JP2000211008A - Preparation of pearl lustrous synthetic paper of biaxially orientated polypropylene(bopp) with thickness of 25-250 micron obtained by three-layer coextrusion system - Google Patents

Preparation of pearl lustrous synthetic paper of biaxially orientated polypropylene(bopp) with thickness of 25-250 micron obtained by three-layer coextrusion system

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Publication number
JP2000211008A
JP2000211008A JP11015365A JP1536599A JP2000211008A JP 2000211008 A JP2000211008 A JP 2000211008A JP 11015365 A JP11015365 A JP 11015365A JP 1536599 A JP1536599 A JP 1536599A JP 2000211008 A JP2000211008 A JP 2000211008A
Authority
JP
Japan
Prior art keywords
paper
layer
weight
synthetic paper
polypropylene
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
JP11015365A
Other languages
Japanese (ja)
Other versions
JP3623681B2 (en
Inventor
Hokin Rin
林豊欽
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.)
Nan Ya Plastics Corp
Original Assignee
Nan Ya Plastics Corp
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 Nan Ya Plastics Corp filed Critical Nan Ya Plastics Corp
Priority to JP01536599A priority Critical patent/JP3623681B2/en
Publication of JP2000211008A publication Critical patent/JP2000211008A/en
Application granted granted Critical
Publication of JP3623681B2 publication Critical patent/JP3623681B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Landscapes

  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Molding Of Porous Articles (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Laminated Bodies (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

PROBLEM TO BE SOLVED: To easily prepare a pearl lustrous synthetic paper by a method wherein extrusions extruded from a screw main extruder with a feeder and screw sub-extruders with two feeders are mixed together to obtain a three-layer sheet through a T-die head and cooling molding, biaxially drawing and corona treatment are applied. SOLUTION: An extruder apparatus 1 consisting of a twin-screw main extruder and two twin-screw sub-extruders respectively with a side feeder is provided and extrusions of a polypropylene resin and an inorg. substance are mixed together and are guided into a T-die head, where they are co-extruded at a temp. of 180-280 deg.C to obtain a three-layer sheet and after this is then cooled and molded by means of a cooling molding roll device 2, it is guided into a longitudinal direction drawing device 3 and it is drawn at two steps at a low speed and a high speed to give a longitudinal strength to a synthetic paper. In addition, after the paper sheet is drawn in the transverse direction by means of a transverse drawing device 4, corona treatment is performed thereon by means of a corona treatment device 5 and a pearl lustrous synthetic paper obtd. is wound by means of a winding device 6.

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】本発明は三層共押出方式で得
られる厚み25〜250ミクロン二軸延伸ポリプロピレ
ンパール光沢合成紙の製造方法に関するもので、とくに
三層共押出方法により、それぞれフィーダーを持つトゥ
イン・スクリュー主押出機1台とフィーダーを持つトゥ
イン・スクリュー副押出機2台から押出されたポリプロ
ピレン樹脂と無機物の混合押出物を合流させ、1つのT
ダイヘッドを経て紙状層または樹脂層/発泡中間層/紙
状層または樹脂層の三層シートとし、さらに冷却成形、
二軸延伸、コロナ処理、巻取りなどのステップを経て、
25〜250ミクロンの厚みを持つ紙状層/発泡中間層
/紙状層の三層共押出両面紙状面パール光沢合成紙、紙
状層/発泡中間層/樹脂層の三層共押出単面紙状面パー
ル光沢合成紙、樹脂層/発泡中間層/樹脂層の三層共押
出両面光沢面パール光沢合成紙を製造し、塗布用合成紙
の塗布紙とするものを指す。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a biaxially stretched polypropylene pearl glossy synthetic paper having a thickness of 25 to 250 μm obtained by a three-layer coextrusion method, and in particular, has a feeder by the three-layer coextrusion method. The mixed extrudate of the polypropylene resin and the inorganic material extruded from one twin screw main extruder and two twin screw sub-extruders having a feeder is combined, and one T
After passing through a die head, it is made into a three-layer sheet of a paper-like layer or a resin layer / foamed intermediate layer / a paper-like layer or a resin layer, and further cooled and formed.
After steps such as biaxial stretching, corona treatment and winding,
Three layers of paper-like layer / foamed intermediate layer / paper-like layer having a thickness of 25 to 250 microns Coextruded double-sided paper-like surface Pearl gloss synthetic paper, three-layer coextruded single-sided paper-like layer / foamed intermediate layer / resin layer Paper-like pearly glossy synthetic paper, refers to the production of a three-layer coextruded double-sided glossy pearly glossy synthetic paper of resin layer / foaming intermediate layer / resin layer, which is used as a synthetic paper for application.

【0002】[0002]

【従来の技術】現在ポリオレフィン合成紙は天然パルプ
抄造紙に取って代わろうとしている。ポリプロピレンの
二軸延伸フィルムを基材層(中間層)とし、裏表に8〜
65重量%の無機微細粉末を含むポリプロピレン1軸延
伸フィルムを紙状層とする合成紙が出願され、実用化さ
れている。王子油化合成紙株式会社は特公昭46−40
794号、特開昭56−141339号、特開昭56−
118437号、特開平3−87255号などの特許出
願を提出している。
2. Description of the Related Art Polyolefin synthetic paper is currently replacing natural pulp paper. A biaxially-stretched polypropylene film is used as the base layer (intermediate layer).
A synthetic paper having a paper-like layer of a uniaxially stretched polypropylene film containing 65% by weight of inorganic fine powder has been filed and put to practical use. Oji Yuka Synthetic Paper Co., Ltd.
794, JP-A-56-141339, JP-A-56-141339
No. 118437 and Japanese Patent Application Laid-Open No. 3-87255 have been filed.

【0004】[0004]

