WO2015029594A1

WO2015029594A1 - Vinylidene chloride resin film and method for producing same

Info

Publication number: WO2015029594A1
Application number: PCT/JP2014/067770
Authority: WO
Inventors: 江尻哲男; 峯岸裕寿; 大森武雄
Original assignee: 株式会社クレハ
Priority date: 2013-08-27
Filing date: 2014-07-03
Publication date: 2015-03-05
Also published as: TWI598382B; CN105745259A; TW201508019A; JP6359543B2; CN105745259B; JPWO2015029594A1

Abstract

Provided are: a vinylidene chloride resin film which has a shear adhesion at 13°C of 5 kgf or more, preferably a vinylidene chloride vinyl chloride copolymer film, in particular, a vinylidene chloride resin film wherein the vinylidene chloride resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent the content of which based on the mass of a monomer component that forms the resin is less than 300 ppm; and a method for producing the vinylidene chloride resin film.

Description

Vinylidene chloride resin film and method for producing the same

The present invention relates to a vinylidene chloride resin film suitable for a wrap film having excellent adhesion between a packaged article and a film, and a method for producing the same.

Vinylidene chloride resin film is a film with excellent oxygen gas barrier properties, water vapor barrier properties (moisture resistance) and transparency, and is a film that can be heated in a microwave oven. In addition, it is widely used as a film for automatic filling and packaging of foods, etc., for the purpose of oxygen shielding, moisture prevention, etc. in the packaging of fresh fish, raw meat, processed meat, fresh vegetables, side dishes, etc.

The vinylidene chloride resin that forms the vinylidene chloride resin film is usually copolymerizable with vinylidene chloride and vinylidene chloride such as vinyl chloride from the viewpoint of film extrudability, crystallinity, transparency, softening temperature, etc. A vinylidene chloride copolymer obtained by copolymerizing a monomer (hereinafter sometimes referred to as “comonomer” or “comonomer”) is used.

Suspension polymerization and emulsion polymerization methods are known as methods for producing vinylidene chloride resins. The vinylidene chloride resin obtained by the emulsion polymerization method is likely to be thermally deteriorated due to the remaining emulsifier and the like, so that the suspension polymerization method is generally employed. The suspension polymerization method is a method in which a polymerization reaction is performed in a state where vinylidene chloride and a comonomer are suspended in an aqueous medium containing a suspending agent and a polymerization initiator. As a suspending agent, Patent Document 1 discloses cellulose ethers such as methylcellulose and hydroxypropylmethylcellulose, and the amount of the suspending agent is preferably 0.05 to 0.1% by weight based on the weight of the monomer. Is described. Patent Document 2 discloses that methylcellulose having a soluble content in 1,2-dichloroethane of 0.1 to 2.0% by weight is used as a suspending agent. Specific examples thereof include vinylidene chloride and vinyl chloride. It is described that 67.5 g of methylcellulose is used for a total of 67.5 kg.

The vinylidene chloride-based resin film is usually produced by melt-extruding a vinylidene chloride-based resin and then stretching in many cases, and is wound around a paper tube and stored in a cosmetic box. It has been attempted to improve extrusion processability and film characteristics by adding various additives such as a plasticizer, a stabilizer, and a tackifier to the vinylidene chloride resin. In addition, especially in the use of the film for automatic filling packaging, in order to prevent the trouble in the manufacturing process and packaging process of a vinylidene chloride-type resin film, a lubricant may be contained if desired.

In particular, since vinylidene chloride-based resin films are used as wrap films and films for automatic filling and packaging, adhesion between the film and an article to be packaged and adhesion between films are required. Patent Document 3 discloses a film provided with a mineral oil such as liquid paraffin, and examples of the application method include application to the film, impregnation, spraying, and kneading in an extrusion process. Patent Document 4 discloses that migration of the liquid paraffin provided to improve the adhesion of the vinylidene chloride resin film, the adhesion of the film, and the drawability from the cosmetic box storing the film Therefore, it is disclosed that liquid paraffin is added to a vinylidene chloride resin before extrusion molding and liquid paraffin is applied to the surface of the molded film.

In addition, Patent Document 5 discloses a liquid paraffin, a surfactant, and the like that are liquid at room temperature and thermally stable at the time of melt molding in order to provide adhesion to the vinylidene chloride-based resin film. It is disclosed that a tackifier having a viscosity of 10 to 100 cps at 25 to 25 ° C. is contained in an amount of 0.01 to 3 parts by weight with respect to 100 parts by weight of the resin. Furthermore, if the addition amount of the tackifier is too large or the viscosity is too small, the extrudability tends to deteriorate, and the film tends to be sticky and difficult to handle, while the viscosity is large. It is disclosed that even if it becomes too much, the extrudability tends to deteriorate and is not preferable.

Therefore, in the vinylidene chloride-based resin film, a vinylidene chloride-based resin film suitable for a wrap film having excellent adhesion between a packaged body and a film is required without containing or applying a tackifier such as liquid paraffin, Furthermore, there is a demand for a vinylidene chloride resin film that is inferior in drawability and transparency.

JP 10-504847 A (corresponding to US Pat. No. 5,342,910) JP 2003-137911 A Japanese Patent Laid-Open No. 10-87876 JP 2004-202752 A JP-A-10-324809

A first aspect of the subject of the present invention is to provide a vinylidene chloride-based resin film suitable for a wrap film having excellent adhesion between a packaged body and a film without requiring addition or application of a tackifier. It is in. Another aspect of the present invention is to provide a method for producing the vinylidene chloride resin film.

As a result of intensive studies on solving the above-mentioned problems, the present inventors have found that a very small amount of vinylidene chloride-based resin film having a shear adhesion at a temperature of 13 ° C. or more, particularly a vinylidene chloride-based resin, of a predetermined value or more. It has been found that the film can be solved by using the film prepared by suspension polymerization in the presence of a suspending agent in a content amount, and the present invention has been completed.

According to the first aspect of the present invention, there is provided (1) a vinylidene chloride resin film characterized by having a shear adhesion at a temperature of 13 ° C. of 5 kgf or more.

According to the first aspect of the present invention, the following vinylidene chloride resin films (2) to (7) are provided as embodiments.
(2) A vinylidene chloride resin was prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the resin is less than 300 ppm. The vinylidene chloride-based resin film of (1) above.
(3) The vinylidene chloride resin film according to (2), wherein the content of the suspending agent based on the total mass including the aqueous medium is less than 150 ppm.
(4) The vinylidene chloride resin film according to any one of (1) to (3), which does not contain a tackifier.
(5) The vinylidene chloride resin film according to any one of (1) to (3), which contains a tackifier.
(6) The vinylidene chloride resin film according to (5), wherein the vinylidene chloride resin is prepared by suspension polymerization in the presence of a tackifier.
(7) The vinylidene chloride resin film according to any one of (1) to (6), wherein the vinylidene chloride resin is a vinylidene chloride / vinyl chloride copolymer.

