JP2000313753A - Polypropylene-based sheet - Google Patents

Polypropylene-based sheet

Info

Publication number
JP2000313753A
JP2000313753A JP11123567A JP12356799A JP2000313753A JP 2000313753 A JP2000313753 A JP 2000313753A JP 11123567 A JP11123567 A JP 11123567A JP 12356799 A JP12356799 A JP 12356799A JP 2000313753 A JP2000313753 A JP 2000313753A
Authority
JP
Japan
Prior art keywords
polypropylene
sheet
melting point
noncrystalline
resin
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
Application number
JP11123567A
Other languages
Japanese (ja)
Inventor
Sadafumi Furukawa
禎史 古川
Masaru Terao
賢 寺尾
Shinji Oono
晋児 大野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sumitomo Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP11123567A priority Critical patent/JP2000313753A/en
Publication of JP2000313753A publication Critical patent/JP2000313753A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a polypropylene-based sheet having a thermoformable wide temperature range and remarkably improved in curl by heat sealing with an aluminum foil. SOLUTION: This sheet is obtained by dispersing a noncrystalline resin, e.g. a noncrystalline polyolefin, a noncrystalline polymethyl methacrylate, a noncrystalline polycarbonate or a noncrystalline polystyrene in the form of a layer in a composition comprising two or more kinds of polypropylenes having 3-40 deg.C difference in melting point measured with a differential scanning calorimeter and a petroleum resin.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、押出成形などの一
般のシーティング方法で成形可能なポリプロピレン系シ
ートに関する。詳しくは、防湿性が要求されるPTPと
称する医薬品(固形剤)包装用ポリプロピレン系シートに
関する。
The present invention relates to a polypropylene sheet which can be formed by a general sheeting method such as extrusion. More specifically, the present invention relates to a polypropylene-based sheet for packaging a drug (solid agent) called PTP, which is required to have moisture-proof properties.

【0002】[0002]

【従来の技術】医薬品包装において、より高い防湿性を
得るためポリプロピレン系シートが使用されつつある。
しかしながら、ポリプロピレンは熱成形性が極めて悪い
という工業上大きな問題がある。すなわち、ポリプロピ
レンは熱成形における予熱の際、熱によるドローダウン
が大きく、良好な成形品を得ることのできる最適な成形
温度幅が2〜3℃程度であり非常に狭い。このため、ポ
リプロピレンの熱成形にあたっては、非常に高度な温度
制御が必要であり、従来の汎用成形機では成形不良率が
高く工程管理は極めて困難である。また、ポリプロピレ
ンはアルミ箔とヒートシールを行うと、シートのカール
が極めて大きくなるという工業上大きな問題がある。す
なわち、ポリプロピレンは線膨張率が大きい為、アルミ
箔をヒートシールした後の収縮が大きく、その為製品が
アルミ箔と反対側にカールして商品価値を損ねたり、自
動包装ライン上での集積不能等のトラブルが発生すると
いうような問題があった。
2. Description of the Related Art In pharmaceutical packaging, polypropylene-based sheets are being used in order to obtain higher moisture resistance.
However, polypropylene has a serious industrial problem that the thermoformability is extremely poor. That is, polypropylene has a large drawdown due to heat at the time of preheating in thermoforming, and the optimum molding temperature width at which a good molded product can be obtained is about 2 to 3 ° C., which is very narrow. For this reason, in thermoforming polypropylene, very high temperature control is required, and the conventional general-purpose molding machine has a high molding defect rate and is extremely difficult to control the process. Further, polypropylene has a major industrial problem that when heat sealing is performed with an aluminum foil, the curl of the sheet becomes extremely large. In other words, since polypropylene has a large coefficient of linear expansion, the shrinkage after heat-sealing the aluminum foil is large, which causes the product to curl on the opposite side to the aluminum foil, impairing its commercial value, and making it impossible to integrate on an automatic packaging line. There is a problem that such troubles occur.

