JPH0739517B2 - Resin composition for shrink film - Google Patents
Resin composition for shrink filmInfo
- Publication number
- JPH0739517B2 JPH0739517B2 JP61278480A JP27848086A JPH0739517B2 JP H0739517 B2 JPH0739517 B2 JP H0739517B2 JP 61278480 A JP61278480 A JP 61278480A JP 27848086 A JP27848086 A JP 27848086A JP H0739517 B2 JPH0739517 B2 JP H0739517B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- propylene
- copolymer
- resin composition
- stretching
- 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.)
- Expired - Fee Related
Links
- 239000011342 resin composition Substances 0.000 title claims description 30
- 229920006300 shrink film Polymers 0.000 title description 3
- 229920001577 copolymer Polymers 0.000 claims description 28
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 25
- 239000000843 powder Substances 0.000 claims description 21
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 21
- 229910000323 aluminium silicate Inorganic materials 0.000 claims description 18
- 239000002245 particle Substances 0.000 claims description 11
- 239000004711 α-olefin Substances 0.000 description 32
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 24
- 230000000903 blocking effect Effects 0.000 description 19
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 16
- 238000000034 method Methods 0.000 description 14
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 13
- 239000005977 Ethylene Substances 0.000 description 13
- 230000000704 physical effect Effects 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 10
- 238000002156 mixing Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 230000009102 absorption Effects 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 8
- 229910021536 Zeolite Inorganic materials 0.000 description 7
- 125000004432 carbon atom Chemical group C* 0.000 description 7
- 239000010457 zeolite Substances 0.000 description 7
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 6
- 229920005604 random copolymer Polymers 0.000 description 6
- 239000002981 blocking agent Substances 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 230000000379 polymerizing effect Effects 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 239000008096 xylene Substances 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 238000011088 calibration curve Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229920005674 ethylene-propylene random copolymer Polymers 0.000 description 2
- 238000012685 gas phase polymerization Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 229920005606 polypropylene copolymer Polymers 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 229920001897 terpolymer Polymers 0.000 description 2
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 1
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000013032 Hydrocarbon resin Substances 0.000 description 1
- 235000010724 Wisteria floribunda Nutrition 0.000 description 1
- 239000011954 Ziegler–Natta catalyst Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000004512 die casting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- UAUDZVJPLUQNMU-KTKRTIGZSA-N erucamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-KTKRTIGZSA-N 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 229920006270 hydrocarbon resin Polymers 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002667 nucleating agent Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920005629 polypropylene homopolymer Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000012748 slip agent Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance 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
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は例えば、低温収縮性が良好で、しかも透明性、
光沢、滑り性、耐ブロッキング性が優れた収縮フィルム
用に適したプロピレン共重合体系樹脂組成物に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The present invention has, for example, good low-temperature shrinkability, transparency, and
The present invention relates to a propylene copolymer-based resin composition suitable for a shrink film having excellent gloss, slipperiness, and blocking resistance.
<従来の技術> ポリプロピレン系樹脂の収縮包装用フィルムは、かなり
以前から使用されており、エチレン−プロピレンランダ
ム共重合体や、エチレン−ブテン−1−プロピレン三元
ランダム共重合体などを延伸処理したフィルムが知られ
ている(例えば特開昭52−16588号公報等)。これらの
フィルムは食品衛生上の問題や、廃棄上の問題が少なく
良好に使用されているが、ポリ塩化ビニル製の収縮フィ
ルムと比べ、低温収縮性が劣り、その改良が望まれてい
る。低温収縮性を改良する為には、より低温で延伸でき
ればよいことが判っているが、それを可能とするには、
プロピレン系共重合体の結晶性を低下させる必要があ
る。しかし、結晶性をより低下させたプロピレン共重合
体に従来から知られているシリカをアンチブロッキング
剤として配合した樹脂組成物を比較的低温で延伸したの
では、フィルムの透明性が悪くなると同時に、結晶性が
低く、柔らかくなったせいか、耐ブロッキング性と滑り
性も悪くなるという問題がある。<Prior Art> Films for polypropylene resin shrink wrapping have been used for a long time, and ethylene-propylene random copolymers, ethylene-butene-1-propylene ternary random copolymers, and the like have been stretched. Films are known (for example, JP-A-52-16588). Although these films have been used favorably due to less food hygiene and disposal problems, they are inferior in low-temperature shrinkability to shrink films made of polyvinyl chloride, and their improvement is desired. In order to improve the low temperature shrinkability, it has been known that it is necessary to be able to stretch at a lower temperature, but in order to make it possible,
It is necessary to reduce the crystallinity of the propylene-based copolymer. However, if the resin composition obtained by blending conventionally known silica as an anti-blocking agent in a propylene copolymer having a reduced crystallinity is stretched at a relatively low temperature, the transparency of the film becomes poor, and at the same time, There is a problem that blocking resistance and slipperiness are deteriorated, probably because of low crystallinity and softness.
一方、高結晶性ポリプロピレンにゼオライト粉末を添加
した組成物が知られているが(特公昭52−16134号公
報)、そこで開示されているのは、高温で延伸して得ら
れる2軸延伸フィルムである。このフィルムは、むしろ
収縮特性は好ましくない自己支持性フィルムであり、添
加されるゼオライトの粒径は、2〜3μと大きく、しか
も添加量も0.2部以下と比較的少量である。本発明者ら
の知見によれば、結晶性のより低いプロピレン系共重合
体に上記ゼオライトを添加して、比較的低温で延伸処理
を行うとこれまたフィルムの透明性が失われると同時
に、耐ブロッキング性と滑り性もよくないものである。On the other hand, a composition in which zeolite powder is added to highly crystalline polypropylene is known (Japanese Patent Publication No. 52-16134), but what is disclosed therein is a biaxially stretched film obtained by stretching at high temperature. is there. This film is a self-supporting film having rather unfavorable shrinkage characteristics, and the particle size of the added zeolite is as large as 2-3 .mu.m, and the addition amount is 0.2 parts or less, which is a relatively small amount. According to the knowledge of the present inventors, when the above-mentioned zeolite is added to a propylene-based copolymer having lower crystallinity and the stretching treatment is performed at a relatively low temperature, the transparency of the film is also lost and at the same time, It also has poor blocking properties and slipperiness.
