JPH0596599A - Manufacture of composite tube of fluoroelastomer - Google Patents

Manufacture of composite tube of fluoroelastomer

Info

Publication number
JPH0596599A
JPH0596599A JP3290660A JP29066091A JPH0596599A JP H0596599 A JPH0596599 A JP H0596599A JP 3290660 A JP3290660 A JP 3290660A JP 29066091 A JP29066091 A JP 29066091A JP H0596599 A JPH0596599 A JP H0596599A
Authority
JP
Japan
Prior art keywords
tube
molding machine
continuously
fluorine
extrusion molding
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.)
Withdrawn
Application number
JP3290660A
Other languages
Japanese (ja)
Inventor
Isao Takeshita
以佐夫 竹下
Hideo Furubayashi
秀雄 古林
Masataka Isogawa
昌孝 五十川
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP3290660A priority Critical patent/JPH0596599A/en
Publication of JPH0596599A publication Critical patent/JPH0596599A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To use the title composite tube preferably as a tool having flexibility and transferring ultra-pure water, etc., by a method wherein a fluorine plastic elastomer is extrusion-molded in a tubular shape by a first extrusion molding machine and cooled and dried, and coated with adhesives, and a general-purpose flexible thermoplastic resin is extrusion-molded onto an outer circumferential surface by a second extrusion molding machine. CONSTITUTION:A fluorine thermoplastic elastomer is extruded in a tubular shape from a first extrusion molding machine 1. An extruded tube 2 is cooled with a cooling device 3 continuously, and dried continuously by a drier 4. The dried tube 2 is forwarded to an adhesive coater 5, and the surface of the tube 2 is coated continuously with adhesives. The tube 2 coated with adhesives is passed in the crosshead-die 7 of a second extrusion molding machine 6 installed at an approximately right angle in the progressive direction of the tube 2, thus extrusion-coating the outer circumferential surface of the tube 2 with a general-purpose flexible thermoplastic resin, then manufacturing a composite tube 10.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はフッ素系複合チューブの
製造方法に関し、更に詳しくは、特に超純水等の移送用
に好適なフッ素系複合チューブの製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a fluorine-based composite tube, and more particularly to a method for producing a fluorine-based composite tube suitable for transferring ultrapure water or the like.

【0002】[0002]

【従来の技術】近年の半導体素子関連工業の著しい発展
にともない、超純水の使用量が増加するとともに超純水
を移送するパイプの需要が急激に高まってきている。従
来、超純水の移送用の器材としてパイプを使用する提案
が多くなされてきたが、その一つに、たとえば超純水の
水質を汚染させないためにフッ化ビニリデン重合体(以
下、PVDFという)などのフッ素系熱可塑性樹脂を材
料としたパイプを使用する試みがある。しかし、これら
の樹脂は非常に高価であるため、パイプの内周面のみを
これらの樹脂層としパイプの外周面を含む大部分の材料
として塩化ビニル系樹脂やABS樹脂などの廉価な樹脂
を使用する改良方法が提案されている。
2. Description of the Related Art With the recent remarkable development of the semiconductor device-related industry, the amount of ultrapure water used has increased and the demand for pipes for transferring ultrapure water has increased rapidly. Conventionally, many proposals have been made to use a pipe as a device for transferring ultrapure water. One of them is, for example, a vinylidene fluoride polymer (hereinafter referred to as PVDF) in order to prevent contamination of the water quality of ultrapure water. There is an attempt to use a pipe made of a fluorine-based thermoplastic resin such as. However, since these resins are extremely expensive, inexpensive resin such as vinyl chloride resin or ABS resin is used as most of the material including the outer peripheral surface of the pipe with these resin layers only on the inner peripheral surface of the pipe. An improved method is proposed.

