JPH0592470A - Manufacture of polypropylene sheet excellent in transparency - Google Patents

Manufacture of polypropylene sheet excellent in transparency

Info

Publication number
JPH0592470A
JPH0592470A JP3278847A JP27884791A JPH0592470A JP H0592470 A JPH0592470 A JP H0592470A JP 3278847 A JP3278847 A JP 3278847A JP 27884791 A JP27884791 A JP 27884791A JP H0592470 A JPH0592470 A JP H0592470A
Authority
JP
Japan
Prior art keywords
sheet
transparency
cooling
polypropylene
rolling
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.)
Granted
Application number
JP3278847A
Other languages
Japanese (ja)
Other versions
JP3445804B2 (en
Inventor
Takeshi Sawazaki
健 沢崎
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.)
Mitsubishi Plastics Inc
Original Assignee
Mitsubishi Plastics Inc
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 Mitsubishi Plastics Inc filed Critical Mitsubishi Plastics Inc
Priority to JP27884791A priority Critical patent/JP3445804B2/en
Publication of JPH0592470A publication Critical patent/JPH0592470A/en
Application granted granted Critical
Publication of JP3445804B2 publication Critical patent/JP3445804B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Packages (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To improve the transparency of a sheet without reducing the thermal formability of a polypropylene sheet. CONSTITUTION:Polypropylene is fusion-extruded on a cooling drum like a sheet, and after its cooling it is rolled between the rolls of the surface temperature of 100-120 deg.C at the rolling ratio of 1.1-1.4, whereby the globular crystal on the surface of the sheet is crushed and its transparency is made excellent. The sheet excellent in transparency may be obtained without using the special cooling method such as water cooling. Since the thermal formability of said sheet is not reduced, it is preferably used for the use of forming such as for PTP.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、医薬品の錠剤、カプセ
ルなどの包装に使用されるPTP包装材として好適な、
透明性良好なポリプロピレンシートの製造方法に関す
る。
BACKGROUND OF THE INVENTION The present invention is suitable as a PTP packaging material used for packaging pharmaceutical tablets, capsules, etc.
The present invention relates to a method for producing a polypropylene sheet having good transparency.

【0002】[0002]

【従来の技術とその課題】PTP包装用のシートとして
は従来ポリ塩化ビニルシートが多用されており、ポリプ
ロピレンシートは、透湿度がポリ塩化ビニルシートより
も低いという利点にもかかわらず、ほとんど使用されて
いない。その主な理由は、ポリプロピレンシートはポリ
塩化ビニルシートに比べ透明度が大幅に劣るためであ
る。すなわち、溶融ポリプロピレンを冷却ドラムなどの
冷却表面上にシート状に押し出して冷却する方法におい
ては、シートの冷却ドラムに接する面は急冷されるが、
接しない面は冷却速度が遅く、球晶が生じて面荒れし透
明性が低下する。
2. Description of the Related Art Polyvinyl chloride sheets have been widely used as sheets for PTP packaging, and polypropylene sheets are mostly used despite the advantage that the moisture permeability is lower than that of polyvinyl chloride sheets. Not not. The main reason for this is that the transparency of polypropylene sheets is significantly inferior to that of polyvinyl chloride sheets. That is, in the method of extruding molten polypropylene in a sheet shape on a cooling surface such as a cooling drum to cool, the surface of the sheet in contact with the cooling drum is rapidly cooled,
The surfaces that are not in contact with each other have a low cooling rate, and spherulites are generated to roughen the surface and reduce the transparency.

【0003】ポリプロピレンシートの透明度を改良する
方法としては、(1)ポリプロピレンにジベンジリデン
ソルビトールなどの造核剤を添加する方法、(2)ポリ
プロピレンシートを溶融状態から冷却する間に延伸する
方法、(3)ポリプロピレンの溶融シートを30℃以下
の温度に水冷法により急冷する方法などがあるが、
(1)の方法は真空成形、圧空成形などの熱成形性を悪
化させる欠点があり、(2)の方法もシートが配向する
ため熱成形性を損ない、(3)の方法は複雑な装置、手
段を要するという難点がある。
As a method for improving the transparency of a polypropylene sheet, (1) a method of adding a nucleating agent such as dibenzylidene sorbitol to polypropylene, (2) a method of stretching the polypropylene sheet while cooling it from a molten state, ( 3) There is a method of rapidly cooling a molten polypropylene sheet to a temperature of 30 ° C. or lower by a water cooling method.
The method (1) has a drawback of deteriorating thermoformability such as vacuum forming and pressure forming, and the method (2) also impairs the thermoformability due to the orientation of the sheet. It has the drawback of requiring means.