According to another aspect of the present invention, (8) the following step 1 and step 2:
1) A vinylidene chloride resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the vinylidene chloride resin is less than 300 ppm. Step 1; and 2) Melting, extruding and stretching a vinylidene chloride-based resin composition containing a vinylidene chloride-based resin Step 2; the shear adhesion at a temperature of 13 ° C. is 5 kgf or more. A method for producing a resin-based resin film is provided.

According to the other aspect of this invention, the manufacturing method of the vinylidene chloride resin film of the following (9) and (10) is provided as an embodiment.
(9) The method for producing a vinylidene chloride-based resin film according to (8), wherein Step 1 and Step 2 are carried out without containing a tackifier.
(10) The method for producing a vinylidene chloride-based resin film according to (8), wherein step 1 is a suspension polymerization in the presence of a tackifier.

According to the first aspect of the present invention, a vinylidene chloride-based resin film, particularly a vinylidene chloride-based resin, which has a shear adhesion at a temperature of 13 ° C. of 5 kgf or more, is a simple substance that forms the resin. By adding the tackifier, the film is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the body component is less than 300 ppm. There is an effect that a vinylidene chloride resin film suitable for a wrap film or the like having excellent adhesion between a packaged body and a film is provided without requiring application.

According to another aspect of the present invention, the following step 1 and step 2:
1) A vinylidene chloride resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the vinylidene chloride resin is less than 300 ppm. Step 1; and 2) Melting, extruding and stretching a vinylidene chloride-based resin composition containing a vinylidene chloride-based resin Step 2; the shear adhesion at a temperature of 13 ° C. is 5 kgf or more. By virtue of the method for producing a resin-based resin film, it is possible to easily produce a vinylidene chloride-based resin film suitable for a wrap film having excellent adhesion between a packaged body and a film without adding or applying a tackifier. The effect that the method which can be performed is provided is show | played.

1. Vinylidene chloride resin According to the present invention, the vinylidene chloride resin for forming the vinylidene chloride resin film characterized in that the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more has conventionally been an oxygen gas barrier property, a water vapor barrier property ( Uses vinylidene chloride resin to form vinylidene chloride resin films that have been used as wrap films or films for automatic filling and packaging, because it is excellent in moisture resistance and transparency, and can be heated in a microwave oven. can do.

Specifically, the vinylidene chloride-based resin in the present invention is 60 to 98% by mass of vinylidene chloride and 2 to 40% by mass of a monomer (comonomer) copolymerizable with vinylidene chloride (a chloride). Vinylidene chloride copolymer formed from the total mass of vinylidene and comonomer is 100% by mass).

Examples of monomers (comonomer) copolymerizable with vinylidene chloride include vinyl chloride; methyl acrylate, ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, lauryl acrylate, and stearyl acrylate. Acrylic acid alkyl esters (alkyl group having 1 to 18 carbon atoms); methyl methacrylate, butyl methacrylate, 2-ethylhexyl methacrylate, lauryl methacrylate, stearyl methacrylate, etc. 18); vinyl cyanide such as acrylonitrile and methacrylonitrile; aromatic vinyl such as styrene; vinyl ester of aliphatic carboxylic acid having 1 to 18 carbon atoms such as vinyl acetate; methyl vinyl ether, ethyl vinyl ether, isobutyl vinyl ether Alkyl vinyl ethers such as lauryl vinyl ether (alkyl group having 1 to 18 carbon atoms); vinyl polymerizable unsaturated carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid; maleic acid, fumaric acid, itaconic acid, etc. In addition to dialkyl monomers, functional group-containing monomers, polyfunctional alkyl esters of vinyl polymerizable unsaturated carboxylic acids (may be partial esters, alkyl groups having 1 to 18 carbon atoms); Can be mentioned. These comonomer can be used individually or in combination of 2 or more types. Among the comonomer, vinyl chloride, methyl acrylate, or butyl acrylate is preferable. A particularly preferred comonomer is vinyl chloride. Therefore, a particularly preferred vinylidene chloride-based resin is a vinylidene chloride / vinyl chloride copolymer.

The content of vinylidene chloride forming the vinylidene chloride resin is preferably 70% by mass or more, more preferably 80% by mass or more, with the total mass of vinylidene chloride and comonomer being 100% by mass. The upper limit of the content ratio of vinylidene chloride is not particularly limited, but is usually 97% by mass and often 95% by mass from the viewpoint of extrudability. Therefore, the content ratio of the comonomer forming the vinylidene chloride resin is preferably 30% by mass or less, more preferably 20% by mass or less. The content of the comonomer has no particular lower limit, but is usually 3% by mass or more, and in many cases 5% by mass or more.

2. Preparation of vinylidene chloride-based resin The shear adhesive strength at a temperature of 13 ° C. of the present invention is 5 kgf or more, vinylidene chloride-based resin forming a vinylidene chloride-based resin film, specifically, vinylidene chloride, and A copolymer of a monomer (comonomer) copolymerizable with vinylidene chloride can be usually produced by suspension polymerization or emulsion polymerization of vinylidene chloride and a comonomer. The suspension polymerization method is a method in which polymerization is performed with a polymerization initiator in an aqueous medium containing a suspending agent in a state where mixed droplets of vinylidene chloride and a comonomer are formed by mechanical stirring. . The emulsion polymerization method is a method of polymerizing vinylidene chloride and a comonomer in a surfactant micelle in an aqueous medium using an emulsifier (surfactant) and a water-soluble polymerization initiator. Generally, a vinylidene chloride resin produced by an emulsion polymerization method tends to cause thermal degradation of the resin due to the remaining emulsifier (surfactant). Since the vinylidene chloride resin film having a shear adhesion of 13 kg at the temperature of the present invention is 5 kgf or more is produced by melt extrusion molding, vinylidene chloride is produced by suspension polymerization using a suspending agent. It is preferable to produce a resin.