【0003】このような2種類の材料を組み合わせたパ
イプは、たとえば特開昭61−171983号公報や実
開昭61−164730号公報に開示されている。特に
実開昭61−164730号公報には、内周面層と外周
面層との界面接着を改良するため、1)内周面層の材料
として使用するPVDF及び外周面層の材料として使用
する汎用熱可塑性樹脂の一方または両方に、エチレン性
不飽和カルボン酸エステルを共重合させるか、あるいは
エチレン性不飽和カルボン酸エステルの重合体または他
の共重合可能な単量体との共重合体を含有させる方法、
2)内周面層と外周面層との間に接着層(接着剤、粘着
剤など)を設ける方法などが提示されている。しかしな
がら、超純水の移送用器材としてパイプを使用すると、
その敷設工事に際し、直線部の施工には特に問題はない
が、曲線部では継手などを使用する複雑な施工が必要で
あるので、曲線部でも自由に且つ簡便に施工できるパイ
プの代替器材が望まれていた。
Such a pipe in which two kinds of materials are combined is disclosed in, for example, Japanese Patent Laid-Open No. 61-171983 and Japanese Utility Model Laid-Open No. 61-164730. In particular, in Japanese Utility Model Application Laid-Open No. 61-164730, in order to improve the interfacial adhesion between the inner peripheral surface layer and the outer peripheral surface layer, 1) PVDF used as the material of the inner peripheral surface layer and the material of the outer peripheral surface layer are used. One or both of the general-purpose thermoplastic resins is copolymerized with an ethylenically unsaturated carboxylic acid ester, or a polymer of an ethylenically unsaturated carboxylic acid ester or a copolymer with another copolymerizable monomer is used. Method of inclusion,
2) A method of providing an adhesive layer (adhesive, pressure-sensitive adhesive, etc.) between the inner peripheral surface layer and the outer peripheral surface layer is proposed. However, if a pipe is used as a device for transferring ultrapure water,
There is no particular problem in the construction of the straight part in the laying work, but complicated construction using joints etc. is required in the curved part, so an alternative device for pipes that can be freely and easily constructed even in curved parts is desired. It was rare.

【0004】一方、2層パイプに関する実開昭61−1
64730号公報に提示されている方法、すなわち2つ
の層の接着を改良するために内周面層の材料であるPV
DFなどのフッ素系熱可塑性樹脂へのエチレン性不飽和
カルボン酸エステル成分の共重合法や該エステルの重合
体のブレンド法により含有させる1)の方法には、フッ
素系熱可塑性樹脂の超純水に対する非汚染性を悪化させ
る問題があり、また、この問題を回避するために外周面
層の汎用熱可塑性樹脂だけを上記の方法で変性させると
2層間の接着が不充分になるという問題がある。また、
実開昭61−164730号公報は、2層間に接着層を
設ける2)の方法について、押出成形法によって接着層
を設ける具体的な方法を開示していない。
On the other hand, Japanese Utility Model Laid-Open No. 61-1 regarding a two-layer pipe.
No. 64730, PV, which is the material of the inner peripheral surface layer to improve the adhesion of the two layers.
The method 1) of incorporating the ethylenically unsaturated carboxylic acid ester component into a fluorine-based thermoplastic resin such as DF by a copolymerization method or a blending method of a polymer of the ester includes ultrapure water of the fluorine-based thermoplastic resin. However, if only the general-purpose thermoplastic resin of the outer peripheral surface layer is modified by the above method in order to avoid this problem, the adhesion between the two layers becomes insufficient. . Also,
Japanese Utility Model Application Laid-Open No. 61-164730 does not disclose a specific method for providing an adhesive layer between two layers 2) by providing an adhesive layer by an extrusion molding method.

【0005】[0005]

【発明が解決しようとする課題】本発明は、従来の超純
水移送用器材に関する下記の二つの課題をともに解決す
ることを目的とするものである。 1)曲線部での煩雑な施工を余儀なくさせられるパイプ
の代替器材の開発。 2)フッ素系熱可塑性樹脂からなる内周面層と汎用熱可
塑性樹脂からなる外周面層との間に強固な接着層を設け
る方法の開発。
SUMMARY OF THE INVENTION It is an object of the present invention to solve both of the following two problems associated with conventional equipment for transferring ultrapure water. 1) Development of alternative equipment for pipes that can complicate the construction of curved sections. 2) Development of a method for providing a strong adhesive layer between the inner peripheral surface layer made of a fluoroplastic and the outer peripheral surface layer made of a general-purpose thermoplastic resin.