又、特開昭58−213031号公報には、高結晶性であるポリ
プロピレンホモポリマーにアルミノシリケート粉末を0.
2部添加した樹脂組成物を高温(150℃)で2軸延伸した
フィルムが開示されているが、本発明者らの知見によれ
ば、結晶性のより低いプロピレン系共重合体に上記アル
ミノシリケート粉末を同じように添加して、比較的低温
で延伸処理を行うと、フィルムの透明性が失われたり、
耐ブロッキング性と滑り性が不良だったりするものであ
る。Further, JP-A-58-213031 discloses that a polypropylene homopolymer having high crystallinity and an aluminosilicate powder of 0.
A film obtained by biaxially stretching a resin composition containing 2 parts at a high temperature (150 ° C.) is disclosed. However, according to the findings of the present inventors, a propylene-based copolymer having a lower crystallinity is added to the above aluminosilicate. If the powder is added in the same way and stretching is performed at a relatively low temperature, the transparency of the film is lost,
They have poor blocking resistance and slipperiness.
<発明が解決しようとする問題点> 本発明は以上のような状況に鑑み、結晶性の比較的低い
プロピレン系共重合体を比較的低温で延伸して得られる
低温収縮性が良好で、しかも透明性、光沢、滑り性、耐
ブロッキング性が優れた収縮包装用フィルムを得る為の
樹脂組成物を提供しようとするものである。<Problems to be Solved by the Invention> In view of the above situation, the present invention has good low-temperature shrinkability obtained by stretching a propylene-based copolymer having relatively low crystallinity at relatively low temperature, and An object of the present invention is to provide a resin composition for obtaining a shrink wrapping film having excellent transparency, gloss, slipperiness, and blocking resistance.
<問題点を解決するための手段> 本発明者等は、ビカット軟化点が、特定温度以下のプロ
ピレン共重合体に、特定のアンチブロッキング剤を特定
含量添加した樹脂組成物を成膜後、延伸処理すれば上記
諸特性を全て合わせ持つ収縮包装用フィルムが得られる
ことを見い出すに到り、本発明を完成した。<Means for Solving the Problems> The inventors of the present invention formed a resin composition in which a specific content of a specific antiblocking agent was added to a propylene copolymer having a Vicat softening point of a specific temperature or lower, and then stretching. It was found that a film for shrink wrapping having all of the above-mentioned various properties can be obtained by processing, and the present invention was completed.
即ち、本発明はビカット軟化点が130℃以下のプロピレ
ン共重合体に平均粒径が1μ以下のアルミノシリケート
粉末を0.25〜2.0重量部添加したことを特徴とする収縮
フィルム用樹脂組成物である。That is, the present invention is a resin composition for a shrinkable film, which is obtained by adding 0.25 to 2.0 parts by weight of an aluminosilicate powder having an average particle size of 1 µ or less to a propylene copolymer having a Vicat softening point of 130 ° C or less.
本発明の樹脂組成物の特徴は、比較的低温での延伸が可
能である上に、延伸後のフィルムは、低温収縮性が良好
で、しかも透明性、光沢、滑り性、耐ブロッキング性が
優れることである。The resin composition of the present invention is characterized in that it can be stretched at a relatively low temperature, and the stretched film has good low-temperature shrinkability and is excellent in transparency, gloss, slipperiness, and blocking resistance. That is.
以下本発明を詳細に説明する。The present invention will be described in detail below.
本発明で使用するプロピレン共重合体は公知の結晶性の
ものである。例えば、周知のエチレン−プロピレンラン
ダム共重合体あるいはエチレン−ブテン−1−プロピレ
ンランダムタ−ポリマーで、コモノマー含有量が1〜15
wt%、並びに冷キシレン可溶部(以下CXSという)が15w
t%以下であるものや、これらのランダム共重合体と下
記に示す特定のプロピレン−α−オレフィン共重合体と
のブレンド組成物で、プロピレン−α−オレフィン共重
合体の配合割合が20重量%以上のものなどである。これ
らの中でも後者のブレンド組成物が比較的低温で延伸し
ても良好な透明性が得られやすい点で好ましい。The propylene copolymer used in the present invention is a known crystalline one. For example, a well-known ethylene-propylene random copolymer or ethylene-butene-1-propylene random terpolymer having a comonomer content of 1 to 15 is used.
wt% and cold xylene soluble part (hereinafter referred to as CXS) 15w
In a blend composition of t% or less or a specific propylene-α-olefin copolymer shown below with these random copolymers, the blending ratio of the propylene-α-olefin copolymer is 20% by weight. More than that. Among these, the latter blend composition is preferable because it is easy to obtain good transparency even when stretched at a relatively low temperature.
本発明で使用するプロピレン共重合体のビカット軟化点
は130℃以下であり、125℃以下が好ましく、115℃以下
がより好ましい。ビカット軟化点が該上限界を上廻る
と、比較的低温での延伸が不可能となり、得られたフィ
ルムの低温収縮性が悪く好ましくない。The Vicat softening point of the propylene copolymer used in the present invention is 130 ° C or lower, preferably 125 ° C or lower, and more preferably 115 ° C or lower. If the Vicat softening point exceeds the upper limit, stretching at a relatively low temperature becomes impossible, and the low temperature shrinkability of the obtained film is unfavorable.
