JP2000272004A - Method for producing polyolefin-based heat-shrinkable film - Google Patents
Method for producing polyolefin-based heat-shrinkable filmInfo
- Publication number
- JP2000272004A JP2000272004A JP11077456A JP7745699A JP2000272004A JP 2000272004 A JP2000272004 A JP 2000272004A JP 11077456 A JP11077456 A JP 11077456A JP 7745699 A JP7745699 A JP 7745699A JP 2000272004 A JP2000272004 A JP 2000272004A
- Authority
- JP
- Japan
- Prior art keywords
- film
- polypropylene
- heat
- shrinkable film
- polyolefin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920006257 Heat-shrinkable film Polymers 0.000 title claims abstract description 36
- 229920000098 polyolefin Polymers 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000004743 Polypropylene Substances 0.000 claims abstract description 51
- 229920001155 polypropylene Polymers 0.000 claims abstract description 51
- -1 polypropylene Polymers 0.000 claims abstract description 45
- 229920005989 resin Polymers 0.000 claims abstract description 29
- 239000011347 resin Substances 0.000 claims abstract description 29
- 239000010410 layer Substances 0.000 claims abstract description 24
- 239000000203 mixture Substances 0.000 claims abstract description 12
- 229920000089 Cyclic olefin copolymer Polymers 0.000 claims abstract description 9
- 229920000092 linear low density polyethylene Polymers 0.000 claims abstract description 9
- 239000004707 linear low-density polyethylene Substances 0.000 claims abstract description 9
- 239000002344 surface layer Substances 0.000 claims abstract description 9
- 239000004711 α-olefin Substances 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims abstract description 7
- 238000002844 melting Methods 0.000 description 12
- 230000008018 melting Effects 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 6
- 229920005673 polypropylene based resin Polymers 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 238000004806 packaging method and process Methods 0.000 description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920013716 polyethylene resin Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 1
- 101001024616 Homo sapiens Neuroblastoma breakpoint family member 9 Proteins 0.000 description 1
- 102100037013 Neuroblastoma breakpoint family member 9 Human genes 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 239000002981 blocking agent Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 229920005677 ethylene-propylene-butene terpolymer Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229920005678 polyethylene based resin Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000011342 resin composition Substances 0.000 description 1
- 150000003623 transition metal compounds Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Landscapes
- Laminated Bodies (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
(57)【要約】
【課題】 ポリオレフィン系熱収縮性フィルムにおい
て、低温収縮性と常温寸法安定性を共に満足せしめるこ
とを課題とする。
【解決手段】 チューブラー延伸法により延伸された、
下記(a)または(b)からなるポリオレフィン系熱収
縮性フィルムを、70〜90℃でMD(機械方向)に1
0〜15%弛緩させる。
(a)ポリプロピレン系樹脂とプロピレン−α−オレフ
ィン共重合体及び/又はシンジオタクチック−ポリプロ
ピレンの混合組成物。
(b)表面層がポリプロピレン系樹脂、中間層が直鎖状
低密度ポリエチレン系樹脂を主体とする組成物。
(57) [Problem] To provide a polyolefin-based heat-shrinkable film which satisfies both low-temperature shrinkability and dimensional stability at room temperature. SOLUTION: The film is stretched by a tubular stretching method,
A polyolefin-based heat-shrinkable film comprising the following (a) or (b) is subjected to MD (machine direction) at 70 to 90 ° C.
Allow 0-15% relaxation. (A) A mixed composition of a polypropylene resin and a propylene-α-olefin copolymer and / or syndiotactic-polypropylene. (B) A composition whose surface layer is mainly composed of a polypropylene resin and whose intermediate layer is mainly composed of a linear low-density polyethylene resin.
Description
【0001】[0001]
【産業上の利用分野】本発明は熱収縮性フィルムの製造
方法に関し、詳しくは低温収縮性と常温寸法安定性に優
れたポリオレフィン系熱収縮性フィルムの製造方法に関
するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a heat-shrinkable film, and more particularly to a method for producing a polyolefin-based heat-shrinkable film having excellent low-temperature shrinkage and dimensional stability at room temperature.
