JP3280904B2 - Polyolefin sheet for thermoforming - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyolefin sheet for thermoforming which is preferably used for various packaging containers such as food packaging and pharmaceutical packaging, and a method for producing the same. More specifically, the present invention relates to a polyolefin-based sheet for thermoforming which is excellent in processability and surface gloss and can be applied to various thermoforming methods.

[0002]

2. Description of the Related Art Conventionally, polyolefin resins, especially polypropylene resins, have excellent properties such as strength, rigidity and heat resistance. It is used for pharmaceutical packaging. However, these resins have a large drawdown due to heating at the time of preheating during thermoforming, and the optimal molding temperature range at the time of molding to obtain good molded products is very narrow,
Very high temperature control is required for a molding machine, and a conventional general-purpose molding machine has a high molding defect rate, and it is very difficult to control a process. Conventionally, the development of polyolefin resins having good thermoformability has been studied. For example, polyethylene and ethylene-
Attempts have already been made to blend and modify propylene copolymers, inorganic fillers and low molecular weight petroleum resins.

For example, Japanese Patent Publication No. 56-15744 discloses a method of adding high-viscosity polyethylene (low-density polyethylene) and hydrous magnesium silicate powder to high-viscosity polypropylene. Discloses a method in which polyethylene (high-density polyethylene) and an ethylene-propylene copolymer are added to polypropylene. Japanese Patent Publication No. 53213/1988 discloses the use of polypropylene and polyethylene having a narrow molecular weight distribution to formability and vibration resistance. A method for improving the properties is disclosed, and Japanese Patent Publication No. 6-89191 discloses a method for adding a petroleum resin and an ethylene-α-olefin copolymer to polypropylene. With these methods,
Although there is an effect on the formability such as sheet softening tension holding time, melt strength, drawability, drawdown, etc. under a specific temperature condition, the moldable temperature width which is substantial formability Has almost no improvement effect, and as a matter of fact, satisfactory moldability has not yet been obtained. In addition, when a low molecular weight compound such as a petroleum resin is used, a considerable amount of bleeding or elution actually occurs, and it is difficult to use it hygienically in food packaging and pharmaceutical packaging which are used most frequently.

[0004] On the other hand, polytetrafluoroethylene has a property of forming fibers with a slight stress, and it is known that when it is blended with a thermoplastic resin, the moldability and mechanical properties are improved. I have. For example, Japanese Patent Application Laid-Open No. 5-214
JP-A-184 and JP-A-6-306212 disclose resin compositions obtained by blending polytetrafluoroethylene with polyolefin. Also, JP-A-8-16
No. 5358 discloses a polyolefin sheet for thermoforming in which fibrous polytetrafluoroethylene is contained with respect to polyolefin. However, polytetrafluoroethylene generally has poor dispersibility in polyolefin resins, and can be uniformly dispersed by a simple blend as described in JP-A-5-214184 and JP-A-6-306212. Absent. Also, it is difficult to fibrillate all polytetrafluoroethylene by the shearing force according to the method of JP-A-8-165358, and the fibrous polytetrafluoroethylene also aggregates in the matrix resin and becomes uniform. A perfect composition cannot be obtained. In other words, all of these methods have a problem in the dispersibility of polytetrafluoroethylene, so that a large amount of polytetrafluoroethylene is required to improve the processability of the polyolefin sheet for thermoforming and the surface gloss However, there was a defect that it became defective.

[0005]

SUMMARY OF THE INVENTION An object of the present invention is to provide a polyolefin sheet for thermoforming which is excellent in thermoformability, in particular, has a wide molding temperature range during molding and is excellent in surface gloss. is there.

[0006]

Means for Solving the Problems The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, have found that a polytetrafluoroethylene-containing mixed polymer composed of polytetrafluoroethylene particles having a particle diameter of 10 μm or less and an organic polymer. The present inventors have found that by adding a powder to a polyolefin-based resin, it is possible to obtain a molded article having good moldability and excellent surface gloss, and arrived at the present invention.