【0003】熱成形性の良好なポリプロピレンについて
の検討はこれまで種々なされており、例えば、ポリプロ
ピレンに比較的成形性の良好なポリエチレンやエチレン
−プロピレン共重合体、無機フィラーあるいは低分子量
の石油樹脂をブレンドして改質することについて提案さ
れている。例えば、溶融時に高粘度のポリプロピレン
に、高粘度のポリエチレン(低密度ポリエチレン)及び含
水ケイ酸マグネシウム粉末を添加する方法(特公昭56
−15744号公報)、ポリプロピレンに、ポリエチレ
ン(高密度ポリエチレン)及びエチレン−プロピレン共重
合体を添加する方法(特公昭63−29704号公報)、
ポリプロピレンと分子量分布の狭いポリエチレンを使用
し、成形加工性・耐振動疲労性を改良する方法(特公昭
63−53213号公報)、ポリプロピレンに石油樹脂
及びエチレン−α−オレフィン共重合体を添加する方法
(特公平6−89191号公報)などが知られている。
Various studies have been made on polypropylene having good thermoformability. For example, polypropylene having relatively good moldability, such as polyethylene, ethylene-propylene copolymer, inorganic filler or petroleum resin having a low molecular weight, has been studied. It has been proposed to blend and modify. For example, a method of adding high-viscosity polyethylene (low-density polyethylene) and hydrous magnesium silicate powder to high-viscosity polypropylene during melting (Japanese Patent Publication No.
No. 15744), a method of adding polyethylene (high-density polyethylene) and an ethylene-propylene copolymer to polypropylene (JP-B-63-29704),
A method using polypropylene and polyethylene having a narrow molecular weight distribution to improve moldability and vibration fatigue resistance (Japanese Patent Publication No. 53213/1988), a method of adding a petroleum resin and an ethylene-α-olefin copolymer to polypropylene
(Japanese Patent Publication No. 6-89191).

【0004】しかしながら、これらは各々特定の温度条
件におけるシート軟化緊張保持時間、溶融体強度、絞り
加工性、ドローダウン等の成形加工性の改善に対しては
効果が認められるものの成形性改良の実質的な指標であ
る成形可能温度幅の拡大についてはほとんど効果がな
く、現実的な成形性の改善について未だ満足できるポリ
プロピレン系シートは得られていなかった。また、カー
ルを改良する為の検討がポリプロピレン多層シートにお
いて行われている。例えば、石油樹脂の添加によりカー
ルを改良する方法(特公平3−4029号公報)等であ
る。しかし、ある程度のカール改良効果は見受けられる
ものの十分とはいえなかった。
However, these are effective in improving the formability such as sheet softening tension holding time, melt strength, drawability, drawdown, etc. under specific temperature conditions. There is almost no effect on the expansion of the moldable temperature range, which is a typical index, and a polypropylene-based sheet that is satisfactory with respect to a practical improvement in moldability has not yet been obtained. Also, studies to improve curl have been made in polypropylene multilayer sheets. For example, there is a method of improving curl by adding a petroleum resin (Japanese Patent Publication No. 3-4029). However, although some curl improvement effects were observed, they were not sufficient.

【0005】[0005]

【発明が解決しようとする課題】本発明は、熱成形可能
な温度幅が広く、しかもアルミ箔とのヒートシールによ
るカールが著しく改良されたポリプロピレン系シートを
提供することを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a polypropylene sheet having a wide temperature range in which thermoforming can be performed and in which curling due to heat sealing with an aluminum foil is remarkably improved.