【0002】[0002]
【従来の技術】従来、熱収縮性フィルムとしては、ポリ
塩化ビニル、ポリプロピレン、ポリエチレン系樹脂の延
伸フィルム等が知られている。中でもポリプロピレン系
熱収縮性フィルムは、高速自動包装適性に優れ、焼却時
における有害ガスの発生もないため、好んで用いられて
いる。しかしながら、ポリプロピレン系熱収縮性フィル
ムは、熱収縮トンネルを比較的高温にしなければ収縮し
ないため、収縮包装体に皺が入りやすく、またコーナー
部のフィルムがツノ状に残りやすい等、包装仕上がり性
に劣るという欠点を有している。このような欠点を解決
するために、特開平8−151454号公報、特開平8
−269265号公報等に開示されているように、ポリ
プロピレン系樹脂に低融点樹脂を混合したり、あるい
は、特開昭58−166049号公報、特開昭63−1
73641号公報、特開昭63−214446号公報等
に開示され、本発明と同一出願人になる特願平10−7
1255号に記載されているように、ポリプロピレン系
樹脂とポリエチレン系樹脂を積層することで、比較的低
温でも収縮する、即ち低温収縮性を有する熱収縮性フィ
ルムが提案されている。前記のように、ポリプロピレン
系樹脂に低融点樹脂を混合したり、ポリプロピレン系樹
脂とポリエチレン系樹脂を積層する方法では、低温収縮
性の改善に伴い、包装仕上がり性を改善することができ
る。しかしながら、常温におけるMDの収縮率も大きく
なる、即ち、常温寸法安定性が悪化するため、フィルム
をロール状で保管している際に、巻締まりをおこし、フ
ィルム同士がブロッキングしたり、フィルムの平面性が
悪化したりすることで包装トラブルを起こすという問題
があった。2. Description of the Related Art Conventionally, as a heat-shrinkable film, a stretched film of polyvinyl chloride, polypropylene, or polyethylene resin is known. Above all, a polypropylene-based heat-shrinkable film is preferably used because it has excellent suitability for high-speed automatic packaging and does not generate harmful gases during incineration. However, since the polypropylene heat-shrinkable film does not shrink unless the heat-shrinkable tunnel is heated to a relatively high temperature, the shrink-wrapped body tends to wrinkle, and the film at the corners tends to remain in a horn shape. It has the disadvantage of being inferior. In order to solve such disadvantages, Japanese Patent Application Laid-Open No. 8-151454 and
As disclosed in JP-A-269265 and the like, a low melting point resin is mixed with a polypropylene resin or disclosed in JP-A-58-166049 and JP-A-63-1.
No. 73641, Japanese Patent Application Laid-Open No. 63-214446, and the like, which are the same applicant as the present invention.
As described in No. 1255, a heat-shrinkable film that shrinks even at a relatively low temperature by laminating a polypropylene-based resin and a polyethylene-based resin, that is, has a low-temperature shrinkability has been proposed. As described above, in the method of mixing the polypropylene resin with the low melting point resin or laminating the polypropylene resin and the polyethylene resin, the packaging finish can be improved with the improvement of the low temperature shrinkage. However, the shrinkage ratio of MD at room temperature also increases, that is, the dimensional stability at room temperature deteriorates. Therefore, when the film is stored in a roll, the film is tightened, and the films are blocked with each other. There is a problem that packaging trouble is caused due to deterioration of properties.
【0003】[0003]
【発明が解決しようとする課題】本発明は、ポリオレフ
ィン系熱収縮性フィルムにおいて、低温収縮性と常温寸
法安定性を共に満足せしめることを課題とするものであ
る。An object of the present invention is to provide a polyolefin-based heat-shrinkable film that satisfies both low-temperature shrinkage and dimensional stability at room temperature.
【0004】[0004]
【課題を解決するための手段】本発明者らは前記の欠点
を解消した熱収縮性フィルムを求めて鋭意検討した結
果、本発明に到達したものである。Means for Solving the Problems The present inventors have intensively studied for a heat-shrinkable film which has solved the above-mentioned disadvantages, and as a result, have reached the present invention.
【0005】即ち、本発明は、チューブラー延伸法によ
り延伸された、下記(a)または(b)からなるポリオ
レフィン系熱収縮性フィルムを、70〜90℃でMD
(機械方向)に10〜15%弛緩させることを特徴とす
るポリオレフィン系熱収縮性フィルムの製造方法であ
る。 (a)ポリプロピレン系樹脂とプロピレン−α−オレフ
ィン共重合体及び/又はシンジオタクチック−ポリプロ
ピレンの混合組成物。 (b)表面層がポリプロピレン系樹脂、中間層が直鎖状
低密度ポリエチレン系樹脂を主体とする組成物。That is, the present invention relates to a method for producing a polyolefin heat-shrinkable film comprising the following (a) or (b) stretched by a tubular stretching method at 70 to 90 ° C.
A method for producing a polyolefin-based heat-shrinkable film, characterized in that the film is relaxed in the machine direction by 10 to 15%. (A) A mixed composition of a polypropylene resin and a propylene-α-olefin copolymer and / or syndiotactic-polypropylene. (B) A composition whose surface layer is mainly composed of a polypropylene resin and whose intermediate layer is mainly composed of a linear low-density polyethylene resin.
