JP6334391B2 - Cylindrical package - Google Patents

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JP6334391B2
JP6334391B2 JP2014265137A JP2014265137A JP6334391B2 JP 6334391 B2 JP6334391 B2 JP 6334391B2 JP 2014265137 A JP2014265137 A JP 2014265137A JP 2014265137 A JP2014265137 A JP 2014265137A JP 6334391 B2 JP6334391 B2 JP 6334391B2
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base material
material film
film
reinforcing tape
cylindrical
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JP2016124567A (en
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智英 持丸
智英 持丸
石井 雄三
雄三 石井
隆久 上山
隆久 上山
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Kureha Corp
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/04Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
    • C08L27/08Homopolymers or copolymers of vinylidene chloride
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D65/00Wrappers or flexible covers; Packaging materials of special type or form
    • B65D65/38Packaging materials of special type or form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D77/00Packages formed by enclosing articles or materials in preformed containers, e.g. boxes, cartons, sacks or bags
    • B65D77/22Details
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D2565/00Wrappers or flexible covers; Packaging materials of special type or form
    • B65D2565/38Packaging materials of special type or form
    • B65D2565/381Details of packaging materials of special type or form
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2327/02Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
    • C08J2327/04Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
    • C08J2327/08Homopolymers or copolymers of vinylidene chloride
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/014Additives containing two or more different additives of the same subgroup in C08K
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/16Applications used for films

Description

本発明は、チーズ、ソーセージ、かまぼこ、ハム等の加工食品を充填物とする筒状包装体に関する。   The present invention relates to a cylindrical package having a processed food such as cheese, sausage, kamaboko, and ham as a filler.

チーズ、ソーセージ、かまぼこ、ハム等の加工食品が充填された筒状フィルムを密封し個々の包装体を得る場合の密封手段として、筒状フィルムの端部を集束シールする方法が知られていた。このように筒状フィルムの端部を集束シールする方法で得られた筒状包装体においては、シール部分或いはその近傍でピンホールが生じ易いという問題があった。そこで、このような問題を解決するために、筒状の母材フィルムの長手方向の両端部を集束シールし、前記母材フィルムの集束シールされた部分に補強テープを溶着する方法が行われるようになってきた。しかしながら、母材フィルムの集束シールされた部分に補強テープを溶着する方法で得られた筒状包装体は、筒状フィルムにおけるピンホールや包装体の密封性の点で必ずしも充分なものではなかった。   As a sealing means for sealing individual tubular films filled with processed foods such as cheese, sausage, kamaboko, ham and the like to obtain individual packages, a method of focusing and sealing the ends of the tubular films has been known. Thus, in the cylindrical package obtained by the method of focusing and sealing the end portions of the cylindrical film, there is a problem that pinholes are likely to occur at or near the seal portion. Therefore, in order to solve such a problem, a method in which both end portions in the longitudinal direction of the cylindrical base film are focused and sealed, and a reinforcing tape is welded to the focused and sealed portion of the base film is performed. It has become. However, the cylindrical package obtained by the method of welding the reinforcing tape to the focus-sealed portion of the base material film is not necessarily sufficient in terms of pinholes in the cylindrical film and the sealing performance of the package. .

このため、特開2009−46148号公報(特許文献1)には、充填物と、長手方向の両端部が集束シールされることにより前記充填物が充填されている筒状の母材フィルムと、前記母材フィルムの集束シールされた部分を巻回し覆うように前記母材フィルムに溶着されている補強テープとを備える筒状包装体において、前記補強テープの溶着前における熱収縮率及び引張割線弾性率を特定の範囲とすることによって、筒状フィルムにおけるピンホールの発生が充分に抑えられ、密封性が向上することが記載されている。   For this reason, JP 2009-46148 A (Patent Document 1) describes a filler and a cylindrical base material film filled with the filler by focusing and sealing at both ends in the longitudinal direction; In a cylindrical package comprising a reinforcing tape welded to the base material film so as to wind and cover a portion of the base material film that has been tightly sealed, the heat shrinkage rate and tensile secant elasticity before welding of the reinforcing tape It is described that by setting the rate within a specific range, the occurrence of pinholes in the tubular film is sufficiently suppressed and the sealing performance is improved.

しかしながら、これは補強テープの検討が主であり、母材フィルムについて検討の余地が残されていた。補強テープの溶着による密封性、特に、補強テープを溶着した部分(以下、「クリップ部」という)の密封性の向上には限界があり、筒状包装体の密封性を更に向上させるための新たな手段が求められていた。   However, this is mainly due to the study of reinforcing tape, leaving room for examination of the base material film. There is a limit to improving the sealing performance of welded reinforcing tape, especially the sealing performance of the welded portion of the reinforcing tape (hereinafter referred to as “clip part”). There was a need for simple means.

特開2009−46148号公報JP 2009-46148 A

本発明は、上記従来技術の有する課題に鑑みてなされたものであり、クリップ部の密封性に優れた筒状包装体を提供することを目的とする。   This invention is made | formed in view of the subject which the said prior art has, and aims at providing the cylindrical package body excellent in the sealing performance of a clip part.

本発明者らは、上記目的を達成すべく鋭意研究を重ねた結果、(A)充填物と、(B)長手方向の両端部が集束シールされることにより前記充填物が充填されている、ポリ塩化ビニリデン系樹脂のフィルムからなる筒状の母材フィルムと、(C)前記母材フィルムが集束シールされた部分を巻回し覆うように前記母材フィルムに溶着されている、ポリ塩化ビニリデン系樹脂のフィルムからなる補強テープとを備える筒状包装体において、前記母材フィルムとして、アセトン抽出率、突刺しエネルギー、熱収縮率が特定の範囲にあるポリ塩化ビニリデン系樹脂フィルムを用いることによって、筒状包装体のクリップ部の密封性が向上することを見出し、本発明を完成するに至った。   As a result of intensive studies to achieve the above object, the present inventors have filled (A) the filling material and (B) the filling material by focusing and sealing both ends in the longitudinal direction. A cylindrical base material film made of a polyvinylidene chloride resin film; and (C) a polyvinylidene chloride system that is welded to the base material film so as to wind and cover the portion where the base material film is focused and sealed. In a cylindrical package including a reinforcing tape made of a resin film, as the base material film, by using a polyvinylidene chloride resin film having a specific range of acetone extraction rate, piercing energy, and heat shrinkage rate, It has been found that the sealing performance of the clip portion of the cylindrical package is improved, and the present invention has been completed.

すなわち、本発明の筒状包装体は、(A)充填物と、(B)長手方向の両端部が集束シールされることにより前記充填物が充填されている、ポリ塩化ビニリデン系樹脂のフィルムからなる筒状の母材フィルムと、(C)前記母材フィルムが集束シールされた部分を巻回し覆うように前記母材フィルムに溶着されている、ポリ塩化ビニリデン系樹脂のフィルムからなる補強テープとを備える筒状包装体であって、
集束シール前における前記母材フィルムの短手方向の100℃における熱収縮率RB−TDが10.0〜18.9%の範囲であり、アセトン抽出率が9.0%以下であり、120℃における突刺しエネルギーが2.1mJ以上である、ことを特徴とするものである。
That is, the cylindrical package of the present invention is made from (A) a filler and (B) a polyvinylidene chloride resin film filled with the filler by focusing and sealing both ends in the longitudinal direction. A cylindrical base material film, and (C) a reinforcing tape made of a polyvinylidene chloride resin film, which is welded to the base material film so as to wind and cover a portion where the base material film is converged and sealed A cylindrical package comprising:
The heat shrinkage ratio RB -TD at 100 ° C. in the short direction of the base material film before the focusing seal is in the range of 10.0 to 18.9%, the acetone extraction rate is 9.0% or less, and 120 The piercing energy at ° C. is 2.1 mJ or more.

本発明の筒状包装体においては、集束シール前における前記母材フィルムの短手方向の100℃における熱収縮率RB−TDと溶着前における前記補強テープの長手方向の100℃における熱収縮率RC−MDとが下記式(F1):
−8%≦RB−TD−RC−MD≦9% (F1)
で表される条件を満たすことが好ましく、下記式(F1a):
4.5%≦RB−TD−RC−MD≦6.5% (F1a)
で表される条件を満たすことがより好ましい。
In the cylindrical package of the present invention, the heat shrinkage ratio RB -TD at 100 ° C. in the short direction of the base material film before the convergence seal and the heat shrinkage rate at 100 ° C. in the longitudinal direction of the reinforcing tape before welding. R C-MD is the following formula (F1):
−8% ≦ R B-TD −R C-MD ≦ 9% (F1)
It is preferable to satisfy the condition represented by the following formula (F1a):
4.5% ≦ RB -TD- RC-MD ≦ 6.5% (F1a)
It is more preferable that the condition represented by

さらに、本発明の筒状包装体においては、集束シール前における前記母材フィルムの120℃における突刺しエネルギーが2.5mJ以上であることが好ましく、また、集束シール前における前記母材フィルムの長手方向の引張割線弾性率EB−MDが332〜450MPaの範囲であることも好ましい。 Furthermore, in the cylindrical package of the present invention, the piercing energy at 120 ° C. of the base material film before the focusing seal is preferably 2.5 mJ or more, and the length of the base film before the focusing seal is increased. It is also preferable that the tensile secant modulus EB -MD in the direction is in the range of 332 to 450 MPa.

また、本発明の筒状包装体において、前記母材フィルムとしては、塩化ビニリデンモノマーと塩化ビニルモノマーとの共重合体を含有するポリ塩化ビニリデン系樹脂のフィルムからなるものが好ましく、また、前記補強テープとしては、塩化ビニリデンモノマーと塩化ビニルモノマーとの共重合体を含有するポリ塩化ビニリデン系樹脂のフィルムからなるものが好ましい。   Further, in the cylindrical package of the present invention, the base material film is preferably composed of a polyvinylidene chloride resin film containing a copolymer of vinylidene chloride monomer and vinyl chloride monomer, and the reinforcement The tape is preferably made of a film of a polyvinylidene chloride resin containing a copolymer of vinylidene chloride monomer and vinyl chloride monomer.

本発明によれば、クリップ部の密封性に優れた筒状包装体を得ることが可能となる。   According to the present invention, it is possible to obtain a cylindrical package with excellent clip portion sealing performance.

以下、本発明をその好適な実施形態に即して詳細に説明する。   Hereinafter, the present invention will be described in detail with reference to preferred embodiments thereof.

本発明の筒状包装体は、(A)充填物と、(B)長手方向の両端部が集束シールされることにより前記充填物が充填されている、ポリ塩化ビニリデン系樹脂のフィルムからなる筒状の母材フィルムと、(C)前記母材フィルムが集束シールされた部分を巻回し覆うように前記母材フィルムに溶着されている、ポリ塩化ビニリデン系樹脂のフィルムからなる補強テープとを備える筒状包装体であって、
集束シール前における前記母材フィルムの短手方向の100℃における熱収縮率RB−TDが10.0〜18.9%の範囲であり、アセトン抽出率が9.0%以下であり、120℃における突刺しエネルギーが2.1mJ以上である、ことを特徴とするものである。
The tubular package of the present invention comprises (A) a filling and (B) a tube made of a polyvinylidene chloride resin film filled with the filling by focusing and sealing both ends in the longitudinal direction. And (C) a reinforcing tape made of a polyvinylidene chloride-based resin film welded to the base film so as to wind and cover a portion where the base film is converged and sealed. A tubular package,
The heat shrinkage ratio RB -TD at 100 ° C. in the short direction of the base material film before the focusing seal is in the range of 10.0 to 18.9%, the acetone extraction rate is 9.0% or less, and 120 The piercing energy at ° C. is 2.1 mJ or more.