【発明が解決しようとする課題】これらの製造方法で
は、基材層を縦方向延伸装置と横方向延伸装置の間に置
き、2台の押出機を利用し、上下フィルムを作り紙状層
を完成している。紙状層は横方向にだけ延伸でき、紙状
層の強度は低い。紙状層の印刷性を高めるため添加され
ている無機微細粉末は印刷加工工程において脱落するた
め、印刷機器を清掃する必要がある。また、一軸延伸で
得られた紙状層と二軸延伸で得られた基材層とは総延伸
率が異なり、このため加熱時に、紙状層と基材層の収縮
率も異なり、紙がウェーブ状に変形してしまう。さらに
製造工程と製品品質の安定性を高めるため、2台の押出
機で上下フィルムを完成する紙状層の製造工程では生産
速度が制限され、延伸後の完成品の幅が最大6メートル
にすぎない。単一の紙状層の厚みが少なくとも10ミク
ロン(通常は30ミクロン)必要なため、製品の厚みは
つねに60ミクロン以上となる。さもなくば、製品の厚
みが不均一となり、印刷加工に影響が出てしまう。総体
的に製造工程の難度が高く、生産コストも高いため、製
品が普及しにくく、応用がむずかしい。
In these production methods, a base material layer is placed between a longitudinal stretching device and a transverse stretching device, and two extruders are used to form upper and lower films, and a paper-like layer is formed. It is completed. The paper-like layer can be stretched only in the transverse direction, and the strength of the paper-like layer is low. Since the inorganic fine powder added to enhance the printability of the paper-like layer falls off in the printing process, it is necessary to clean the printing device. In addition, the paper-like layer obtained by uniaxial stretching and the base layer obtained by biaxial stretching have different total stretching ratios. Therefore, when heated, the shrinkage ratios of the paper-like layer and the base material layer also differ, and It deforms into a wave shape. Furthermore, in order to enhance the stability of the manufacturing process and product quality, the production speed of the paper-like layer, in which the upper and lower films are completed by two extruders, is limited, and the width of the finished product after stretching is only up to 6 meters. Absent. Since the thickness of a single paper layer needs to be at least 10 microns (typically 30 microns), the thickness of the product will always be 60 microns or more. Otherwise, the thickness of the product will be uneven, which will affect the printing process. As a whole, the manufacturing process is difficult and the production cost is high, making it difficult for products to spread and its application to be difficult.

【0005】[0005]

【課題を解決するための手段】上記問題を解決するた
め、本発明出願人は新しい三層構造合成紙の製造方法を
提出する。当該合成紙は紙状層または樹脂層/発泡中間
層/紙状層または樹脂層から構成され、発泡中間層のポ
リプロピレン樹脂混合物を1台のフィーダーを持つトゥ
イン・スクリュー主押出機から、紙状層または樹脂層の
樹脂混合物を2台のフィーダーを持つトゥイン・スクリ
ュー副押出機からそれぞれ押出し、これらの押出物を合
流させ、1つのTダイヘッドを経て三層シートとし、さ
らに冷却成形、二軸延伸、コロナ処理、巻取りなどのス
テップを経て、25〜250ミクロンの厚みを持つ三層
共押出単/両面紙状面および両面光沢面のパール光沢合
成紙を得る。本発明の製造方法は三層共押出方式を採用
する。各層の押出物を合流させた後に共押出し、さらに
二軸圧延して得られた合成紙は、従来の方法により二軸
延伸した中間層に一軸延伸した紙状面を貼付して得られ
た合成紙とは構造、製造方法とも異なる。同時に副押出
機から押出す原料を、無機充填剤を使用した紙状層と無
機充填剤を添加していない樹脂層から選ぶことで、紙状
層/発泡中間層/紙状層の三層共押出両面紙状面パール
光沢合成紙、紙状層/発泡中間層/樹脂層の三層共押出
単面紙状面パール光沢合成紙、樹脂層/発泡中間層/樹
脂層の三層共押出両面光沢面パール光沢合成紙を製造
し、塗布用合成紙の塗布紙とすることができる。
In order to solve the above-mentioned problems, the present applicant proposes a new method for producing a three-layer synthetic paper. The synthetic paper is composed of a paper-like layer or a resin layer / a foamed intermediate layer / a paper-like layer or a resin layer, and the polypropylene resin mixture of the foamed intermediate layer is formed from a twin screw main extruder having one feeder into a paper-like layer. Alternatively, the resin mixture of the resin layer is respectively extruded from a twin screw sub-extruder having two feeders, these extrudates are merged, formed into a three-layer sheet via one T-die head, and further cooled, biaxially stretched, Through steps such as corona treatment and winding, a three-layer coextruded single / double-sided paper-like surface and a double-sided glossy pearl glossy synthetic paper having a thickness of 25 to 250 microns are obtained. The production method of the present invention employs a three-layer coextrusion method. The combined paper obtained by co-extrusion after extruding the extrudates of each layer and further biaxially rolling is obtained by attaching a uniaxially stretched paper-like surface to a biaxially stretched intermediate layer by a conventional method. It differs from paper in both structure and manufacturing method. At the same time, the raw material extruded from the sub-extruder is selected from a paper-like layer using an inorganic filler and a resin layer to which no inorganic filler is added, so that the three layers of paper-like layer / foamed intermediate layer / paper-like layer can be used. Extruded double-sided paper-like surface pearl glossy synthetic paper, three-layer coextruded paper-like layer / foamed intermediate layer / resin layer Single-sided paper-shaped surface pearly glossy synthetic paper, three-layer coextruded resin layer / foamed intermediate layer / resin layer A glossy pearly glossy synthetic paper can be manufactured and used as a coated paper for synthetic paper for application.

【0006】[0006]