【0004】[0004]

【課題を解決するための手段】本発明は、簡便で生産性
の高い冷却ドラム法により、熱成形性を悪化させずに透
明性を改良するものであって、ポリプロピレンを冷却表
面上にシート状に溶融押出して冷却した後、表面温度1
00〜120℃のロール間で、圧延比1.1〜1.4で
圧延することを特徴とする透明性良好なポリプロピレン
シートの製造方法である。
The present invention provides a simple and highly productive cooling drum method for improving transparency without deteriorating thermoformability. Surface temperature 1 after melt extrusion and cooling
A method for producing a polypropylene sheet having good transparency, which comprises rolling at a rolling ratio of 1.1 to 1.4 between rolls at 00 to 120 ° C.

【0005】以下本発明を詳しく説明する。本発明にお
いてポリプロピレン樹脂としては、プロピレン単独重合
体あるいはプロピレンとエチレン、ブテン−1などのα
−オレフィンとの共重合体を用いることができる。なか
でも、JIS−K7210の条件下で測定したメルトフ
ローインデックス(MI、単位g/10分)が1〜4の
ものが好ましく、さらに透明性と熱成形性のバランスの
点でプロピレン単独重合体が好適である。MIが1未満
では透明性が悪くなり、MIが4を越えると熱成形時に
シートがべとつき成形性が悪くなる。また必要に応じ、
水添石油樹脂、酸化防止剤、紫外線吸収剤、ポリエチレ
ン、エチレン−プロピレン共重合体などの他の熱可塑性
樹脂などを添加することもできる。
The present invention will be described in detail below. In the present invention, as the polypropylene resin, propylene homopolymer or propylene and ethylene, α such as butene-1
-A copolymer with an olefin can be used. Among them, those having a melt flow index (MI, unit g / 10 minutes) of 1 to 4 measured under the conditions of JIS-K7210 are preferable, and a propylene homopolymer is more preferable in terms of the balance between transparency and thermoformability. It is suitable. If the MI is less than 1, the transparency will be poor, and if the MI is more than 4, the sheet will be sticky during thermoforming and the formability will be poor. If necessary,
Other thermoplastic resins such as hydrogenated petroleum resin, antioxidant, ultraviolet absorber, polyethylene and ethylene-propylene copolymer may be added.

【0006】ポリプロピレンの溶融押出および冷却は、
公知の技術により実施できる。すなわち、樹脂を押出機
に供給して溶融し、Tダイから冷却ドラム、冷却ベルト
などの冷却表面上に押し出して冷却し未延伸シートにす
る。冷却表面の温度は60〜80℃の範囲が適当であ
る。このシートは冷却表面に接しない面が急速に冷却さ
れず、球晶が生成するため透明性が低いものとなる。特
に、熱成形用に供する厚手シートの場合にはこの現象が
顕著になる。
Melt extrusion and cooling of polypropylene is
It can be carried out by a known technique. That is, the resin is supplied to an extruder, melted, and extruded from a T die onto a cooling surface such as a cooling drum or a cooling belt to be cooled to obtain an unstretched sheet. The temperature of the cooling surface is appropriately in the range of 60 to 80 ° C. The surface of this sheet, which is not in contact with the cooling surface, is not rapidly cooled, and spherulites are generated, so that the transparency is low. In particular, this phenomenon becomes remarkable in the case of a thick sheet used for thermoforming.

【0007】次に上記シートを一対のロール間で圧延す
る。この圧延によりシートの片側表面に生成した球晶を
つぶして、シートの透明性を向上させることができる。
ロールの表面温度は100〜120℃の範囲に設定す
る。100℃未満では透明性向上効果が不十分であり、
また120℃を越えると熱による結晶化が進んで成形性
が低下する。ロールは、球晶が生成している側(冷却表
面に接しなかった面)だけを加熱することもできるが、
両方のロールとも温度制御するのが好ましい。
Next, the sheet is rolled between a pair of rolls. By this rolling, the spherulites generated on one surface of the sheet are crushed, and the transparency of the sheet can be improved.
The surface temperature of the roll is set in the range of 100 to 120 ° C. If it is less than 100 ° C, the effect of improving transparency is insufficient,
On the other hand, if it exceeds 120 ° C., crystallization due to heat progresses and the formability is lowered. The roll can heat only the side where spherulites are generated (the surface that did not contact the cooling surface),
Both rolls are preferably temperature controlled.