本発明にかかる(A)充填物としては、特に限定されないが、例えば、チーズ、ソーセージ、かまぼこ、ハム等の加工食品が挙げられる。   Although it does not specifically limit as (A) filling concerning this invention, For example, processed foods, such as cheese, sausage, kamaboko, and ham, are mentioned.

(母材フィルム)
本発明にかかる(B)母材フィルムは、長手方向の両端部が集束シールされることにより前記充填物が充填されている筒状のものである。そして、本発明にかかる母材フィルムは、ポリ塩化ビニリデン系樹脂フィルムからなるものであることが必要である。本明細書において、ポリ塩化ビニリデン系樹脂(以下、「PVDC系樹脂」と略す)とは、塩化ビニリデンを主成分とする共重合体樹脂のことをいう。このようなPVDC系樹脂は、酸素と水蒸気の遮断性に優れているため、母材フィルムとして使用した場合に充填物の酸化や目減りといった劣化を抑え、商品価値を維持することができる。また、このようなPVDC系樹脂は、ホットフィル適性、ボイルやレトルトのような高温殺菌処理に対する適性も優れるため、チーズ、ソーセージ、かまぼこ、ハム等の加工食品を充填物とする筒状包装体の母材フィルムの材料として特に好適である。
(Base material film)
The base material film (B) according to the present invention has a cylindrical shape filled with the filler by converging and sealing both end portions in the longitudinal direction. And the base material film concerning this invention needs to consist of a polyvinylidene chloride resin film. In this specification, the polyvinylidene chloride resin (hereinafter abbreviated as “PVDC resin”) refers to a copolymer resin mainly composed of vinylidene chloride. Since such a PVDC-type resin is excellent in the barrier | blocking property of oxygen and water vapor | steam, when used as a base material film, deterioration, such as oxidation of a filler and a loss, can maintain commercial value. Moreover, since such a PVDC-type resin is excellent also in hot fill aptitude and the high temperature sterilization process like a boil and a retort, it is the cylindrical package body which uses processed foods, such as cheese, sausage, kamaboko, and ham, as a filler. It is particularly suitable as a base material film material.

本発明にかかる母材フィルムにおいて、集束シール前における短手方向(TD)の100℃での熱収縮率RB−TDは10.0〜18.9%の範囲にあることが必要である。熱収縮率RB−TDが10.0%未満では、レトルト時の収縮が不足することにより、筒状包装体にしわが発生し、他方、18.9%を超えると、クリップ部の密封性が低下する。また、レトルト時に十分に収縮することにより筒状包装体にしわが発生しにくくなるという観点から、前記熱収縮率RB−TDとしては、15.0〜18.9%が好ましい。なお、このような集束シール前における前記母材フィルムの熱収縮率は、フィルム製膜時の延伸倍率などを制御することによって適宜調整することができる。 In the base material film according to the present invention, the heat shrinkage ratio RB -TD at 100 ° C. in the short-side direction (TD) before the focusing seal needs to be in the range of 10.0 to 18.9%. If the thermal shrinkage ratio R B-TD is less than 10.0%, the shrinkage at the time of retort is insufficient, so that wrinkles occur in the cylindrical package. On the other hand, if it exceeds 18.9%, the sealing property of the clip portion is reduced. descend. Moreover, from the viewpoint that wrinkles are less likely to occur in the cylindrical package by sufficiently shrinking during retorting, the heat shrinkage rate RB -TD is preferably 15.0 to 18.9%. In addition, the thermal contraction rate of the base material film before such focusing sealing can be adjusted as appropriate by controlling the draw ratio during film formation.

また、本発明にかかる母材フィルムにおいて、集束シール前におけるアセトン抽出率は9.0%以下であることが必要である。母材フィルムのアセトン抽出率が9.0%を超えると、本発明にかかる母材フィルムの材料であるPVDC系樹脂の融解後の溶融粘度の低下が大きく、補強テープで母材フィルムを収束してシールする際に、強固な融着が行えず、クリップ部の密封性が低下する。また、クリップ部の密封性が更に向上するという観点から、このような母材フィルムの集束シール前におけるアセトン抽出率は、6.0%以下であることが好ましく、4.0%以下であることがより好ましく、3.0%以下であることが特に好ましい。なお、アセトン抽出率の下限値としては特に制限はないが、フィルムの押出性の観点から1.0%以上が好ましい。また、このような集束シール前における前記母材フィルムのアセトン抽出率は、本発明にかかる母材フィルムの材料であるPVDC系樹脂を重合する際の温度、反応時間を制御することによって適宜調整することができる。   Further, in the base material film according to the present invention, the acetone extraction rate before the focusing seal needs to be 9.0% or less. If the acetone extraction rate of the base material film exceeds 9.0%, the melt viscosity of the PVDC resin that is the material of the base material film according to the present invention is greatly reduced, and the base film is converged with the reinforcing tape. When sealing, the strong fusion cannot be performed, and the sealing performance of the clip portion is lowered. Further, from the viewpoint that the sealing performance of the clip portion is further improved, the acetone extraction rate of the base material film before the focusing seal is preferably 6.0% or less, and preferably 4.0% or less. Is more preferable, and 3.0% or less is particularly preferable. In addition, although there is no restriction | limiting in particular as a lower limit of acetone extraction rate, 1.0% or more is preferable from a viewpoint of the extrudability of a film. Moreover, the acetone extraction rate of the base material film before such a focusing seal is appropriately adjusted by controlling the temperature and reaction time when polymerizing the PVDC resin that is the material of the base material film according to the present invention. be able to.

さらに、本発明にかかる母材フィルムにおいて、集束シール前における突刺しエネルギーは2.1mJ以上であることが必要である。母材フィルムの突刺しエネルギーが2.1mJ未満では、母材フィルムがレトルト時のフィルム収縮応力に耐えられず、クリップ部にピンホールが発生する場合があり、クリップ部の密封性が低下する。また、クリップ部の密封性が更に向上するという観点から、このような母材フィルムの集束シール前における突刺しエネルギーは、2.5mJ以上であることが好ましく、2.8mJ以上であることがより好ましく、3.2mJ以上であることが更に好ましく、3.5mJ以上であることが特に好ましい。また、このような集束シール前における前記母材フィルムの突刺しエネルギーは、本発明にかかる母材フィルムの材料であるPVDC系樹脂の分子量、塩化ビニリデン・塩化ビニル共重合比などを制御することによって適宜調整することができる。   Furthermore, in the base material film according to the present invention, the piercing energy before the focusing seal needs to be 2.1 mJ or more. When the piercing energy of the base material film is less than 2.1 mJ, the base material film cannot withstand the film shrinkage stress at the time of retorting, and pinholes may be generated in the clip portion, thereby reducing the sealing performance of the clip portion. Further, from the viewpoint that the sealing performance of the clip portion is further improved, the piercing energy of such a base material film before the focusing seal is preferably 2.5 mJ or more, more preferably 2.8 mJ or more. Preferably, it is 3.2 mJ or more, more preferably 3.5 mJ or more. In addition, the piercing energy of the base material film before the convergence seal is controlled by controlling the molecular weight of the PVDC resin that is the material of the base material film according to the present invention, the vinylidene chloride / vinyl chloride copolymerization ratio, and the like. It can be adjusted appropriately.

また、本発明にかかる母材フィルムにおいて、集束シール前における長手方向(MD)の引張割線弾性率EB−MDは332〜450MPaの範囲にあることが好ましく、また、短手方向(TD)の引張割線弾性率EB−TDは、220〜370MPaの範囲にあることが好ましい。長手方向の引張割線弾性率EB−MD又は短手方向の引張割線弾性率EB−TDが前記下限未満になると、母材フィルムに十分な強度がないため、集束シールされた部分でピンホールが発生することがあり、他方、前記上限を超えると、補強テープの装着性(フィット性)が低下して、補強テープが母材フィルムと溶着しないことがあり、得られる筒状包装体の密封性が低下することがある。なお、このような集束シール前における前記母材フィルムの引張割線弾性率は、塩化ビニリデン・塩化ビニル共重合比、可塑剤などの添加剤の添加量を制御することによって適宜調整することができる。 In the base material film according to the present invention, the tensile secant modulus E B-MD in the longitudinal direction (MD) before the bundling seal is preferably in the range of 332 to 450 MPa, and in the short direction (TD). The tensile secant modulus EB -TD is preferably in the range of 220 to 370 MPa. If the tensile secant modulus E B-MD in the longitudinal direction or the tensile secant modulus E B-TD in the short direction is less than the lower limit, the base film does not have sufficient strength. On the other hand, when the above upper limit is exceeded, the mounting property (fit property) of the reinforcing tape is lowered, and the reinforcing tape may not be welded to the base material film, and the resulting cylindrical package is sealed. May decrease. In addition, the tensile secant modulus of the base material film before such convergent sealing can be appropriately adjusted by controlling the addition amount of additives such as vinylidene chloride / vinyl chloride copolymerization ratio and plasticizer.

本発明にかかる母材フィルムの集束シール前における厚みは、特に限定されないが、20〜80μmの範囲にあることが好ましく、30〜60μmの範囲にあることがより好ましい。厚みが前記下限未満では、得られる筒状包装体において、輸送時等における外部からの衝撃や摩擦によるピンホールが生じ易くなる傾向にあり、他方、前記上限を超えると、母材フィルム端部の集束が不充分となり、補強テープを含めて溶着しない部分を生じて、得られる筒状包装体の密封性が不充分となる傾向にある。   The thickness of the base material film according to the present invention before the focusing seal is not particularly limited, but is preferably in the range of 20 to 80 μm, and more preferably in the range of 30 to 60 μm. If the thickness is less than the lower limit, the resulting cylindrical package tends to easily cause pinholes due to external impact or friction during transportation or the like, and on the other hand, if the upper limit is exceeded, Insufficient bundling, and a part that does not weld including the reinforcing tape is generated, and the sealing property of the obtained cylindrical package tends to be insufficient.

本発明にかかる母材フィルムの材料であるPVDC系樹脂は、塩化ビニリデンと塩化ビニリデン以外のモノマーとを共重合させることにより得ることができる。このような塩化ビニリデン以外のモノマーとしては、特に限定されないが、例えば、塩化ビニル、アクリロニトリル、(メタ)アクリル酸エステルが挙げられる。   The PVDC resin, which is the material of the base film according to the present invention, can be obtained by copolymerizing vinylidene chloride and a monomer other than vinylidene chloride. Such a monomer other than vinylidene chloride is not particularly limited, and examples thereof include vinyl chloride, acrylonitrile, and (meth) acrylic acid esters.