That is, the gist of the present invention is to provide a polytetrafluoroethylene-containing mixed powder comprising an organic polymer and polytetrafluoroethylene particles having a particle diameter of 10 μm or less with respect to 100 parts by weight of a polyolefin resin (A). B) The amount of the polytetrafluoroethylene component is 0.0001 to
Polyolefin-based sheet for thermoforming comprising a resin composition blended to be 20 parts by weight, and a particle diameter of 10 μm
m and a master pellet consisting of a polytetrafluoroethylene-containing mixed powder (B) composed of polytetrafluoroethylene particles and an organic polymer and a portion of the polyolefin resin (A), and the remaining polyolefin resin (A)
The amount of the polytetrafluoroethylene component is 0.000 with respect to 100 parts by weight of the total amount of the polyolefin resin (A).
It is a polyolefin-based sheet for thermoforming comprising a resin composition blended in an amount of 1 to 20 parts by weight.

[0008]

DESCRIPTION OF THE PREFERRED EMBODIMENTS The polyolefin resin (A) used in the present invention is a component used as a base resin in the resin composition, and examples thereof include polypropylene, high-density polyethylene, low-density polyethylene, and linear low-density polyethylene. Density polyethylene, poly-1-butene, polyisobutylene, random copolymer or block copolymer at any ratio of propylene and ethylene and / or 1-butene, 50 weight% of diene component at every ratio of ethylene and propylene % Or less of ethylene-propylene-diene terpolymer, polymethylpentene, cyclic polyolefin such as copolymer of cyclopentadiene and ethylene and / or propylene, ethylene or propylene and 50% or less by weight of vinyl acetate, for example, Alkyl methacrylate Examples include random copolymers, block copolymers, and graft copolymers with vinyl compounds such as steles, alkyl acrylates, and aromatic vinyls. These may be used alone or as a mixture of two or more. Can be.

In the present invention, as the polyolefin resin (A), a propylene polyolefin obtained by polymerizing a monomer component containing 50% by weight or more of propylene, and the propylene polyolefin 1
A mixture of 0.1 to 100 parts by weight of an ethylene-based polyolefin obtained by polymerizing a monomer component containing 50% by weight or more of ethylene with respect to 00 parts by weight is easily available and inexpensive. It is preferred in that respect.

Further, as the propylene-based polyolefin, at least one selected from the group consisting of polypropylene, ethylene-propylene random copolymer and ethylene-propylene block copolymer is preferable because of its high versatility and low cost. In addition, as the ethylene-based polyolefin, at least one selected from low-density polyethylene, linear low-density polyethylene, and high-density polyethylene is also preferable because of its high versatility and low cost.

The polyolefin resin (A) has a melt flow index of 10 g / 10 minutes or less,
Preferably, the powder having a content of 5 g / 10 minutes or less is desirable in view of the fact that when the polytetrafluoroethylene-containing mixed powder (B) is blended, effects such as excellent workability are sufficiently exhibited. The melt flow index is
It is measured at a load of 2.16 kg according to ASTM D1238. For example, it is a value at 230 ° C. for a propylene-based polyolefin and a value at 190 ° C. for an ethylene-based polyolefin.

The polytetrafluoroethylene-containing mixed powder (B) used in the present invention is composed of polytetrafluoroethylene particles having a particle size of 10 μm or less and an organic polymer. It is necessary that they are not aggregated. As such a polytetrafluoroethylene-containing mixed powder, an aqueous dispersion of polytetrafluoroethylene particles having a particle diameter of 0.05 to 1.0 μm and an aqueous dispersion of organic polymer particles are mixed, and coagulated or sprayed. After the monomers constituting the organic polymer are polymerized in the presence of an aqueous dispersion of polytetrafluoroethylene particles having a particle diameter of 0.05 to 1.0 μm or obtained by drying into a powder, solidification or In a dispersion obtained by pulverizing by spray drying, or a dispersion obtained by mixing an aqueous dispersion of polytetrafluoroethylene particles having a particle diameter of 0.05 to 1.0 μm and an aqueous dispersion of organic polymer particles, ethylene is added. What is obtained by carrying out emulsion polymerization of the monomer which has an unsaturated unsaturated bond, and pulverizing by coagulation or spray drying is preferable.