【0006】[0006]

【課題を解決するための手段】本発明者らは、上記問題
について研究を行った結果、特定の組合せのポリプロピ
レンと石油樹脂に、非結晶性樹脂を層状に分散してなる
ポリプロピレン系シートが、熱成形可能な温度幅が広く
かつアルミ箔とのヒートシールによるカールが著しく改
良されることを見いだし本発明を完成させるに至った。
すなわち本発明は、示差走査熱量計によって測定された
融点の差が3〜40℃である2種以上のポリプロピレン
及び石油樹脂からなる組成物に、非結晶性樹脂を層状に
分散してなるポリプロピレン系シートである。
Means for Solving the Problems The present inventors have conducted research on the above problems, and as a result, have found that a polypropylene-based sheet obtained by dispersing an amorphous resin in a layered manner in a specific combination of polypropylene and petroleum resin has been developed. The present inventors have found that the temperature range in which thermoforming can be performed is wide and the curl due to heat sealing with aluminum foil is remarkably improved, and the present invention has been completed.
That is, the present invention relates to a polypropylene-based composition obtained by dispersing a non-crystalline resin in a layered form in a composition comprising two or more types of polypropylene and a petroleum resin whose difference in melting point measured by a differential scanning calorimeter is 3 to 40 ° C. It is a sheet.

【0007】[0007]

【発明の実施の形態】本発明に用いられるポリプロピレ
ンの種類としてはプロピレンを単独重合したホモポリマ
ー、プロピレンとエチレンやα−オレフィンとのブロッ
クコポリマー、ランダムコポリマーなどがあげられる。
本発明における2種以上のポリプロピレンは示差走査熱
量計によって測定された融点(JIS−K−7121)
の差は3〜40℃、さらに好ましくは5〜35℃であ
る。ここに示す融点差とは、2種類以上のポリプロピレ
ンのうち最も融点が高いものと、最も融点が低いものの
差である。ポリプロピレンの融点差が3℃より小さい場
合、得られたシートの真空、圧空成形性が悪くなり好ま
しくない。ポリプロピレンの融点差が40℃より大きい
場合、シートの外観が悪くなる。
BEST MODE FOR CARRYING OUT THE INVENTION The types of polypropylene used in the present invention include homopolymers obtained by homopolymerizing propylene, block copolymers of propylene and ethylene or α-olefin, and random copolymers.
Two or more kinds of polypropylenes in the present invention have melting points (JIS-K-7121) measured by a differential scanning calorimeter.
Is 3 to 40C, more preferably 5 to 35C. The melting point difference shown here is the difference between the highest melting point and the lowest melting point of the two or more types of polypropylene. If the difference in melting point of the polypropylene is less than 3 ° C., the vacuum and pressure forming properties of the obtained sheet deteriorate, which is not preferable. If the difference in melting point of polypropylene is greater than 40 ° C., the appearance of the sheet will be poor.

【0008】シートの耐熱性が要求される分野では、組
み合わせるポリプロピレンにおいて最も融点が高いポリ
プロピレンの融点は150℃以上であるのが好ましく、
155℃以上であるのがさらに好ましい。最も融点が高
いポリプロピレンの融点が150℃より小さいとシート
の耐熱性が悪くなる。また、組み合わせるポリプロピレ
ンにおいて最も融点が高いポリプロピレンの含量は95
〜50重量%であるのが好ましく、85〜60重量%で
あるのがさらに好ましい。最も融点が高いポリプロピレ
ンの含量が95重量%より大きいと、真空、圧空成形性
が悪くなり、50重量%より小さいとシートの耐熱性が
悪くなる。組み合わせるポリプロピレンの種類に特に制
限はないが、シートに水蒸気バリア性が要求される場
合、ホモポリマーとランダムコポリマーまたはブロック
コポリマーの組み合わせが好ましく、より好ましくはホ
モポリマー同士の組み合わせである。
In the field where the heat resistance of the sheet is required, the melting point of the highest melting point of the polypropylene to be combined is preferably 150 ° C. or higher,
More preferably, it is 155 ° C. or higher. If the melting point of the polypropylene having the highest melting point is lower than 150 ° C., the heat resistance of the sheet deteriorates. The content of the polypropylene having the highest melting point in the combined polypropylene is 95%.
It is preferably from 50 to 50% by weight, more preferably from 85 to 60% by weight. If the content of the polypropylene having the highest melting point is more than 95% by weight, vacuum and pressure forming properties will be poor, and if it is less than 50% by weight, the heat resistance of the sheet will be poor. The type of polypropylene to be combined is not particularly limited, but when a sheet is required to have a water vapor barrier property, a combination of a homopolymer and a random copolymer or a block copolymer is preferable, and a combination of homopolymers is more preferable.