また、このようなPVDC系樹脂は、塩化ビニリデン78〜84質量%(より好ましくは79〜83質量%、特に好ましくは80〜82質量%)と、前記塩化ビニル22〜16質量%(より好ましくは21〜17質量%、特に好ましくは20〜18質量%)との共重合体を含有するものであることが好ましい。塩化ビニリデンの配合量が前記下限未満では、溶融押出し延伸製膜する際において結晶化が充分に進行せず、安定した製膜を行うことが困難となる傾向にあり、また得られる母材フィルム耐熱性が不足することによって、レトルト殺菌処理等の高温加熱処理により得られる筒状包装体が破裂するという問題を生ずる傾向にあり、他方、前記上限を超えると、結晶性の増大に伴う融点の上昇のために、溶融押出の負荷が大きくなる傾向にある。   Moreover, such PVDC-type resin contains 78 to 84% by mass of vinylidene chloride (more preferably 79 to 83% by mass, particularly preferably 80 to 82% by mass) and 22 to 16% by mass of vinyl chloride (more preferably). 21 to 17% by mass, and particularly preferably 20 to 18% by mass). When the blending amount of vinylidene chloride is less than the lower limit, crystallization does not proceed sufficiently during melt extrusion stretch film formation, and stable film formation tends to be difficult, and the obtained base material film has heat resistance. When the upper limit is exceeded, the melting point increases due to the increase in crystallinity, which tends to cause a problem that the tubular package obtained by high-temperature heat treatment such as retort sterilization is ruptured. Therefore, the load of melt extrusion tends to increase.

本発明にかかる母材フィルムの材料であるPVDC系樹脂には、必要に応じて、他の樹脂を配合してもよい。このような他の樹脂としては、例えば、エチレン−酢酸ビニル共重合体、(メタ)アクリル酸エステル(好ましくは、アルキル基の炭素数が1〜18の(メタ)アクリル酸アルキルエステルの共重合体(例えば、(メタ)アクリル酸メチル−(メタ)アクリル酸ブチル共重合体))、メタクリル酸メチル−ブタジエン−スチレン共重合体)等が挙げられる。このような他の樹脂は、PVDC系樹脂に添加してPVDC系樹脂組成物としてもよいし、その一部又は全部を顔料を含有する着色用樹脂組成物に予め配合し、この着色用樹脂組成物をPVDC系樹脂に配合してもよい。また、ガスバリア性や耐熱性等の観点から、このような他の樹脂は、PVDC系樹脂との混合物中の塩化ビニリデン成分の含有割合が50質量%以上となるように配合することが好ましい。   You may mix | blend another resin with the PVDC-type resin which is the material of the base material film concerning this invention as needed. Examples of such other resins include ethylene-vinyl acetate copolymer, (meth) acrylic acid ester (preferably a copolymer of (meth) acrylic acid alkyl ester having 1 to 18 carbon atoms in the alkyl group). (For example, methyl (meth) acrylate-butyl (meth) acrylate copolymer)), methyl methacrylate-butadiene-styrene copolymer), and the like. Such other resin may be added to the PVDC resin to form a PVDC resin composition, or a part or all of the resin may be preliminarily blended in the coloring resin composition containing the pigment, and the coloring resin composition. You may mix | blend a thing with a PVDC-type resin. Further, from the viewpoint of gas barrier properties, heat resistance, and the like, such other resins are preferably blended so that the content ratio of the vinylidene chloride component in the mixture with the PVDC resin is 50% by mass or more.

さらに、本発明にかかる母材フィルムの材料であるPVDC系樹脂には、溶融押出性、熱安定性、延伸性、柔軟性、着色、充填物との剥離性等の特性を付与するために、可塑剤、安定剤、滑剤、着色剤、界面活性剤、梨地化剤等の添加剤を添加してもよい。また、PVDC系樹脂には、成形加工時に発生するリサイクル可能なPVDC系樹脂組成物の成形屑などを混合することができる。   Furthermore, in order to impart properties such as melt extrudability, thermal stability, stretchability, flexibility, coloring, and releasability from fillers to the PVDC resin that is the material of the base film according to the present invention, Additives such as a plasticizer, a stabilizer, a lubricant, a colorant, a surfactant, and a finishing agent may be added. In addition, recyclable PVDC resin composition molding waste generated during molding can be mixed with the PVDC resin.

前記添加剤としては、公知の可塑剤、安定剤、粘着剤、粘着付与剤、顔料、滑剤、助剤、フィラー、界面活性剤等が挙げられる。液状の可塑剤としては、アセチルトリブチルサイトレート(ATBC)、グリセリンジアセチルモノラウレート(GDAML)、ジブチルセバケート(DBS)、ジオクチルセバケート及びジアセチル化モノグリセライド(DALG)等が挙げられる。安定剤としては、エポキシ化植物油(例えば、エポキシ化大豆油(ESBO)、エポキシ化亜麻仁油(ELO))、アルキルエステルのアミド誘導体、水酸化マグネシウム、ピロリン酸四ナトリウム等が挙げられる。粘着剤としては、ポリイソブチレン(PIB)、ポリブテン(PB)、ポリブタジエン、ポリエチレングリコール、ポリグリセリン、ポリプロピレングリコールといったポリ多価アルコール等が挙げられる。粘着付与剤としては、ソルビタン脂肪酸エステル、プロピレングリコール脂肪酸エステル、グリセリン脂肪酸エステル(例えば、ソルビタンモノ(トリ)オレート、グリセリンモノ(トリ)オレート等の界面活性剤)、パラフィン系又はシクロパラフィン系の液状飽和炭化水素(例えば、ナフテン系のプロセスオイル、パラフィンワックス、流動パラフィン(ミネラルオイル))等が挙げられる。滑剤としては、ワックス類(例えば、酸化ポリエチレン、パラフィンワックス)、飽和脂肪酸アミド(例えば、ブチルアミド、吉草酸アミド、カプロン酸アミド、力プリル酸アミド、力プリン駿アミド、ラウリン酸アミド、ミリスチン酸アミド、パルミチン酸アミド、ステアリン酸アミド、アラキジン酸アミド、ベヘニン酸アミド)、不飽和脂肪酸アミド(例えば、オレイン酸アミド、エル力酸アミド)、ソルビタン脂肪酸エステル、ポリグリセリン脂肪酸エステル、置換アミド(例えば、N−オレイルパルチミン酸アミド、N−ステアリルステアリン酸アミド、N−ステアリルオレイン酸アミド、N−オレイルステアリン酸アミド、N−ステアリルエルカ酸アミド)、メチロールアミド(例えば、メチロールステアリン酸アミド)、飽和脂肪酸ビスアミド(例えば、メチレンビスステアリン酸アミド、エチレンビスヒドロキシステアリン酸アミド)、不飽和脂肪酸ビスアミド(例えば、エチレンビスエル力酸アミド)、芳香族系ビスアミド(例えば、m−キシリレンビスヒドロキシステアリン酸アミド)等が挙げられる。助剤としては、エチレン−酢酸ビニル共重合体、フェノール系抗酸化剤(例えば、2,6−ジ−tert−ブチル−4−メチル−フェノール(BHT)、トリエチレングリコール−ビス[3−(3−tert−ブチル−5−メチル−4−ヒドロキシフェニル)プロピオネート]、2,4−ジメチル―6−S一アルキルフェノール、2,4−ジメチル−6−(1−メチルペンタデシル)フェノール、及びこれらの混合物)、チオエーテル系抗酸化剤(例えば、チオジプロピオン酸、ジステアリルチオジプロピオネート)、ホスファイト系抗酸化剤(例えば、トリスノニルフェニルホスファイト、ジステアリルペンタエリスリトールジホスファイト)等が挙げられる。フィラーとしては、二酸化珪素、炭酸カルシウム、ゼオライト等が挙げられる。界面活性剤としては、ソルビタン脂肪酸エステル類等が挙げられる。   Examples of the additive include known plasticizers, stabilizers, pressure-sensitive adhesives, tackifiers, pigments, lubricants, auxiliaries, fillers, and surfactants. Examples of the liquid plasticizer include acetyl tributyl cytolate (ATBC), glycerin diacetyl monolaurate (GDAML), dibutyl sebacate (DBS), dioctyl sebacate and diacetylated monoglyceride (DALG). Stabilizers include epoxidized vegetable oils (eg, epoxidized soybean oil (ESBO), epoxidized linseed oil (ELO)), amide derivatives of alkyl esters, magnesium hydroxide, tetrasodium pyrophosphate, and the like. Examples of the pressure-sensitive adhesive include polypolybutyl alcohol such as polyisobutylene (PIB), polybutene (PB), polybutadiene, polyethylene glycol, polyglycerin, and polypropylene glycol. Tackifiers include sorbitan fatty acid esters, propylene glycol fatty acid esters, glycerin fatty acid esters (for example, surfactants such as sorbitan mono (tri) oleate and glycerin mono (tri) oleate), paraffinic or cycloparaffinic liquid saturation Examples thereof include hydrocarbons (for example, naphthenic process oil, paraffin wax, liquid paraffin (mineral oil)) and the like. Examples of lubricants include waxes (eg, polyethylene oxide, paraffin wax), saturated fatty acid amides (eg, butyramide, valeric acid amide, caproic acid amide, strong prillic acid amide, strong purine amide, lauric acid amide, myristic acid amide, Palmitic acid amide, stearic acid amide, arachidic acid amide, behenic acid amide), unsaturated fatty acid amide (eg, oleic acid amide, ergic acid amide), sorbitan fatty acid ester, polyglycerin fatty acid ester, substituted amide (eg, N- Oleyl palmitic acid amide, N-stearyl stearic acid amide, N-stearyl oleic acid amide, N-oleyl stearic acid amide, N-stearyl erucic acid amide), methylol amide (for example, methylol stearic acid amide), saturated fat Acid bisamide (eg, methylene bis stearic acid amide, ethylene bishydroxy stearic acid amide), unsaturated fatty acid bisamide (eg, ethylene bisphenol acid amide), aromatic bisamide (eg, m-xylylene bishydroxy stearic acid amide) ) And the like. As the auxiliary agent, ethylene-vinyl acetate copolymer, phenol antioxidant (for example, 2,6-di-tert-butyl-4-methyl-phenol (BHT), triethylene glycol-bis [3- (3 -Tert-butyl-5-methyl-4-hydroxyphenyl) propionate], 2,4-dimethyl-6-S monoalkylphenol, 2,4-dimethyl-6- (1-methylpentadecyl) phenol, and mixtures thereof ), Thioether antioxidants (eg, thiodipropionic acid, distearyl thiodipropionate), phosphite antioxidants (eg, trisnonylphenyl phosphite, distearyl pentaerythritol diphosphite), etc. . Examples of the filler include silicon dioxide, calcium carbonate, and zeolite. Examples of the surfactant include sorbitan fatty acid esters.

本発明にかかる母材フィルムの製造方法としては、例えば、前記PVDC系樹脂を溶融押出機により加熱溶融して管状ノズルから押出し、急冷後にインフレーション法等の手段によって二軸延伸する方法を採用できる。二軸延伸における縦方向(MD)の延伸倍率は2〜5倍であることが好ましく、2.2〜3.5倍であることがより好ましい。また、横方向(TD)の延伸倍率は2〜5倍であることが好ましく、3.5〜4.5倍であることがより好ましい。延伸温度は15〜40℃程度が好ましく、15〜30℃程度がより好ましい。   As a method for producing a base film according to the present invention, for example, a method in which the PVDC resin is heated and melted by a melt extruder, extruded from a tubular nozzle, and rapidly cooled and biaxially stretched by means such as an inflation method can be employed. The stretching ratio in the machine direction (MD) in biaxial stretching is preferably 2 to 5 times, and more preferably 2.2 to 3.5 times. Moreover, it is preferable that the draw ratio of a horizontal direction (TD) is 2-5 times, and it is more preferable that it is 3.5-4.5 times. The stretching temperature is preferably about 15 to 40 ° C, more preferably about 15 to 30 ° C.