The polytetrafluoroethylene-containing mixed powder (B) used in the present invention has a particle diameter of 0.1 to be used.
The aqueous dispersion of the 0.5 to 1.0 μm polytetrafluoroethylene particles is obtained by polymerizing a tetrafluoroethylene monomer by emulsion polymerization using a fluorinated surfactant. In the emulsion polymerization of polytetrafluoroethylene particles, a fluorine-containing olefin such as hexafluoropropylene, chlorotrifluoroethylene, fluoroalkylethylene, or perfluoroalkylvinyl ether is used as a copolymer component within a range that does not impair the properties of polytetrafluoroethylene. Alternatively, a fluorinated alkyl (meth) acrylate such as perfluoroalkyl (meth) acrylate may be used. The content of these copolymer components is preferably 10% by weight or less based on tetrafluoroethylene.

Commercially available raw materials for the polytetrafluoroethylene particle dispersion include Fluon AD-1 and AD-936 manufactured by Asahi ICI Fluoropolymer Co., Ltd., and Polyflon D-1 and D-2 manufactured by Daikin Industries, and DuPont Mitsui Fluoro. A typical example is Teflon 30J manufactured by Chemical Company. The organic polymer constituting the polytetrafluoroethylene-containing mixed powder (B) used in the present invention is not particularly limited, but the polyolefin resin (A)
From the viewpoint of dispersibility at the time of compounding with the propylene resin, it is preferable that the compound has high compatibility with the propylene-based resin.

Specific examples of the monomer for forming the organic polymer include styrene, p-methylstyrene, o-methylstyrene, p-chlorostyrene, o-chlorostyrene, p-methoxystyrene, and o-methylstyrene. Methoxystyrene,
Styrene monomers such as 2,4-dimethylstyrene and α-methylstyrene; methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, butyl methacrylate, 2-ethylhexyl acrylate, (Meth) acrylate monomers such as 2-ethylhexyl methacrylate, dodecyl acrylate, dodecyl methacrylate, tridecyl acrylate, tridecyl methacrylate, octadecyl acrylate, octadecyl methacrylate, cyclohexyl acrylate, and cyclohexyl methacrylate Vinyl cyanide monomers such as acrylonitrile and methacrylonitrile; vinyl ether monomers such as vinyl methyl ether and vinyl ethyl ether; vinyl carboxylate monomers such as vinyl acetate and vinyl butyrate; Emissions, propylene, olefin monomers such as isobutylene; butadiene, isoprene, may be mentioned diene monomers and the like of dimethyl butadiene and the like. These monomers can be used alone or in combination of two or more.

Among these monomers, styrene-based monomers, (meth) acrylate-based monomers, and olefin-based monomers are preferred from the viewpoint of compatibility with the polyolefin-based resin (A). The body can be mentioned. Particularly preferred are long chain alkyl (meth) acrylate monomers having 12 or more carbon atoms, styrene,
Monomers containing at least 20% by weight of one or more monomers selected from the group consisting of olefin monomers can be mentioned.

The content of polytetrafluoroethylene in the polytetrafluoroethylene-containing mixed powder (B) used in the present invention is preferably 0.1% to 90%. The polytetrafluoroethylene-containing mixed powder (B) used in the present invention is prepared by charging an aqueous dispersion thereof into hot water in which metal salts such as calcium chloride and magnesium sulfate are dissolved, and then salting out and coagulating. The powder can be formed by drying or spray drying.

The ordinary polytetrafluoroethylene fine powder becomes an aggregate having a size of 100 μm or more in the step of recovering a powder from the state of the particle dispersion, and thus it is difficult to uniformly disperse it in the thermoplastic resin. On the other hand, the polytetrafluoroethylene-containing mixed powder (B) used in the present invention is dispersed in the polyolefin resin (A) because polytetrafluoroethylene alone does not form a domain having a particle diameter of more than 10 μm. Excellent in nature. As a result, in the thermoforming sheet of the present invention, polytetrafluoroethylene is efficiently fiberized in the polyolefin resin (A), the forming temperature range is extremely wide, and the surface gloss is excellent.