【0008】また圧延比(圧延前のシート厚さと圧延後
のシート厚さの比)は1.1〜1.4の範囲が好まし
い。圧延比が1.1未満では透明性改良効果が少なく、
1.4倍を越えると配向による結晶増により成形性が悪
くなる。
The rolling ratio (ratio of sheet thickness before rolling and sheet thickness after rolling) is preferably in the range of 1.1 to 1.4. If the rolling ratio is less than 1.1, the transparency improving effect is small,
If it exceeds 1.4 times, the crystallinity increases due to the orientation, resulting in poor moldability.

【0009】なお、冷却表面により冷却されたシート
は、必ずしも室温近くまで冷却されている必要はなく、
十分な形状保持性があり、ポリプロピレンの結晶化開始
温度よりも低温にまで冷却された段階であれば比較的高
温の状態でも圧延処理を行うことができる。また、冷却
されたシートを一旦巻き取って、別工程でシートを巻き
戻しながら圧延を行っても良い。
The sheet cooled by the cooling surface does not necessarily have to be cooled to near room temperature.
As long as it has sufficient shape retention and is cooled to a temperature lower than the crystallization start temperature of polypropylene, the rolling treatment can be performed even at a relatively high temperature. Alternatively, the cooled sheet may be wound up once and rolled in another step while being rewound.

【0010】圧延後のシートは、ポリプロピレン樹脂の
結晶化開始温度である約130℃よりも低温になってい
るため、特に冷却手段を講ぜずに自然空冷しても良い
が、空気吹き付けなどの強制冷却を行うのも好ましい。
Since the rolled sheet has a temperature lower than about 130 ° C., which is the crystallization start temperature of polypropylene resin, it may be naturally air-cooled without any cooling means, but it may be forced by air blowing. It is also preferable to perform cooling.

【0011】本発明によるシートは、真空成形、圧空成
形などの熱成形を施して、PTP包装、ブリスタ包装な
どの用途に使用するのに適しており、その厚さは特に制
限はないが、通常200〜500μm、特に200〜4
00μm程度である。
The sheet according to the present invention is suitable for use in applications such as PTP packaging and blister packaging after thermoforming such as vacuum forming and pressure forming, and its thickness is not particularly limited, 200-500 μm, especially 200-4
It is about 00 μm.

【0012】[0012]

【発明の効果】本発明によれば、水冷法などの特殊な装
置、手段を必要とせず、熱成形性を損なうことなく透明
性を向上させることができ、PTP用などの成形用途に
好適なシートが得られる。
EFFECTS OF THE INVENTION According to the present invention, it is possible to improve the transparency without deteriorating the thermoformability without requiring a special device or means such as a water cooling method, and it is suitable for molding applications such as PTP. Sheets are obtained.

【0013】[0013]

【実施例】【Example】

(実施例1〜4)ジタ−シヤリブチル−p−クレゾール
を0.1重量部、ステアリン酸カルシウムを0.1重量
部配合したポリプロピレン(単独重合体、MI=2)
を、シリンダ径40mmの押出機により溶融、混練を行
い、温度240℃のTダイにより、表面温度70℃の冷
却ドラム上にキヤストし、無延伸シートとした。引き続
き、表面温度110℃の一対のロール間で表1に示す圧
延比で圧延し、幅200mm、厚さ300μmのシート
を作成し、PTP成形機で圧空成形を行い成形性を評価
した。成形性の評価は、成形後の形状がシヤープに表れ
ているものを「良好」、成形後の形状がシヤープに表れ
ていないものを「不良」とした。また得られたシートの
透明度(ヘーズ)をJIS−K7105により測定し
た。これらの結果を表1に示す。
Examples 1 to 4 Polypropylene (homopolymer, MI = 2) in which 0.1 part by weight of zita-sialybutyl-p-cresol and 0.1 part by weight of calcium stearate were blended.
Was melted and kneaded by an extruder having a cylinder diameter of 40 mm, and cast on a cooling drum having a surface temperature of 70 ° C. by a T die having a temperature of 240 ° C. to obtain a non-stretched sheet. Subsequently, rolling was performed at a rolling ratio shown in Table 1 between a pair of rolls having a surface temperature of 110 ° C. to form a sheet having a width of 200 mm and a thickness of 300 μm, which was subjected to pressure forming with a PTP molding machine to evaluate formability. The moldability was evaluated as "good" when the shape after molding was visible in the shape, and "bad" when the shape after molding was not visible in the shape. The transparency (haze) of the obtained sheet was measured according to JIS-K7105. The results are shown in Table 1.