本発明の好ましい態様として使用する上記の特定のプロ
ピレン−α−オレフィン共重合体は、触媒系として、公
知のα−オレフィンの立体規則性重合用触媒であり、い
わゆるチーグラー・ナッタ触媒すなわち周期律表第IV〜
VIII族遷移金属化合物と周期律表第I〜III族典型金属
の有機化合物と電子供与性化合物等の第3成分からなる
ものを使用し、重合法として、溶剤中で重合する溶剤重
合法あるいは、気相中で重合する気相重合法などにより
製造することができる。例えば、特願昭61−164505号公
報に記載された共重合体(B)を重合する方法で得るこ
とができるが、以下に規定する条件を満足するものなら
ばそれでよい。The above-mentioned specific propylene-α-olefin copolymer used as a preferred embodiment of the present invention is a known catalyst for stereoregular polymerization of α-olefins, that is, a so-called Ziegler-Natta catalyst, that is, the periodic table. IV-
A group VIII transition metal compound, an organic compound of a group I to III typical metal of the periodic table, and a third component such as an electron donating compound are used, and the polymerization method is a solvent polymerization method of polymerizing in a solvent, or It can be produced by a gas phase polymerization method of polymerizing in a gas phase. For example, it can be obtained by the method of polymerizing the copolymer (B) described in Japanese Patent Application No. 61-164505, but any polymer satisfying the conditions specified below may be used.
該プロピレン−α−オレフィン共重合体は、プロピレン
と炭素数4以上のα−オレフィン又はプロピレンと炭素
数4以上のα−オレフィンとエチレンとの共重合体で 共重合体の炭素数4以上のα−オレフィン含有量が8
〜35モル% 共重合体のエチレン含有量が5モル%以下 共重合体の冷キシレン可溶部が15〜70wt%なる条件を
満足する共重合体である。The propylene-α-olefin copolymer is a copolymer of propylene and α-olefin having 4 or more carbon atoms, or a copolymer of propylene, α-olefin having 4 or more carbon atoms and ethylene, and α having 4 or more carbon atoms of the copolymer. -Olefin content 8
-35 mol% The ethylene content of the copolymer is 5 mol% or less. The copolymer satisfies the condition that the cold xylene-soluble part of the copolymer is 15 to 70 wt%.
該プロピレン−α−オレフィン共重合体は、コモノマー
として炭素数4以上のα−オレフィンあるいはエチレン
を少量併用して使用する。炭素数4以上のα−オレフィ
ンとしては、ブテン−1、ペンテン−1、ヘキセン−
1、4メチル−ペンテン−1等の単独あるいは併用系が
あげられるが、例えば、気相重合を実施した場合、液化
しにくいことから分圧を高くとれるブテン−1が好まし
い。The propylene-α-olefin copolymer is used in combination with a small amount of α-olefin having 4 or more carbon atoms or ethylene as a comonomer. As the α-olefin having 4 or more carbon atoms, butene-1, pentene-1, hexene-
Examples thereof include 1,4-methyl-pentene-1 and the like, which may be used alone or in combination, but for example, butene-1 is preferable because it is difficult to liquefy when gas phase polymerization is carried out and a high partial pressure is obtained.
該プロピレン−α−オレフィン共重合体の炭素数4以上
のα−オレフィン含有量は、8〜35モル%であり、10〜
30モル%が好ましい。炭素数4以上のα−オレフィン含
有量が該下限界を下廻ると、本プロピレン−α−オレフ
ィン共重合体を配合して得られるブレンド組成物は、比
較的低温での延伸が不可能になったり、延伸後のフィル
ムの透明性が悪くなったりして好ましくない。炭素数4
以上のα−オレフィン含有量が該上限界を上廻ると、延
伸後のフィルムの滑り性や耐ブロッキング性が悪くなり
好ましくない。The content of α-olefin having 4 or more carbon atoms in the propylene-α-olefin copolymer is 8 to 35 mol%,
30 mol% is preferred. When the content of the α-olefin having 4 or more carbon atoms falls below the lower limit, the blend composition obtained by blending the propylene-α-olefin copolymer cannot be stretched at a relatively low temperature. Or, the transparency of the film after stretching is deteriorated, which is not preferable. Carbon number 4
If the above α-olefin content exceeds the upper limit, the slidability and blocking resistance of the stretched film are deteriorated, which is not preferable.
該プロピレン−α−オレフィン共重合体のエチレン含有
量は5モル%以下であり、3モル%以下が好ましい。エ
チレン含有量が該上限界を上廻るとフィルムの透明性が
経時的に悪化したり、耐ブロッキング性や滑りが悪くな
ったり好ましくない。The ethylene content of the propylene-α-olefin copolymer is 5 mol% or less, preferably 3 mol% or less. When the ethylene content exceeds the upper limit, the transparency of the film is deteriorated with time, the blocking resistance and the slip are deteriorated, which is not preferable.
該プロピレン−α−オレフィン共重合体の冷キシレン可
溶部(CXS)は15〜70wt%であり、16〜60wt%がより好
ましい。CXSが該下限界を下廻ると、本プロピレン−α
−オレフィン共重合体を配合して得られるブレンド組成
物は、比較的低温での延伸が不可能になったり、延伸後
のフィルムの透明性が悪くなったりして好ましくない。
CXSが該上限界を上廻ると、延伸後のフィルムの滑り
や、耐ブロッキング性が悪くなり好ましくない。The cold xylene-soluble part (CXS) of the propylene-α-olefin copolymer is 15 to 70 wt%, more preferably 16 to 60 wt%. When CXS falls below the lower limit, the propylene-α
The blend composition obtained by blending the olefin copolymer is not preferable because it cannot be stretched at a relatively low temperature, or the transparency of the stretched film becomes poor.
If the CXS exceeds the upper limit, it is not preferable because the film after stretching has poor slip resistance and blocking resistance.