【発明の実施の形態】本発明の技術内容を明確に示すた
め、ポリプロピレン樹脂混合物と製造工程(押出し、三
層共押出、冷却、二軸延伸、コロナ処理、巻取り)につ
いて以下に説明する。本発明の二軸延伸ポリプロピレン
パール光沢合成紙は三層構造を有する。その発泡中間層
は1台のサイドフィーダーを持つトゥイン・スクリュー
主押出機で押出す。アイソタクチック度97%以上の高
結晶性ポリプロピレン39〜95重量%、静電気防止剤
1〜5重量%を主押出機の前方にあるホッパーで均一に
攪拌し、主押出機に入れる。さらに炭酸カルシウム粉末
0〜40重量%と二酸化チタン粉末0〜20重量%を計
量後、1台または2台のサイドフィーダーで主押出機に
入れる。主押出機のトゥイン・スクリューで均一に混練
した後、樹脂と無機粉末の混合物をTダイヘッドの中間
ラナー(runner)に押し入れる。また、紙状層はサイド
フィーダーを持つトゥイン・スクリュー主押出機2台で
押出す。ポリプロピレン20〜99.5重量%、ポリエ
チレン0〜12重量%、静電気防止剤0〜3重量%、粘
着防止剤0.5〜3重量%、紫外線吸収剤0〜2重量%
を副押出機前方にあるホッパーで均一に攪拌した後、副
押出機に入れる。さらに炭酸カルシウム粉末0〜40重
量%と二酸化チタン粉末0〜20重量%を計量後、1台
または2台のサイドフィーダーで副押出機に入れる。副
押出機のトゥイン・スクリューで均一に混練した後、樹
脂と無機粉末の混合物をTダイヘッドの両側道に押し入
れる。上述の押出機3台からの押出物を合流させ、Tダ
イヘッドで共押出し、樹脂層または紙状層/発泡中間層
/樹脂層または紙状層のシートを形成する。二軸延伸、
コロナ処理、巻取のステップを経て、厚み20〜250
ミクロンの両/単面紙状面のパール光沢合成紙を製造す
る。本発明の製造方法で製造された合成紙は文化紙に適
しており、高結晶性ポリプロピレンを主要原料としてい
る。本発明で使用されるポリプロピレン樹脂は溶融指数
(MFI)が0.5〜8(230℃/2.16kg A
STM D1238)で、大部分がアイソタクチックな
均一重合物とする。この種の高分子構造は分子同士が配
列正しく結合している。原料の分子量とその分布状況に
より、パール光沢合成紙の機械強度と品質の均一性を制
御することができる。本発明の製造方法で得られたパー
ル光沢合成紙は三層構造を呈している。図1に示す通
り、紙状層の紙模倣効果を高めるため、ポリエチレン、
無機粉末を配合し、その用量で光沢度、筆記性、印刷性
を調整することができる。ポリエチレンのMFIは0.
1〜7のものを採用する。ポリエチレンのMFIで紙状
面の強度を調整できる。本発明で使用される無機粉末
は、発泡中間層の密度を下げる(延伸工程における微細
孔発生を利用)ほか、紙状層にプラスチック紙とは異な
る優れた筆記性と印刷性をもたらすことができる。無機
粉末は炭酸カルシウム、けい藻土、クレー、酸化カルシ
ウム、硫酸バリウム、二酸化チタンなどのグループから
1種類または多種類を選んで使用する。その粒径は0.
1〜10ミクロンとし、用量は製品の需要によって決定
する。本発明は側方から配合料を給送するトゥイン・ス
クリュー押出機で製造する。その無機粉末はサイドフィ
ーダーから押出機に入れる。トゥイン・スクリューを利
用した押出機で均一に混練することができる。このほ
か、無機粉末と樹脂を先に混練した複合粒を最前方のホ
ッパーに入れ、各種樹脂と混合した後さらに押出機に入
れることもできる。本発明では製品の不透明度、白色
度、抗紫外線性を調整するため、二酸化チタン粉末を使
用している。本発明の静電気防止剤は、通常の二軸延伸
ポリプロピレン(BOPP)で使用されている静電気防
止剤をすべて使用することができる。三級アミン類が主
に使用されている。三級アミンは電荷移行性を有するた
め、加工摩擦で発生した静電気を除去することができ
る。本発明において、合成紙を巻き取る時互いに粘着す
るため、粘着防止剤を添加する必要がある。通常の二軸
延伸ポリプロピレンで使用されているシリカ、クレー、
ポリメチルアクリル酸メチルエステル(PMMA)、ガ
ラスビーズなどから1種類を選ぶことができる。本発明
で得られるポリプロピレンパール光沢合成紙の比重は
0.75以下であり、混合物の組成比で調整することが
できる。これは特開平3―87255号の合成紙の0.
79に比べて低く、同じ重さでより広い面積の合成紙を
製造することができるため、経済性が高い。本発明で得
られる二軸延伸ポリプロピレンパール光沢合成紙は、紙
状層/発泡中間層/紙状層または樹脂層の三層構造を有
し、物性、生産能力は材料の配合、設備、操作と深い関
係がある。通常のポリプロピレン膜の二軸延伸製品は、
ほとんどが充填剤を添加していない、透明な製品であ
る。本発明では紙を模倣するため、製造工程において大
量の無機充填剤を添加する必要があり、二軸延伸製造工
程の生産性、生産能力、品質安定に関して問題を克服し
なければならない。本発明のポリプロピレンパール光沢
合成紙(厚み25〜250ミクロン)で使用する製造工
程の装置とステップを図4に示す。 押出機装置(図4の(1)):サイドフィーダーを持つト
ゥイン・スクリュー主押出機1台とサイドフィーダーを
持つトゥイン・スクリュー副押出機2台から成る。その
温度設定条件は樹脂混合物の組成、MFI、結晶度、粘
度、生産ラインの速度、製品の厚みによって異なるが、
通常は180〜280℃とする。180℃以下では樹脂
の可塑化が進まず、Tダイヘッドで押出すことができな
い。280℃以上では樹脂が過度に可塑化し、亀裂が入
ってしまう。本発明では三層共押出方式で三層合成紙
(紙状層または樹脂層/発泡中間層/紙状層または樹脂
層)を製造する。Tダイヘッドの流道設計により三層の
押出物を合流させ、Tダイヘッドで三層を共押出する。 冷却成形ロール装置(図4の(2)):水冷式またはガス
冷却式の冷却装置とする。180〜280℃で三層共押
出された溶融共押出物を冷却し、成形する。冷却温度の
制御は、その後のステップが順調にいくかどうかを大き
く左右する。冷却温度は通常15〜60℃に設定し、合
成紙板の厚みと生産ラインの速度によりこの範囲で調整
できる。 縦方向延伸装置(図4の(3)):冷却成形を経た紙板を
縦方向延伸装置に入れる。先ず115〜150℃(紙板
の厚みと生産ラインの速度で選択する)に加熱し、紙板
を軟化させ、さらに低速および高速の2段階で延伸し、
合成紙に縦方向強度を与える。また、アニーリングで成
形する。縦方向の延伸率は通常3〜6倍に設定する。 横方向延伸装置(図4の(4)):縦方向延伸処理で薄く
なった紙板を140〜195℃(紙板の厚みと生産ライ
ンの速度で選択する)に加熱して軟化させ、横方向に延
伸し、さらにアニーリングで成形し、パール合成紙の部
分収縮によりサイズの安定性を高める。通常、横方向延
伸倍率は5〜12倍に設定する。製品の特性により選ぶ
ことができる。 コロナ処理装置(図4の(5)):コロナ処理はポリプロ
ピレンパール光沢合成紙の物性を改善するために行わ
れ、印刷、塗布、コーティングなどの加工が容易にな
る。処理効率を20〜120KWとする高周波放電装置
(生産ラインの速度により調整)でコロナ処理を行う。
これにより表面の湿潤張力は36〜48ダイン/cmに
達する。 巻取装置(図4の(6)):鉄パイプを利用し、完成した
パール光沢合成紙を巻き取り、幅8メートルの完成品と
する。必要により縦または横にカットし、包装して、厚
み25〜250ミクロンのロール状またはシート状製品
とする。本発明の製造方法で得られた厚み25〜250
ミクロン二軸延伸ポリプロピレンパール光沢合成紙にお
ける三層の厚みを表1に示す。紙状層と樹脂層の厚みは
1〜30ミクロンの範囲で調整できる。
BEST MODE FOR CARRYING OUT THE INVENTION In order to clearly show the technical contents of the present invention, a polypropylene resin mixture and production steps (extrusion, three-layer coextrusion, cooling, biaxial stretching, corona treatment, winding) will be described below. The biaxially oriented polypropylene pearl glossy synthetic paper of the present invention has a three-layer structure. The foamed intermediate layer is extruded in a twin screw main extruder with one side feeder. 39 to 95% by weight of a highly crystalline polypropylene having an isotacticity of 97% or more and 1 to 5% by weight of an antistatic agent are uniformly stirred by a hopper in front of the main extruder, and put into the main extruder. Further, 0 to 40% by weight of calcium carbonate powder and 0 to 20% by weight of titanium dioxide powder are weighed and then put into the main extruder by one or two side feeders. After uniformly kneading with the twin screw of the main extruder, the mixture of the resin and the inorganic powder is pushed into the intermediate runner of the T-die head. The paper layer is extruded by two twin screw main extruders having side feeders. 20 to 99.5% by weight of polypropylene, 0 to 12% by weight of polyethylene, 0 to 3% by weight of antistatic agent, 0.5 to 3% by weight of antiblocking agent, 0 to 2% by weight of ultraviolet absorber
Is uniformly stirred with a hopper in front of the sub-extruder, and then put into the sub-extruder. Further, 0 to 40% by weight of calcium carbonate powder and 0 to 20% by weight of titanium dioxide powder are weighed, and then put into a sub-extruder by one or two side feeders. After uniformly kneading with the twin screw of the auxiliary extruder, the mixture of the resin and the inorganic powder is pushed into both sides of the T-die head. The extrudates from the three extruders described above are combined and co-extruded with a T-die head to form a resin layer or paper-like layer / foamed intermediate layer / resin layer or paper-like sheet. Biaxial stretching,
Through the steps of corona treatment and winding, the thickness is 20 to 250
Produces micron double / single sided pearly glossy paper. The synthetic paper produced by the production method of the present invention is suitable for culture paper, and uses highly crystalline polypropylene as a main raw material. The polypropylene resin used in the present invention has a melt index (MFI) of 0.5 to 8 (230 ° C./2.16 kg A).
According to STM D1238), the polymer is mostly isotactic and homogeneous. In this type of polymer structure, the molecules are bonded to each other in the correct sequence. The uniformity of the mechanical strength and quality of the pearl glossy synthetic paper can be controlled by the molecular weight of the raw material and its distribution. The pearl glossy synthetic paper obtained by the production method of the present invention has a three-layer structure. As shown in FIG. 1, in order to enhance the paper imitation effect of the paper-like layer, polyethylene,
The inorganic powder is blended, and the glossiness, writing property, and printability can be adjusted by the amount of the inorganic powder. The MFI of polyethylene is 0.