In the resin composition used in the present invention, the polytetrafluoroethylene-containing mixed powder (B) has a polytetrafluoroethylene component content of 0.0001 to 100 parts by weight based on 100 parts by weight of the polyolefin resin (A). It was blended so as to be 20 parts by weight. If the amount is less than 0.0001 part by weight, the effect of improving workability is poor, and if it exceeds 20 parts by weight, the melt viscosity decreases.

The resin composition of the present invention may further contain a nucleating agent. Examples of the nucleating agent include sodium benzoate, bisbenzylidene sorbitol, bis (p-methylbenzylidene) sorbitol, bis (p
-Ethylbenzylidene) sorbitol, sodium-
2,2-methylenebis (4,6-di-t-butylphenyl) phosphite, talc, titanium oxide, aluminum hydroxy-di-pt-butylbenzoate, and the like. These may be used alone or in combination of two or more. They can be used in combination. If the compounding amount of the nucleating agent is too small, the effect of improving transparency and surface properties by using such a nucleating agent tends not to be sufficiently exhibited, so that the polyolefin-based resin (A) 100 wt. Parts by weight, preferably 0.001 part by weight or more, more preferably 0.01 part by weight or more, and if it is too large, the transparency of the polyolefin sheet for thermoforming formed from the resin composition is rather increased. Since it tends to decrease, the amount is preferably 2 parts by weight or less, more preferably 1.5 parts by weight or less based on 100 parts by weight of the polyolefin resin (A).

If necessary, additives such as stabilizers, lubricants and inorganic fillers may be added to the resin composition as long as the transparency of the obtained polyolefin sheet for thermoforming is not reduced. Can be. Representative examples of the stabilizer include, for example, pentaerythrityl-
Tetrakis [3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate], triethylene glycol-bis [3- (3-t-butyl-5-methyl-4)
-Hydroxyphenyl) propionate], phosphorus stabilizers such as tris (monononylphenyl) phosphite and tris (2,4-di-t-butylphenyl) phosphite, dilaurylthiodipropionate And the like, and these can be used alone or in combination of two or more. The amount of the stabilizer is usually 0.01 to 3 parts by weight, preferably 0.05 to 2 parts by weight, per 100 parts by weight of the polyolefin resin (A).

Representative examples of the lubricant include sodium, calcium and magnesium salts of saturated or unsaturated fatty acids such as lauric acid, palmitic acid, oleic acid and stearic acid. These may be used alone or in combination of two or more. These can be used in combination. The blending amount of such a lubricant is determined based on the polyolefin resin (A) 10
Usually 0.1 to 3 parts by weight, more preferably 0.1 to 3 parts by weight based on 0 parts by weight.
It is preferably from 1 to 2 parts by weight.

Representative examples of the inorganic filler include, for example, calcium carbonate, talc, glass fiber, magnesium carbonate, mica, kaolin, calcium sulfate, barium sulfate, titanium white, white carbon, carbon black, aluminum hydroxide, oxide oxide Examples thereof include aluminum, magnesium hydroxide, silica, clay, and zeolite, and these can be used alone or in combination of two or more. It is preferable that these particles have an average particle size of 1 to 70 μm. The amount of the inorganic filler is usually 0.001 to 100 parts by weight, more preferably 0.001 to 100 parts by weight based on 100 parts by weight of the polyolefin resin (A).
It is preferably 5 to 50 parts by weight. When such an inorganic substance is contained in a large amount, the obtained molded body has improved heat resistance and can reduce the calorie burned during the incineration treatment.