該プロピレン−α−オレフィン共重合体と該ランダム共
重合体とのブレンドで本発明の好ましい態様としてのプ
ロピレン共重合体を得るに際し、該プロピレン−α−オ
レフィン共重合体の配合割合は20重量%以上であり、30
重量%以上が好ましく40重量%以上がより好ましい。該
プロピレン−α−オレフィン共重合体の配合割合が該下
限界を下廻ると、比較的低温での延伸で、フィルムの良
好な透明性が得られにくくなり好ましくない。In obtaining a propylene copolymer as a preferred embodiment of the present invention by blending the propylene-α-olefin copolymer and the random copolymer, the blending ratio of the propylene-α-olefin copolymer is 20% by weight. Is over, 30
It is preferably at least wt%, more preferably at least 40 wt%. If the blending ratio of the propylene-α-olefin copolymer is below the lower limit, it is difficult to obtain good transparency of the film by stretching at a relatively low temperature, which is not preferable.
本発明で使用するプロピレン共重合体のメルトインデッ
クスは、0.5〜50g/10分であるのが好ましい。メルトイ
ンデックスが該下限界を下廻ると、加工性が悪くなり好
ましくなく、該上限界を上廻るとフィルムの延伸性が悪
くなり好ましくない。The melt index of the propylene copolymer used in the present invention is preferably 0.5 to 50 g / 10 minutes. If the melt index is lower than the lower limit, the processability is deteriorated, which is not preferable, and if the melt index is higher than the upper limit, the stretchability of the film is deteriorated, which is not preferable.
本発明で使用するアルミノシリケート粉末は、天然ゼオ
ライトや合成ゼオライトあるいは、例えば特開昭58−21
3031に示されたような無定形のアルミノシリケートなど
であり、アルミナ分とシリカ分の必須成分以外に塩基性
成分を含んでもよい。The aluminosilicate powder used in the present invention is a natural zeolite or a synthetic zeolite, or, for example, JP-A-58-21.
It is an amorphous aluminosilicate as shown in 3031 and may contain a basic component in addition to the essential components of the alumina component and the silica component.
本発明で使用するアルミノシリケート粉末の平均粒径
(コールターカウンターによる)は1μ以下のものであ
る。平均粒径が1μを超えると、それを含む樹脂組成物
を比較的低温で延伸した時フィルムの透明性が悪くな
り、好ましいない。The aluminosilicate powder used in the present invention has an average particle size (by Coulter counter) of 1 μm or less. If the average particle size exceeds 1 μ, the transparency of the film deteriorates when a resin composition containing it is stretched at a relatively low temperature, which is not preferable.
本発明で使用するアルミノシリケート粉末の吸油量は10
0(ml/100g)以下であるのが好ましい。吸油量が小さい
方がフィルムの滑り性を改良しやすく、好ましい。The oil absorption of the aluminosilicate powder used in the present invention is 10
It is preferably 0 (ml / 100 g) or less. The smaller the oil absorption is, the easier it is to improve the slipperiness of the film, which is preferable.
本発明の樹脂組成物は、該アルミノシリケート粉末を上
記で規定したプロピレン共重合体に0.25〜2.0重量部添
加して得られるが、添加量として、0.30〜1.5重量部が
好ましい。添加量が該下限界を下廻ると、フィルムの耐
ブロッキング性と滑りが悪く好ましくない。添加量が該
上限界を上廻ると、フィルムの透明性が悪くなり好まし
くない。The resin composition of the present invention is obtained by adding 0.25 to 2.0 parts by weight of the aluminosilicate powder to the propylene copolymer defined above, and the addition amount is preferably 0.30 to 1.5 parts by weight. If the amount added is less than the lower limit, the film has poor blocking resistance and slippage, which is not preferable. If the amount added exceeds the upper limit, the transparency of the film deteriorates, which is not preferable.
本発明において、比較的低結晶性のプロピレン共重合
体、とりわけ、特定のプロピレン−α−オレフィン共重
合体を含有するプロピレン共重合体については、微細な
アルミノシリケート粉末を従来になく、多量に添加した
樹脂組成物に限り、比較的低温の延伸により透明性が良
好でしかも耐ブロッキング性と滑り性が良好であるフィ
ルムが始めて得られた訳であり、この事実は予想外であ
った。In the present invention, a relatively low crystallinity propylene copolymer, in particular, for a propylene copolymer containing a specific propylene-α-olefin copolymer, fine aluminosilicate powder is not present in the past, and a large amount is added. Only with the resin composition described above, a film having good transparency and good blocking resistance and slipperiness was obtained for the first time by stretching at a relatively low temperature, which was unexpected.
本発明の樹脂組成物には、滑り剤を好適に添加できる。
又、帯電防止剤、防曇剤、安定剤、造核剤などの添加剤
を添加することができる。なお、耐ブロッキング剤とし
ても、少なくとも本発明で規定したものが、規定量含ま
れていればよいのであって、規定外のものを併用して使
用してもよい。A slip agent can be suitably added to the resin composition of the present invention.
Further, additives such as an antistatic agent, an antifogging agent, a stabilizer and a nucleating agent can be added. As the anti-blocking agent, at least the anti-blocking agent specified in the present invention may be contained in the specified amount, and non-specified anti-blocking agents may be used in combination.
本発明の樹脂組成物には、少量の高分子化合物(例えば
石油樹脂などの炭化水素樹脂)を添加することができ
る。又本発明の樹脂組成物を得る方法としては、公知の
任意の方法で、均一分散させて得ることができる。例え
ば、ヘンシェル混合した後、押出溶融ブレンドする方法
や、バンバリーブレンドする方法などである。A small amount of a polymer compound (for example, a hydrocarbon resin such as petroleum resin) can be added to the resin composition of the present invention. The resin composition of the present invention can be obtained by uniformly dispersing it by any known method. For example, a method of extrusion-melt blending after mixing with Henschel, a method of Banbury blending, and the like.