【0006】以下、本発明を詳細に説明すると、先ず
、チューブラー延伸法により延伸されたポリオレフィ
ン系熱収縮性フィルムの熱処理条件としては、温度が7
0〜90℃、MDの弛緩率が10〜15%である。温度
が70℃未満では、常温寸法安定性が劣るため好ましく
なく、90℃を超えると低温収縮性が劣るため好ましく
ない。また、縦の弛緩率が10%未満では常温寸法安定
性が劣るため好ましくなく、15%を超えると熱処理工
程においてフィルムに弛みが生じ、フィルムがロールに
巻き付く等のトラブルが発生するため好ましくない。Hereinafter, the present invention will be described in detail. First, as a heat treatment condition of a polyolefin heat-shrinkable film stretched by a tubular stretching method, a temperature of 7 is used.
0-90 ° C., MD relaxation rate is 10-15%. If the temperature is lower than 70 ° C., the dimensional stability at room temperature is inferior. On the other hand, if the longitudinal relaxation rate is less than 10%, the dimensional stability at room temperature is inferior, which is not preferable. If it exceeds 15%, the film is loosened in the heat treatment step, and trouble such as winding of the film around the roll is not preferred. .
【0007】ポリプロピレン系樹脂とプロピレン−α−
オレフィン共重合体及び/又はシンジオタクチック−ポ
リプロピレンの混合組成物からなるポリプロピレン系熱
収縮性フィルムは、フィルムの腰が強く、高速自動包装
適性に優れるという特長を有する。[0007] Polypropylene resin and propylene-α-
A polypropylene-based heat-shrinkable film comprising an olefin copolymer and / or a syndiotactic-polypropylene mixed composition has the features that the film is strong and excellent in suitability for high-speed automatic packaging.
【0008】本発明で用いられるポリプロピレン系樹脂
としては、エチレン−プロピレン共重合体あるいはエチ
レン−プロピレン−ブテン3元共重合体であり、プロピ
レンにエチレンあるいはエチレンとブテンを2〜10%
ランダム共重合されたもので、融点が130〜145℃
のものが用いられる。融点が145℃を超えると低温収
縮性が劣るため好ましくなく、130℃未満のものは耐
ブロッキング性が劣るため好ましくない。The polypropylene resin used in the present invention is an ethylene-propylene copolymer or an ethylene-propylene-butene terpolymer, and ethylene or ethylene and butene is added to propylene in an amount of 2 to 10%.
Random copolymerized, melting point 130-145 ° C
Is used. If the melting point exceeds 145 ° C., the low-temperature shrinkage is inferior, which is not preferable. If the melting point is lower than 130 ° C., the blocking resistance is inferior, which is not preferable.
【0009】ポリプロピレン系樹脂に混合されるプロピ
レン−α−オレフィン共重合体及びシンジオタクチック
−ポリプロピレンは、融点が105〜130℃のものが
用いられる。融点が105℃未満のものは耐ブロッキン
グ性が劣るため好ましくなく、130℃を超えると低温
収縮性が劣るため好ましくない。As the propylene-α-olefin copolymer and the syndiotactic polypropylene mixed with the polypropylene resin, those having a melting point of 105 to 130 ° C. are used. Those having a melting point of less than 105 ° C are not preferred because of poor blocking resistance, and those having a melting point of more than 130 ° C are not preferred because of low shrinkage at low temperatures.
【0010】本発明で用いられるプロピレン−α−オレ
フィン共重合体としては、プロピレンに比較的多量のブ
テンを共重合させたプロピレン−ブテン共重合体等が用
いられる。また、シンジオタクチック−ポリプロピレン
としては、13C−NMRで測定したシンジオタクチッ
クペンタッド分率が0.7以上のシンジオタクチシテイ
ーの良好なポリプロピレンが用いられる。このようなシ
ンジオタクチック−ポリプロピレンは、例えば特開平2
−41303号公報、特開平2−41305号公報、特
開平2−274703号公報、特開平2−274704
号公報、特開平3−179005号公報、特開平3−1
79006号公報等に記載されているような互いに非対
称な配位子を有する架橋型遷移金属化合物および助触媒
からなる触媒を用いて得られる。As the propylene-α-olefin copolymer used in the present invention, a propylene-butene copolymer obtained by copolymerizing propylene with a relatively large amount of butene is used. Further, as the syndiotactic-polypropylene, a syndiotacticity having a syndiotactic pentad fraction of 0.7 or more measured by 13 C-NMR is used.
Good polypropylene is used. Such syndiotactic-polypropylene is disclosed in, for example,
-41303, JP-A-2-41305, JP-A-2-274703, JP-A-2-274704
JP, JP-A-3-179005, JP-A-3-1
It can be obtained by using a catalyst comprising a crosslinked transition metal compound having mutually asymmetric ligands and a cocatalyst as described in JP 79006B.