[Suspension]
Examples of the suspending agent used for producing the vinylidene chloride resin by suspension polymerization include water-soluble cellulose derivatives such as methyl cellulose, ethyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropoxymethyl cellulose, and carboxymethyl cellulose; polyvinylpyrrolidone, Homopolymers such as polyacrylic acid, polyvinyl alcohol, polymethyl vinyl ether, polyacrylamide, and polyethyleneimine; maleic anhydride / vinyl acetate copolymers, various random copolymers, graft copolymers, block copolymers, macromonomers And the like; natural polymer substances such as starch and gelatin. As the suspending agent, methyl cellulose, hydroxypropyl cellulose, and hydroxypropoxymethyl cellulose are preferable, and methyl cellulose is particularly preferable. One suspending agent may be used, or two or more suspending agents may be used in combination. Further, the suspending agent may be used as it is, may be used in the form of an aqueous solution, water emulsion or water suspension, or may be used after being dissolved in an organic solvent such as toluene. If desired, a co-stabilizer may be used in addition to the suspending agent described above. Examples of the auxiliary stabilizer include anionic surfactants, cationic surfactants, nonionic surfactants, amphoteric surfactants, and long-chain alcohols.

The content of the suspending agent in preparing the vinylidene chloride-based resin for forming the vinylidene chloride-based resin film, characterized in that the shear adhesive strength at a temperature of 13 ° C. of the present invention is 5 kgf or more. The content based on the mass of the monomer, that is, the monomer component forming the vinylidene chloride resin, is preferably less than 300 ppm. Therefore, in the vinylidene chloride resin film of the present invention, the content of the vinylidene chloride resin based on the mass of the monomer component forming the resin (hereinafter referred to as “content based on monomer mass”) Is preferably prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent of less than 300 ppm. That is, vinylidene chloride / vinyl chloride prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the vinylidene chloride resin is less than 300 ppm. A vinylidene chloride-based resin film formed from a copolymer and having a shear adhesion at a temperature of 13 ° C. of 5 kgf or more is preferable. The content of the suspending agent based on the monomer mass is more preferably less than 280 ppm, and still more preferably less than 260 ppm. The content based on the monomer mass of the suspending agent has no particular lower limit, but from the viewpoint of dispersion stability of the monomer component forming the vinylidene chloride resin during suspension polymerization in an aqueous medium, Usually, it is 30 ppm or more, and in many cases, 50 ppm or more. Suspending agents can be added all at once, or can be added in portions, and the timing of their addition is not limited.

When the vinylidene chloride resin is prepared by suspension polymerization in the presence of a suspending agent having a monomer mass basis content of 300 ppm or more, the resulting vinylidene chloride resin film at a temperature of 13 ° C. The shear adhesion may not be 5 kgf or more, or the molding processability of the vinylidene chloride resin may be deteriorated. For example, from the viewpoint of dispersion stability of the monomer component that forms the vinylidene chloride resin during suspension polymerization, conventionally, the content of the suspending agent in the aqueous medium based on the monomer mass is 300 to 8000 ppm, In many cases, it is 350 to 5000 ppm, and in most cases 400 to 3000 ppm. However, if the content of the suspending agent is too large, the vinylidene chloride resin (usually in the form of particles) obtained by suspension polymerization is surrounded. As a result of the strong coating of the suspending agent, it is assumed that the resin (particles) will not be sufficiently melted in the melt molding, which will deteriorate the moldability of the film. As a result of increasing the non-uniformity of the surface of the vinylidene chloride-based resin film obtained by a minute amount of insoluble matter, the shear adhesion is less than 5 kgf, often less than 4.7 kgf, If Tondono is assumed that less than 4.5 kgf.

Furthermore, from the viewpoint of the balance between the stability of the polymerization reaction system during suspension polymerization and the molding processability and film properties of the vinylidene chloride resin, the content of the suspending agent during suspension polymerization is determined based on the vinylidene chloride resin. In addition to the monomer components that form the suspension, other components contained in the polymerization reaction system in which suspension polymerization is performed in an aqueous medium and the total suspension including the aqueous medium (water, alcohol, etc.) of the suspension Of the suspending agent based on the total mass including the aqueous medium (hereinafter sometimes referred to as “total mass-based content”) is preferably less than 150 ppm, and less than 135 ppm. More preferably, it is more preferably less than 120 ppm. The content of the suspending agent based on the total mass is not particularly limited, but is usually 15 ppm from the viewpoint of dispersion stability of the monomer component forming the vinylidene chloride resin during suspension polymerization in an aqueous medium. Above, in many cases 25 ppm or more.

Also, from the viewpoint of further improving the balance between the stability of the polymerization reaction system during suspension polymerization and the above-described moldability and film properties, the suspension agent during suspension polymerization is based on the mass of the aqueous medium. The content (hereinafter sometimes referred to as “content based on an aqueous medium”) is preferably less than 260 ppm, more preferably less than 240 ppm, and even more preferably less than 220 ppm. The content of the suspending agent based on the aqueous medium has no particular lower limit, but is usually 25 ppm from the viewpoint of dispersion stability of the monomer component forming the vinylidene chloride resin during suspension polymerization in the aqueous medium. Above, in many cases 40 ppm or more.

(Polymerization initiator)
Examples of the polymerization initiator used for producing the vinylidene chloride resin include percarbonate initiators such as diisopropyl peroxydicarbonate, dioctyl peroxydicarbonate, and dilauryl peroxydicarbonate; Perester initiators such as oxyneodecanate, tertiary hexyl peroxyneodecanoate, amyl peroxyneodecanate; lauroyl peroxide, diisobutyl peroxide, 2 ethylhexanoyl peroxide, 3.5.5 trimethyl Diacyl peroxide initiators such as hexanoyl peroxide; di-tertiary alkyls such as tertiary butyl hydroperoxide, di-tertiary butyl peroxide and di-isopropyl peroxydicarbonate -Oxydiglycolate initiators; 2.2 'azobisisobutyronitrile, 2.2' azobis-2.4 dimethylvaleronitrile, 2.2 'azobis-4methoxy-2.4 dimethylvaleronitrile, etc. Examples thereof include azo initiators; water-soluble peroxides such as potassium persulfate and ammonium persulfate, or systems obtained by adding a reducing agent such as amine and sodium bisulfite to these. One polymerization initiator may be used, or two or more polymerization initiators may be used in combination. The polymerization initiator may be used as it is, may be used as an aqueous solution or an aqueous dispersion, or may be used as an organic solvent solution such as toluene.

The amount of the polymerization initiator used is preferably 100 to 7000 ppm, more preferably 300 to 5000 ppm, based on the weight of vinylidene chloride and a comonomer, that is, the monomer component forming the vinylidene chloride resin. is there. More preferably, it is 500 to 3000 ppm.