1 to 7 are adopted. The strength of the paper-like surface can be adjusted by MFI of polyethylene. The inorganic powder used in the present invention can lower the density of the foamed intermediate layer (utilize the generation of micropores in the stretching step) and can provide the paper-like layer with excellent writing and printing properties different from plastic paper. . One or more inorganic powders are used by selecting one or more from the group of calcium carbonate, diatomaceous earth, clay, calcium oxide, barium sulfate, titanium dioxide and the like. Its particle size is 0.
It is between 1 and 10 microns and the dose is determined by the demand of the product. The invention is manufactured in a twin screw extruder that feeds the compound from the side. The inorganic powder is put into an extruder from a side feeder. The mixture can be uniformly kneaded with an extruder using a twin screw. In addition, the composite particles obtained by first kneading the inorganic powder and the resin can be put in the forefront hopper, mixed with various resins, and then put into an extruder. In the present invention, titanium dioxide powder is used to adjust the opacity, whiteness, and anti-ultraviolet property of the product. As the antistatic agent of the present invention, all the antistatic agents used in ordinary biaxially oriented polypropylene (BOPP) can be used. Tertiary amines are mainly used. Since tertiary amines have charge transfer properties, they can remove static electricity generated by processing friction. In the present invention, it is necessary to add an anti-adhesion agent because the synthetic papers stick to each other when they are wound up. Silica, clay, used in ordinary biaxially oriented polypropylene,
One type can be selected from polymethylacrylic acid methyl ester (PMMA), glass beads, and the like. The specific gravity of the polypropylene pearl glossy synthetic paper obtained in the present invention is 0.75 or less, and can be adjusted by the composition ratio of the mixture. This is equivalent to the synthetic paper of JP-A-3-87255.
As compared with 79, it is possible to manufacture a synthetic paper having a larger area with the same weight, and thus the economic efficiency is high. The biaxially stretched polypropylene pearl glossy synthetic paper obtained in the present invention has a three-layer structure of paper-like layer / foamed intermediate layer / paper-like layer or resin layer. There is a deep relationship. The usual biaxially stretched product of polypropylene film is
Most are clear products with no added filler. In the present invention, in order to imitate paper, it is necessary to add a large amount of an inorganic filler in the production process, and the problems concerning productivity, production capacity, and quality stability of the biaxial stretching production process must be overcome. FIG. 4 shows the apparatus and steps of the manufacturing process used for the polypropylene pearl glossy synthetic paper (25 to 250 microns) of the present invention. Extruder device ((1) in FIG. 4): One twin-screw main extruder with side feeders and two twin-screw sub-extruders with side feeders. The temperature setting conditions vary depending on the composition of the resin mixture, MFI, crystallinity, viscosity, production line speed, and product thickness,
Usually, the temperature is 180 to 280 ° C. If the temperature is lower than 180 ° C., plasticization of the resin does not proceed, and the resin cannot be extruded with a T-die head. Above 280 ° C., the resin is excessively plasticized and cracks occur. In the present invention, a three-layer synthetic paper (paper-like layer or resin layer / foamed intermediate layer / paper-like layer or resin layer) is manufactured by a three-layer coextrusion method. The extrudates of three layers are merged by the flow path design of the T-die head, and the three layers are co-extruded with the T-die head. Cooling roll device ((2) in FIG. 4): A water-cooled or gas-cooled cooling device. The three-layer coextruded molten coextrudate at 180-280 ° C is cooled and molded. The control of the cooling temperature has a great influence on whether the subsequent steps go smoothly. The cooling temperature is usually set at 15 to 60 ° C, and can be adjusted within this range by the thickness of the synthetic paper board and the speed of the production line. Longitudinal stretching device ((3) in FIG. 4): The paper sheet that has been subjected to cooling molding is placed in a longitudinal stretching device. First, heat to 115-150 ° C (choose according to the thickness of the paperboard and the speed of the production line) to soften the paperboard and stretch it in two steps, low speed and high speed.
Gives synthetic paper longitudinal strength. Also, it is formed by annealing. The stretching ratio in the machine direction is usually set to 3 to 6 times. Lateral stretching device ((4) in FIG. 4): The paper board thinned by the longitudinal stretching process is heated to 140 to 195 ° C. (select according to the thickness of the paper board and the speed of the production line) to be softened, It is stretched and further formed by annealing, and the size stability is enhanced by the partial shrinkage of the pearl synthetic paper. Usually, the transverse stretching ratio is set to 5 to 12 times. It can be selected according to the characteristics of the product. Corona treatment device ((5) in FIG. 4): Corona treatment is performed to improve the physical properties of the polypropylene pearl glossy synthetic paper, and processing such as printing, coating, and coating is facilitated. Corona treatment is performed with a high-frequency discharge device (adjusted according to the speed of the production line) with a treatment efficiency of 20 to 120 KW.
This results in a surface wet tension of 36-48 dynes / cm. Winding device ((6) in FIG. 4): The finished pearly glossy synthetic paper is wound up using an iron pipe to obtain a finished product having a width of 8 meters. If necessary, it is cut lengthwise or widthwise and packaged to obtain a roll or sheet product having a thickness of 25 to 250 microns. 25-250 thickness obtained by the production method of the present invention
Table 1 shows the thickness of the three layers of the micron biaxially stretched polypropylene pearl glossy synthetic paper. The thickness of the paper-like layer and the resin layer can be adjusted in the range of 1 to 30 microns.