また、本発明にかかる母材フィルムの製造方法においては、母材フィルムの寸法安定性を高めるために、延伸したフィルムを縦方向(MD)と横方向(TD)に緩和(収縮)させてもよい。縦方向(MD)の緩和率は1〜20%程度であることが好ましく、5〜9%程度であることがより好ましい。また、横方向(TD)の緩和率は1〜20%程度であることが好ましく、5〜10%程度であることがより好ましい。緩和温度は40〜80℃程度が好ましく、50〜70℃程度がより好ましい。   Moreover, in the manufacturing method of the base material film concerning this invention, in order to improve the dimensional stability of a base material film, even if the stretched film is relaxed (shrinks) to the vertical direction (MD) and the horizontal direction (TD). Good. The relaxation rate in the machine direction (MD) is preferably about 1 to 20%, and more preferably about 5 to 9%. Further, the relaxation rate in the transverse direction (TD) is preferably about 1 to 20%, and more preferably about 5 to 10%. The relaxation temperature is preferably about 40 to 80 ° C, more preferably about 50 to 70 ° C.

(補強テープ)
本発明にかかる(C)補強テープは、前記母材フィルムが集束シールされた部分を巻回し覆うように前記母材フィルムに溶着されているものである。そして、本発明にかかる補強テープは、ポリ塩化ビニリデン系樹脂フィルムからなるものであることが必要である。補強テープとしてポリ塩化ビニリデン系樹脂フィルムからなるものを用いることによって、補強テープと前記母材フィルムとの溶着性が増す。
(Reinforcing tape)
The reinforcing tape (C) according to the present invention is welded to the base material film so as to wind and cover the portion where the base material film is converged and sealed. And the reinforcement tape concerning this invention needs to consist of a polyvinylidene chloride resin film. By using a material composed of a polyvinylidene chloride resin film as the reinforcing tape, the weldability between the reinforcing tape and the base material film is increased.

本発明にかかる補強テープにおいて、溶着前における長手方向(MD)の100℃での熱収縮率RC−MDは、10〜27%の範囲にあることが好ましく、12〜25%の範囲にあることがより好ましく、13〜24%の範囲にあることが特に好ましい。熱収縮率RC−MDが前記範囲内にあると、得られる筒状包装体の密封性と補強テープとしての寸法変化等とのバランスが良好となる。一方、熱収縮率RC−MDが前記下限未満になると、得られる筒状包装体の両端部においてピンホールを充分に抑制することができず、得られる筒状包装体の密封性が不充分となる傾向にあり、他方、前記上限を超えると、補強テープとして使用する前の寸法変化や過収縮による縮れが生じ、また、補強テープが収縮し硬化した部分が周辺にある包装体と接触することにより傷つきピンホールを誘発する傾向にある。また、溶着前における前記補強テープの短手方向(TD)の100℃での熱収縮率RC−TDは、母材フィルムとの収縮差によるクリップ部の密封不良や補強テープの過剰収縮によるクリップ部の形状不良を抑制するという観点から、8〜35%の範囲にあることが好ましい。なお、このような溶着前における前記補強テープの熱収縮率は、フィルム製膜時の延伸倍率などを制御することによって適宜調整することができる。 In the reinforcing tape according to the present invention, the thermal shrinkage ratio RC-MD at 100 ° C in the longitudinal direction (MD) before welding is preferably in the range of 10 to 27%, and in the range of 12 to 25%. It is more preferable that it is in the range of 13 to 24%. When the heat shrinkage ratio R C-MD is within the above range, the balance between the sealing property of the obtained cylindrical package and the dimensional change as the reinforcing tape becomes good. On the other hand, if the heat shrinkage ratio RC-MD is less than the lower limit, pinholes cannot be sufficiently suppressed at both ends of the obtained cylindrical package, and the resulting cylindrical package has insufficient sealing properties. On the other hand, if the above upper limit is exceeded, shrinkage due to dimensional change and overcontraction before use as a reinforcing tape occurs, and the portion where the reinforcing tape contracts and hardens comes into contact with the surrounding packaging. It tends to induce pinholes that are damaged. Further, the thermal shrinkage ratio RC-TD at 100 ° C. in the short direction (TD) of the reinforcing tape before welding is a clip due to poor sealing of the clip part due to shrinkage difference from the base material film or excessive shrinkage of the reinforcing tape. From the viewpoint of suppressing the shape defect of the portion, it is preferably in the range of 8 to 35%. In addition, the thermal contraction rate of the said reinforcement tape before such welding can be suitably adjusted by controlling the draw ratio etc. at the time of film forming.

また、本発明にかかる補強テープにおいて、溶着前における長手方向(MD)の引張割線弾性率EC−MDは、250〜450MPaの範囲にあることが好ましく、260〜420MPaの範囲にあることがより好ましく、270〜400MPaの範囲にあることが特に好ましく、また、短手方向(TD)の引張割線弾性率EC−TDは、220〜370MPaの範囲にあることが好ましい。長手方向の引張割線弾性率EC−MD及び短手方向の引張割線弾性率EC−TDが前記範囲内にあると、得られる筒状包装体の密封性と補強テープの硬さ等とのバランスが良好となる。一方、長手方向の引張割線弾性率EC−MD又は短手方向の引張割線弾性率EC−TDが前記下限未満になると、補強テープに充分な硬さがないため、母材フィルムの集束シールされた部分に補強テープを添える際に、補強テープを添える箇所のばらつきが生じ易くなり、そのため得られる筒状包装体の両端部においてピンホールを充分に抑制することができず、得られる筒状包装体の密封性が低下する傾向にあり、他方、前記上限を超えると、母材フィルムの集束シールされた部分への補強テープの装着性(フィット性)が低下して、補強テープが母材フィルムと溶着しないことがあり、得られる筒状包装体の密封性が低下する傾向にある。なお、このような溶着前における前記補強テープの引張割線弾性率は、可塑剤などの添加剤の添加量を制御することによって適宜調整することができる。 In the reinforcing tape according to the present invention, the tensile secant modulus E C-MD in the longitudinal direction (MD) before welding is preferably in the range of 250 to 450 MPa, and more preferably in the range of 260 to 420 MPa. Preferably, it is particularly preferably in the range of 270 to 400 MPa, and the tensile secant modulus E C-TD in the short direction (TD) is preferably in the range of 220 to 370 MPa. When the tensile secant modulus E C-MD in the longitudinal direction and the tensile secant modulus E C-TD in the short direction are within the above ranges, the sealing property of the resulting cylindrical package and the hardness of the reinforcing tape, etc. Balance becomes good. On the other hand, if the tensile secant modulus E C-MD in the longitudinal direction or the tensile secant modulus E C-TD in the short direction is less than the lower limit, the reinforcing tape does not have sufficient hardness. When attaching a reinforcing tape to the part, the variation of the location where the reinforcing tape is attached tends to occur, and pinholes cannot be sufficiently suppressed at both ends of the obtained cylindrical package, and the resulting cylindrical shape On the other hand, when the upper limit is exceeded, the mounting property (fit property) of the reinforcing tape to the portion of the base material film that is focused and sealed decreases, and the reinforcing tape becomes the base material. There is a case where it does not weld to the film, and the sealing property of the obtained cylindrical package tends to be lowered. In addition, the tensile secant modulus of the reinforcing tape before such welding can be appropriately adjusted by controlling the amount of additive such as a plasticizer.

本発明にかかる補強テープの溶着前における厚みは、10〜150μmの範囲にあることが好ましく、30〜120μmの範囲にあることがより好ましく、40〜100μmの範囲にあることが特に好ましい。厚みが前記下限未満では、筒状包装体の製造工程において両端部に巻き付けるのが困難となり、また、補強テープとしての強度が不足する傾向にある。他方、厚みが前記上限を超えると、母材フィルムの集束シールされた部分と溶着しないことがあり、得られる筒状包装体の密封性が低下する傾向にある。   The thickness of the reinforcing tape according to the present invention before welding is preferably in the range of 10 to 150 μm, more preferably in the range of 30 to 120 μm, and particularly preferably in the range of 40 to 100 μm. If the thickness is less than the lower limit, it is difficult to wind around both ends in the manufacturing process of the cylindrical package, and the strength as a reinforcing tape tends to be insufficient. On the other hand, if the thickness exceeds the above upper limit, the base film may not be welded to the portion of the base film that has been sealed, and the sealing performance of the resulting cylindrical package tends to be reduced.

本発明にかかる補強テープの材料であるPVDC系樹脂は、塩化ビニリデンと塩化ビニリデン以外のモノマーと共重合させることにより得ることができる。このような塩化ビニリデン以外のモノマーとしては、特に限定されないが、例えば、塩化ビニル、アクリロニトリル、(メタ)アクリル酸エステルが挙げられる。これらの中でも、塩化ビニリデンとの反応性に優れ、また得られる共重合体の物性の制御が容易となるという観点から、塩化ビニルが好ましい。   The PVDC resin, which is a material for the reinforcing tape according to the present invention, can be obtained by copolymerization with monomers other than vinylidene chloride and vinylidene chloride. Such a monomer other than vinylidene chloride is not particularly limited, and examples thereof include vinyl chloride, acrylonitrile, and (meth) acrylic acid esters. Among these, vinyl chloride is preferable from the viewpoints of excellent reactivity with vinylidene chloride and easy control of physical properties of the resulting copolymer.

また、このようなPVDC系樹脂は、塩化ビニリデン78〜84質量%(より好ましくは79〜83質量%、特に好ましくは80〜82質量%)と、前記塩化ビニル22〜16質量%(より好ましくは21〜17質量%、特に好ましくは20〜18質量%)との共重合体を含有するものであることが好ましい。塩化ビニリデンの配合量が前記下限未満では、溶融押出し延伸製膜する際において結晶化が充分に進行せず、安定した製膜を行うことが困難となる傾向にあり、また得られる補強テープの耐熱性が不足することによって、レトルト殺菌処理等の高温加熱処理により得られる筒状包装体が破裂するという問題を生ずる傾向にあり、他方、前記上限を超えると、結晶性の増大に伴う融点の上昇のために、溶融押出の負荷が大きくなる傾向にある。   Moreover, such PVDC-type resin contains 78 to 84% by mass of vinylidene chloride (more preferably 79 to 83% by mass, particularly preferably 80 to 82% by mass) and 22 to 16% by mass of vinyl chloride (more preferably). 21 to 17% by mass, and particularly preferably 20 to 18% by mass). When the blending amount of vinylidene chloride is less than the lower limit, crystallization does not proceed sufficiently during melt extrusion stretch film formation, and it tends to be difficult to perform stable film formation, and the heat resistance of the resulting reinforcing tape When the upper limit is exceeded, the melting point increases due to the increase in crystallinity, which tends to cause a problem that the tubular package obtained by high-temperature heat treatment such as retort sterilization is ruptured. Therefore, the load of melt extrusion tends to increase.

本発明にかかる補強テープの材料であるPVDC系樹脂には、得られる補強テープの熱収縮率や引張割線弾性率を制御するために、例えば、セバシン酸ジブチル等の可塑剤、エポキシ化植物油等の安定剤、脂肪酸エステル等の滑剤、炭酸カルシウム等の梨地化剤を添加してもよい。   In order to control the thermal shrinkage rate and tensile secant modulus of the resulting reinforcing tape, the PVDC resin that is the material of the reinforcing tape according to the present invention includes, for example, a plasticizer such as dibutyl sebacate, an epoxidized vegetable oil, etc. Stabilizers, lubricants such as fatty acid esters, and maturing agents such as calcium carbonate may be added.