A predetermined amount of each of the essential components and optional components as described above is blended in a predetermined amount, and the resulting mixture is kneaded with a usual kneader such as a roll, a Banbury mixer, a single-screw extruder, or a twin-screw extruder to obtain a resin composition. Although it is prepared, it is usually preferable to make it into a pellet. Further, a master batch containing the polytetrafluoroethylene-containing mixed powder (B) at a high concentration may be diluted with the polyolefin-based resin (A) to form a resin composition. In this case, the amount of the polytetrafluoroethylene component of the polytetrafluoroethylene-containing mixed powder (B) is 0.0001 to 20 parts by weight based on 100 parts by weight of the total amount of the polyolefin-based resin (A).

The polyolefin sheet for thermoforming of the present invention is obtained by molding the resin composition. The molding method used when obtaining the polyolefin sheet for thermoforming of the present invention is not particularly limited, for example, a single screw extruder,
An extrusion molding method using a twin-screw extruder or the like is preferably employed. Also, calender molding can be performed on the polyolefin sheet for thermoforming obtained by, for example, the extrusion molding method.

The thickness of the polyolefin sheet for thermoforming thus obtained is not particularly limited, and may be appropriately adjusted depending on the purpose of use, but is usually 0.05 to 3 mm.
It is preferred that it is about. The polyolefin sheet for thermoforming of the present invention has a markedly improved workability and surface glossiness, etc., and various thermoforming methods, including methods that were difficult when using a conventional polyolefin sheet, were used. A useful molded article can be produced by the method.

Representative examples of the thermoforming method applicable to the polyolefin sheet for thermoforming of the present invention include, for example, a vacuum forming method, a pressure forming method and the like. A thermoformed article having an appearance such as glossiness can be obtained.

[0028]

EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited to these examples.
In the examples, "parts" indicates parts by weight, "%" indicates weight%, and various physical properties were measured by the following methods. (1) Solid concentration: determined by drying the particle dispersion at 170 ° C. for 30 minutes.

(2) Particle size distribution, weight average particle size: A solution obtained by diluting a particle dispersion with water was used as a sample solution, and a dynamic light scattering method (ELS800, manufactured by Otsuka Electronics Co., Ltd., temperature: 25 ° C., scattering angle: 90) Degree). (3) Zeta potential: Measured by electrophoresis (ELS800, manufactured by Otsuka Electronics Co., Ltd., temperature 25 ° C., scattering angle 10 °) using a sample dispersion prepared by diluting the particle dispersion with a 0.01 mol / l NaCl aqueous solution. did.

(4) Melt flow rate: JISK72
The measurement was performed at 230 ° C. under a load of 2.16 kg by the method described in No. 10. (5) Total light transmittance, haze, gloss (45 °) of the sheet
(Gloss): Measured by the method described in JIS K7105. (6) Formable temperature range of the sheet: The sheet is formed into a molded product (diameter 10 mm, height 6 mm) at a constant pressure by a compressed air molding machine (FBP-M2 manufactured by CK Corporation), and the overall thickness of the molded product is uniform. The optimum moldable temperature range that resulted in was determined. Reference Example 1 <Production of polytetrafluoroethylene-containing mixed powder (B-1)> In a separable flask equipped with a stirring blade, a condenser, a thermocouple, and a nitrogen inlet, 190 parts of distilled water and sodium dodecylbenzenesulfonate. 5 parts, 100 parts of styrene and 0.5 part of cumene hydroperoxide were charged and heated to 40 ° C. under a nitrogen stream. Then, iron (II) sulfate 0.001
Parts, disodium ethylenediaminetetraacetate 0.003
, A mixed solution of 0.24 parts of Rongalite salt and 10 parts of distilled water was added to initiate radical polymerization. After the fever ends,
The temperature in the system was maintained at 40 ° C. for 1 hour to complete the polymerization,
A styrene polymer particle dispersion (hereinafter referred to as P-1) was obtained.

The solid content concentration of P-1 was 33.3%, the particle size distribution showed a single peak, and the weight average particle size was 96 n.
m, and the surface potential was -32 mV. On the other hand, Fluon AD936 manufactured by Asahi ICI Fluoropolymers was used as a polytetrafluoroethylene-based particle dispersion. AD936
Has a solid content of 63.0% and contains 5 parts of polyoxyethylene alkylphenyl ether per 100 parts of polytetrafluoroethylene. AD936
Showed a single peak, the weight average particle diameter was 290 nm, and the surface potential was -20 mV.