【0011】プロピレン−α−オレフィン共重合体及び
/又はシンジオタクチック−ポリプロピレンは、ポリプ
ロピレン系樹脂に対して2〜20重量%の範囲で混合さ
れ、どちらか一方のみを混合しても、両者を混合しても
構わない。混合率が2重量%未満では低温収縮性が劣る
ため好ましくなく、20重量%を超えると耐ブロッキン
グ性が低下するので好ましくない。The propylene-α-olefin copolymer and / or the syndiotactic polypropylene are mixed in a range of 2 to 20% by weight based on the weight of the polypropylene-based resin. You may mix them. If the mixing ratio is less than 2% by weight, the low-temperature shrinkage is inferior because it is inferior, and if it exceeds 20% by weight, the blocking resistance is undesirably reduced.
【0012】表面層がポリプロピレン系樹脂、中間層が
直鎖状低密度ポリエチレンを主体とする組成物からなる
ポリオレフィン系多層熱収縮性フィルムは、耐引裂性が
高いという特長を有する。A polyolefin-based multilayer heat-shrinkable film whose surface layer is composed of a composition mainly composed of a polypropylene-based resin and whose intermediate layer is mainly composed of linear low-density polyethylene has a feature of high tear resistance.
【0013】表面層に用いられるポリプロピレン系樹脂
としては、前記のポリプロピレン系熱収縮性フィルムと
同様のポリプロピレン系樹脂が用いられる。As the polypropylene resin used for the surface layer, the same polypropylene resin as the above-mentioned polypropylene heat-shrinkable film is used.
【0014】中間層に用いられる直鎖状低密度ポリエチ
レンは、エチレンとα−オレフィンとの共重合体であ
り、密度が0.900〜0.925g/cm3 の範囲
のものが用いられる。密度が0.900g/cm3 未
満のものはフィルム強度が低下するため好ましくなく、
0.925g/cm3 を超えると低温収縮性が劣るた
め好ましくない。The linear low-density polyethylene used for the intermediate layer is a copolymer of ethylene and an α-olefin, and has a density in the range of 0.900 to 0.925 g / cm 3 . Those having a density of less than 0.900 g / cm 3 are not preferred because the film strength decreases,
If it exceeds 0.925 g / cm 3 , the low-temperature shrinkability is inferior, so that it is not preferable.
【0015】全層に対する中間層の厚み比率としては、
30〜80%の範囲が好ましい。中間層の厚み比率が3
0%未満では低温収縮性が劣るため好ましくなく、80
%を超えるとフィルムの腰が低下するため好ましくな
い。The thickness ratio of the intermediate layer to all layers is as follows:
A range of 30 to 80% is preferred. The thickness ratio of the intermediate layer is 3
If it is less than 0%, the low-temperature shrinkage is inferior, so that it is not preferable.
%, It is not preferable because the stiffness of the film is reduced.
【0016】中間層には、製造工程で発生するスクラッ
プをリサイクルすることができ、その場合、中間層は直
鎖状低密度ポリエチレンと表面層に使用したポリプロピ
レン系樹脂との混合組成物となる。In the intermediate layer, scrap generated in the production process can be recycled. In this case, the intermediate layer is a mixed composition of linear low-density polyethylene and the polypropylene resin used for the surface layer.
【0017】更に、前記のポリプロピレン系熱収縮性フ
ィルムおよびポリオレフィン系多層熱収縮性フィルムに
は、本発明の目的に支障をきたさない範囲で、他の樹脂
や滑剤、アンチブロッキング剤、帯電防止剤、防曇剤等
の添加剤を適宜使用することができる。Further, the above-mentioned heat-shrinkable polypropylene-based film and multi-layer heat-shrinkable polyolefin-based film may contain other resins, lubricants, anti-blocking agents, antistatic agents, and the like, as long as the object of the present invention is not hindered. Additives such as anti-fogging agents can be used as appropriate.
【0018】次に本発明のポリオレフィン系熱収縮性フ
ィルムの製造方法を、3層積層環状製膜延伸の場合を例
にあげ、具体的に説明する。Next, the method for producing the polyolefin-based heat-shrinkable film of the present invention will be specifically described with reference to an example of a three-layer laminated annular film-forming stretching.