本発明にかかる補強テープは、例えば、前記PVDC系樹脂を溶融押出機により加熱溶融して管状ノズルから押出し、急冷後にインフレーション法等の手段によって二軸延伸し、得られた補強テープ用フィルムを適切なサイズに裁断することによって製造することができる。二軸延伸における縦方向(MD)の延伸倍率は2〜5倍であることが好ましく、2.2〜3.5倍であることがより好ましい。また、横方向(TD)の延伸倍率は2〜5倍であることが好ましく、3.5〜4.5倍であることがより好ましい。延伸温度は15〜40℃程度が好ましく、15〜30℃程度がより好ましい。   The reinforcing tape according to the present invention can be obtained by, for example, heating and melting the PVDC resin with a melt extruder and extruding it from a tubular nozzle. After quenching, the film is biaxially stretched by means of an inflation method or the like. It can be manufactured by cutting into various sizes. The stretching ratio in the machine direction (MD) in biaxial stretching is preferably 2 to 5 times, and more preferably 2.2 to 3.5 times. Moreover, it is preferable that the draw ratio of a horizontal direction (TD) is 2-5 times, and it is more preferable that it is 3.5-4.5 times. The stretching temperature is preferably about 15 to 40 ° C, more preferably about 15 to 30 ° C.

また、本発明にかかる補強テープ用フィルムの製造方法においては、補強テープの寸法安定性を高めるために、延伸したフィルムを縦方向(MD)と横方向(TD)に緩和(収縮)させてもよい。縦方向(MD)の緩和率は1〜20%程度であることが好ましく、5〜9%程度であることがより好ましい。また、横方向(TD)の緩和率は1〜20%程度であることが好ましく、5〜15%程度であることがより好ましい。緩和温度は40〜80℃程度が好ましく、50〜70℃程度がより好ましい。   In the method for producing a reinforcing tape film according to the present invention, the stretched film may be relaxed (shrinked) in the machine direction (MD) and the transverse direction (TD) in order to increase the dimensional stability of the reinforcement tape. Good. The relaxation rate in the machine direction (MD) is preferably about 1 to 20%, and more preferably about 5 to 9%. Further, the relaxation rate in the lateral direction (TD) is preferably about 1 to 20%, and more preferably about 5 to 15%. The relaxation temperature is preferably about 40 to 80 ° C, more preferably about 50 to 70 ° C.

なお、本発明で使用するPVDC系樹脂は、懸濁重合、乳化重合、溶液重合などの任意の重合法により合成されたものでよいが、粉体レジンとしてコンパウンドを形成するには、40〜600μm程度の粒度を有し、粉砕工程を必要としない懸濁重合法により得られたものが好ましい。また、PVDC系樹脂には、その重合時に、抗酸化剤、可塑剤、エポキシ化合物などを含有させることができる。PVDC系樹脂の粉体レジンは、一般に、40〜600μm程度の平均粒径を有するものである。本発明では、重合時にエポキシ化合物や可塑剤などの添加剤を含有させた粉体レジンを用いることができる。もちろん、エポキシ化合物や可塑剤などの添加剤を含有しない粉体レジンであっても、本発明において使用することができる。重合時にエポキシ化合物や可塑剤などの添加剤を含有させたPVDC系樹脂の粉体レジンは、これらの添加剤を重合前または重合中または重合後の少なくともいずれかの時点において重合反応系に加えて、生成PVDC系樹脂中に含有させてから、粉体レジンとして回収したものである。   The PVDC resin used in the present invention may be synthesized by any polymerization method such as suspension polymerization, emulsion polymerization, solution polymerization, etc., but in order to form a compound as a powder resin, it is 40 to 600 μm. What was obtained by the suspension polymerization method which has a particle size of a grade and does not require a grinding | pulverization process is preferable. In addition, the PVDC resin can contain an antioxidant, a plasticizer, an epoxy compound, and the like during the polymerization. The PVDC resin powder resin generally has an average particle size of about 40 to 600 μm. In the present invention, a powder resin containing an additive such as an epoxy compound or a plasticizer can be used during polymerization. Of course, even a powder resin not containing an additive such as an epoxy compound or a plasticizer can be used in the present invention. A powder resin of a PVDC resin containing an additive such as an epoxy compound or a plasticizer at the time of polymerization is added to the polymerization reaction system at least at any time before, during or after the polymerization. Then, after being contained in the produced PVDC resin, it is recovered as a powder resin.

また、本発明において、母材フィルム又は補強テープの熱収縮率は、母材フィルム又は補強テープ用フィルムを試料フィルムとして、JIS:Z1709に記載の方法に準拠して測定されるものである。すなわち、試料フィルムの長手方向(MD)又は短手方向(TD)に2点間の距離が100mmとなるように印をつけ、100℃の沸騰水に3分間浸漬した後に、水道水中で冷却する、その後、前記2点間の距離(すなわち沸騰水に浸漬後の二点間の距離)d(単位:mm)を測定し、沸騰水に浸漬した際の2点間の距離の減少値(100−d)mmの沸騰水に浸漬前の2点間の距離100mmに対する百分率を算出し、これを母材フィルム又は補強テープの100℃における熱収縮率(単位:%)とする。   In the present invention, the thermal shrinkage rate of the base material film or the reinforcing tape is measured in accordance with the method described in JIS: Z1709 using the base material film or the reinforcing tape film as a sample film. That is, the sample film is marked in the longitudinal direction (MD) or the short direction (TD) so that the distance between the two points is 100 mm, immersed in boiling water at 100 ° C. for 3 minutes, and then cooled in tap water. Thereafter, the distance between the two points (that is, the distance between the two points after immersion in boiling water) d (unit: mm) is measured, and the decrease value of the distance between the two points when immersed in boiling water (100 -D) The percentage with respect to the distance of 100 mm between two points before being immersed in boiling water of mm is calculated, and this is defined as the heat shrinkage rate (unit:%) at 100 ° C. of the base material film or the reinforcing tape.

母材フィルム又は補強テープの引張割線弾性率は、母材フィルム又は補強テープ用フィルムを試料フィルムとして、引張り試験機(A&D社製テンシロン)を用い、JIS:K7113項目8.5に記載の方法に準拠して測定されるものである。すなわち、母材フィルム又は補強テープ用フィルムから長手方向(MD)測定用試料フィルム又は短手方向(TD)測定用試料フィルムをそれぞれ幅20mmとなるように切り出した後、この試料フィルムの長手方向又は短手方向の試験長(チャック間距離)が100mmとなるように、引張り試験機に試料フィルムをセットし(測定条件:23℃、50%RH)、10mm/分の速度で引張り試験を行う。そして、規定ひずみ:εを0.025とし、試料フィルムの歪量が0.025に達するまでに要する応力:F(単位:N)を読み取り、さらに試料フィルムの断面積:S(単位:mm)から下記関係式:
(引張割線弾性率:E)=〔F/(ε×S)〕
を用いて母材フィルム又は補強テープの引張割線弾性率(単位:MPa)を算出する。
The tensile secant modulus of the base material film or the reinforcing tape is determined by the method described in JIS: K7113 item 8.5 using a tensile tester (A & D Tensilon) using the base material film or the reinforcing tape film as a sample film. It is measured in conformity. That is, after a sample film for longitudinal direction (MD) measurement or a sample film for transverse direction (TD) measurement is cut out from the base material film or the reinforcing tape film so as to have a width of 20 mm, the longitudinal direction of the sample film or A sample film is set on a tensile tester so that the test length in the short direction (distance between chucks) is 100 mm (measurement conditions: 23 ° C., 50% RH), and a tensile test is performed at a speed of 10 mm / min. Then, the specified strain: ε is set to 0.025, the stress: F (unit: N) required until the strain amount of the sample film reaches 0.025 is read, and the cross-sectional area of the sample film: S (unit: mm 2). ) To the following relation:
(Tensile secant modulus: E) = [F / (ε × S)]
Is used to calculate the tensile secant modulus (unit: MPa) of the base material film or the reinforcing tape.

母材フィルムのアセトン抽出率は、以下の方法により測定されるものである。すなわち、試料として母材フィルム5gを60℃のテトラヒドロフラン(THF)100mlに浸漬して溶解させる。得られたTHF溶液を撹拌しながらメタノールを少量ずつ総量500ml滴下して、試料を再沈殿させた後、混合溶媒を90℃でドライアップさせる。その後、メタノール50mlを添加し、再沈殿させた試料を含めて溶液をソックスレー抽出器に入れ、上部に脱脂綿を乗せる。次いで、予め乾燥して質量を測定した150mlの平底フラスコにメタノール70mlを入れ、ソックスレー抽出器に装着して85℃で24時間抽出する。抽出後の試料をソックスレー抽出器に入れ、上部に脱脂綿を乗せる。次いで、予め乾燥して質量を測定した平底フラスコにアセトン120mlを入れ、ソックスレー抽出器に装着して75℃で24時間抽出する。抽出液をろ紙No.5A(「JIS P3801−1995 ろ紙(化学分析用)」の規格に準ずるもの)を用いてメスシリンダーに100mlろ過し、予め乾燥して質量を測定した150mlの平底フラスコに入れる。使用したメスシリンダーを四塩化炭素で洗浄し、洗浄液を平底フラスコに加える。80℃に調整した恒温水槽中でソックスレー抽出器を用いてアセトンをドライアップさせる。その後、105℃に調整した乾燥機で1時間乾燥し、デシケータ中で1時間放冷して抽出物が入った平底フラスコの質量を求め、次式により母材フィルムのアセトン抽出率(単位:%)を求める。
アセトン抽出量%={(A−B)×E/(C×D)}×100%
A:抽出物が入った平底フラスコの質量(g)。
B:予め乾燥した平底フラスコの質量(g)。
C:試料の質量(g)。
D:ろ紙No.5Aろ過した抽出液の量(100ml)。
E:抽出に使用したアセトンの量(120ml)。
The acetone extraction rate of the base material film is measured by the following method. That is, 5 g of a base material film as a sample is dissolved by being immersed in 100 ml of tetrahydrofuran (THF) at 60 ° C. While stirring the obtained THF solution, 500 ml of methanol is added dropwise little by little to reprecipitate the sample, and then the mixed solvent is dried up at 90 ° C. Thereafter, 50 ml of methanol is added, the solution including the reprecipitated sample is put into a Soxhlet extractor, and absorbent cotton is placed on the top. Next, 70 ml of methanol is placed in a 150 ml flat bottom flask that has been dried and measured in mass, and is attached to a Soxhlet extractor and extracted at 85 ° C. for 24 hours. Place the sample after extraction into a Soxhlet extractor and place absorbent cotton on top. Next, 120 ml of acetone is placed in a flat bottom flask that has been dried and measured for mass, and is attached to a Soxhlet extractor and extracted at 75 ° C. for 24 hours. Extract the extract with filter paper no. Using 5A (according to the standard of “JIS P3801-1995 filter paper (for chemical analysis)”), 100 ml is filtered through a graduated cylinder and placed in a 150 ml flat-bottomed flask that has been dried and measured for mass. Wash the used graduated cylinder with carbon tetrachloride and add the wash to the flat bottom flask. Acetone is dried up using a Soxhlet extractor in a constant temperature water bath adjusted to 80 ° C. Thereafter, the sample was dried for 1 hour in a dryer adjusted to 105 ° C., allowed to cool in a desiccator for 1 hour, and the mass of the flat bottom flask containing the extract was determined. The acetone extraction rate (unit:%) )
Acetone extraction amount% = {(A−B) × E / (C × D)} × 100%
A: Mass (g) of a flat bottom flask containing the extract.
B: Mass (g) of a previously dried flat bottom flask.
C: Mass of the sample (g).
D: Filter paper No. 5A amount of filtered extract (100 ml).
E: Amount of acetone used for extraction (120 ml).