【0009】また、カレンダー法により本発明のポリプ
ロピレン系シートを作成する場合、使用するポリプロピ
レンは、分子量1万以下の低分子量成分が全体の5重量
%以下であるのが好まく、さらに好ましくは3重量%以
下、最も好ましくは1重量%以下である。分子量1万以
下の低分子量成分が5重量%より多いと、カレンダー加
工時に熱ロールへの粘着が起こり、得られるシートの平
滑性、外観が悪くなる。低分子量成分の割合はゲルパー
ミエーションクロマトグラフィーによって測定した微分
分子量分布曲線から求めることができる。
When the polypropylene sheet of the present invention is prepared by the calendering method, it is preferable that the polypropylene used has a low molecular weight component having a molecular weight of 10,000 or less at 5% by weight or less, more preferably 3% by weight or less. Wt% or less, most preferably 1 wt% or less. If the low molecular weight component having a molecular weight of 10,000 or less is more than 5% by weight, sticking to a hot roll occurs at the time of calendering, resulting in poor smoothness and appearance of the obtained sheet. The ratio of the low molecular weight component can be determined from a differential molecular weight distribution curve measured by gel permeation chromatography.

【0010】本発明に用いられる石油樹脂は、シクロペ
ンタジエン留分を熱重合したジシクロペンタジエン系樹
脂、C9芳香族オレフィン類混合物をカチオン重合した
芳香族系(C9系)石油樹脂、C5の鎖状オレフィン類混
合物をカチオン重合した脂肪族系(C5系)石油樹脂、
およびこれらから選ばれる少なくとも2成分の共重合体
又はブレンド物、さらにこれらを水素添加した石油樹
脂、および水素添加した石油樹脂の中から選ばれる少な
くとも2成分のブレンド物等が挙げられ、中でも色調、
臭気、安定性が優れた水素添加石油樹脂が好ましく、さ
らに高い防湿性が要求される包装品では、ジシクロペン
タジエン系水素添加石油樹脂が好ましい。
The petroleum resin used in the present invention is a dicyclopentadiene resin obtained by thermally polymerizing a cyclopentadiene fraction, an aromatic (C9) petroleum resin obtained by cationic polymerization of a C9 aromatic olefin mixture, and a C5 chain. Aliphatic (C5) petroleum resin obtained by cationic polymerization of olefin mixture,
And copolymers or blends of at least two components selected therefrom, furthermore, hydrogenated petroleum resins, and blends of at least two components selected from hydrogenated petroleum resins.
A hydrogenated petroleum resin having excellent odor and stability is preferable, and a dicyclopentadiene-based hydrogenated petroleum resin is preferable for a package requiring higher moisture resistance.

【0011】石油樹脂の軟化点については、50〜16
0℃のものが好ましく、更に好ましくは、100〜16
0℃のものである。ポリプロピレンに石油樹脂を添加す
ると、常温付近の弾性率が向上し、アルミシールにおけ
るカールが小さくなる。石油樹脂の軟化点が50℃未満
であれば常温付近での弾性率向上が小さくなるのでカー
ル低減の効果が少なくなり、160℃を越えると熱成形
性が悪くなる。石油樹脂の分子量は、3000以下のも
のが好ましく、更に好ましくは1000以下のものであ
る。石油樹脂の分子量が3000を超えると成形性が悪
くなるという問題がある。石油樹脂の添加量は、ポリプ
ロピレン100重量部に対して、1〜30重量部であ
り、好ましくは3〜20重量部であり、さらに好ましく
は5〜15重量部である。石油樹脂の添加量が1重量部
未満では常温付近での弾性率向上が小さくなるのでカー
ル低減の効果が少なくなり、また30重量部を超えると
耐衝撃性が悪くなり好ましくない。
The softening point of petroleum resin is 50 to 16
0 ° C. is preferable, and more preferably 100 to 16 ° C.
It is at 0 ° C. When petroleum resin is added to polypropylene, the elastic modulus near normal temperature is improved, and the curl in the aluminum seal is reduced. If the softening point of the petroleum resin is less than 50 ° C., the effect of curl reduction is reduced because the improvement in the elastic modulus near normal temperature is reduced, and if it exceeds 160 ° C., the thermoformability deteriorates. The molecular weight of the petroleum resin is preferably 3000 or less, more preferably 1000 or less. If the molecular weight of the petroleum resin exceeds 3,000, there is a problem that moldability deteriorates. The addition amount of the petroleum resin is 1 to 30 parts by weight, preferably 3 to 20 parts by weight, and more preferably 5 to 15 parts by weight based on 100 parts by weight of the polypropylene. If the addition amount of the petroleum resin is less than 1 part by weight, the effect of curl reduction is reduced because the improvement in the elastic modulus near normal temperature is reduced, and if it exceeds 30 parts by weight, the impact resistance is deteriorated, which is not preferable.