【0007】本発明の技術内容を明確に説明するため、
以下に筆記用、印刷用、包装用及び各種用途の合成紙を
製造した本発明の実施例を示す。ただし、本発明の特許
範囲はこれに限定されない。 [実施例1]厚み250ミクロン以下の単面紙状面パー
ル光沢合成紙 ポリプロピレン(MFI:2.4)67重量%、静電気
防止剤3重量%を混合した後、ホッパーからサイドフィ
ーダーを持つトゥイン・スクリュー主押出機に入れ、さ
らに炭酸カルシウム粉末20重量%及び二酸化チタン1
0重量%を計量後、それぞれフィーダーを持つトゥイン
・スクリュー主押出機に入れる。また、ポリプロピレン
(MFI:5)62重量%、ポリエチレン(MFI:
1)12重量%、静電気防止剤2重量%、粘着防止剤3
重量%、紫外線吸収剤1重量%をミキサーで混合した
後、ホッパーからサイドフィーダーを持つトゥイン・ス
クリュー#1副押出機に入れる。さらに炭酸カルシウム
粉末10重量%及び二酸化チタン10重量%を計量後、
それぞれ2つのフィーダーからトゥイン・スクリュー#
2副押出機に入れる。別に、ポリプロピレン(MFI:
2.4)97重量%、粘着防止剤3重量%をミキサーで
混合した後、ホッパーからサイドフィーダーを持つトゥ
イン・スクリュー#2副押出機に入れる。押出機の温度
を200〜280℃に設定し、三層共押出方式によりT
ダイヘッドから押出す。15〜60℃に設定された冷却
ロールを経て、ポリプロピレンパール光沢合成紙板が冷
却、成形される。成形された紙板は縦方向延伸装置に入
れ、120〜150℃に加熱した後、縦方向に5倍延伸
を行う。延伸後はアニーリングを行う。冷却後に再び横
方向延伸装置に入れ、150〜185℃に加熱し、再び
横方向に9倍延伸を行う。延伸後はアニーリングを行
い、合成紙の収縮率を制御する。横方向延伸装置を出た
後、コロナ処理装置に入れ、合成紙の印刷性を向上し、
最後に巻取装置で巻き取る。上記の方法で得られた厚み
250ミクロン以下の単面紙状面パール光沢合成紙は、
筆記、印刷、包装およびその他の用途に汎用することが
できる。本実施例で選られた厚み60ミクロン、100
ミクロン、120ミクロンの単面紙状面パール光沢合成
紙の物性を表2に示す。 [実施例2]厚み250ミクロン以下の両面紙状面パー
ル光沢合成紙 ポリプロピレン(MFI:2.4)68重量%、静電気
防止剤2重量%を混合した後、ホッパーからサイドフィ
ーダーを持つトゥイン・スクリュー主押出機に入れ、さ
らに炭酸カルシウム粉末15重量%及び二酸化チタン1
5重量%を計量後、それぞれ2つのフィーダーからトゥ
イン・スクリュー主押出機に入れる。また、ポリプロピ
レン(MFI:5)58重量%、ポリエチレン(MF
I:1)12重量%、静電気防止剤2重量%、粘着防止
剤3重量%、紫外線吸収剤1重量%をミキサーで混合し
た後、ホッパーからそれぞれ#1、#2のサイドフィー
ダーを持つトゥイン・スクリュー副押出機2台に入れ
る。さらに炭酸カルシウム粉末12重量%及び二酸化チ
タン12重量%を計量後、それぞれ2つのサイドフィー
ダーから#1、#2トゥイン・スクリュー副押出機に入
れる。押出機の温度を200〜280℃に設定し、三層
共押出方式によりTダイヘッドから押出す。25〜60
℃に設定された冷却ロールを経て、ポリプロピレンパー
ル光沢合成紙板が冷却、成形される。成形された紙板は
縦方向延伸装置に入れ、120〜150℃に加熱した
後、縦方向に4.5倍延伸を行う。延伸後はアニーリン
グを行う。冷却後に再び横方向延伸装置に入れ、155
〜190℃に加熱し、再び横方向に8.5倍延伸を行
う。延伸後はアニーリングを行い、合成紙の収縮率を制
御する。横方向延伸装置を出た後、コロナ処理装置に入
れ、合成紙の印刷性を向上し、最後に巻取装置で巻き取
る。上記の方法で得られた厚み250ミクロン以下の両
面紙状面パール光沢合成紙は、筆記、印刷、包装および
その他の用途に汎用することができる。本実施例で選ら
れた厚み60ミクロン、100ミクロン、150ミクロ
ンの両面紙状面パール光沢合成紙の物性を表3に示す。 [実施例3]厚み250ミクロン以下の両面光沢面パー
ル光沢合成紙 ポリプロピレン(MFI:2.4)62重量%、静電気
防止剤3重量%を混合した後、ホッパーからサイドフィ
ーダーを持つトゥイン・スクリュー主押出機に入れ、さ
らに炭酸カルシウム粉末20重量%及び二酸化チタン1
5重量%を計量後、それぞれ2つのフィーダーからトゥ
イン・スクリュー主押出機に入れる。また、ポリプロピ
レン(MFI:3.0)96重量%、静電気防止剤2重
量%、粘着防止剤2重量%をミキサーで混合した後、そ
れぞれ#1、#2のサイドフィーダーを持つトゥイン・
スクリュー副押出機に入れる。押出機の温度を200〜
280℃に設定し、三層共押出方式によりTダイヘッド
から押出す。15〜60℃に設定された冷却ロールを経
て、ポリプロピレンパール光沢合成紙板が冷却、成形さ
れる。成形された紙板は縦方向延伸装置に入れ、120
〜150℃に加熱した後、縦方向に5倍延伸を行う。延
伸後はアニーリングを行う。冷却後に再び横方向延伸装
置に入れ、150〜185℃に加熱し、再び横方向に9
倍延伸を行う。延伸後はアニーリングを行い、合成紙の
収縮率を制御する。横方向延伸装置を出た後、コロナ処
理装置に入れ、合成紙の印刷性を向上し、最後に巻取装
置で巻き取る。上記の方法で得られた厚み250ミクロ
ン以下の両面光沢面パール光沢合成紙は、筆記、印刷、
包装およびその他の用途に汎用することができる。本実
施例で選られた厚み70ミクロン、110ミクロン、1
40ミクロンの両面光沢面パール光沢合成紙の物性を表
4に示す。
To clearly explain the technical contents of the present invention,
Examples of the present invention in which synthetic papers for writing, printing, packaging and various uses are manufactured are shown below. However, the patent scope of the present invention is not limited to this. Example 1 Single-sided paper-like surface pearly glossy synthetic paper having a thickness of 250 microns or less After mixing 67% by weight of polypropylene (MFI: 2.4) and 3% by weight of an antistatic agent, a twin with a side feeder from a hopper. Put into a screw main extruder, and further add 20% by weight of calcium carbonate powder and titanium dioxide 1
After weighing out 0% by weight, they are fed into a twin screw main extruder, each with a feeder. Also, 62% by weight of polypropylene (MFI: 5) and polyethylene (MFI:
1) 12% by weight, 2% by weight of antistatic agent, 3 anti-sticking agents
% By weight and 1% by weight of an ultraviolet absorber were mixed by a mixer, and then put into a twin screw # 1 sub-extruder having a side feeder from a hopper. Further, after measuring 10% by weight of calcium carbonate powder and 10% by weight of titanium dioxide,
Twin screw # from two feeders each
Put into 2 extruders. Separately, polypropylene (MFI:
2.4) 97% by weight and 3% by weight of an antiblocking agent are mixed by a mixer, and then put into a twin screw # 2 sub-extruder having a side feeder from a hopper. The temperature of the extruder was set at 200 to 280 ° C, and T
Extrude from die head. Via a cooling roll set at 15 to 60 ° C., the polypropylene pearl glossy synthetic paper board is cooled and formed. The formed paper board is placed in a longitudinal stretching device, heated to 120 to 150 ° C., and then stretched 5 times in the longitudinal direction. After stretching, annealing is performed. After cooling, it is again placed in a transverse stretching device, heated to 150 to 185 ° C, and stretched 9 times in the transverse direction again. After stretching, annealing is performed to control the shrinkage of the synthetic paper. After exiting the transverse stretching device, put it in a corona treatment device to improve the printability of synthetic paper,
Finally, it is wound by a winding device. The single-sided paper-like surface pearl glossy synthetic paper having a thickness of 250 microns or less obtained by the above method,
It can be widely used for writing, printing, packaging and other uses. The thickness selected in this example is 60 microns, 100
Table 2 shows the physical properties of the single-sided paper-like surface pearly glossy synthetic paper of 120 μm and 120 μm. Example 2 Double-sided paper-like surface pearly glossy synthetic paper having a thickness of 250 microns or less After mixing 68% by weight of polypropylene (MFI: 2.4) and 2% by weight of an antistatic agent, a twin screw having a side feeder from a hopper. Put into the main extruder, further add 15% by weight of calcium carbonate powder and titanium dioxide 1
After weighing out 5% by weight, each is fed into the twin screw main extruder from two feeders. Further, 58% by weight of polypropylene (MFI: 5) and polyethylene (MFF)
I: 1) 12% by weight, 2% by weight of an antistatic agent, 3% by weight of an anti-blocking agent, and 1% by weight of an ultraviolet absorber were mixed by a mixer, and then twins having # 1 and # 2 side feeders from a hopper, respectively. Put in two screw sub-extruders. Further, after weighing 12% by weight of calcium carbonate powder and 12% by weight of titanium dioxide, they are fed into a # 1, # 2 twin screw sub-extruder from two side feeders, respectively. The temperature of the extruder is set at 200 to 280 ° C., and the extruder is extruded from a T-die head by a three-layer coextrusion method. 25-60
Via a cooling roll set to ° C., the polypropylene pearl glossy synthetic paper board is cooled and formed. The formed paper board is placed in a longitudinal stretching apparatus, heated to 120 to 150 ° C., and then stretched 4.5 times in the longitudinal direction. After stretching, annealing is performed. After cooling, it is put into the transverse stretching device again and 155
Heat to ~ 190 ° C and stretch again 8.5 times in the transverse direction. After stretching, annealing is performed to control the shrinkage of the synthetic paper. After exiting the transverse stretching device, it is put into a corona treatment device to improve the printability of the synthetic paper, and finally wound up by a winding device. The double-sided paper-like surface pearl glossy synthetic paper having a thickness of 250 μm or less obtained by the above method can be widely used for writing, printing, packaging and other uses. Table 3 shows the physical properties of the double-sided paper-like pearly glossy synthetic paper having a thickness of 60 microns, 100 microns, and 150 microns selected in this example. Example 3 Double-sided glossy pearly glossy synthetic paper having a thickness of 250 microns or less After mixing 62% by weight of polypropylene (MFI: 2.4) and 3% by weight of an antistatic agent, a twin screw main unit having a side feeder from a hopper Put into an extruder, and further add 20% by weight of calcium carbonate powder and titanium dioxide 1
After weighing out 5% by weight, each is fed into the twin screw main extruder from two feeders. Also, after mixing 96% by weight of polypropylene (MFI: 3.0), 2% by weight of an antistatic agent and 2% by weight of an anti-adhesive agent by a mixer, a twin / # 2 side feeder having # 1 and # 2 side feeders, respectively.
Put in screw co-extruder. Extruder temperature 200 ~
The temperature is set to 280 ° C., and extruded from the T-die head by a three-layer coextrusion method. Via a cooling roll set at 15 to 60 ° C., the polypropylene pearl glossy synthetic paper board is cooled and formed. The formed paper board is placed in a longitudinal stretching device, and the
After heating to ~ 150 ° C, the film is stretched 5 times in the machine direction. After stretching, annealing is performed. After cooling, it is again placed in a transverse stretching apparatus, heated to 150 to 185 ° C.,
Perform double stretching. After stretching, annealing is performed to control the shrinkage of the synthetic paper. After exiting the transverse stretching device, it is put into a corona treatment device to improve the printability of the synthetic paper, and finally wound up by a winding device. The double-sided glossy pearly glossy synthetic paper having a thickness of 250 microns or less obtained by the above method is written, printed,
Can be widely used for packaging and other uses. The thickness selected in this example is 70 microns, 110 microns, 1
Table 4 shows the physical properties of a 40-micron double-sided glossy pearly glossy synthetic paper.