【0019】まず、前記の直鎖状低密度ポリエチレンと
ポリプロピレンから成る混合組成物を中間層、ポリプロ
ピレン系樹脂を表面層となるように、3台の押出機によ
り溶融混練し、3層環状ダイより環状に共押し出しし、
延伸することなく一旦急冷固化してチューブ状未延伸フ
ィルムを作製する。得られたチューブ状未延伸フィルム
を例えば図1で示すようなチューブラー延伸装置に供給
し、高度の配向可能な温度範囲、例えばポリプロピレン
系樹脂の融点以下10℃、好ましくは融点以下15℃よ
りも低い温度で、チューブ内部にガス圧を適用して膨張
延伸せしめ同時二軸配向を起こさせる。延伸倍率は必ず
しも縦横同一でなくともよいが、優れた強度、収縮率等
の物性を得るためには縦横何れの方向にも3倍以上、よ
り好ましくは3.5倍以上に延伸するのが好ましい。延
伸装置から取り出したフィルムは、本発明の熱処理条
件、即ち、70〜90℃でMDに10〜15%の弛緩率
で熱処理を施す。熱処理の方法としては、特に限定され
ないが、複数の熱ロールによるロール熱処理あるいはテ
ンター熱処理が好ましい。First, the above-mentioned mixed composition comprising linear low-density polyethylene and polypropylene is melt-kneaded by three extruders so as to form an intermediate layer and a polypropylene-based resin as a surface layer. Co-extrusion in a ring,
It is quenched once without being stretched to produce a tubular unstretched film. The obtained tubular unstretched film is supplied to, for example, a tubular stretching apparatus as shown in FIG. At a low temperature, a gas pressure is applied inside the tube to expand and stretch to cause simultaneous biaxial orientation. The stretching ratio is not necessarily the same in the vertical and horizontal directions, but in order to obtain excellent properties such as excellent strength and shrinkage, it is preferable that the film is stretched in the vertical and horizontal directions at least 3 times or more, more preferably at least 3.5 times. . The film taken out of the stretching apparatus is subjected to the heat treatment conditions of the present invention, that is, to a heat treatment at 70 to 90 ° C. in the MD at a relaxation rate of 10 to 15%. The heat treatment method is not particularly limited, but roll heat treatment with a plurality of heat rolls or tenter heat treatment is preferable.
【0020】[0020]
【実施例】次に実施例によって本発明をより具体的に説
明するが、本発明はこれらの実施例に限定されるもので
はない。尚、本実施例中に示した100℃熱収縮率、常
温寸法安定性の評価は以下の方法によった。Next, the present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples. In addition, the following methods were used to evaluate the heat shrinkage at 100 ° C. and the dimensional stability at room temperature shown in this example.
【0021】1)100℃熱収縮率 フィルムを縦横ともに100mmを目標に切断し、寸法
を実測する。次いで、100℃のグリセリン浴に10秒
間浸漬し、浸漬後の寸法を実測後、下記の式1により算
出した。なお、この数値が25%以上であれば、低温収
縮性が優れていることを示す。 式1 100℃熱収縮率(%)=(L0−L1)×100/L0 但し、L0=収縮前のサンプルの寸法(mm)、L1=
グリセリンに浸漬後のサンプルの寸法(mm)MD、T
Dそれぞれを測定1) Heat shrinkage at 100 ° C. The film is cut with a target of 100 mm in both length and width, and the dimensions are measured. Next, it was immersed in a glycerin bath at 100 ° C. for 10 seconds, the dimensions after immersion were measured, and calculated by the following formula 1. In addition, when this numerical value is 25% or more, it shows that low-temperature shrinkability is excellent. Formula 1 100 ° C. Heat shrinkage (%) = (L 0 −L 1 ) × 100 / L 0 where L 0 = dimension of sample before shrinkage (mm), L 1 =
Dimensions of sample after immersion in glycerin (mm) MD, T
Measure each D
【0022】2)常温寸法安定性 フィルムを縦横ともに200mmを目標に切断し、MD
の寸法を実測する。次いで、35℃のギヤオーブン中に
16時間放置し、MDの寸法を実測後、下記の式2によ
り算出した。なお、この数値が2%以下であれば、常温
寸法安定性が優れていることを示す。 式2 常温寸法安定性(%)=(L0−L1)×100/L0 但し、L0=収縮前のサンプルの寸法(mm)、L1=
ギヤーオーブンに放置後のサンプルの寸法(mm)2) Room-temperature dimensional stability The film was cut to a target of 200 mm in both length and width, and
Measure the dimensions of Then, after being left in a gear oven at 35 ° C. for 16 hours, the dimensions of the MD were measured and then calculated by the following equation 2. When this value is 2% or less, it indicates that the dimensional stability at normal temperature is excellent. Equation 2 Room temperature dimensional stability (%) = (L 0 −L 1 ) × 100 / L 0 where L 0 = dimension of sample before shrinkage (mm), L 1 =
Dimension of sample after leaving in gear oven (mm)
【0023】実施例1 融点が136℃のポリプロピレン系樹脂(F233D