[Other additives]
In preparing the vinylidene chloride-based resin for forming the vinylidene chloride-based resin film, characterized in that the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more, the suspending agent and the polymerization initiator described above are prepared. In addition to these, various other additives usually used in the preparation of vinylidene chloride-based resins can be contained. That is, in order to improve the extrusion processability of the obtained vinylidene chloride resin or to improve various properties of the vinylidene chloride resin film formed from the vinylidene chloride resin in a balanced manner, for example, plastic Agents, stabilizers, antioxidants, pH adjusters, UV absorbers, tackifiers, antistatic agents, antiblocking agents, antifogging agents, fillers (fillers), pigments, etc. The optimal combination is selected. Moreover, depending on a use or desired, a lubricant can be contained as another additive. As the other additive, either an organic substance (which may be another polymer) or an inorganic substance can be used.

Conventionally, a vinylidene chloride-based resin film suitable for a wrap film having excellent adhesion between a packaged body and a film usually contains a tackifier, and the tackifier is a step of preparing a vinylidene chloride-based resin. That is, it is added to the monomer component forming the vinylidene chloride resin in the polymerization stage, or is added in the process of melt-extruding and stretching the prepared vinylidene chloride resin, that is, in the film production stage. The vinylidene chloride resin film having a shear adhesion at a temperature of 13 ° C. of the present invention of 5 kgf or more is a polymerization stage (a process for preparing a vinylidene chloride resin) or a film production stage (vinylidene chloride system). In any of the steps of melt extrusion and stretching of the resin composition), it can be obtained by a production method that does not contain a tackifier, but in the polymerization stage (step of preparing vinylidene chloride resin) It can also be obtained by preparing a vinylidene chloride resin by suspension polymerization in the presence of an agent.

[Tackifier]
The tackifier imparts a property of easily adhering to an object. Examples of the tackifier include surfactants such as sorbitan fatty acid ester, propylene glycol fatty acid ester, glycerin fatty acid ester, such as sorbitan mono (tri) oleate and glycerin mono (tri) oleate, paraffinic or cycloparaffinic liquid. And saturated hydrocarbons. One type of tackifier may be used, or two or more types may be used in combination. Examples of the liquid saturated hydrocarbon include naphthenic process oil, paraffin wax, liquid paraffin and the like, and liquid paraffin is particularly preferable. The vinylidene chloride resin film characterized by having a shear adhesion at a temperature of 13 ° C. of the present invention of 5 kgf or more can be free of a tackifier. However, the vinylidene chloride-based resin film of the present invention may contain a tackifier, and in that case, the shear adhesion at a temperature of 13 ° C. of the film can often be further increased.

The content of the tackifier when preparing a vinylidene chloride resin by suspension polymerization in the presence of the tackifier is based on the mass of the monomer component that forms the vinylidene chloride resin from the viewpoint of drawability. The content (content based on the mass of the monomer) is usually in the range of 100 to 10000 ppm, preferably 200 to 5000 ppm, more preferably 300 to 3000 ppm, and still more preferably 400 to 1000 ppm. When there is too much content of a tackifier, extrusion processability may fall, or the vinylidene chloride-type resin film obtained may become sticky, and handling may become difficult. The above-mentioned total mass content of the tackifier is usually 50 to 5000 ppm, preferably 100 to 2500 ppm.

[Plasticizer]
As the plasticizer, a plasticizer conventionally contained in a vinylidene chloride resin can be used. Examples include tributyl acetyl citrate (ATBC), glycerin diacetyl monolaurate (GDAML), dibutyl sebacate (DBS), dioctyl sebacate, and diacetylated monoglyceride (DALG). The plasticizer is used in a proportion of usually 500 to 100,000 ppm, in many cases 5000 to 80,000 ppm based on the monomer mass.

[Stabilizer]
As a stabilizer, the stabilizer conventionally contained in the vinylidene chloride resin can be used. Examples include epoxidized oils such as epoxidized soybean oil (ESBO) or epoxidized linseed oil (ELO); amide derivatives of fatty acid alkyl esters; magnesium hydroxide; tetrasodium pyrophosphate and the like. The stabilizer is used in a proportion of usually 300 to 50,000 ppm, often 1000 to 40000 ppm based on the monomer mass.

[Antioxidant]
As an antioxidant, the antioxidant conventionally contained in the vinylidene chloride resin can be used. For example, phenolic antioxidants such as triethylene glycol bis-3- (3-tertiarybutyl-4-hydroxy-5-methylphenyl) propionate (sometimes referred to as “antioxidant T”); dilaurylthio Dipropionate (also referred to as "antioxidant S"), distearyl thiodipropionate, etc., alkyl thiodipropionate alkyl ester having 12 to 18 carbon atoms; trisnonylphenyl phosphite, distearyl pentaerythritol diester Phosphite antioxidants such as phosphite; and the like. One antioxidant may be used, or two or more antioxidants may be used in combination. Preferably, triethylene glycol bis-3- (3-tertiarybutyl-4-hydroxy-5-methylphenyl) propionate (antioxidant T) and thiodipropionic acid alkyl ester are used in combination. The antioxidant is used in a proportion of usually 5 to 50000 ppm, often 15 to 10000 ppm, based on the monomer mass. In addition, it is preferable that a part of the antioxidant is present in the polymerization system in advance to initiate the polymerization. In addition, the polymerization reaction can be stopped by adding an antioxidant to the polymerization system.

[PH adjuster]
It is preferable to adjust the pH of the polymerization system to pH 3 to 9, more preferably to pH 4 to 8. In order to adjust the pH, it is preferable to use an inorganic phosphate as a pH adjuster. As the inorganic phosphate, phosphates such as alkali metal salts such as phosphoric acid, metaphosphoric acid and polyphosphoric acid, or alkaline earth metal salts are preferable. For example, there are sodium pyrophosphate, potassium pyrophosphate, disodium dihydrogen pyrophosphate, dipotassium dihydrogen pyrophosphate, monobasic sodium phosphate, monobasic potassium phosphate, etc., and these hydrates can also be used. . In particular, the combined use of sodium pyrophosphate and disodium dihydrogen pyrophosphate, or the combined use of sodium pyrophosphate and sodium monophosphate is preferable because the pH of the polymerization system can be easily adjusted. The pH adjuster is usually used at a monomer mass-based content of 1 to 10000 ppm, often 10 to 1000 ppm.

[Lubricant]
The vinylidene chloride resin forming the vinylidene chloride resin film, characterized in that the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more, particularly when used for wrap film applications, needs to contain a lubricant. However, if used for autofill packaging applications, it can optionally contain a lubricant.