本発明の樹脂組成物は収縮包装用フィルムとして好適に
使用されるが、フィルム成形後、延伸処理されて使用さ
れる。フィルム成形する方法としては、Tダイキャスト
方、水冷インフレ法などの公知の加工法を採用すること
ができる。又、延伸処理を施す方法としては、ロール延
伸やロール圧延、テンター横1軸延伸などの公知の1軸
延伸方法ならびに、テンター2軸延伸やチューブラー2
軸延伸などの公知の2軸延伸方法が採用できる。延伸温
度は常温〜共重合体の融点以下であるが、プロピレン共
重合体のビカット軟化点が低ければ低いだけ、より低温
での延伸が行い易くなる。延伸倍率としては2〜10倍が
好ましい。この場合、MD、TDの延伸倍率については、必
ずしもバランスさせる必要はなく、各々の用途に応じて
任意に選択することができる。又、ヒートセットを行っ
てもよい。The resin composition of the present invention is suitably used as a film for shrink wrapping, but it is used after being stretched after forming the film. As a method for forming a film, a known processing method such as a T-die casting method or a water cooling inflation method can be adopted. As a method for performing the stretching treatment, known uniaxial stretching methods such as roll stretching, roll rolling and tenter transverse uniaxial stretching, as well as tenter biaxial stretching and tubular 2 are used.
A known biaxial stretching method such as axial stretching can be adopted. The stretching temperature is from room temperature to the melting point of the copolymer or lower, but the lower the Vicat softening point of the propylene copolymer, the easier the stretching at a lower temperature. The draw ratio is preferably 2 to 10 times. In this case, the MD and TD stretch ratios do not necessarily have to be balanced, and can be arbitrarily selected according to their respective uses. Moreover, you may heat-set.
なお、実施例及び比較例におけるデータ及び評価は次の
方法に従って行ったものである。The data and evaluations in Examples and Comparative Examples were carried out according to the following methods.
(1)ビカット軟化点 ASTM D 1525に準拠 (2)メルトインデックス(MI) ASTM D 1238に準拠 (3)ヘイズ値(Haze) ASTM D 1003に準拠 (4)滑り(μs…静摩擦係数) ASTM D 1894に準拠 (5)加熱収縮率 5cm角のフィルム試片を所定温度のグリセリン浴に10秒
間浸漬した時のMD、TDの収縮率を測定する。(1) Vicat softening point Compliant with ASTM D 1525 (2) Melt index (MI) Compliant with ASTM D 1238 (3) Haze value (Haze) Compliant with ASTM D 1003 (4) Sliding (μs ... static friction coefficient) ASTM D 1894 (5) Heat shrinkage rate A 5 cm square film sample is immersed in a glycerin bath at a predetermined temperature for 10 seconds, and the MD and TD shrinkage rates are measured.
(6)ブロッキング 2枚のフィルムを重ね合わせ、面積25cm2当たり20Kgの
荷重をかけたまま、23℃で3hr状態調節する。その後2
枚のフィルムをフィルム面に直角方向に、荷重増加速度
10g/minで剥り、その時の最大荷重(g)を求めフィル
ム面積100cm2当たりに換算して表わす。 (6) Blocking Two films are superposed on each other, and the condition is adjusted at 23 ° C. for 3 hours while applying a load of 20 kg per area of 25 cm 2 . Then 2
Load increasing speed for a sheet of film in the direction perpendicular to the film surface
Peeling is performed at 10 g / min, and the maximum load (g) at that time is calculated and expressed in terms of 100 cm 2 of film area.
(7)共重合体中のα−オレフィン含量 赤外分光光度計を用いて測定した。ブテン−1について
は、770cm-1の特性吸収から常法により定量した。な
お、赤外分光光度計による測定は、プロピレン、ブテン
−1、コポリマーについて、13C−NMRによる定量値によ
り検量線を作成し、定量した。(7) α-Olefin content in copolymer Measured using an infrared spectrophotometer. Butene-1 was quantified by a conventional method from the characteristic absorption at 770 cm -1 . In the measurement with the infrared spectrophotometer, propylene, butene-1, and the copolymer were quantified by preparing a calibration curve from the quantitative value by 13 C-NMR.
(8)共重合体中のエチレン含量 赤外分光光度計を用いて、732cm-1、720cm-1の特性吸収
から常法により定量した。なお、赤外分光光度計による
測定は、14Cでラベルしたエチレンコポリマーの放射線
測定による定量値により検量線を作成し定量した。(8) Ethylene content in copolymer Using an infrared spectrophotometer, it was quantified by a conventional method from characteristic absorptions at 732 cm −1 and 720 cm −1 . In the measurement with an infrared spectrophotometer, a calibration curve was prepared and quantified by the quantified value of the 14 C-labeled ethylene copolymer measured by radiation.
(9)冷キシレン可溶部(CXS) ポリマー5gをキシレン500mlに溶解後、室温まで除冷す
る。ついで20℃のバス中に4時間放置した後濾過し、濾
液を濃縮、乾固、乾燥して秤量する。(9) Cold xylene soluble part (CXS) After dissolving 5 g of the polymer in 500 ml of xylene, it is cooled to room temperature. Then, the mixture is left in a bath at 20 ° C. for 4 hours and then filtered, and the filtrate is concentrated, dried, dried and weighed.
以下本発明を実施例により、さらに詳しく説明するが、
本発明はその要旨を超えない限り、実施例に限定される
ものではない。Hereinafter, the present invention will be described in more detail with reference to Examples.
The present invention is not limited to the examples as long as the gist thereof is not exceeded.