【0012】本発明に用いられる非結晶性樹脂として
は、例えば非結晶性ポリオレフィン、ポリメチルメタク
リレート、ポリカーボネート、ポリスチレン等である。
これらの中でも、ガラス転移温度が80℃以上の非結晶
性樹脂が、アルミ箔をヒートシールした後の収縮が小さ
くなり、カールは低減する効果が高く好ましい。ここで
いう非結晶性樹脂を層状に分散するとは、ポリプロピレ
ン中に非結晶性樹脂がシートの流動方向(MD)に板状
に分散したものである。
The non-crystalline resin used in the present invention is, for example, non-crystalline polyolefin, polymethyl methacrylate, polycarbonate, polystyrene and the like.
Among these, an amorphous resin having a glass transition temperature of 80 ° C. or higher is preferable because the shrinkage after heat-sealing the aluminum foil is reduced and the curl is reduced. The expression "dispersing the non-crystalline resin in a layered form" as used herein means that the non-crystalline resin is dispersed in the polypropylene in the form of a plate in the flow direction (MD) of the sheet.

【0013】層状に分散した非結晶性樹脂は平均アスペ
クト比2〜30、かつ長さ0.1〜30μmが好まし
い。さらに、好ましくは、平均アスペクト比3〜10、
かつ長さ0.5〜10μmである。層状に分散した非結
晶性樹脂の平均アスペクト比が2を下回るとアルミ箔と
のヒートシール時の収縮改良が十分ではなく、カールの
低減効果が不十分であり、30を上回ると配向の影響が
大きく、機械特性等の異方性が顕著となる。また、層状
に分散した非結晶性樹脂の長さが、0.1μmを下回る
とアルミ箔とのヒートシール時の収縮改良が十分ではな
く、カールの低減効果が不十分であり、30μmを上回
ると透明性等の他の特性が顕著に低下する。非結晶性樹
脂の添加量としては、当該ポリプロピレン100重量部
に対して、5重量部から45重量部が好ましい。非結晶
性樹脂の添加量が5重量部を下回るとアルミ箔とのヒー
トシール時の収縮改良効果が小さく、45重量部を上回
るとシートが白化、成形温度幅が低下するなどの問題が
生じる。
The amorphous resin dispersed in a layered form preferably has an average aspect ratio of 2 to 30 and a length of 0.1 to 30 μm. Furthermore, preferably, the average aspect ratio is 3 to 10,
And the length is 0.5 to 10 μm. If the average aspect ratio of the non-crystalline resin dispersed in a layer is less than 2, the shrinkage improvement at the time of heat sealing with aluminum foil is not sufficient, and the curling reduction effect is insufficient. It is large, and the anisotropy such as mechanical properties becomes remarkable. Further, if the length of the amorphous resin dispersed in a layer is less than 0.1 μm, the shrinkage improvement at the time of heat sealing with the aluminum foil is not sufficient, and the curling reduction effect is insufficient, and if it exceeds 30 μm. Other properties, such as transparency, are significantly reduced. The amount of the non-crystalline resin to be added is preferably from 5 to 45 parts by weight based on 100 parts by weight of the polypropylene. If the amount of the non-crystalline resin is less than 5 parts by weight, the effect of improving shrinkage during heat sealing with the aluminum foil is small, and if it exceeds 45 parts by weight, problems such as whitening of the sheet and reduction in the molding temperature range arise.