To 833 parts of AD936, 1167 parts of distilled water was added to obtain a polytetrafluoroethylene particle dispersion F-1 having a solid content of 26.2%. F-1 contains 25% of polytetrafluoroethylene particles and 1.2% of polyoxyethylene nonylphenyl ether. 1
60 parts of F-1 (40 parts of polytetrafluoroethylene)
And 181.8 parts of P-1 (60 parts of polystyrene) were charged into a separable flask equipped with a stirring blade, a condenser, a thermocouple, and a nitrogen inlet, and stirred at room temperature for 1 hour under a nitrogen stream. Thereafter, the inside of the system was heated to 80 ° C. and maintained for 1 hour. No solid matter was separated through a series of operations, and a uniform particle dispersion was obtained. The solid concentration of the particle dispersion is 29.
3%, the particle size distribution was relatively broad, and the weight average particle size was 168 nm.

341.8 parts of the particle dispersion is poured into 700 parts of 85 ° C. hot water containing 5 parts of calcium chloride to separate a solid, filtered and dried to obtain a mixed powder containing polytetrafluoroethylene (B). -1) 98 parts were obtained. B-1 is 25
After shaping into a strip shape at 0 ° C. by a press molding machine, ultrathin sections were observed with a microtome without transmission using a transmission electron microscope. Polytetrafluoroethylene was observed as a dark part, but no aggregate exceeding 10 μm was observed. Reference Example 2 <Production of polytetrafluoroethylene-containing mixed powder (B-2)> F used in Reference Example 1 in a separable flask equipped with a stirring blade, a condenser, a thermocouple, a nitrogen inlet, and a dropping funnel.
-1 to 160 parts (polytetrafluoroethylene 40
Parts), 1.0 part of dodecylbenzenesulfonic acid, 7 parts of distilled water
0 parts were charged, and the temperature was raised to 80 ° C. under a nitrogen stream. Next, 0.001 part of iron (II) sulfate, 0.003 part of disodium ethylenediaminetetraacetate, 0.24 of Rongalit salt
And a mixture of 10 parts of distilled water, a mixture of 20 parts of n-butyl acrylate, 40 parts of styrene and 0.3 part of tertiary butyl peroxide was added dropwise from a dropping funnel for 90 minutes to allow radical polymerization to proceed. After completion of the dropwise addition, the internal temperature was maintained at 80 ° C. for 1 hour. No solid matter was separated through a series of operations, and a uniform particle dispersion was obtained. The solid content concentration of the particle dispersion was 33.2%, the particle size distribution was relatively broad, and the weight average particle size was 248 nm.

301.5 parts of this particle dispersion is poured into 700 parts by weight of hot water at 85 ° C. containing 5 parts of calcium chloride, the solid is separated, filtered and dried to obtain a mixed powder containing polytetrafluoroethylene ( B-2) 98 parts were obtained. After B-2 was shaped into a strip shape at 250 ° C. by a press molding machine, ultrathin sections were observed with a microtome without staining using a transmission electron microscope. Polytetrafluoroethylene was observed as a dark part, but no aggregate exceeding 10 μm was observed. Reference Example 3 <Production of polytetrafluoroethylene-containing mixed powder (B-3)> A mixture of 75 parts of dodecyl methacrylate and 25 parts of methyl methacrylate was added with 0.1% of azobisdimethylvaleronitrile.
One part was dissolved. A mixture of 2.0 parts of sodium dodecylbenzenesulfonate and 300 parts of distilled water was added to the mixture, and the mixture was stirred at 10,000 rpm for 4 minutes using a homomixer, and then added to a homogenizer at a pressure of 300 kg / cm2.
The dispersion was passed to obtain a stable dodecyl methacrylate / methyl methacrylate pre-dispersion. This was charged into a separable flask equipped with a stirring blade, a condenser, a thermocouple, and a nitrogen inlet, the internal temperature was raised to 80 ° C. under a nitrogen stream, and the mixture was stirred for 3 hours to undergo radical polymerization to obtain dodecyl methacrylate /
Methyl methacrylate copolymer particle dispersion (hereinafter referred to as P-2
).