母材フィルムの突刺しエネルギーは、以下の方法により測定されるものである。すなわち、内径が45mmの抑えリングに母材フィルムを装着し、120℃(レトルト時の温度)の温度下、突刺し速度50mm/分でφ1mmのニードルを母材フィルムに突刺して、伸度0%から破断点までの荷重を変位で積分した値を母材フィルムの120℃における突刺しエネルギー(単位:mJ)とする。   The piercing energy of the base material film is measured by the following method. That is, a base material film is attached to a holding ring having an inner diameter of 45 mm, a needle of φ1 mm is pierced into the base material film at a piercing speed of 50 mm / min at a temperature of 120 ° C. (temperature during retort), and the elongation is 0 The value obtained by integrating the load from% to the breaking point by the displacement is defined as the piercing energy (unit: mJ) at 120 ° C. of the base film.

(筒状包装体)
本発明の筒状包装体は、以上説明したような充填物、母材フィルム及び補強テープを備えるものである。本発明の筒状包装体においては、集束シール前における前記母材フィルムの短手方向の100℃における熱収縮率RB−TDと溶着前における前記補強テープの長手方向の100℃における熱収縮率RC−MDとが下記式(F1):
−8%≦RB−TD−RC−MD≦9% (F1)
で表される条件を満たすことが好ましく、下記式(F1a):
4.5%≦RB−TD−RC−MD≦6.5% (F1a)
で表される条件を満たすことがより好ましい。このように母材フィルム及び補強テープのそれぞれの熱収縮率の差を制御することにより、得られる筒状包装体のクリップ部の密封性が向上する傾向にある。一方、RB−TD−RC−MDの値が前記下限未満では、レトルト殺菌処理等の高温加熱処理の際に補強テープが過度に収縮するため、得られる筒状包装体の肩口部に位置する補強テープの端部にめくれが生じ易くなる傾向にある。他方、RB−TD−RC−MDの値が前記上限を超えると、補強テープによる母材フィルムの集束シールされた部分の締め付けが不充分となるため、得られる筒状包装体のクリップ部の密封性が不充分となる傾向にあり、また、補強テープが筒状包装体から脱離し易くなる傾向にある。
(Tubular package)
The cylindrical package of the present invention includes the filler, the base material film, and the reinforcing tape as described above. In the cylindrical package of the present invention, the heat shrinkage ratio RB -TD at 100 ° C. in the short direction of the base material film before the convergence seal and the heat shrinkage rate at 100 ° C. in the longitudinal direction of the reinforcing tape before welding. R C-MD is the following formula (F1):
−8% ≦ R B-TD −R C-MD ≦ 9% (F1)
It is preferable to satisfy the condition represented by the following formula (F1a):
4.5% ≦ RB -TD- RC-MD ≦ 6.5% (F1a)
It is more preferable that the condition represented by Thus, by controlling the difference in thermal shrinkage between the base material film and the reinforcing tape, the sealing performance of the clip portion of the obtained cylindrical package tends to be improved. On the other hand, if the value of RB -TD- RC-MD is less than the lower limit, the reinforcing tape shrinks excessively during high-temperature heat treatment such as retort sterilization treatment, so that it is located at the shoulder portion of the resulting cylindrical package. The end of the reinforcing tape to be turned tends to be easily turned. On the other hand, when the value of RB -TD- RC-MD exceeds the upper limit, the portion of the base film that has been tightly sealed with the reinforcing tape is insufficiently tightened, and therefore the clip portion of the obtained cylindrical package body The sealing property tends to be insufficient, and the reinforcing tape tends to be easily detached from the cylindrical package.

また、本発明の筒状包装体においては、集束シール前における前記母材フィルムの短手方向の引張割線弾性率EB−TDと溶着前における前記補強テープの長手方向の引張割線弾性率EC−MDとが下記式(F2):
−140MPa≦EB−TD−EC−MD≦80MPa (F2)
で表される条件を満たすことが好ましく、下記式(F2a):
−135MPa≦EB−TD−EC−MD≦−50MPa (F2a)
で表される条件を満たすことがより好ましい。このように母材フィルム及び補強テープのそれぞれの引張割線弾性率の差を制御することにより、得られる筒状包装体のクリップ部の密封性が向上する傾向にある。一方、EB−TD−EC−MDの値が前記下限未満では、補強テープが母材フィルムに対して相対的に硬くなりすぎる結果、母材フィルムの集束シールされた部分への補強テープの装着性(フィット性)が低下して、補強テープが母材フィルムと溶着しないことがあり、得られる筒状包装体のクリップ部の密封性が低下する傾向にある。他方、EB−TD−EC−MDの値が前記上限を超えると、補強テープが母材フィルムに対して相対的に柔らかすぎる結果、補強テープによる母材フィルムの集束シールされた部分の締め付けが不充分となるために、得られる筒状包装体の密封性が減じる傾向にある。
Moreover, in the cylindrical package of the present invention, the tensile secant modulus E B-TD in the short direction of the base film before the focusing seal and the tensile secant modulus E C in the longitudinal direction of the reinforcing tape before welding. -MD is the following formula (F2):
−140 MPa ≦ E B-TD −E C-MD ≦ 80 MPa (F2)
It is preferable to satisfy the condition represented by the following formula (F2a):
−135 MPa ≦ EB −TD− E C-MD ≦ −50 MPa (F2a)
It is more preferable that the condition represented by Thus, by controlling the difference between the tensile secant elastic moduli of the base film and the reinforcing tape, the sealing performance of the clip portion of the obtained cylindrical package tends to be improved. On the other hand, if the value of E B-TD -E C-MD is less than the lower limit, the reinforcing tape becomes too hard relative to the base film, and as a result, the reinforcing tape on the converged and sealed portion of the base film is removed. Wearability (fitness) falls, a reinforcement tape may not weld with a base material film, and it exists in the tendency for the sealing performance of the clip part of the obtained cylindrical package to fall. On the other hand, if the value of E B-TD -E C-MD exceeds the upper limit, the reinforcing tape is too soft with respect to the base film, and as a result, the tightly sealed portion of the base film with the reinforcing tape is tightened. Is insufficient, the sealing performance of the resulting cylindrical package tends to be reduced.

このような本発明の筒状包装体の製造方法としては、例えば、母材フィルムを筒状に成形しながら、充填物を充填し、その後、超音波シールによって母材フィルムの端部を集束しつつ、補強テープを添えてシールして密封し、筒状包装体を得る方法を採用することができる。そして、このような方法に用いる装置としては、例えば、クレハ社製の商品名称KAP自動充填包装機を用いることができる。   As a method for producing such a cylindrical package of the present invention, for example, while forming the base film into a cylindrical shape, the filler is filled, and then the end of the base film is focused by ultrasonic sealing. On the other hand, it is possible to employ a method of sealing and sealing with a reinforcing tape to obtain a cylindrical package. And as an apparatus used for such a method, the product name KAP automatic filling packaging machine made from Kureha can be used, for example.

以下、実施例及び比較例に基づいて本発明をより具体的に説明するが、本発明は以下の実施例に限定されるものではない。   EXAMPLES Hereinafter, although this invention is demonstrated more concretely based on an Example and a comparative example, this invention is not limited to a following example.

(実施例1)
先ず、塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が81/19の共重合体A(100質量部)に、クエン酸アセチルトリブチル(ATBC)、セバシン酸ジブチル(DBS)及びエポキシ化植物油を合計9質量部配合し、さらに界面活性剤、滑材及び梨地化剤を合計0.2質量部加えて、ポリ塩化ビニリデン系樹脂を得た。そして、得られたポリ塩化ビニリデン系樹脂を、直径90mmの押出機スクリューを用いて溶融押出し、得られたフィルムを、表1に示した延伸温度及び延伸倍率で二軸延伸し、さらに、表1に示した緩和温度及び緩和率で緩和した後、母材フィルムを得た。得られた母材フィルムの厚み、アセトン抽出率、120℃における突刺しエネルギー、100℃における熱収縮率(長手方向及び短手方向)、引張割線弾性率(長手方向及び短手方向)を測定した。その結果を表1に示す。
Example 1
First, copolymer A (100 parts by mass) of monomer charge mass ratio (VD / VC) at the time of polymerization of vinylidene chloride (VD) and vinyl chloride (VC) is 81/19, acetyltributyl citrate (ATBC), A total of 9 parts by mass of dibutyl sebacate (DBS) and epoxidized vegetable oil was blended, and a total of 0.2 parts by mass of a surfactant, a lubricant and a satinizing agent was added to obtain a polyvinylidene chloride resin. Then, the obtained polyvinylidene chloride resin was melt-extruded using an extruder screw having a diameter of 90 mm, and the obtained film was biaxially stretched at the stretching temperature and stretch ratio shown in Table 1. Further, Table 1 After relaxing at the relaxation temperature and relaxation rate shown in 1. above, a base material film was obtained. The thickness of the obtained base material film, the acetone extraction rate, the piercing energy at 120 ° C., the heat shrinkage rate (longitudinal direction and short direction) at 100 ° C., and the tensile secant modulus (longitudinal direction and short direction) were measured. . The results are shown in Table 1.

また、塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が81/19の共重合体A(100質量部)に、クエン酸アセチルトリブチル(ATBC)、セバシン酸ジブチル(DBS)及びエポキシ化植物油を合計8質量部配合し、さらに界面活性剤、滑材及び梨地化剤を合計0.1質量部加えて、ポリ塩化ビニリデン系樹脂を得た。そして、得られたポリ塩化ビニリデン系樹脂を、直径90mmの押出機スクリューを用いて溶融押出し、得られたフィルムを、表1に示した延伸温度及び延伸倍率で二軸延伸し、さらに、表1に示した緩和温度及び緩和率で緩和した後、補強テープ用フィルムを得た。得られた補強テープ用フィルムを用いて、補強テープの厚み、100℃における熱収縮率(長手方向及び短手方向)、引張割線弾性率(長手方向及び短手方向)を測定した。その結果を表1に示す。   Further, copolymer A (100 parts by mass) having a monomer charge mass ratio (VD / VC) of 81/19 during polymerization of vinylidene chloride (VD) and vinyl chloride (VC) was added to acetyltributyl citrate (ATBC), A total of 8 parts by mass of dibutyl sebacate (DBS) and epoxidized vegetable oil was blended, and a total of 0.1 parts by mass of a surfactant, a lubricant and a satinizing agent was added to obtain a polyvinylidene chloride resin. Then, the obtained polyvinylidene chloride resin was melt-extruded using an extruder screw having a diameter of 90 mm, and the obtained film was biaxially stretched at the stretching temperature and stretch ratio shown in Table 1. Further, Table 1 After relaxing at the relaxation temperature and relaxation rate shown in 1), a film for reinforcing tape was obtained. Using the obtained film for reinforcing tape, the thickness of the reinforcing tape, the heat shrinkage rate (longitudinal direction and short direction) at 100 ° C., and the tensile secant modulus (longitudinal direction and short direction) were measured. The results are shown in Table 1.