【0014】更に、本発明の示差走査熱量計によって測
定された融点(JIS−K−7121)の差が3〜40
℃である2種以上のポリプロピレンと非結晶性樹脂は、
JIS K 7199に従ってキャピラリーレオメータに
より230℃、剪断速度121.6sec-1において測定し
たポリプロピレンの溶融粘度(ρPP)及び非結晶性樹脂の
溶融粘度(ρam)の粘度比(ρam/ρPP)が0.01〜1.0
であるものが好ましく、更に好ましくは0.05〜1.
0である。溶融粘度比が0.01を下回るとアルミ箔と
のヒートシール時の収縮改良効果が小さく、1.0を上
回ると非結晶性樹脂をポリプロピレン中に層状に分散さ
せるのが困難となる。示差走査熱量計によって測定され
た融点(JIS−K−7121)の差が3〜40℃であ
る2種以上のポリプロピレンに非結晶性樹脂を層状に分
散させる方法は、シート作製後に一軸方向に延伸する方
法、あるいは2軸混練機を用いてせん断速度100sec
-1以上で混練した後、シート化する方法により得られ
る。また、上記の粘度比を有するポリプロピレンと非結
晶性樹脂の場合、直接T−ダイ法等を用いた公知の成形
法でシート化しても良い。
Further, the difference in melting point (JIS-K-7121) measured by the differential scanning calorimeter of the present invention is 3 to 40.
The two or more types of polypropylene and amorphous resin at
The viscosity ratio (ρam / ρPP) of the melt viscosity (ρPP) of polypropylene and the melt viscosity (ρam) of the non-crystalline resin measured at 230 ° C. and a shear rate of 121.6 sec −1 using a capillary rheometer according to JIS K 7199 is 0.01. ~ 1.0
Is more preferable, and more preferably 0.05-1.
0. If the melt viscosity ratio is less than 0.01, the effect of improving shrinkage during heat sealing with the aluminum foil is small, and if it exceeds 1.0, it becomes difficult to disperse the amorphous resin in polypropylene in a layered manner. A method of dispersing an amorphous resin in a layered manner in two or more types of polypropylene having a difference in melting point (JIS-K-7121) of 3 to 40 ° C. measured by a differential scanning calorimeter is to stretch uniaxially after sheet production. Method, or using a twin-screw kneader to shear at a rate of 100 sec.
After kneading at -1 or more, it is obtained by a method of forming a sheet. Further, in the case of the polypropylene and the non-crystalline resin having the above-mentioned viscosity ratio, the sheet may be formed by a known molding method using a direct T-die method or the like.

【0015】[0015]

