymerization of propylene and an α-olefin having 2 to 20 carbon atoms excluding propylene in the presence of a metallocene catalyst. The propylene-based polymer for shrink film according to any one of claims 1 to 3.   The polypropylene resin composition for shrink films which consists of the propylene polymer for shrink films in any one of Claims 1-4, and petroleum resin.   The shrink film or shrink label obtained from the propylene-type polymer for shrink films in any one of Claims 1-4.   The shrink film or shrink label obtained from the polypropylene resin composition for shrink films according to claim 5.