G;グランドポリマー株式会社製)95重量%と、融点
が110℃のプロピレン−α−オレフィン共重合体(タ
フマーXR110T;三井石油化学株式会社製)5重量
%を押出機で170〜240℃で溶融混練し、240℃
に保った環状ダイスより押出した。形成されたチューブ
を、内側は冷却水が循環している円筒状冷却マンドレル
の外表面を摺動させながら、外側は水槽を通すことによ
り冷却して引き取り、チューブ状の未延伸フィルムを得
た。このチューブ状未延伸フィルムを図1のチューブラ
ー二軸延伸装置に導き、加熱し、縦横それぞれ4倍に延
伸し、延伸フィルムを得た。その後、2本の熱ロールを
用いて、温度75℃、縦の弛緩率11%で熱処理を行
い、厚み15μのポリプロピレン系熱収縮性フィルムを
得た。得られた延伸フィルムは、表1に示すように、低
温収縮性、常温寸法安定性ともに良好であった。Example 1 A polypropylene resin having a melting point of 136 ° C. (F233D
G: 95% by weight of Grand Polymer Co., Ltd. and 5% by weight of a propylene-α-olefin copolymer having a melting point of 110 ° C. (Tuffmer XR110T; Mitsui Petrochemical Co., Ltd.) at 170 to 240 ° C. by an extruder. Knead, 240 ° C
Extruded from an annular die maintained at a constant pressure. The formed tube was cooled and drawn by passing through a water tank while sliding the outer surface of a cylindrical cooling mandrel in which cooling water circulates, thereby obtaining a tubular unstretched film. This tubular unstretched film was guided to the tubular biaxial stretching apparatus of FIG. 1, heated, stretched four times in each of length and width, and a stretched film was obtained. Thereafter, heat treatment was performed using two heat rolls at a temperature of 75 ° C. and a vertical relaxation rate of 11% to obtain a 15 μm thick polypropylene heat-shrinkable film. As shown in Table 1, the obtained stretched film had good low-temperature shrinkage and dimensional stability at room temperature.
【0024】実施例2 実施例1と同一の条件で延伸フィルムを作製した後、表
1に示す条件で熱処理を行い、厚み15μのポリプロピ
レン系熱収縮性フィルムを得た。得られたポリプロピレ
ン系熱収縮性フィルムは、低温収縮性、常温寸法安定性
ともに良好であった。Example 2 A stretched film was prepared under the same conditions as in Example 1, and then heat-treated under the conditions shown in Table 1 to obtain a heat-shrinkable polypropylene film having a thickness of 15 μm. The obtained polypropylene-based heat-shrinkable film was excellent in both low-temperature shrinkage and dimensional stability at room temperature.
【0025】実施例3 実施例1のプロピレン−α−オレフィン共重合体を、融
点が125℃、シンジオタクチックペンタッド分率が
0.79のシンジオタクチックポリプロピレン(チアロ
SPT−0159;三井化学株式会社製)に変更した他
は、実施例1と同一条件にて延伸フィルムを作製した。
その後、表1に示す条件で熱処理を行い、厚み15μの
ポリプロピレン系熱収縮性フィルムを得た。得られたポ
リプロピレン系熱収縮性フィルムは、低温収縮性、常温
寸法安定性ともに良好であった。Example 3 The propylene-α-olefin copolymer of Example 1 was prepared using a syndiotactic polypropylene (Thiaro SPT-0159; Mitsui Chemicals, Inc.) having a melting point of 125 ° C. and a syndiotactic pentad fraction of 0.79. A stretched film was produced under the same conditions as in Example 1 except that the film was changed to (manufactured by the company).
Thereafter, heat treatment was performed under the conditions shown in Table 1 to obtain a 15-μm-thick polypropylene heat-shrinkable film. The obtained polypropylene-based heat-shrinkable film was excellent in both low-temperature shrinkage and dimensional stability at room temperature.
【0026】実施例4 表面層に実施例1と同一のポリプロピレン系樹脂を用
い、中間層に密度が0.916g/cm3 の直鎖状低
密度ポリエチレン(ウルトゼックス1510S;三井化学株
式会社製)を80重量%と、表面層と同一のポリプロピ
レン系樹脂20重量%の混合組成物を用い、内層、中間
層、外層の厚み比率が1/5/1になるように、3層環
状ダイを用いてチューブ状未延伸フィルムを作製した。
その後、実施例1と同様の方法で、縦横の延伸倍率をそ
れぞれ4倍で延伸フィルムを作製し、表1に示す条件で
熱処理を行い、厚み15μのポリオレフィン系多層熱収
縮性フィルムを得た。得られたポリオレフィン系多層熱
収縮性フィルムは、低温収縮性、常温寸法安定性ともに
良好であった。Example 4 The same polypropylene resin as in Example 1 was used for the surface layer, and a linear low-density polyethylene (Ultzex 1510S; manufactured by Mitsui Chemicals, Inc.) having a density of 0.916 g / cm 3 was used for the intermediate layer. Using a mixed composition of 80% by weight and 20% by weight of the same polypropylene-based resin as the surface layer, using a three-layer annular die so that the thickness ratio of the inner layer, the intermediate layer, and the outer layer becomes 1/5/1. A tubular unstretched film was produced.