【実施例】以下、実施例により、本発明を詳細に説明す
る。実施例、比較例は下記に示す方法で評価を行った。 (融点の測定)JIS−K−7121に従い、示差走査
型熱量計で融点を測定した。 (真空、圧空成形性)圧空方式成形機[FBP−M2;
シーケーディ(株)製]を用いて一定圧力(5kgf/cm2
で、熱板温度を120〜160℃の間において1℃単位
で上昇させ、得られたシートの成形性を評価した。成形
型は直径10mm、高さ4.5mm、R1.5とした。
得られた成形品の全体厚みが均一である温度を成形可能
温度とし、その温度幅を求めた。 (カールの評価)圧空方式成形機[FBP−M2;シー
ケーディ(株)製]を用いて、良好な成形性を示す条件
で成形し、内容物を充填せずにアルミ箔と熱ロール20
0℃でヒートシールし、130℃でスリッターを入れた
後、幅;37mm、長さ;94mm、コーナーR;5m
mに打ち抜いた成形品をフラットな面に置き、打ち抜き
10分後の成形品のカールを測定した。10個の成形品
について、各成形品の四隅を測定し平均値で評価を行っ
た。カールの大きさが4mm未満のものを○、カールが
4mm以上のものを×とした。
The present invention will be described below in detail with reference to examples. Examples and comparative examples were evaluated by the following methods. (Measurement of Melting Point) The melting point was measured with a differential scanning calorimeter according to JIS-K-7121. (Vacuum, compressed air molding) Compressed air molding machine [FBP-M2;
Constant pressure (5kgf / cm 2 )
Then, the hot plate temperature was increased in 1 ° C. units between 120 and 160 ° C., and the formability of the obtained sheet was evaluated. The mold was 10 mm in diameter, 4.5 mm in height, and R1.5.
The temperature at which the entire thickness of the obtained molded article was uniform was defined as the moldable temperature, and the temperature range was determined. (Evaluation of curl) Using a pneumatic molding machine [FBP-M2; manufactured by CK Ltd.], molding was performed under conditions showing good moldability, and aluminum foil and heat roll 20 were filled without filling the contents.
After heat sealing at 0 ° C and inserting a slitter at 130 ° C, width: 37 mm, length: 94 mm, corner R: 5 m
The molded product punched to m was placed on a flat surface, and the curl of the molded product 10 minutes after punching was measured. Four corners of each molded product were measured for 10 molded products, and evaluated by an average value. When the size of the curl was less than 4 mm, the result was ○.

【0016】実施例及び比較例において用いた各成分を
以下に示す。 (ポリプロピレン) PP−A(ホモPP);日本ポリケム(株)製 EA7
A(融点:164℃) PP−B(ホモPP);日本ポリオレフィン(株)製
PC410A(融点:158℃) PP−C(ランダムPP);日本ポリオレフィン(株)
製 PB322M(融点:149℃) (非結晶性樹脂) COC(非晶性ポリオレフィン);三井化学(株)製
APL6509 PMMA(ポリメチルメタクリレート);住友化学工業
(株)製 スミペックスLG21 (石油樹脂) PR;トーネックス(株)製 エスコレッツ5320
(ジシクロペンタジエン系水添石油樹脂、軟化点125
℃、分子量420)
The components used in the examples and comparative examples are shown below. (Polypropylene) PP-A (Homo PP); EA7 manufactured by Nippon Polychem Co., Ltd.
A (melting point: 164 ° C) PP-B (homo PP); manufactured by Japan Polyolefin Co., Ltd.
PC410A (melting point: 158 ° C) PP-C (random PP); Japan Polyolefin Co., Ltd.
PB322M (melting point: 149 ° C) (non-crystalline resin) COC (non-crystalline polyolefin); manufactured by Mitsui Chemicals, Inc.
APL6509 PMMA (polymethyl methacrylate); SUMIPEX LG21 (petroleum resin) manufactured by Sumitomo Chemical Co., Ltd. PR; ESCOLETTS 5320 manufactured by Tonex Corporation
(Dicyclopentadiene-based hydrogenated petroleum resin, softening point 125
° C, molecular weight 420)

【0017】実施例、比較例について、以下の方法でシ
ートを作製した。示差走査熱量計によって測定された融
点の差が3〜40℃である2種以上のポリプロピレン、
石油樹脂及び非結晶性樹脂とをシリンダー温度230℃
に設定した50mm二軸押出機にて溶融混練後、Tダイ
法により厚さ0.3mmのシートを作製した。
In Examples and Comparative Examples, sheets were prepared in the following manner. Two or more types of polypropylene having a difference in melting point measured by a differential scanning calorimeter of 3 to 40 ° C.,
230 ° C cylinder temperature with petroleum resin and amorphous resin
After melt-kneading with a 50 mm twin-screw extruder set as described above, a sheet having a thickness of 0.3 mm was produced by a T-die method.