Conventionally, the lubricant contained in the vinylidene chloride resin can be selected as the lubricant. Examples thereof include inorganic lubricants such as silicon dioxide, zeolite and calcium carbonate, and organic lubricants such as saturated fatty acid amides, unsaturated fatty acid amides and substituted amides. The content of the lubricant based on the monomer mass is usually in the range of 100 to 10,000 ppm, preferably 150 to 7000 ppm, more preferably 200 to 5000 ppm.

[Other additives]
In addition to the additives already specifically described, other additives can be further added in the step of preparing the vinylidene chloride-based resin, that is, the polymerization stage. As other additives, various additives conventionally contained in vinylidene chloride resins can be selected, and the content thereof can be determined as appropriate. For example, titanium oxide pigments, which are also fillers, are effective in preventing discoloration of food contents such as sausages due to ultraviolet rays, but may easily cause resin degradation products to adhere to the die outlet. Accordingly, selection of the optimum additive and its content is important.

(Suspension polymerization)
The method for suspension polymerization of a vinylidene chloride resin for forming a vinylidene chloride resin film characterized in that the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more is not particularly limited, but usually 20 to Suspension polymerization can be carried out batchwise or continuously under the conditions of a polymerization temperature of 95 ° C. and a polymerization pressure of normal pressure to 1 MPa. Specifically, for example, in a stainless steel reactor (polymerizer), a suspending agent (which may be an aqueous solution) and a pH adjusting agent are dissolved in an aqueous medium such as deionized water or distilled water, and necessary. Accordingly, the air in the system is replaced to create an atmosphere such as nitrogen or argon gas. Next, a polymerization initiator, a stabilizer, a plasticizer, and, if necessary, a tackifier and other additives are dissolved in a mixed monomer of vinylidene chloride and a comonomer, and pressed into the aqueous medium. To prepare a raw material mixture that is a suspension. Subsequently, the charged raw material mixture is stirred with a stirrer to form droplets of a mixed monomer of vinylidene chloride and a comonomer, and polymerization is usually started by raising the temperature. Further, the polymerization reaction is continued while adjusting the temperature (preferably raising the temperature continuously). The polymerization temperature and polymerization time are appropriately determined depending on the type and amount of vinylidene chloride and comonomer, the type and amount of polymerization initiator, and the like. It is ˜100 hours, preferably 2 to 60 hours, more preferably 3 to 50 hours. After the polymerization reaction proceeds, the polymerization can be stopped by introducing an antioxidant into the polymerization system. After the polymerization reaction is completed, the slurry containing the vinylidene chloride resin is collected and dehydrated, washed, and dried to obtain the vinylidene chloride resin.

3. The vinylidene chloride resin film is characterized in that the shear adhesion at 13 ° C. of the present invention is 5 kgf or more, and the vinylidene chloride resin film is suitable for wrapping films and the like having excellent adhesion between the package and the film. It is a vinylidene-based resin film, and is formed from a vinylidene chloride-based resin composition that contains a vinylidene chloride-based resin and additives and / or other resins that are included as necessary.

[Vinylidene chloride resin composition]
In order to form a vinylidene chloride resin film from a vinylidene chloride resin, in order to improve the various properties of the vinylidene chloride resin film in a balanced manner according to the purpose, for example, a plasticizer, a stabilizer, an antioxidant, etc. , UV absorbers, tackifiers, antistatic agents, antiblocking agents, antifogging agents, antibacterial agents, fillers (fillers), pigments, lubricants, etc., depending on the application or desired. The vinylidene chloride resin prepared by the suspension polymerization described above contains the stabilizer, plasticizer and other various components added during the polymerization reaction, so that the desired vinylidene chloride resin film is contained. Depending on the characteristics, various components added during the polymerization reaction may be added, or various components not added during the polymerization reaction may be added to the vinylidene chloride resin to obtain a desired composition. It can be set as the vinylidene chloride-type resin composition which has these. The quantity of the component mix | blended with a vinylidene chloride type-resin can be suitably determined according to the kind of component and the various characteristics of the vinylidene chloride-type resin film calculated | required.

[Other polymers]
If desired, the vinylidene chloride-based resin composition may contain other polymers as a resin component in addition to the vinylidene chloride-based resin. Thereby, the extrudability of the vinylidene chloride resin can be improved, and various properties of the vinylidene chloride resin film formed from the vinylidene chloride resin can be improved in a balanced manner according to the purpose. Other polymers include ethylene / vinyl acetate copolymers, copolymers of ethylene and acrylic acid, methacrylic acid or their alkyl esters, or MBS resins (methyl methacrylate / butadiene / styrene copolymers). Is mentioned. The content when these other polymers are contained is not particularly limited, but is usually 0.1 to 20 parts by mass with respect to 100 parts by mass of the vinylidene chloride resin, and in many cases 1 to 15 parts by mass. It is.

The thickness of the vinylidene chloride resin film of the present invention is not particularly limited, but is usually in the range of 1 to 50 μm, preferably 4 to 45 μm, more preferably 7 to 40 μm. If the thickness is too large, the cutability may be insufficient, or the feel of the film may be inferior. If the thickness is too small, the film may be easily broken.

[Shear adhesion at a temperature of 13 ° C]
The vinylidene chloride resin film of the present invention is characterized in that the shear adhesion at a temperature of 13 ° C. is 5 kgf or more. Since the vinylidene chloride resin film has a shear adhesion of 5 kgf or more, the vinylidene chloride resin film has sufficient adhesion to tableware and the like, in particular, food containers that contain and store food in the refrigerator, and has a drawability. And a vinylidene chloride-based resin film that is not inferior in transparency. The vinylidene chloride resin film preferably has a shear adhesion at a temperature of 13 ° C. of 5.5 kgf or more, more preferably 6 kgf or more. The shear adhesive strength of the vinylidene chloride-based resin film at a temperature of 13 ° C. has no particular upper limit, but from the viewpoint of having good drawability and transparency, it is usually 30 kgf or less, often 15 kgf or less. Or less than 8 kgf.

[Measurement method of shear adhesion at a temperature of 13 ° C.]
The measuring method of the shear adhesive strength of the vinylidene chloride resin film at a temperature of 13 ° C. is as follows. That is, from a vinylidene chloride resin film stored for 24 hours or more in a thermostatic chamber at a temperature of 13 ° C., the sample film is cut into a size of 50 mm wide and 155 mm long. In an environment with a temperature of 13 ° C., a substantially rectangular parallelepiped box having a surface roughness Ra of 0.05 μm, a mirror finished stainless steel plate with a thickness of 2 mm, a length of 125 mm, a width of 290 mm, and a height of 90 mm and having a top surface opened, The sample film is bridged in the length direction of the box, and both ends of the sample film are in close contact with both side surfaces of the stainless steel box so as to be 15 mm (width 50 mm) in the height direction of the box. And press with your finger. Next, using a Tensilon universal testing machine, the substantially central portion of the sample film is pressed with a φ45 mm push rod at a speed of 50 mm / min. The maximum value of the pressing load when the sample film is removed from the adhesion surface to the stainless steel box without breaking is measured and taken as the shear adhesion strength (unit: kgf) of the vinylidene chloride resin film at a temperature of 13 ° C.