次に、幅82mmに裁断した母材フィルムと幅16mmに裁断した補強テープとを用い、充填物(魚肉スリミ50質量%、氷水28.6質量%、植物油10質量%、コーンスターチ8質量%、大豆たんぱく2質量%、食塩1.4質量%からなるペースト)を自動充填包装機(クレハ社製、商品名称KAP3000型自動充填包装機)にて充填し、筒状包装体を得た。すなわち、母材フィルムを筒状に成形しながら、充填物を充填し、超音波シールによって母材フィルムの端部を集束しつつ、補強テープを添えて溶融シールし密封して筒状包装体を得た。なお、筒状の母材フィルムにおいては、折幅(円周の半分の長さ)が36mm、カット長(筒状包装体から充填物を抜き取り、残った筒状の母材フィルムを平らに押し広げて長手方向に測定した長さのことをいう。)が225mm、質量が75gとなるように条件を調整した。また、自動充填包装機の運転条件は、以下に示した通りとした。
充填速度:150本/分。
ホーン・アンビルクリアランス:0.1mm。
シール圧力:450kPa。
振幅ボリューム目盛:69(16μm相当)。
シールデザイン:フラット6.5mmシール幅。
母材フィルムと補強テープの融着部の厚み(レトルト前):80〜160μm。
縦シール条件:ローレット目を設けた加工品。
集束度合い:直径2mm。
フィルムカッター:オルファ社製市販刃。
Next, using a base material film cut to a width of 82 mm and a reinforcing tape cut to a width of 16 mm, a filling (fish meat slime 50 mass%, ice water 28.6 mass%, vegetable oil 10 mass%, corn starch 8 mass%, soybean A paste comprising 2% by mass of protein and 1.4% by mass of salt) was filled with an automatic filling and packaging machine (trade name KAP3000 type automatic filling and packaging machine manufactured by Kureha Co., Ltd.) to obtain a cylindrical package. That is, while forming the base material film into a cylindrical shape, filling the filler, concentrating the ends of the base material film by ultrasonic sealing, melting and sealing with a reinforcing tape, and sealing the cylindrical packaging body Obtained. In the case of a cylindrical base material film, the folding width (half the circumference) is 36 mm, the cut length (the filling material is extracted from the cylindrical package, and the remaining cylindrical base film is pressed flat. The length was measured in the longitudinal direction after spreading.) Was adjusted to 225 mm and mass 75 g. The operating conditions of the automatic filling and packaging machine were as shown below.
Filling speed: 150 / min.
Horn anvil clearance: 0.1 mm.
Seal pressure: 450 kPa.
Amplitude volume scale: 69 (equivalent to 16 μm).
Seal design: flat 6.5mm seal width.
Thickness (before retort) of the fused portion of the base material film and the reinforcing tape: 80 to 160 μm.
Vertical seal condition: Processed product with knurled eyes.
Convergence degree: 2 mm in diameter.
Film cutter: commercially available blade from Olfa.

(実施例2)
塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が81/19の共重合体A(100質量部)に、クエン酸アセチルトリブチル(ATBC)、セバシン酸ジブチル(DBS)及びエポキシ化植物油を合計8質量部配合し、さらに界面活性剤、滑材及び梨地化剤を合計0.4質量部加えて、ポリ塩化ビニリデン系樹脂を得た。そして、得られたポリ塩化ビニリデン系樹脂を、直径90mmの押出機スクリューを用いて溶融押出し、得られたフィルムを、表1に示した延伸温度及び延伸倍率で二軸延伸し、さらに、表1に示した緩和温度及び緩和率で緩和した後、母材フィルムを得た。得られた母材フィルムの厚み、アセトン抽出率、120℃における突刺しエネルギー、100℃における熱収縮率(長手方向及び短手方向)、引張割線弾性率(長手方向及び短手方向)を測定した。その結果を表1に示す。
(Example 2)
Copolymer A (100 parts by mass) having a monomer charge mass ratio (VD / VC) of 81/19 during polymerization of vinylidene chloride (VD) and vinyl chloride (VC) was added to acetyltributyl citrate (ATBC) and sebacic acid. A total of 8 parts by mass of dibutyl (DBS) and epoxidized vegetable oil was blended, and a total of 0.4 parts by mass of a surfactant, a lubricant and a satinizing agent was added to obtain a polyvinylidene chloride resin. Then, the obtained polyvinylidene chloride resin was melt-extruded using an extruder screw having a diameter of 90 mm, and the obtained film was biaxially stretched at the stretching temperature and stretch ratio shown in Table 1. Further, Table 1 After relaxing at the relaxation temperature and relaxation rate shown in 1. above, a base material film was obtained. The thickness of the obtained base material film, the acetone extraction rate, the piercing energy at 120 ° C., the heat shrinkage rate (longitudinal direction and short direction) at 100 ° C., and the tensile secant modulus (longitudinal direction and short direction) were measured. . The results are shown in Table 1.

次に、この母材フィルムを、実施例1で得られた母材フィルムの代わりに用いた以外は実施例1と同様にして筒状包装体を得た。   Next, a cylindrical package was obtained in the same manner as in Example 1 except that this base material film was used instead of the base material film obtained in Example 1.

(実施例3)
塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が81/19の共重合体Aと、塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が71/29の共重合体Bとの混合物(100質量部、A/B(質量比)=75/25)に、クエン酸アセチルトリブチル(ATBC)、セバシン酸ジブチル(DBS)及びエポキシ化植物油を合計6質量部配合し、さらに界面活性剤、滑材及び梨地化剤を合計0.25質量部加えて、ポリ塩化ビニリデン系樹脂を得た。そして、得られたポリ塩化ビニリデン系樹脂を、直径90mmの押出機スクリューを用いて溶融押出し、得られたフィルムを、表1に示した延伸温度及び延伸倍率で二軸延伸し、さらに、表1に示した緩和温度及び緩和率で緩和した後、母材フィルムを得た。得られた母材フィルムの厚み、アセトン抽出率、120℃における突刺しエネルギー、100℃における熱収縮率(長手方向及び短手方向)、引張割線弾性率(長手方向及び短手方向)を測定した。その結果を表1に示す。
(Example 3)
Copolymer A having a monomer charge mass ratio (VD / VC) of 81/19 during polymerization of vinylidene chloride (VD) and vinyl chloride (VC), and during polymerization of vinylidene chloride (VD) and vinyl chloride (VC) A mixture (100 parts by mass, A / B (mass ratio) = 75/25) of copolymer B having a monomer charge mass ratio (VD / VC) of 71/29, acetyltributyl citrate (ATBC), and sebacic acid A total of 6 parts by mass of dibutyl (DBS) and epoxidized vegetable oil was added, and a total of 0.25 parts by mass of a surfactant, a lubricant and a satinizing agent was added to obtain a polyvinylidene chloride resin. Then, the obtained polyvinylidene chloride resin was melt-extruded using an extruder screw having a diameter of 90 mm, and the obtained film was biaxially stretched at the stretching temperature and stretch ratio shown in Table 1. Further, Table 1 After relaxing at the relaxation temperature and relaxation rate shown in 1. above, a base material film was obtained. The thickness of the obtained base material film, the acetone extraction rate, the piercing energy at 120 ° C., the heat shrinkage rate (longitudinal direction and short direction) at 100 ° C., and the tensile secant modulus (longitudinal direction and short direction) were measured. . The results are shown in Table 1.

次に、この母材フィルムを、実施例1で得られた母材フィルムの代わりに用いた以外は実施例1と同様にして筒状包装体を得た。   Next, a cylindrical package was obtained in the same manner as in Example 1 except that this base material film was used instead of the base material film obtained in Example 1.

(比較例1)
塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が80/20の共重合体Cと、塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が71/29の共重合体Bとの混合物(100質量部、C/B(質量比)=75/25)に、クエン酸アセチルトリブチル(ATBC)、セバシン酸ジブチル(DBS)及びエポキシ化植物油を合計8質量部配合し、さらに界面活性剤、滑材及び梨地化剤を合計0.2質量部加えて、ポリ塩化ビニリデン系樹脂を得た。そして、得られたポリ塩化ビニリデン系樹脂を、直径90mmの押出機スクリューを用いて溶融押出し、得られたフィルムを、表1に示した延伸温度及び延伸倍率で二軸延伸し、さらに、表1に示した緩和温度及び緩和率で緩和した後、母材フィルムを得た。得られた母材フィルムの厚み、アセトン抽出率、120℃における突刺しエネルギー、100℃における熱収縮率(長手方向及び短手方向)、引張割線弾性率(長手方向及び短手方向)を測定した。その結果を表1に示す。
(Comparative Example 1)
Copolymer C having a monomer charge mass ratio (VD / VC) of 80/20 during polymerization of vinylidene chloride (VD) and vinyl chloride (VC), and during polymerization of vinylidene chloride (VD) and vinyl chloride (VC) A mixture (100 parts by mass, C / B (mass ratio) = 75/25) of copolymer B having a monomer charge mass ratio (VD / VC) of 71/29, acetyltributyl citrate (ATBC), and sebacic acid A total of 8 parts by mass of dibutyl (DBS) and epoxidized vegetable oil was blended, and a total of 0.2 parts by mass of a surfactant, a lubricant and a satinizing agent was added to obtain a polyvinylidene chloride resin. Then, the obtained polyvinylidene chloride resin was melt-extruded using an extruder screw having a diameter of 90 mm, and the obtained film was biaxially stretched at the stretching temperature and stretch ratio shown in Table 1. Further, Table 1 After relaxing at the relaxation temperature and relaxation rate shown in 1. above, a base material film was obtained. The thickness of the obtained base material film, the acetone extraction rate, the piercing energy at 120 ° C., the heat shrinkage rate (longitudinal direction and short direction) at 100 ° C., and the tensile secant modulus (longitudinal direction and short direction) were measured. . The results are shown in Table 1.

次に、この母材フィルムを、実施例1で得られた母材フィルムの代わりに用いた以外は実施例1と同様にして筒状包装体を得た。   Next, a cylindrical package was obtained in the same manner as in Example 1 except that this base material film was used instead of the base material film obtained in Example 1.