<実施例> 実施例1 エチレン−ブテン−1−プロピレンランダムタ−ポリマ
ー(エチレン2.1wt%、ブテン−1含量5.5wt%、ビカッ
ト軟化点123℃、CXS4.3wt%、MI5.9g/10分)に安定剤と
してBHT0.1部、水沢化学製シルトンAMT(無定形アルミ
ノシリケート粉末、平均粒径0.8μ、吸油量62ml/100g)
を0.3部、エルカ酸アミド0.2部添加したものを、ヘンシ
ェルミキサーで混合後、65φ押出機により、溶融ブレン
ドをして樹脂組成物を得た。この樹脂の性質を評価する
為に以下の実験を行った。<Example> Example 1 Ethylene-butene-1-propylene random terpolymer (2.1 wt% ethylene, butene-1 content 5.5 wt%, Vicat softening point 123 ° C, CXS 4.3 wt%, MI 5.9 g / 10 min) As a stabilizer, BHT 0.1 part, Mizusawa Chemical's Shilton AMT (amorphous aluminosilicate powder, average particle size 0.8μ, oil absorption 62ml / 100g)
Of 0.3 parts and 0.2 parts of erucic acid amide were mixed with a Henschel mixer, and melt-blended with a 65φ extruder to obtain a resin composition. The following experiments were conducted to evaluate the properties of this resin.
該樹脂組成物から、プレス法にて、約500μのシートを
得、それから90角のシートを採取して以下の条件で2軸
延伸フィルムを得た。A sheet of about 500μ was obtained from the resin composition by a pressing method, and then a 90-square sheet was collected to obtain a biaxially stretched film under the following conditions.
延伸機:東洋精機製卓上2軸延伸機 温度:110℃ 予熱時間:3分 延伸倍率:MD 5倍、TD 5倍 延伸速度:15m/分 上記で得た約20μ厚さのフィルムの物性を第1表に示し
た。なお、フィルム物性についてはMD、TDの平均値で示
した。Stretching machine: Tabletop biaxial stretching machine manufactured by Toyo Seiki Temperature: 110 ° C Preheating time: 3 minutes Stretching ratio: MD 5 times, TD 5 times Stretching speed: 15 m / min Physical properties of the film with a thickness of about 20μ obtained above The results are shown in Table 1. The physical properties of the film are shown by the average value of MD and TD.
このフィルムは透明性、滑り、耐ブロッキング性が優れ
ており、しかも低温収縮性もそこそこ優れていた。This film was excellent in transparency, slippage and blocking resistance, and was also excellent in low temperature shrinkability.
実施例2 プロピレン−α−オレフィン共重合体(ブテン−1含有
量16.9モル%、CXS20.5wt%、ビカット軟化点100℃、MI
5.5g/10分)に、実施例1で使用したのと同じアルミノ
シリケート粉末を0.4部の添加として他は、実施例1と
同じようにして樹脂組成物を得た。次に実施例1の条件
で延伸温度を90℃とした他は、同一の条件で2軸延伸フ
ィルムを得た。フィルム物性を第1表に示した。このフ
ィルムは、透明性、滑り、耐ブロッキング性が優れてお
り、低温収縮性も優れていた。Example 2 Propylene-α-olefin copolymer (butene-1 content 16.9 mol%, CXS 20.5 wt%, Vicat softening point 100 ° C., MI
A resin composition was obtained in the same manner as in Example 1 except that 0.4 part of the same aluminosilicate powder used in Example 1 was added to 5.5 g / 10 minutes). Next, a biaxially stretched film was obtained under the same conditions except that the stretching temperature was 90 ° C. under the conditions of Example 1. The physical properties of the film are shown in Table 1. This film was excellent in transparency, slippage and blocking resistance, and also excellent in low temperature shrinkability.
実施例3 実施例2と同じプロピレン−α−オレフィン共重合体
に、A型ゼオライト粉末(平均粒径0.8μ、吸油量60ml/
100g)を0.3部添加とした他は、実施例1と同じように
して樹脂組成物を得た。次に実施例1の条件で、延伸温
度を100℃とした他は、同一の条件で、2軸延伸フィル
ムを得た。フィルム物性を第1表に示した。このフィル
ムは実施例2のフィルムと同様優れたものであった。Example 3 The same propylene-α-olefin copolymer as in Example 2 was added to A-type zeolite powder (average particle size 0.8 μ, oil absorption 60 ml /
A resin composition was obtained in the same manner as in Example 1 except that 0.3 part of 100 g) was added. Next, a biaxially stretched film was obtained under the same conditions as in Example 1 except that the stretching temperature was 100 ° C. The physical properties of the film are shown in Table 1. This film was as good as the film of Example 2.
実施例4 実施例2で使ったのと同じプロピレン−α−オレフィン
共重合体70重量%と、エチレンランダム共重合体(エチ
レン含有量4.8wt%、CXS4.1wt%、MI8.4g/10分)30重量
%とからなるプロピレン共重合体(ビカット軟化点103
℃)に実施例1で使用したのと同じアルミノシリケート
粉末を0.4部の添加とした他は、実施例1と同じように
して樹脂組成物を得た。次に実施例1の条件で延伸温度
を90℃とした他は、同一の条件で2軸延伸フィルムを得
た。フィルム物性を第1表に示した。このフィルムは実
施例2のフィルムと同様優れたものであった。Example 4 70% by weight of the same propylene-α-olefin copolymer as used in Example 2 and an ethylene random copolymer (ethylene content 4.8 wt%, CXS 4.1 wt%, MI 8.4 g / 10 min). Propylene copolymer consisting of 30% by weight (Vicat softening point 103
A resin composition was obtained in the same manner as in Example 1 except that 0.4 part of the same aluminosilicate powder as used in Example 1 was added to (° C.). Next, a biaxially stretched film was obtained under the same conditions except that the stretching temperature was 90 ° C. under the conditions of Example 1. The physical properties of the film are shown in Table 1. This film was as good as the film of Example 2.