【0008】[0008]

【発明の効果】本発明の製造方法で得られた合成紙は、
紙状層を縦方向に延伸したが、横方向延伸していないフ
ィルムを一軸延伸層とする従来の製品とは、製造工程、
使用原料の配合に関して大きな差がある。これにより、
天然紙に取って代わり用途を広げることができ、以下の
長所を持つ。紙状層の原料はポリプロピレン、ポリエチ
レン、二酸化チタン、無機粉末を主成分とし、マッドな
光沢を持ち、白色度と遮蔽度は従来の紙を上回る。二軸
延伸の紙状層は優れた剛性を持ち、無機粉末の定着性も
良好で、印刷過程において粉末が脱落することはない。
紙状層及び樹脂層と発泡中間層は同じ延伸率を持ち、紙
の収縮が均一となるため、加熱された面がウェーブ状に
変形しにくい。また同じ延伸率を持つ紙状層と発泡中間
層は剥離しにくい。紙状層及び樹脂層の厚みは1〜30
ミクロンの範囲で副押出機からの押出量により制御する
ことができる(製品の厚みは需要と用途により変化させ
ることができる)。製造工程の生産速度が速く、最大
3.5トン/時間に達する。最大幅は8メートルで、厚
みも25〜250ミクロンと選択範囲が広い。紙状層、
樹脂層及び発泡中間層は側面にフィーダーを持つトゥイ
ン・スクリュー押出機から押出され、原料の混練が均一
なため、製品の厚みを±2%以内に制御することができ
る。押出機は粉末状の無機粉末を側面のフィーダーに入
れることができるため、無機粉末の複合粒(マスターバ
ッチ)だけを使用する必要がなく、原料コストを大幅に
削減できる。このほか、無機粉末の複合粒を単ねじ棒押
出機で生産することもできる。ただし、押出機のねじ棒
のL/D率(長さ/直径)を高めて、原料の混練を均一
にする必要がある。生産コストが低く、市場競争力を有
する。
The synthetic paper obtained by the production method of the present invention is
A conventional product in which a paper-like layer is stretched in the longitudinal direction, but a film that has not been stretched in the transverse direction, is used as a uniaxially stretched layer.
There is a great difference in the composition of the raw materials used. This allows
It can replace natural paper and expand its applications, and has the following advantages. The raw material of the paper-like layer is mainly composed of polypropylene, polyethylene, titanium dioxide, and inorganic powder, has a mad luster, and has higher whiteness and shielding degree than conventional paper. The biaxially stretched paper-like layer has excellent rigidity and good fixability of the inorganic powder, and the powder does not fall off during the printing process.
Since the paper-like layer, the resin layer, and the foamed intermediate layer have the same stretching ratio and the paper shrinks uniformly, the heated surface is unlikely to be deformed into a wave shape. Further, the paper-like layer and the foamed intermediate layer having the same stretching ratio are not easily separated. The thickness of the paper-like layer and the resin layer is 1 to 30
It can be controlled in the micron range by the output from the co-extruder (the thickness of the product can be varied according to demand and application). The production speed of the manufacturing process is fast, reaching up to 3.5 tons / hour. The maximum width is 8 meters and the thickness is 25-250 microns, giving you a wide choice. Paper-like layer,
The resin layer and the foamed intermediate layer are extruded from a twin screw extruder having a feeder on the side surface, and since the kneading of the raw materials is uniform, the thickness of the product can be controlled within ± 2%. Since the extruder can put the powdered inorganic powder into the side feeder, it is not necessary to use only composite particles (master batch) of the inorganic powder, and the raw material cost can be greatly reduced. In addition, composite grains of inorganic powder can be produced by a single screw extruder. However, it is necessary to increase the L / D ratio (length / diameter) of the threaded rod of the extruder to make the kneading of the raw materials uniform. Low production cost and market competitiveness.