Thereafter, in the same manner as in Example 1, a stretched film was prepared at a stretch ratio of 4 times in each of the longitudinal and transverse directions, and heat-treated under the conditions shown in Table 1 to obtain a polyolefin-based multilayer heat-shrinkable film having a thickness of 15 μm. The obtained polyolefin-based multilayer heat-shrinkable film had good low-temperature shrinkage and dimensional stability at room temperature.
【0027】比較例1 実施例1と同一の条件で延伸フィルムを作製した後、表
1に示す条件で熱処理を行い、厚み15μのポリプロピ
レン系熱収縮性フィルムを得た。得られたポリプロピレ
ン系熱収縮性フィルムは、低温収縮性は良好であった
が、常温寸法安定性が劣るものであった。Comparative Example 1 A stretched film was prepared under the same conditions as in Example 1, and then heat-treated under the conditions shown in Table 1 to obtain a 15 μm thick heat-shrinkable polypropylene film. The resulting polypropylene-based heat-shrinkable film had good low-temperature shrinkability but poor dimensional stability at room temperature.
【0028】比較例2 実施例1と同一の条件で延伸フィルムを作製した後、表
1に示す条件で熱処理を行い、厚み15μのポリプロピ
レン系熱収縮性フィルムを得た。得られたポリプロピレ
ン系熱収縮性フィルムは、常温寸法安定性は良好であっ
たが、低温収縮性が劣るものであった。Comparative Example 2 A stretched film was prepared under the same conditions as in Example 1, and then heat-treated under the conditions shown in Table 1 to obtain a heat-shrinkable polypropylene-based film having a thickness of 15 μm. The resulting polypropylene-based heat-shrinkable film had good room-temperature dimensional stability but poor low-temperature shrinkage.
【0029】比較例3 実施例1と同一の条件で延伸フィルムを作製した後、表
1に示す条件で熱処理を行ったが、フィルムに弛みが生
じ、フィルムがロールに巻き付くというトラブルが発生
した。Comparative Example 3 A stretched film was prepared under the same conditions as in Example 1, and then heat-treated under the conditions shown in Table 1. However, the film was loosened, and a problem that the film was wound around a roll occurred. .
【0030】比較例4 実施例3と同一の条件で延伸フィルムを作製した後、表
1に示す条件で熱処理を行い、厚み15μのポリオレフ
ィン系熱収縮性フィルムを得た。得られたポリオレフィ
ン系熱収縮性フィルムは、低温収縮性は良好であった
が、常温寸法安定性が劣るものであった。Comparative Example 4 A stretched film was prepared under the same conditions as in Example 3 and then heat-treated under the conditions shown in Table 1 to obtain a polyolefin-based heat-shrinkable film having a thickness of 15 μm. The resulting polyolefin-based heat-shrinkable film had good low-temperature shrinkability but poor dimensional stability at room temperature.
【0031】比較例5 実施例3と同一の条件で延伸フィルムを作製した後、表
1に示す条件で熱処理を行い、厚み15μのポリオレフ
ィン系熱収縮性フィルムを得た。得られたポリオレフィ
ン系熱収縮性フィルムは、常温寸法安定性は良好であっ
たが、低温収縮性が劣るものであった。Comparative Example 5 A stretched film was prepared under the same conditions as in Example 3 and then heat-treated under the conditions shown in Table 1 to obtain a polyolefin-based heat-shrinkable film having a thickness of 15 μm. The resulting polyolefin-based heat-shrinkable film had good room-temperature dimensional stability, but poor low-temperature shrinkability.
【0032】比較例6 融点が142℃のポリプロピレン系樹脂(F233D
F;グランドポリマー株式会社製)を用いて、実施例1
と同一の条件で延伸フィルムを作製した後、表1に示す
条件で熱処理を行い、厚み15μのポリプロピレン系熱
収縮性フィルムを得た。得られたポリプロピレン系熱収
縮性フィルムは、常温寸法安定性は良好であったが、低
温収縮性が劣るものであった。Comparative Example 6 A polypropylene resin having a melting point of 142 ° C. (F233D
F; Grand Polymer Co., Ltd.)
After producing a stretched film under the same conditions as in Example 1, heat treatment was performed under the conditions shown in Table 1 to obtain a 15-μm-thick polypropylene heat-shrinkable film. The resulting polypropylene-based heat-shrinkable film had good room-temperature dimensional stability but poor low-temperature shrinkage.