The vinylidene chloride resin film characterized in that the shear adhesive strength at a temperature of 13 ° C. of the present invention is 5 kgf or more is a vinylidene chloride resin film suitable for a wrap film having excellent adhesion between a packaged body and films. Therefore, it is not necessary to apply a tackifier, such as liquid paraffin, to the film surface that has been conventionally used to achieve the above-mentioned adhesion. However, if desired, it can also be used as a vinylidene chloride resin film in which a tackifier is applied to the film surface.

[Drawability]
The vinylidene chloride resin film characterized in that the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more has good drawability, and the film is wound around and stored in a paper tube (decorative box etc.) Can be easily pulled out from. The drawability of the vinylidene chloride resin film can be evaluated by the following method. That is, a vinylidene chloride resin film wound around a paper tube having an outer diameter of 36 mm is slit into a width of 30 cm, and stored in a commercially available wrap film case (manufactured by Kureha Co., Ltd.), and kept in a temperature-controlled room at 23 ° C. for 24 hours. After storage, evaluate by pulling out by hand. The evaluation criteria are as follows. If the evaluation is “◎”, it can be evaluated that the drawability is good.
<Evaluation criteria>
A: There is no blocking between the films, and the film can be pulled out smoothly. ○: There is almost no blocking between the films. X: There is a blocking between the films, and the paper tube may jump out of the case.

〔transparency〕
The vinylidene chloride resin film characterized in that the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more has good transparency. The transparency of the film can be evaluated by the following method. That is, when the HAZE value measured for a vinylidene chloride resin film stored in a thermostatic chamber at a temperature of 23 ° C. for 24 hours is 2% or less, the vinylidene chloride resin film is evaluated as transparent. When the HAZE value exceeds 2%, the vinylidene chloride resin film cannot be evaluated as transparent, and when it exceeds 5%, it is evaluated as opaque.

4). Method for producing film formed from vinylidene chloride resin The film formed from a vinylidene chloride resin characterized in that the shear adhesion at a temperature of 13 ° C of the present invention is 5 kgf or more is a film known per se. It can manufacture by a manufacturing method and the manufacturing method is not specifically limited. From the viewpoint of obtaining a film that is efficient and stable and has excellent adhesion, the following Step 1 and Step 2:
1) A vinylidene chloride resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the vinylidene chloride resin is less than 300 ppm. Step 1; and 2) Melting, extruding and stretching a vinylidene chloride-based resin composition containing a vinylidene chloride-based resin Step 2; the shear adhesion at a temperature of 13 ° C. is 5 kgf or more. A method for producing a resin film is preferred.

That is, the vinylidene chloride resin film characterized in that the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more is preferably (Step 1) the mass of the monomer component forming the vinylidene chloride resin. Vinylidene chloride containing a vinylidene chloride resin prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent having a content of less than 300 ppm based on It can be produced by melt-extruding a resin-based resin composition and further stretching as necessary, and more preferably, (step 2) a step of melt-extruding and stretching the vinylidene chloride-based resin composition. Can be easily manufactured.

Specifically, vinylidene chloride prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the vinylidene chloride resin is less than 300 ppm. As described above, a vinylidene chloride resin composition containing an additive and / or other resin to be contained as necessary is melt-extruded by a commonly practiced method. More specifically, a vinylidene chloride resin, additives, and / or other resins (sometimes collectively referred to as “raw materials”) that form the vinylidene chloride resin composition are used as a Henschel high-speed mixer, blade A method of mixing by using a known dry mixing apparatus such as a blender or ribbon blender, usually at room temperature to 80 ° C., and in some cases over 80 ° C., or on the extruder Depending on the method of mixing these raw materials using a screw feeder or the like in the hopper device, the raw material of the powder mixture is supplied to the extruder, or the raw material once extruded into pellets is supplied to the extruder. Then, it is melt extruded into a sheet. In melt extrusion, a raw material is heated and melted in a cylinder, and extruded from a T die or an annular die (circular die) to obtain a flat film or a tubular film. If desired, the tubular film may be cut in the direction of the extrusion axis to form a flat film having a single thickness or a double thickness.

Subsequently, a vinylidene chloride resin film can be obtained by stretching a flat film or a tubular film uniaxially or biaxially by a known stretching method such as a tenter method, a drum method, an inflation method, etc., and is not particularly limited. However, the inflation method is preferred. In addition, after extending | stretching, a tubular film is good also as a flat film of single thickness or double thickness by cutting in the direction of an extrusion axis if desired. The draw ratio can be appropriately determined and is not particularly limited, but is usually 2 to 6 times in both the machine direction (sometimes referred to as “MD”) and the transverse direction (sometimes referred to as “TD”), preferably 2.5 to 5.5 times.

According to the present invention, the shear adhesion at a temperature of 13 ° C. of the present invention is 5 kgf or more by the method for producing a vinylidene chloride-based resin film, wherein Step 1 and Step 2 are performed without containing a tackifier. A vinylidene chloride-based resin film can be produced. Further, according to the present invention, the step 1 for preparing the vinylidene chloride-based resin is carried out according to the above-described method for producing a vinylidene chloride-based resin film in which suspension polymerization is performed in the presence of a tackifier. A vinylidene chloride resin film having a shear adhesion at 5 ° C. of 5 kgf or more can be produced.

Hereinafter, the present invention will be further described with reference to examples and comparative examples, but the present invention is not limited to these examples. The measurement methods of the properties or physical properties of the resin raw materials and films in the examples and comparative examples are as follows.

[Film thickness]
The thickness of the vinylidene chloride-based resin film was measured using a 0.001 mm dial gauge manufactured by Teclock Co., Ltd.

[Shear adhesion at a temperature of 13 ° C]
As described above, the shear adhesion strength of the vinylidene chloride resin film at a temperature of 13 ° C. was cut into a size of 50 mm in width and 155 mm in length from a vinylidene chloride resin film stored in a temperature-controlled room at a temperature of 13 ° C. for 24 hours or more. And a rectangular parallelepiped box having a length of 125 mm, a width of 290 mm and a height of 90 mm made of a mirror-finished stainless steel plate having a surface roughness Ra of 0.05 μm and a thickness of 2 mm. Measurement was performed using a Tensilon universal testing machine RTG-1210 manufactured by Day.