The solid content concentration of P-2 was 25.1%, the particle size distribution showed a single peak, and the weight average particle size was 198.
nm, and the surface potential was -39 mV. 160 parts of F-1 used in Reference Example 1 (polytetrafluoroethylene 40
Parts) and 159.4 parts of P-2 (dodecyl methacrylate / methyl methacrylate copolymer 40 parts) with a stirring blade,
The mixture was charged into a separable flask equipped with a condenser, a thermocouple, a nitrogen inlet, and a dropping funnel, and stirred at room temperature for 1 hour under a nitrogen stream. Thereafter, the temperature inside the system was raised to 80 ° C., and iron sulfate (I
I) 0.001 part, disodium ethylenediaminetetraacetate 0.003 part, Rongalit salt 0.24 part, distilled water 1
After adding 0 parts of the mixture, a mixture of 20 parts of methyl methacrylate and 0.1 part of tertiary butyl peroxide was added dropwise over 30 minutes, and after completion of the addition, the internal temperature was maintained at 80 ° C. for 1 hour to perform radical polymerization. Was completed. No solid matter was separated through a series of operations, and a uniform particle dispersion was obtained.
The solid content concentration of the particle dispersion was 28.5%, the particle size distribution was relatively broad, and the weight average particle size was 248 nm.

349.7 parts of this particle dispersion was poured into 600 parts of 75 ° C. hot water containing 5 parts of calcium chloride, and the solid was separated, filtered and dried to obtain a mixed powder containing polytetrafluoroethylene (B). -3) 97 parts were obtained. Dried B-
3 was formed into a strip shape by a press molding machine at 220 ° C., and ultrathin sections were observed with a microtome without staining using a transmission electron microscope. Polytetrafluoroethylene was observed as a dark part, but no aggregate exceeding 10 μm was observed. Reference Example 4 <Production of master pellet (M-1) of mixed powder containing polytetrafluoroethylene> 75 parts of linear homopolypropylene pellet (EA7, manufactured by Nippon Polychem Co., Ltd .: melt flow rate 1.2 g / 10 min) After blending 25 parts of the tetrafluoroethylene-containing mixed powder B-3 obtained in Reference Example 3 and hand blending,
Using a twin-screw extruder (ZSK30 manufactured by WERNER & PFLEIDERER), melt-kneading is performed at a barrel temperature of 200 ° C. and a screw rotation speed of 200 rpm, and the mixture is shaped into pellets. 1). Examples 1-4, Comparative Examples 1-3 Linear homopolypropylene pellets (manufactured by Nippon Polychem, EA7: melt flow rate 1.2 g / 10 min),
Tetrafluoroethylene-containing mixed powder (B
-1 to 3) or a master pellet (M-1) at a ratio shown in Table 1 and a single screw extruder (screw diameter 50 mm, L / D = 28) equipped with a T die at 230 ° C., 5 ° C.
The mixture was kneaded at 0 rpm and extruded to obtain a polyolefin sheet for thermoforming having a thickness of 0.3 mm. Table 1 shows the results of evaluating the total light transmittance, haze, glossiness, and moldable temperature range of the obtained sheet.

In Examples 1 to 4, the amount of the polytetrafluoroethylene component in the polytetrafluoroethylene-containing mixed powder was 0.1 parts per 100 parts of the propylene resin.
Department. Extruded without adding a polytetrafluoroethylene-containing mixed powder for comparison (Comparative Example 1),
Polytetrafluoroethylene fine powder (Asahi IC
(Comparative Examples 2 and 3) to which CD123 (Company I) was added was evaluated in the same manner. Table 1 shows the results.