実施例5 プロピレン−α−オレフィン共重合体(ブテン−1含有
量22.3モル%、CXS27.8wt%、MI3.1g/10分)30重量%
と、エチレンランダム共重合体(エチレン含有量4.8wt
%、CXS4.1wt%、MI8.4g/10分)70重量%とからなるプ
ロピレン共重合体(ビカット軟化点110℃に実施例1で
使用したのと同じアルミノシリケート粉末を0.4部の添
加とした他は、実施例1と同じようにして樹脂組成物を
得た。次に実施例1の条件で延伸温度を100℃とした他
は、同一の条件で2軸延伸フィルムを得た。フィルム物
性を第1表に示した。このフィルムは実施例2のフィル
ムと同様優れたものであった。Example 5 Propylene-α-olefin copolymer (butene-1 content 22.3 mol%, CXS 27.8 wt%, MI 3.1 g / 10 min) 30 wt%
And ethylene random copolymer (ethylene content 4.8wt
%, CXS 4.1 wt%, MI 8.4 g / 10 min) 70 wt% propylene copolymer (Vicat softening point 110 ° C. 0.4 part addition of the same aluminosilicate powder used in Example 1) Aside from the above, a resin composition was obtained in the same manner as in Example 1. Next, a biaxially stretched film was obtained under the same conditions as in Example 1, except that the stretching temperature was 100 ° C. The results are shown in Table 1. This film was as excellent as the film of Example 2.
実施例6 プロピレンα−オレフィン共重合体(ブテン−1含有量
11.7モル%、エチレン含有量1.6モル%、CXS21.0wt%、
ビカット軟化点101℃、MI2.5g/10分)に実施例1で使用
したのと同じアルミノシリケート粉末を0.4部の添加と
した他は、実施例1と同じようにして樹脂組成物を得
た。次に実施例1の条件で延伸温度を90℃とした他は、
同一の条件で2軸延伸フィルムを得た。フィルム物性を
第1表に示した。このフィルムは、実施例2のフィルム
と同様優れたものであった。Example 6 Propylene α-olefin copolymer (butene-1 content
11.7 mol%, ethylene content 1.6 mol%, CXS21.0 wt%,
A resin composition was obtained in the same manner as in Example 1 except that 0.4 part of the same aluminosilicate powder used in Example 1 was added to the Vicat softening point of 101 ° C., MI 2.5 g / 10 minutes). . Next, except that the stretching temperature was 90 ° C. under the conditions of Example 1,
A biaxially stretched film was obtained under the same conditions. The physical properties of the film are shown in Table 1. This film was as good as the film of Example 2.
比較例1 実施例2で使用したのと同じプロピレン−α−オレフィ
ン共重合体に、水沢化学製シルトンAMT(無定形アルミ
ノシリケート 平均粒径1.9μ、吸油量64ml/100g)を0.
2部の添加とした他は、実施例1と同じようにして樹脂
組成物を得た。次に実施例1の条件で延伸温度を90℃と
した他は、同一の条件で2軸延伸フィルムを得た。フィ
ルム物性を第1表に示した。このフィルムは、透明性、
滑り、耐ブロッキングが悪いものであった。Comparative Example 1 The same propylene-α-olefin copolymer as that used in Example 2 was supplemented with Mizusawa Chemical Co., Ltd. Shilton AMT (amorphous aluminosilicate average particle size 1.9 μ, oil absorption 64 ml / 100 g).
A resin composition was obtained in the same manner as in Example 1 except that 2 parts were added. Next, a biaxially stretched film was obtained under the same conditions except that the stretching temperature was 90 ° C. under the conditions of Example 1. The physical properties of the film are shown in Table 1. This film is transparent,
The slip resistance and blocking resistance were poor.
比較例2 実施例2で使用したのと同じプロピレン−α−オレフィ
ン共重合体に、水沢化学製ミズカシルp−527(シリカ
粉末 平均粒径1.5μ)を0.2部の添加とした他は、実施
例1と同じようにして樹脂組成物を得た。次に実施例1
の条件で延伸温度を90℃とした他は、同一の条件で2軸
延伸フィルムを得た。フィルム物性を第1表に示した。
このフィルムは、透明性が幾分悪く、滑りと耐ブロッキ
ング性の悪いものであった。Comparative Example 2 The same propylene-α-olefin copolymer as that used in Example 2 was added with 0.2 part of Mizusukasil p-527 (silica powder average particle size: 1.5 μm) manufactured by Mizusawa Chemical Co., Ltd. A resin composition was obtained in the same manner as in 1. Next, Example 1
A biaxially stretched film was obtained under the same conditions except that the stretching temperature was 90 ° C. under the above conditions. The physical properties of the film are shown in Table 1.
The film had somewhat poor transparency and poor sliding and blocking resistance.
比較例3 実施例2で使用したのと同じプロピレン−α−オレフィ
ン共重合体に、実施例1で使用したのと同じアルミノシ
リケート粉末を0.2部の添加とした他は、実施例1と同
じようにして樹脂組成物を得た。次に実施例1の条件で
延伸温度を90℃とした他は、同一の条件で2軸延伸フィ
ルムを得た。フィルム物性を第1表に示した。このフィ
ルムは、透明性は優れているが、滑りと、耐ブロッキン
グ性の悪いものであった。Comparative Example 3 Same as Example 1 except that 0.2 part of the same aluminosilicate powder used in Example 1 was added to the same propylene-α-olefin copolymer used in Example 2. To obtain a resin composition. Next, a biaxially stretched film was obtained under the same conditions except that the stretching temperature was 90 ° C. under the conditions of Example 1. The physical properties of the film are shown in Table 1. This film was excellent in transparency but poor in slip resistance and blocking resistance.
比較例4 実施例2で使用したのと同じプロピレン−α−オレフィ
ン共重合体に、富士デヴィソン製サイロイド−150(シ
リカ粉末平均粒径2.5μm)を0.2部の添加とした他は、
実施例1と同じようにして樹脂組成物を得た。次に、実
施例1の条件で延伸温度を90℃とした他は、同一の条件
で2軸延伸フィルムを得た。フィルム物性を第1表に示
した。このフィルムは、比較例1と同様悪い特性もので
あった。Comparative Example 4 Aside from the same propylene-α-olefin copolymer used in Example 2, 0.2 parts of Fuji DeVison Syroid-150 (silica powder average particle size 2.5 μm) was added,
A resin composition was obtained in the same manner as in Example 1. Next, a biaxially stretched film was obtained under the same conditions except that the stretching temperature was 90 ° C. under the conditions of Example 1. The physical properties of the film are shown in Table 1. This film had the same bad characteristics as in Comparative Example 1.