[Drawability]
The drawability of the vinylidene chloride resin film was evaluated by the following method. That is, a vinylidene chloride resin film wound around a paper tube having an outer diameter of 36 mm is slit into a width of 30 cm, and stored in a commercially available wrap film case (manufactured by Kureha Co., Ltd.), and kept in a temperature-controlled room at 23 ° C. for 24 hours. After storage, it was pulled out by hand for evaluation. The evaluation criteria were as follows. When the evaluation was “◎”, it was evaluated that the drawability was good.
<Evaluation criteria>
A: There is no blocking between the films, and the film can be pulled out smoothly. ○: There is almost no blocking between the films. X: There is a blocking between the films, and the paper tube may jump out of the case.

〔transparency〕
The transparency of the film was evaluated by the following method. That is, when the HAZE value measured for a vinylidene chloride resin film stored in a thermostatic chamber at a temperature of 23 ° C. for 24 hours was 2% or less, the vinylidene chloride resin film was evaluated as transparent.

[Example 1]
(Preparation of vinylidene chloride resin)
In a stainless steel 20 L autoclave having a chi-type stirrer, 1.662 g of methylcellulose as a suspending agent, 2.4 g of sodium pyrophosphate decahydrate and 2.4 g of sodium dihydrogen pyrophosphate decahydrate as a pH adjuster were dissolved. 7700 g of deionized water was added, and the inside of the system was purged with nitrogen. Next, 10 g of diisopropyl peroxydicarbonate as a polymerization initiator, 295 g of tributyl acetyl citrate as a plasticizer, 161.0 g of epoxidized soybean oil as a stabilizer, triethylene glycol bis-3- (3-tertiary as an antioxidant Butyl-4-hydroxy-5-methylphenyl) propionate (Ciba Geigy, trade name: Irganox (registered trademark) 245: antioxidant T) 0.166 g, mixed monomer of 5453 g of vinylidene chloride and 1197 g of vinyl chloride (The content ratio of vinylidene chloride was 82% by mass.) The mixture dissolved in the mixture was press-fitted to obtain a charged raw material mixture. The suspending agent in the raw material mixture is a mixed monomer, that is, a content based on the mass of the monomer component forming the prepared vinylidene chloride resin (hereinafter referred to as “monomer standard”). Is 250 ppm, the content based on the mass of the aqueous medium (hereinafter referred to as “aqueous medium standard”) is 216 ppm, and the content based on the total mass including the aqueous medium (hereinafter referred to as “total mass standard”). Was 112 ppm.

Polymerization is started by raising the temperature of these charged raw material mixtures to 47 ° C. with stirring, and the temperature is continuously raised to 57 ° C. over 22 hours. Thereafter, this temperature is maintained, and the polymerization reaction is further performed for 5 hours. It was. Note that the pH of the polymerization system at the completion of the charging was adjusted to 7.2. To stop the polymerization reaction, 1.35 g of triethylene glycol bis-3- (3-tertiarybutyl-4-hydroxy-5-methylphenyl) propionate (antioxidant T) and dilauryl thiodipropionate (DLTDP; A solution prepared by dissolving 1.35 g of antioxidant S) in 50 g of vinylidene chloride monomer was injected and stirring was continued for 1 hour, then the internal pressure was released, and the polymer slurry was taken out from the autoclave. The obtained slurry was dehydrated and then dried for 20 hours in a dryer at a temperature of 50 ° C. to obtain a powder of vinylidene chloride resin (1) (vinylidene chloride / vinyl chloride copolymer). The polymerization yield was 87.5%.

(Manufacture of vinylidene chloride resin film)
The vinylidene chloride resin (1) was melt-extruded into a tubular film using an annular die having a diameter of 40 mm adjusted to a temperature of 167 ° C. After cooling, propylene glycol was injected into the tubular film as an opening agent. Next, by encapsulating compressed air in the tubular film, the film is stretched by inflation three times in the longitudinal direction and four times in the transverse direction, and then wound around a paper tube having an outer diameter of 36 mm by a take-up roller, and is 30 μm thick and 110 mm wide. A vinylidene chloride resin film was obtained. The obtained vinylidene chloride resin film was transparent and “extractable” that could be easily pulled out from the paper tube around which the film was wound. For vinylidene chloride-based resin films, the measurement results of the suspending agent content (monomer basis and total mass basis), film thickness and shear adhesion at a temperature of 13 ° C. (hereinafter simply referred to as “shear adhesion”) are shown. Table 1 shows.

[Example 2]
A vinylidene chloride resin film was obtained in the same manner as in Example 1 except that the thickness of the obtained vinylidene chloride resin film was changed to 10 μm by adjusting the melt extrusion speed. The obtained vinylidene chloride resin film was transparent and had good drawability. Table 1 shows the measurement results of the content of the suspending agent, the film thickness, and the shear adhesion strength of the vinylidene chloride resin film.

[Example 3]
In the preparation of vinylidene chloride resin, 1.33 g of methylcellulose was used as a suspending agent, and liquid paraffin 5 was used as a tackifier together with a polymerization initiator, a plasticizer, a stabilizer, an antioxidant and a mixed monomer. A vinylidene chloride resin was prepared in the same manner as in Example 1, except that .2 g was used, and a powder of vinylidene chloride resin (2) (vinylidene chloride / vinyl chloride copolymer) was obtained. The suspending agent was 200 ppm on a mass basis relative to the mixed monomer and 90 ppm on a total mass basis. Moreover, the tackifier was 782 ppm on the mass basis with respect to the mixed monomer, and 351 ppm on the total mass basis. Subsequently, by using the vinylidene chloride resin (2) and adjusting the melt extrusion speed, a vinylidene chloride resin film having a thickness of 20 μm and a width of 110 mm was obtained in the same manner as in Example 1. The obtained vinylidene chloride resin film was transparent and had good drawability. Table 1 shows the measurement results of the content of the suspending agent, the content of the tackifier (the content based on the monomer mass, the same applies hereinafter), the film thickness and the shear adhesion strength of the vinylidene chloride resin film.