【0033】[0033]
【表1】 *樹脂構成 A:ポリプロピレン系樹脂(mp;136℃)/タフマーXR110T
=95/5 B:ポリプロピレン系樹脂(mp;136℃)/チアロSPT0159
=95/5 C:内外層;ポリプロピレン系樹脂(mp;136℃) 中間層;直鎖状低密度ポリエチレン/ポリプロピレン系
樹脂(mp;136℃)=80/20 各層厚み比;内層/中間層/外層=1/5/1 D:ポリプロピレン系樹脂(mp:142℃)[Table 1] * Resin composition A: Polypropylene resin (mp; 136 ° C) / Toughmer XR110T
= 95/5 B: Polypropylene resin (mp; 136 ° C) / Thiaro SPT0159
= 95/5 C: Inner / Outer layer; Polypropylene resin (mp; 136 ° C) Intermediate layer; Linear low density polyethylene / polypropylene resin (mp; 136 ° C) = 80/20 Thickness ratio of each layer; Inner layer / Intermediate layer / Outer layer = 1/5/1 D: Polypropylene resin (mp: 142 ° C)
【0034】[0034]
【発明の効果】本発明は、ポリオレフィン系熱収縮性フ
ィルムの熱処理条件を特定することにより、低温収縮性
と常温寸法安定性の優れたポリオレフィン系熱収縮性フ
ィルムの製造が可能になった。According to the present invention, it is possible to produce a polyolefin-based heat-shrinkable film having excellent low-temperature shrinkability and room-temperature dimensional stability by specifying heat treatment conditions for the polyolefin-based heat-shrinkable film.
【図1】 実施例で用いたチューブラー二軸延伸装置の
概略断面図である。FIG. 1 is a schematic sectional view of a tubular biaxial stretching apparatus used in Examples.
【符号の説明】 1:未延伸フィルム 2:低速ニップロール 3:高速ニップロール 4:予熱器 5:主熱器 6:冷却エアーリング 7:折り畳みロール群[Description of Signs] 1: Unstretched film 2: Low speed nip roll 3: High speed nip roll 4: Preheater 5: Main heater 6: Cooling air ring 7: Folding roll group
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B29K 105:02 B29L 7:00 9:00 Fターム(参考) 4F100 AK07A AK07B AK63C AK66A AK66B AL05A AL05B BA02 BA03 BA06 BA10A BA10B BA15 EH171 EJ382 EJ422 JA03 JL04 4F210 AA03 AA08 AA11 AA11A AA11E AE01 AG01 AG03 QA05 QC07 QG01 QG15 QG18 QW12 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) B29K 105: 02 B29L 7:00 9:00 F term (Reference) 4F100 AK07A AK07B AK63C AK66A AK66B AL05A AL05B BA02 BA03 BA06 BA10A BA10B BA15 EH171 EJ382 EJ422 JA03 JL04 4F210 AA03 AA08 AA11 AA11A AA11E AE01 AG01 AG03 QA05 QC07 QG01 QG15 QG18 QW12
Claims (1)
下記(a)または(b)からなるポリオレフィン系熱収
縮性フィルムを、70〜90℃でMD(機械方向)に1
0〜15%弛緩させることを特徴とするポリオレフィン
系熱収縮性フィルムの製造方法。 (a)ポリプロピレン系樹脂とプロピレン−α−オレフ
ィン共重合体及び/又はシンジオタクチック−ポリプロ
ピレンの混合組成物。 (b)表面層がポリプロピレン系樹脂、中間層が直鎖状
低密度ポリエチレン系樹脂を主体とする組成物。Claims: 1. A film stretched by a tubular stretching method,
A polyolefin-based heat-shrinkable film comprising the following (a) or (b) is subjected to MD (machine direction) at 70 to 90 ° C.
A method for producing a polyolefin-based heat-shrinkable film, wherein the film is relaxed by 0 to 15%. (A) A mixed composition of a polypropylene resin and a propylene-α-olefin copolymer and / or syndiotactic-polypropylene. (B) A composition whose surface layer is mainly composed of a polypropylene resin and whose intermediate layer is mainly composed of a linear low-density polyethylene resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11077456A JP2000272004A (en) | 1999-03-23 | 1999-03-23 | Method for producing polyolefin-based heat-shrinkable film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11077456A JP2000272004A (en) | 1999-03-23 | 1999-03-23 | Method for producing polyolefin-based heat-shrinkable film |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000272004A true JP2000272004A (en) | 2000-10-03 |
Family
ID=13634525
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11077456A Pending JP2000272004A (en) | 1999-03-23 | 1999-03-23 | Method for producing polyolefin-based heat-shrinkable film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000272004A (en) |
-
1999
- 1999-03-23 JP JP11077456A patent/JP2000272004A/en active Pending
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