【図面の簡単な説明】[Brief description of the drawings]

【図1】三層共押出方式で得られる厚み25〜250ミ
クロン二軸延伸ポリプロピレンパール光沢合成紙の三層
構造(紙状層/発泡中間層/紙状層)
FIG. 1 shows a three-layer structure of a biaxially stretched polypropylene pearl glossy synthetic paper having a thickness of 25 to 250 μm obtained by a three-layer coextrusion method (paper layer / foamed intermediate layer / paper layer).

【図2】三層共押出方式で得られる厚み25〜250ミ
クロン二軸延伸ポリプロピレンパール光沢合成紙の三層
構造(紙状層/発泡中間層/樹脂層)
FIG. 2 shows a three-layer structure of a biaxially stretched polypropylene pearl glossy synthetic paper having a thickness of 25 to 250 μm obtained by a three-layer coextrusion method (paper-like layer / foaming intermediate layer / resin layer).

【図3】三層共押出方式で得られる厚み25〜250ミ
クロン二軸延伸ポリプロピレンパール光沢合成紙の三層
構造(樹脂層/発泡中間層/樹脂層)
FIG. 3 shows a three-layer structure of a biaxially stretched polypropylene pearl glossy synthetic paper having a thickness of 25 to 250 μm obtained by a three-layer coextrusion method (resin layer / foaming intermediate layer / resin layer).

【図4】本発明の製造装置説明図 押出機装置 冷却成形ロール装置 縦方向延伸装置 横方向延伸装置 コロナ処理装置 巻取装置FIG. 4 is an explanatory view of a manufacturing apparatus according to the present invention.

【表1】 [Table 1]

【表2】 [Table 2]

【表3】 [Table 3]

【表4】 [Table 4]

───────────────────────────────────────────────────── 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) B32B 27/10 B32B 27/10 27/32 27/32 Z // B29K 23:00 105:04 105:16 B29L 7:00 9:00 Fターム(参考) 4F073 AA01 BA07 BA08 BA44 BA45 BA46 BA52 BB01 CA21 GA01 GA05 HA05 4F100 AA08A AA08B AA21A AA21B AK04B AK07A AK07B AL05B BA03 BA06 BA07 BA10A BA10B BA25 CA07B CA13A CA13B CA17B CA22A CA22B CA23A DE01A DE01B DJ01 EH202 EJ383 EJ413 EJ553 GB15 JA11A JA20A JK01 JN22 JN30 YY00 4F207 AA04 AA11 AB06 AB09 AB14 AB16 AB20 AC04 AF05 AF14 AG01 AG03 AH53 KA01 KA11 KA17 KB22 KK13 KK52 KL58 KL84 KW41 4F210 AA04 AA11 AB06 AB09 AB14 AB16 AB20 AC04 AF05 AF14 AG01 AG03 AH53 QC06 QD10 QD13 QD31 QD44 QG01 QG12 QG15 QG18 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B32B 27/10 B32B 27/10 27/32 27/32 Z // B29K 23:00 105: 04 105: 16 B29L 7:00 9:00 9:00 F term (reference) 4F073 AA01 BA07 BA08 BA44 BA45 BA46 BA52 BB01 CA21 GA01 GA05 HA05 4F100 AA08A AA08B AA21A AA21B AK04B AK07A AK07B AL05B BA03 BA06 BA07 BA10 CABAA CAB CAB CAB CAB CAB CAB CAB CAB CAB CAB CAB EH202 EJ383 EJ413 EJ553 GB15 JA11A JA20A JK01 JN22 JN30 YY00 4F207 AA04 AA11 AB06 AB09 AB14 AB16 AB20 AC04 AF05 AF14 AG01 AG03 AH53 KA01 KA11 KA17 KB22 KK13 KK52 KL58 KL84 KW41 4F210 AB06A13A06A03 QD13 QD31 QD44 QG01 QG12 QG15 QG18