【0018】[0018]

【表1】 [Table 1]

【0019】[0019]

【発明の効果】本発明によれば、熱成形可能な温度幅が
広く、しかもアルミ箔とのヒートシールによるカールが
著しく改良されたポリプロピレン系シートを提供でき
る。
According to the present invention, it is possible to provide a polypropylene sheet having a wide thermoformable temperature range and significantly improved curl due to heat sealing with an aluminum foil.

フロントページの続き Fターム(参考) 4F071 AA14 AA20 AA21 AA22 AA33 AA50 AA84 AF53 AF56 AH19 BB06 BC01 4J002 BA013 BB034 BB121 BB122 BB134 BC044 BG054 CG004 GB01 Continued on the front page F term (reference) 4F071 AA14 AA20 AA21 AA22 AA33 AA50 AA84 AF53 AF56 AH19 BB06 BC01 4J002 BA013 BB034 BB121 BB122 BB134 BC044 BG054 CG004 GB01

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 示差走査熱量計によって測定された融点
の差が3〜40℃である2種以上のポリプロピレン及び
石油樹脂からなる組成物に、非結晶性樹脂を層状に分散
してなるポリプロピレン系シート。
1. A polypropylene-based composition obtained by dispersing an amorphous resin in a layered form in a composition comprising two or more types of polypropylene and a petroleum resin having a difference in melting point of 3 to 40 ° C. measured by a differential scanning calorimeter. Sheet.
JP11123567A 1999-04-30 1999-04-30 Polypropylene-based sheet Pending JP2000313753A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11123567A JP2000313753A (en) 1999-04-30 1999-04-30 Polypropylene-based sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11123567A JP2000313753A (en) 1999-04-30 1999-04-30 Polypropylene-based sheet

Publications (1)

Publication Number Publication Date
JP2000313753A true JP2000313753A (en) 2000-11-14

Family

ID=14863786

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11123567A Pending JP2000313753A (en) 1999-04-30 1999-04-30 Polypropylene-based sheet

Country Status (1)

Country Link
JP (1) JP2000313753A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003113274A (en) * 2001-10-02 2003-04-18 Sumitomo Chem Co Ltd Thermoplastic resin composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003113274A (en) * 2001-10-02 2003-04-18 Sumitomo Chem Co Ltd Thermoplastic resin composition

Similar Documents

Publication Publication Date Title
WO2007015415A1 (en) Polypropylene resin composition, film or sheet, stretched film obtained from such film or sheet, multilayer body, and stretched film obtained from such multilayer body
JP5255433B2 (en) Polypropylene resin composition, molded body, sheet, and container
EP1814942B1 (en) Elastomeric compositions with improved resistance to necking for high speed sheet extrusion applications
US6288168B1 (en) Propylene based resin composition
JP2000313753A (en) Polypropylene-based sheet
JP4076672B2 (en) Polypropylene sheet
JP3396153B2 (en) Thermoforming resin composition and sheet
JP2003342429A (en) Polypropylene resin composition and its application
JP3637829B2 (en) Polypropylene sheet for PTP packaging and packaging method using the same
JP3868076B2 (en) Olefin-based composite resin laminate sheet
JP4221805B2 (en) Polypropylene sheet
EP0920990A2 (en) Composite olefin resin laminated sheet
JP3360532B2 (en) Thermoforming resin composition and sheet
JPH11170454A (en) Polypropylene sheet
JP2000248079A (en) Polypropylene-based sheet
JP4001358B2 (en) Laminated sheet for thermoforming
JP2003277526A (en) Polypropylene-based sheet for ptp
JP4076661B2 (en) Polypropylene sheet
JP3360544B2 (en) Method for producing resin composition for thermoforming and resin composition obtained therefrom
JPH11172059A (en) Polypropylene sheet for packaging medicine
JPH09104060A (en) Drug packing polypropylene sheet and production thereof
JP2003277556A (en) Polypropylene sheet for ptp
JPH09104059A (en) Thermoforming polypropylene sheet and production thereof
JPH10152587A (en) Resin composition for thermal molding and sheet
JPH10182898A (en) Resin composition for thermoforming and its sheet