【0014】(比較例)ロールによる圧延を行わない以
外は実施例1と同様にして厚さ300μmのシートを作
成し、実施例1と同様の評価を行った。
Comparative Example A sheet having a thickness of 300 μm was prepared in the same manner as in Example 1 except that rolling with a roll was not performed, and the same evaluation as in Example 1 was performed.

【表1】 以上の結果から、圧延比1.1〜1.4の範囲で圧延す
ることにより、成形性を損なわずに透明性を大幅に改善
できることがわかる。
[Table 1] From the above results, it is understood that by rolling in the rolling ratio range of 1.1 to 1.4, the transparency can be significantly improved without impairing the formability.

【0015】(実施例5〜8)実施例1と同じ無延伸シ
ートを、圧延ロールの温度を表2のように変えて、圧延
比1.3で圧延して300μmのシートを作成し、実施
例1と同じ評価を行った。その結果を表2に示す。
(Examples 5 to 8) The same unstretched sheet as in Example 1 was rolled at a rolling ratio of 1.3 with the temperature of the rolling roll changed as shown in Table 2 to prepare a sheet of 300 μm. The same evaluation as in Example 1 was performed. The results are shown in Table 2.

【表2】 [Table 2]

【0016】この結果から、圧延するロールの表面温度
は、100〜120℃の範囲が好適なことがわかる。
From these results, it is understood that the surface temperature of the roll to be rolled is preferably in the range of 100 to 120 ° C.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B29K 105:32 B29L 7:00 4F ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI Technical display area B29K 105: 32 B29L 7:00 4F

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポリプロピレンを冷却表面上にシート状
に溶融押出して冷却した後、表面温度100〜120℃
のロール間で、圧延比1.1〜1.4で圧延することを
特徴とする透明性良好なポリプロピレンシートの製造方
法。
1. A surface temperature of 100 to 120 ° C. after melt-extruding polypropylene into a sheet on a cooling surface and cooling.
A method for producing a polypropylene sheet having good transparency, which comprises rolling between the rolls at a rolling ratio of 1.1 to 1.4.
JP27884791A 1991-09-30 1991-09-30 Method for producing polypropylene sheet with good transparency Expired - Fee Related JP3445804B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27884791A JP3445804B2 (en) 1991-09-30 1991-09-30 Method for producing polypropylene sheet with good transparency

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27884791A JP3445804B2 (en) 1991-09-30 1991-09-30 Method for producing polypropylene sheet with good transparency

Publications (2)

Publication Number Publication Date
JPH0592470A true JPH0592470A (en) 1993-04-16
JP3445804B2 JP3445804B2 (en) 2003-09-08

Family

ID=17602978

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27884791A Expired - Fee Related JP3445804B2 (en) 1991-09-30 1991-09-30 Method for producing polypropylene sheet with good transparency

Country Status (1)

Country Link
JP (1) JP3445804B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6640444B1 (en) 1998-12-16 2003-11-04 Kioritz Corporation Portable trimmer with brake device for cutter
JP2004307671A (en) * 2003-04-08 2004-11-04 National Institute Of Advanced Industrial & Technology High strength, highly transparent polypropylene sheet and method for manufacturing the same
WO2010084766A1 (en) * 2009-01-23 2010-07-29 サンアロマー株式会社 Process and apparatus for producing crystalline resin film or sheet
WO2010084750A1 (en) * 2009-01-23 2010-07-29 国立大学法人広島大学 Polymer sheet and method for producing same
US8735523B2 (en) 2007-03-02 2014-05-27 Hiroshima University Polymer crystalline materials

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6640444B1 (en) 1998-12-16 2003-11-04 Kioritz Corporation Portable trimmer with brake device for cutter
JP2004307671A (en) * 2003-04-08 2004-11-04 National Institute Of Advanced Industrial & Technology High strength, highly transparent polypropylene sheet and method for manufacturing the same
US8735523B2 (en) 2007-03-02 2014-05-27 Hiroshima University Polymer crystalline materials
WO2010084766A1 (en) * 2009-01-23 2010-07-29 サンアロマー株式会社 Process and apparatus for producing crystalline resin film or sheet
WO2010084750A1 (en) * 2009-01-23 2010-07-29 国立大学法人広島大学 Polymer sheet and method for producing same
JP2010168485A (en) * 2009-01-23 2010-08-05 Sunallomer Ltd Method and system for producing crystalline resin film or sheet
US8728616B2 (en) 2009-01-23 2014-05-20 Hiroshima University Polymer sheet and method for producing same
US9138933B2 (en) 2009-01-23 2015-09-22 Sunallomer Ltd. Process and apparatus for producing crystalline resin film or sheet

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