[Example 4]
A vinylidene chloride resin (3) (vinylidene chloride) was prepared in the same manner as in Example 3 except that 0.997 g of methylcellulose was used as a suspending agent in the preparation of the vinylidene chloride resin. -Vinyl chloride copolymer) powder was obtained. The suspending agent was 150 ppm on a mass basis relative to the mixed monomer and 67 ppm on a total mass basis. The tackifier was 782 ppm on a mass basis relative to the mixed monomer and 351 ppm on a total mass basis. Subsequently, a vinylidene chloride resin film having a thickness of 20 μm was obtained in the same manner as in Example 3 using the vinylidene chloride resin (3). The obtained vinylidene chloride resin film was transparent and had good drawability. Table 1 shows the measurement results of the content of the suspending agent, the content of the tackifier, the film thickness, and the shear adhesion strength of the vinylidene chloride resin film.

[Comparative Example 1]
In the preparation of vinylidene chloride resin, 2.68 g of methylcellulose was used as a suspending agent, and liquid paraffin 5 was used as a tackifier together with a polymerization initiator, a plasticizer, a stabilizer, an antioxidant and a mixed monomer. Except for using 2 g, a vinylidene chloride resin was prepared in the same manner as in Example 1 to obtain a powder of vinylidene chloride resin (4) (vinylidene chloride / vinyl chloride copolymer). The suspending agent was 403 ppm on a mass basis relative to the mixed monomer and 181 ppm on a total mass basis. Moreover, the tackifier was 782 ppm on the mass basis with respect to the mixed monomer, and 351 ppm on the total mass basis. Subsequently, using the vinylidene chloride resin (4), a vinylidene chloride resin film having a thickness of 30 μm and a width of 110 mm was obtained in the same manner as in Example 1. Table 1 shows the measurement results of the content of the suspending agent, the content of the tackifier, the film thickness, and the shear adhesion strength of the vinylidene chloride resin film.

[Comparative Example 2]
A vinylidene chloride resin was prepared in the same manner as in Example 3 except that 2.68 g of methylcellulose was used as a suspending agent in the preparation of the vinylidene chloride resin, and the vinylidene chloride resin (5) (vinylidene chloride) was prepared. -Vinyl chloride copolymer) powder was obtained. The suspending agent was 403 ppm on a mass basis relative to the mixed monomer and 181 ppm on a total mass basis. The tackifier was 782 ppm on a mass basis relative to the mixed monomer and 351 ppm on a total mass basis. Subsequently, a vinylidene chloride resin film having a thickness of 20 μm was obtained in the same manner as in Example 3 using the vinylidene chloride resin (5). Table 1 shows the measurement results of the content of the suspending agent, the content of the tackifier, the film thickness, and the shear adhesion strength of the vinylidene chloride resin film.

From Table 1, a vinylidene chloride resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the resin is less than 300 ppm. Since the vinylidene chloride resin films of the present invention of Examples 1 to 4 have a shear adhesion of 5 kgf or more at a temperature of 13 ° C., food is stored and stored in tableware or the like, particularly in a refrigerator. It was found to be a vinylidene chloride-based resin film that has sufficient adhesion to food containers and the like and that is inferior in drawability and transparency.

In particular, Example 1 in which a vinylidene chloride-based resin was prepared by suspension polymerization in the presence of a suspending agent having a suspending agent content of less than 150 ppm based on the total mass including the aqueous medium. 2 and 2 are vinylidene chloride resin films that do not contain a tackifier, but the shear adhesion at a temperature of 13 ° C. is 5.5 kgf and 5.7 kgf, which is sufficient for tableware and the like. It had a good adhesion.

Further, since the vinylidene chloride resin films of Examples 3 and 4 which are further vinylidene chloride resin films containing a tackifier have a shear adhesion of 6.2 kgf and 7.2 kgf at a temperature of 13 ° C. It has been found that it has a more sufficient adhesion to the same.

In contrast, the vinylidene chloride resin was prepared by suspension polymerization in the presence of 403 ppm suspension based on the mass of the monomer component forming the resin. Although the vinylidene chloride resin film is a vinylidene chloride resin film containing a tackifier, the shear adhesion at a temperature of 13 ° C. is 4.2 kgf and 4.6 kgf. It was found that the adhesive strength to food containers or the like that contain and store foods is not sufficient.

The present invention provides, as a first aspect, a vinylidene chloride resin film, particularly a vinylidene chloride resin, which has a shear adhesion at a temperature of 13 ° C. of 5 kgf or more. By being a film prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the component is less than 300 ppm, A vinylidene chloride resin film that has sufficient adhesion to food containers that contain and store food and that is inferior in drawability and transparency is provided. high.

In addition, as another aspect, the present invention provides the following step 1 and step 2:
1) A vinylidene chloride resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the vinylidene chloride resin is less than 300 ppm. Step 1; and 2) Melting, extruding and stretching a vinylidene chloride-based resin composition containing a vinylidene chloride-based resin Step 2; the shear adhesion at a temperature of 13 ° C. is 5 kgf or more. With a method for producing a resin-based resin film, it has sufficient adhesion to tableware and the like, particularly food containers that contain and store food in a refrigerator, and has no inferiority in drawability and transparency. Since a method capable of easily producing a vinylidene chloride-based resin film is provided, the industrial applicability is high.

Claims

A vinylidene chloride-based resin film having a shear adhesion at a temperature of 13 ° C. of 5 kgf or more.
A vinylidene chloride-based resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the resin is less than 300 ppm. The vinylidene chloride resin film according to claim 1.
The vinylidene chloride resin film according to claim 2, wherein the content of the suspending agent based on the total mass including the aqueous medium is less than 150 ppm.
The vinylidene chloride resin film according to any one of claims 1 to 3, which does not contain a tackifier.
The vinylidene chloride resin film according to any one of claims 1 to 3, which contains a tackifier.
6. The vinylidene chloride resin film according to claim 5, wherein the vinylidene chloride resin is prepared by suspension polymerization in the presence of a tackifier.
The vinylidene chloride resin film according to any one of claims 1 to 6, wherein the vinylidene chloride resin is a vinylidene chloride / vinyl chloride copolymer.
Step 1 and Step 2 below:
1) A vinylidene chloride resin is prepared by suspension polymerization in an aqueous medium in the presence of a suspending agent whose content based on the mass of the monomer component forming the vinylidene chloride resin is less than 300 ppm. Step 1; and 2) Melting, extruding and stretching a vinylidene chloride-based resin composition containing a vinylidene chloride-based resin Step 2; the shear adhesion at a temperature of 13 ° C. is 5 kgf or more. Of a resin-based resin film.
The method for producing a vinylidene chloride-based resin film according to claim 8, wherein Step 1 and Step 2 are carried out without containing a tackifier.
9. The process for producing a vinylidene chloride-based resin film according to claim 8, wherein the step 1 is a suspension polymerization in the presence of a tackifier.