比較例5 実施例2で使用したのと同じプロピレン−α−オレフィ
ン共重合体に、A型ゼオライト粉末(平均粒径2.2μ、
吸油量50ml/100g)を0.2部添加とした他は、実施例1と
同じようにして樹脂組成物を得た。次に実施例1の条件
で延伸温度を90℃とした他は、同一の条件で2軸延伸フ
ィルムを得た。フィルム物性を第1表に示した。このフ
ィルムは比較例1と同様悪い特性のものであった。Comparative Example 5 The same propylene-α-olefin copolymer used in Example 2 was added to A-type zeolite powder (average particle size 2.2 μ,
A resin composition was obtained in the same manner as in Example 1 except that 0.2 part of oil absorption 50 ml / 100 g) was added. Next, a biaxially stretched film was obtained under the same conditions except that the stretching temperature was 90 ° C. under the conditions of Example 1. The physical properties of the film are shown in Table 1. This film had the same bad characteristics as in Comparative Example 1.
比較例6 プロピレン−ランダム共重合体(エチレン含有量2.1wt
%、CXS3.1wt%、ビカット軟化点139℃、MI8.6g/10分)
に比較例1で使用したのと同じアルミノシリケート粉末
を0.2部添加とした他は、実施例1と同じようにして樹
脂組成物を得た。次に実施例1の条件で、延伸温度を15
0℃とした他は、同一の条件で2軸延伸フィルムを得
た。フィルム物性を第1表に示した。このフィルムは、
透明性、耐ブロッキング性が良好で滑りも幾分悪い程度
のものであったが、低温収縮性が全くなく本発明の主旨
に沿わないものであった。Comparative Example 6 Propylene-random copolymer (ethylene content 2.1 wt
%, CXS3.1wt%, Vicat softening point 139 ° C, MI8.6g / 10 minutes)
A resin composition was obtained in the same manner as in Example 1 except that 0.2 part of the same aluminosilicate powder as used in Comparative Example 1 was added. Next, under the conditions of Example 1, the stretching temperature was set to 15
A biaxially stretched film was obtained under the same conditions except that the temperature was 0 ° C. The physical properties of the film are shown in Table 1. This film is
The transparency and blocking resistance were good, and the slippage was somewhat bad, but there was no low-temperature shrinkage at all, which was beyond the scope of the present invention.
<発明の効果> 以上詳述した通り、本発明の樹脂組成物は、例えば低温
収縮性が良好で、しかも透明性、滑り性、及び耐ブロッ
キング性とが優れた収縮包装用フィルムを作製するのに
大変優れたものである。<Effects of the Invention> As described in detail above, the resin composition of the present invention produces a shrink-wrapping film having, for example, good low-temperature shrinkability and excellent transparency, slipperiness, and blocking resistance. It is a very good one.
フロントページの続き (56)参考文献 特開 昭60−118727(JP,A) 特開 昭56−4642(JP,A) 特開 昭61−9448(JP,A)Continuation of front page (56) References JP-A-60-118727 (JP, A) JP-A-56-4642 (JP, A) JP-A-61-9448 (JP, A)
Claims (1)
共重合体に平均粒径が1μ以下のアルミノシリケート粉
末を0.25〜2.0重量部添加したことを特徴とする収縮フ
ィルム用樹脂組成物。1. A resin composition for a shrinkable film, comprising 0.25 to 2.0 parts by weight of an aluminosilicate powder having an average particle size of 1 μm or less added to a propylene copolymer having a Vicat softening point of 130 ° C. or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61278480A JPH0739517B2 (en) | 1986-11-20 | 1986-11-20 | Resin composition for shrink film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61278480A JPH0739517B2 (en) | 1986-11-20 | 1986-11-20 | Resin composition for shrink film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63130650A JPS63130650A (en) | 1988-06-02 |
| JPH0739517B2 true JPH0739517B2 (en) | 1995-05-01 |
Family
ID=17597918
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61278480A Expired - Fee Related JPH0739517B2 (en) | 1986-11-20 | 1986-11-20 | Resin composition for shrink film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0739517B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0759655B2 (en) * | 1987-10-16 | 1995-06-28 | 住友化学工業株式会社 | Film for shrink wrapping |
| JP2560546B2 (en) * | 1990-12-21 | 1996-12-04 | 住友化学工業株式会社 | Polyolefin resin composition for film |
| JP2560547B2 (en) * | 1990-12-21 | 1996-12-04 | 住友化学工業株式会社 | Stabilized polyolefin resin composition for film molding |
| US5798172A (en) * | 1994-12-07 | 1998-08-25 | Idemitsu Petrochemical Co., Ltd. | Styrenic resin composition and polystyrene oriented film |
| CN104479217A (en) * | 2014-11-20 | 2015-04-01 | 苏州新区佳合塑胶有限公司 | Fridge drawer material |
| CN112745586B (en) * | 2020-12-25 | 2023-03-07 | 泉州市创绿机械工贸有限公司 | High-strength polypropylene composite material pressure filter plate and preparation method thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS564642A (en) * | 1979-06-26 | 1981-01-19 | Mitsubishi Petrochem Co Ltd | Propylene polymer film |
| JPS60118727A (en) * | 1983-12-01 | 1985-06-26 | Toyo Soda Mfg Co Ltd | Soft polypropylene composition for film |
-
1986
- 1986-11-20 JP JP61278480A patent/JPH0739517B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63130650A (en) | 1988-06-02 |
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