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】三層共押出方式で得られる厚み25〜25
0ミクロン二軸延伸ポリプロピレン(BOPP)パール
光沢合成紙の製造方法において、アイソタクチック度9
7%以上の高結晶性ポリプロピレン(MFI:0.5〜
8)39〜95重量%及び炭酸カルシウム粉末0〜40
重量%、二酸化チタン0〜20重量%、静電気防止剤1
〜5重量%から成るポリプロピレン樹脂混合物と、ポリ
プロピレン22〜99.5重量%、ポリエチレン樹脂0
〜12重量%、二酸化チタン粉末0〜20重量%、該炭
酸カルシウム粉末0〜40重量%、該静電気防止剤0〜
3重量%、粘着防止剤0.5〜3重量%、紫外線吸収剤
0〜2重量%から成る樹脂混合物を、それぞれサイドフ
ィーダーを持つトゥイン・スクリュー主押出機1台と該
サイドフィーダーを持つトゥイン・スクリュー副押出機
2台のホッパーとフィーダーからそれぞれ入れ、押出機
の温度を180〜280℃に設定し、合流後にTダイヘ
ッドから押出し、パール光沢合成紙シートとし、15〜
60℃の冷却ロールで冷却、成形し、その後二軸延伸す
る紙シートを、150〜150℃に加熱した後、延伸、
アニーリングして縦方向に3〜6倍延伸を行い、さらに
140〜195℃に加熱し、延伸、該アニーリングして
横方向に5〜12倍延伸を行い、次に20〜120KW
効率の高周波コロナ処理を行い、巻取装置で巻き取り、
厚み25〜250ミクロンの紙状層/発泡中間層/該紙
状層、該紙状層/該発泡中間層/樹脂層、該樹脂層/該
発泡中間層/該樹脂層の3種類の三層共押出ポリプロピ
レンパール光沢合成紙とし、塗布用合成紙の塗布紙とす
ることを特徴とする、三層共押出方式で得られる厚み2
5〜250ミクロン二軸延伸ポリプロピレンパール光沢
合成紙の製造方法。
A thickness of 25 to 25 obtained by a three-layer coextrusion method.
In a method for producing a 0-micron biaxially oriented polypropylene (BOPP) pearl glossy synthetic paper, an isotacticity of 9
Highly crystalline polypropylene of 7% or more (MFI: 0.5 to
8) 39-95% by weight and calcium carbonate powder 0-40
Weight%, titanium dioxide 0-20 weight%, antistatic agent 1
-5% by weight of a polypropylene resin mixture, and 22-99.5% by weight of polypropylene and 0% of a polyethylene resin.
-12% by weight, titanium dioxide powder 0-20% by weight, calcium carbonate powder 0-40% by weight, antistatic agent 0
A resin mixture consisting of 3% by weight, 0.5 to 3% by weight of an antiblocking agent, and 0 to 2% by weight of an ultraviolet absorber was mixed with one twin screw main extruder having a side feeder and a twin The screw sub-extruder was put in from two hoppers and feeders, the extruder temperature was set to 180 to 280 ° C, and after merging, it was extruded from a T-die head to form a pearl glossy synthetic paper sheet,
After cooling and forming with a cooling roll at 60 ° C., and then biaxially stretching the paper sheet, the sheet is heated to 150 to 150 ° C., and then stretched.
Annealing, stretching 3 to 6 times in the machine direction, further heating to 140 to 195 ° C, stretching, annealing, stretching in the transverse direction 5 to 12 times, and then 20 to 120 KW
Efficient high-frequency corona treatment, winding by winding device,
Three types of three layers: a paper layer having a thickness of 25 to 250 microns / foaming intermediate layer / the paper layer, the paper layer / the foaming intermediate layer / the resin layer, the resin layer / the foaming intermediate layer / the resin layer. Co-extruded polypropylene pearl glossy synthetic paper and coated paper of coating synthetic paper, characterized in that the thickness obtained by the three-layer co-extrusion method is 2
A method for producing 5-250 micron biaxially oriented polypropylene pearl glossy synthetic paper.
JP01536599A 1999-01-25 1999-01-25 Method for producing 25-250 micron biaxially oriented polypropylene (BOPP) pearl gloss synthetic paper obtained by three-layer coextrusion method Expired - Lifetime JP3623681B2 (en)

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EP1231054A2 (en) 2001-02-09 2002-08-14 Yupo Corporation Stretched film of void-containing thermoplastic resin and process for producing the same
US7041243B2 (en) * 2003-10-27 2006-05-09 Nan Ya Plastics Corp. 5-layer co-extruded biaxial-oriented polypropylene synthetic paper and its production process
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EP1231054A3 (en) * 2001-02-09 2004-01-21 Yupo Corporation Stretched film of void-containing thermoplastic resin and process for producing the same
US7094460B2 (en) 2002-05-24 2006-08-22 Eastman Kodak Company Imaging element with improved surface and stiffness
US7041243B2 (en) * 2003-10-27 2006-05-09 Nan Ya Plastics Corp. 5-layer co-extruded biaxial-oriented polypropylene synthetic paper and its production process
JP2010052345A (en) * 2008-08-29 2010-03-11 Dainippon Printing Co Ltd Method of manufacturing decorative sheet with hydrophilic property
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JP2013010931A (en) * 2011-05-31 2013-01-17 Tbm Co Ltd Method for producing inorganic substance powder highly-oriented thin film sheet
US9492964B2 (en) 2011-05-31 2016-11-15 Tbm Co., Ltd. Method for producing inorganic substance powder highly-oriented thin film sheet
US10363701B2 (en) 2011-05-31 2019-07-30 Tbm Co., Ltd. Method for producing inorganic substance powder highly-oriented thin film sheet
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JP2014058139A (en) * 2012-09-19 2014-04-03 Nan Ya Plastics Corp Method for producing biaxially oriented polypropylene synthetic paper on which printing ink is quickly dried and which is environment-friendly

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