(比較例2)
塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が81/19の共重合体Aと、塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が71/29の共重合体Bとの混合物(100質量部、A/B(質量比)=85/15)に、クエン酸アセチルトリブチル(ATBC)、セバシン酸ジブチル(DBS)及びエポキシ化植物油を合計6.5質量部配合し、さらに界面活性剤、滑材及び梨地化剤を合計0.4質量部加えて、ポリ塩化ビニリデン系樹脂を得た。そして、得られたポリ塩化ビニリデン系樹脂を、直径90mmの押出機スクリューを用いて溶融押出し、得られたフィルムを、表1に示した延伸温度及び延伸倍率で二軸延伸し、さらに、表1に示した緩和温度及び緩和率で緩和した後、母材フィルムを得た。得られた母材フィルムの厚み、アセトン抽出率、120℃における突刺しエネルギー、100℃における熱収縮率(長手方向及び短手方向)、引張割線弾性率(長手方向及び短手方向)を測定した。その結果を表1に示す。
(Comparative Example 2)
Copolymer A having a monomer charge mass ratio (VD / VC) of 81/19 during polymerization of vinylidene chloride (VD) and vinyl chloride (VC), and during polymerization of vinylidene chloride (VD) and vinyl chloride (VC) A mixture (100 parts by mass, A / B (mass ratio) = 85/15) of copolymer B having a monomer charge mass ratio (VD / VC) of 71/29, acetyltributyl citrate (ATBC), and sebacic acid A total of 6.5 parts by mass of dibutyl (DBS) and epoxidized vegetable oil was blended, and a total of 0.4 parts by mass of a surfactant, a lubricant and a satinizing agent was added to obtain a polyvinylidene chloride resin. Then, the obtained polyvinylidene chloride resin was melt-extruded using an extruder screw having a diameter of 90 mm, and the obtained film was biaxially stretched at the stretching temperature and stretch ratio shown in Table 1. Further, Table 1 After relaxing at the relaxation temperature and relaxation rate shown in 1. above, a base material film was obtained. The thickness of the obtained base material film, the acetone extraction rate, the piercing energy at 120 ° C., the heat shrinkage rate (longitudinal direction and short direction) at 100 ° C., and the tensile secant modulus (longitudinal direction and short direction) were measured. . The results are shown in Table 1.

次に、この母材フィルムを、実施例1で得られた母材フィルムの代わりに用いた以外は実施例1と同様にして筒状包装体を得た。   Next, a cylindrical package was obtained in the same manner as in Example 1 except that this base material film was used instead of the base material film obtained in Example 1.

(比較例3)
塩化ビニリデン(VD)と塩化ビニル(VC)の重合時におけるモノマー仕込み質量比(VD/VC)が82/18の共重合体D(100質量部)に、クエン酸アセチルトリブチル(ATBC)、セバシン酸ジブチル(DBS)及びエポキシ化植物油を合計6質量部配合し、さらに界面活性剤、滑材及び梨地化剤を合計0.4質量部加えて、ポリ塩化ビニリデン系樹脂を得た。そして、得られたポリ塩化ビニリデン系樹脂を、直径90mmの押出機スクリューを用いて溶融押出し、得られたフィルムを、表1に示した延伸温度及び延伸倍率で二軸延伸し、さらに、表1に示した緩和温度及び緩和率で緩和した後、母材フィルムを得た。得られた母材フィルムの厚み、アセトン抽出率、120℃における突刺しエネルギー、100℃における熱収縮率(長手方向及び短手方向)、引張割線弾性率(長手方向及び短手方向)を測定した。その結果を表1に示す。
(Comparative Example 3)
Copolymer D (100 parts by mass) having a monomer charge mass ratio (VD / VC) of 82/18 during polymerization of vinylidene chloride (VD) and vinyl chloride (VC) was added to acetyltributyl citrate (ATBC) and sebacic acid. A total of 6 parts by mass of dibutyl (DBS) and epoxidized vegetable oil was blended, and a total of 0.4 parts by mass of a surfactant, a lubricant and a satinizing agent was added to obtain a polyvinylidene chloride resin. Then, the obtained polyvinylidene chloride resin was melt-extruded using an extruder screw having a diameter of 90 mm, and the obtained film was biaxially stretched at the stretching temperature and stretch ratio shown in Table 1. Further, Table 1 After relaxing at the relaxation temperature and relaxation rate shown in 1. above, a base material film was obtained. The thickness of the obtained base material film, the acetone extraction rate, the piercing energy at 120 ° C., the heat shrinkage rate (longitudinal direction and short direction) at 100 ° C., and the tensile secant modulus (longitudinal direction and short direction) were measured. . The results are shown in Table 1.

次に、この母材フィルムを、実施例1で得られた母材フィルムの代わりに用いた以外は実施例1と同様にして筒状包装体を得た。   Next, a cylindrical package was obtained in the same manner as in Example 1 except that this base material film was used instead of the base material film obtained in Example 1.

<筒状包装体の密封性の評価>
実施例及び比較例で得られた筒状包装体の密封性を以下のようにして評価した。すなわち、筒状包装体に貯湯式レトルト殺菌装置(日阪製作所社製、商品名称フレーバーエース)を用い、温度120℃、設定圧力2.5kg/cmにて15分間のレトルト処理を行ったものを試料とした。レトルト処理を行った翌日に、100本の試料を無作為に抽出し、これらを0.4質量%青色1号色素溶液に浸漬して温度5〜10℃の条件下において5日間放置した。その後、試料を色素溶液中から取り出し、外表面を水洗してからフィルムを開封して、中身の充填物ヘの着色の有無を調べることによって密封性を評価した。なお、色素溶液が浸透して中身の充填物に着色が認められたクリップ部(補強テープを溶着した部分)を密封不良クリップ部と判定し、試料100本のクリップ部200か所中における密封不良クリップ部の割合(百分率)を求めてクリップ部の密封不良率とした。その結果を表1に示す。
<Evaluation of sealing performance of cylindrical package>
The sealing properties of the cylindrical packages obtained in the examples and comparative examples were evaluated as follows. That is, a retort treatment for 15 minutes at a temperature of 120 ° C. and a set pressure of 2.5 kg / cm 2 using a hot water storage-type retort sterilizer (manufactured by Nisaka Manufacturing Co., Ltd., product name Flavor Ace) on a cylindrical package. Was used as a sample. On the next day after the retort treatment, 100 samples were randomly extracted and immersed in a 0.4 mass% blue No. 1 dye solution and left at a temperature of 5 to 10 ° C. for 5 days. Thereafter, the sample was taken out from the dye solution, the outer surface was washed with water, the film was opened, and the sealing property was evaluated by examining the presence or absence of coloring in the filling material. Note that the clip portion (the portion where the reinforcing tape was welded) in which the dye solution had permeated and the filling of the contents was recognized was determined to be a poorly sealed clip portion, and poorly sealed in the 200 clip portions of 100 samples. The ratio (percentage) of the clip portion was determined and used as the sealing failure rate of the clip portion. The results are shown in Table 1.

表1に示した結果から明らかなように、本発明の筒状包装体(実施例1〜3)は、筒状包装体のクリップ部の密封性に優れたものであった。   As is clear from the results shown in Table 1, the tubular package (Examples 1 to 3) of the present invention was excellent in the sealing performance of the clip portion of the tubular package.

以上説明したように、本発明によれば、クリップ部の密封性に優れた筒状包装体を得ることが可能となる。
したがって、本発明の筒状包装体は、チーズ、ソーセージ、かまぼこ、ハム等の加工食品を充填物とする筒状包装体として有用である。
As described above, according to the present invention, it is possible to obtain a cylindrical package with excellent clip portion sealing performance.
Therefore, the cylindrical package of the present invention is useful as a cylindrical package having a processed food such as cheese, sausage, kamaboko and ham as a filler.

Claims (7)

(A)充填物と、(B)長手方向の両端部が集束シールされることにより前記充填物が充填されている、ポリ塩化ビニリデン系樹脂のフィルムからなる筒状の母材フィルムと、(C)前記母材フィルムが集束シールされた部分を巻回し覆うように前記母材フィルムに溶着されている、ポリ塩化ビニリデン系樹脂のフィルムからなる補強テープとを備える筒状包装体であって、
集束シール前における前記母材フィルムの短手方向の100℃における熱収縮率RB−TDが10.0〜18.9%の範囲であり、アセトン抽出率が9.0%以下であり、120℃における突刺しエネルギーが2.1mJ以上である、ことを特徴とする筒状包装体。
(A) a filler, and (B) a cylindrical base material film made of a polyvinylidene chloride-based resin film filled with the filler by focusing and sealing at both ends in the longitudinal direction; and (C And a reinforcing tape made of a polyvinylidene chloride-based resin film welded to the base material film so as to wind and cover the portion where the base material film is converged and sealed,
The heat shrinkage ratio RB -TD at 100 ° C. in the short direction of the base material film before the focusing seal is in the range of 10.0 to 18.9%, the acetone extraction rate is 9.0% or less, and 120 A cylindrical package characterized by having a piercing energy at 2.1 ° C. of 2.1 mJ or more.
集束シール前における前記母材フィルムの短手方向の100℃における熱収縮率RB−TDと溶着前における前記補強テープの長手方向の100℃における熱収縮率RC−MDとが下記式(F1):
−8%≦RB−TD−RC−MD≦9% (F1)
で表される条件を満たすことを特徴とする請求項1に記載の筒状包装体。
The thermal shrinkage rate R B-TD at 100 ° C. in the short direction of the base material film before the focusing seal and the thermal shrinkage rate R C-MD at 100 ° C. in the longitudinal direction of the reinforcing tape before welding are expressed by the following formula (F1) ):
−8% ≦ R B-TD −R C-MD ≦ 9% (F1)
The cylindrical package body according to claim 1, wherein the condition expressed by
集束シール前における前記母材フィルムの短手方向の100℃における熱収縮率RB−TDと溶着前における前記補強テープの長手方向の100℃における熱収縮率RC−MDとが下記式(F1a):
4.5%≦RB−TD−RC−MD≦6.5% (F1a)
で表される条件を満たすことを特徴とする請求項2に記載の筒状包装体。
The thermal shrinkage rate R B-TD at 100 ° C. in the short direction of the base material film before the focusing seal and the thermal shrinkage rate R C-MD at 100 ° C. in the longitudinal direction of the reinforcing tape before welding are expressed by the following formula (F1a ):
4.5% ≦ RB -TD- RC-MD ≦ 6.5% (F1a)
The cylindrical package body according to claim 2, wherein the condition expressed by
集束シール前における前記母材フィルムの120℃における突刺しエネルギーが2.5mJ以上であることを特徴とする請求項1〜3のうちのいずれか一項に記載の筒状包装体。   The cylindrical packaging body according to any one of claims 1 to 3, wherein the piercing energy at 120 ° C of the base material film before the focusing seal is 2.5 mJ or more. 集束シール前における前記母材フィルムの長手方向の引張割線弾性率EB−MDが332〜450MPaの範囲であることを特徴とする請求項1〜4のうちのいずれか一項に記載の筒状包装体。 The cylindrical shape according to any one of claims 1 to 4, wherein a tensile secant modulus EB -MD in a longitudinal direction of the base material film before the focusing seal is in a range of 332 to 450 MPa. Packaging body. 前記母材フィルムが、塩化ビニリデンモノマーと塩化ビニルモノマーとの共重合体を含有するポリ塩化ビニリデン系樹脂のフィルムからなるものであることを特徴とする請求項1〜5のうちのいずれか一項に記載の筒状包装体。   The said base material film consists of a film of the polyvinylidene chloride resin containing the copolymer of a vinylidene chloride monomer and a vinyl chloride monomer, The any one of Claims 1-5 characterized by the above-mentioned. The cylindrical package body as described in 2. 前記補強テープが、塩化ビニリデンモノマーと塩化ビニルモノマーとの共重合体を含有するポリ塩化ビニリデン系樹脂のフィルムからなるものであることを特徴とする請求項1〜6のうちのいずれか一項に記載の筒状包装体。   The said reinforcing tape consists of a film of the polyvinylidene chloride type-resin containing the copolymer of a vinylidene chloride monomer and a vinyl chloride monomer, It is any one of Claims 1-6 characterized by the above-mentioned. The cylindrical package of description.
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