[0038]

[Table 1]

Examples 5 to 8, Comparative Examples 4 and 6 Linear homopolypropylene pellets (manufactured by Nippon Polychem, EA7: melt flow rate 1.2 g / 10 min),
Talc, tetrafluoroethylene-containing mixed powder (B-1 to 3) or master pellet (M-1) obtained in Reference Example
In the proportions shown in Table 2 and a twin-screw extruder (WERNER).
& PFLEIDERER Co., Ltd., and melt-kneaded at a barrel temperature of 200 ° C. and a screw rotation speed of 200 rpm, and formed into pellets. Using the obtained pellet, a single screw extruder (screw diameter 5
(0 mm, L / D = 28) at 230 ° C. and 50 rpm, and extruded to obtain a polyolefin sheet for thermoforming having a thickness of 0.3 mm. Table 2 shows the results of evaluating the glossiness and the moldable temperature range of the obtained sheet.

In Examples 5 to 8, the amount of the polytetrafluoroethylene component in the polytetrafluoroethylene-containing mixed powder was 0.1 to 100 parts of the propylene resin.
Department. Extruded without adding a polytetrafluoroethylene-containing mixed powder for comparison (Comparative Example 4),
Polytetrafluoroethylene fine powder (Asahi IC
The sample (Comparative Examples 5 and 6) to which CD123 manufactured by Company I was added was evaluated in the same manner. Table 2 shows the results.

[0041]

[Table 2]

[0042]

The polyolefin sheet for thermoforming of the present invention is excellent in surface gloss and has a very wide range of moldable temperatures in vacuum moldability, pressure moldability and the like. That is,
ADVANTAGE OF THE INVENTION According to this invention, the polyolefin sheet for thermoforming excellent in thermoformability which can be preferably utilized for various packaging containers, such as food packaging and pharmaceutical packaging, can be provided.

──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. ⁷ identification code FI C08L 27:18) C08L 27:18) (58) Investigated field (Int.Cl. ⁷ , DB name) C08L 23/00-23 / 36 C08F 2/44 C08J 3/12 C08J 5/18 C08L 27/18

Claims (5)

(57) [Claims] 1. A polytetrafluoroethylene-containing mixed powder (B) comprising polytetrafluoroethylene particles having a particle diameter of 10 μm or less and an organic polymer is mixed with 100 parts by weight of a polyolefin resin (A). A polyolefin sheet for thermoforming comprising a resin composition blended so that the amount of the ethylene component is 0.0001 to 20 parts by weight. 2. A master pellet comprising a polytetrafluoroethylene-containing mixed powder (B) comprising polytetrafluoroethylene particles having an average particle size of 10 μm or less and an organic polymer and a part of a polyolefin resin (A) is left. The amount of the polytetrafluoroethylene component in the polyolefin resin (A) is 100 in the total amount of the polyolefin resin (A).
A polyolefin-based sheet for thermoforming comprising a resin composition blended in an amount of 0.0001 to 20 parts by weight with respect to parts by weight. 3. A polytetrafluoroethylene-containing mixed powder (B) is prepared by mixing an aqueous dispersion of polytetrafluoroethylene particles having a particle diameter of 0.05 to 1.0 μm and an aqueous dispersion of organic polymer particles. 3. The polyolefin sheet for thermoforming according to claim 1, which is obtained by pulverization by solidification or spray drying. 4. A monomer constituting an organic polymer in the presence of an aqueous dispersion of polytetrafluoroethylene particles having a particle diameter of 0.05 to 1.0 μm, wherein the polytetrafluoroethylene-containing mixed powder (B) is 2. A polymer obtained by polymerizing and then pulverizing by coagulation or spray drying.
Or the polyolefin sheet for thermoforming according to 2. 5. A polytetrafluoroethylene-containing mixed powder (B) is prepared by mixing an aqueous dispersion of polytetrafluoroethylene particles having a particle diameter of 0.05 to 1.0 μm and an aqueous dispersion of organic polymer particles. The polyolefin sheet for thermoforming according to claim 1 or 2, which is obtained by emulsion-polymerizing a monomer having an ethylenically unsaturated bond in a dispersion, and then pulverizing the emulsion by coagulation or spray drying.