【0006】[0006]

【課題を解決するための手段】すなわち、本発明は2機
の押出成形機を使用して、第1の押出成形機によりフッ
素系熱可塑性エラストマーを連続的にチューブ状に押出
成形し該チューブを連続的に冷却し乾燥させた後、、該
チューブ表面に接着剤を連続的に塗布して該チューブの
進行方向にほぼ直角に設置した第2の押出成形機のクロ
スヘッド・ダイの中を通過させ、第2の押出成形機によ
り汎用軟質熱可塑性樹脂を該チューブの外周面に押出成
形させることを特徴とするフッ素系複合チューブの製造
方法を内容とするものである。
That is, the present invention uses two extruders to continuously extrude a fluorinated thermoplastic elastomer into a tube by the first extruder to form the tube. After being continuously cooled and dried, an adhesive was continuously applied to the surface of the tube and passed through a crosshead die of a second extruder, which was installed almost at right angles to the traveling direction of the tube. Then, the method for producing a fluorine-based composite tube is characterized in that a general-purpose soft thermoplastic resin is extruded on the outer peripheral surface of the tube by a second extruder.

【0007】本発明で使用するフッ素系熱可塑性エラス
トマーとは、フッ素系ソフトセグメントとフッ素系ハー
ドセグメントとのブロック共重合体からなり、たとえば
フッ素系ソフトセグメントとしてのフッ化ビニリデン−
ヘキサフルオロプロピレンランダム共重合体とフッ素系
ハードセグメントとしてのテトラフルオロエチレン−エ
チレンランダム共重合体とのブロック共重合体、フッ素
系ソフトセグメントとしてのフッ化ビニリデン−ヘキサ
フルオロプロピレンランダム共重合体とフッ素系ハード
セグメントとしてのフッ化ビニリデン重合体とのブロッ
ク共重合体などで、これらは単独又は2種以上組み合わ
せて用いられる。
The fluorine-based thermoplastic elastomer used in the present invention comprises a block copolymer of a fluorine-based soft segment and a fluorine-based hard segment. For example, vinylidene fluoride as the fluorine-based soft segment.
Block copolymer of hexafluoropropylene random copolymer and tetrafluoroethylene-ethylene random copolymer as a fluorine-based hard segment, vinylidene fluoride-hexafluoropropylene random copolymer and fluorine-based as a fluorine-based soft segment A block copolymer with a vinylidene fluoride polymer as a hard segment and the like, which are used alone or in combination of two or more kinds.

【0008】本発明で使用する汎用軟質熱可塑性樹脂と
は軟質塩化ビニル系樹脂組成物、オレフィン系樹脂など
である。軟質塩化ビニル系樹脂組成物とは、塩化ビニル
樹脂及び塩化ビニル単量体とこれと共重合可能な単量体
との共重合体からなる塩化ビニル系樹脂群から選ばれる
少なくとも1種に可塑剤を添加した組成物であり、これ
らには必要に応じて、ニトリルブタジエンゴム、エチレ
ン−酢酸ビニル共重合体(以下、EVAという)などの
エラストマーや炭酸カルシウム、タルク、クレイなどの
無機充填剤を配合することができる。またオレフィン系
樹脂とは、EVA、エチレン−(メタ)アクリル酸アル
キルエステル(アルキル基の炭素数:4〜8)共重合
体、塩素化ポリエチレンなどである。これらは単独又は
2種以上組み合わせて用いられる。
The general-purpose soft thermoplastic resins used in the present invention include soft vinyl chloride resin compositions and olefin resins. The soft vinyl chloride resin composition means at least one plasticizer selected from the vinyl chloride resin group consisting of a vinyl chloride resin and a copolymer of a vinyl chloride monomer and a monomer copolymerizable therewith. Are added, and if necessary, an elastomer such as nitrile butadiene rubber and ethylene-vinyl acetate copolymer (hereinafter referred to as EVA) and an inorganic filler such as calcium carbonate, talc and clay are compounded. can do. The olefin-based resin is EVA, ethylene- (meth) acrylic acid alkyl ester (alkyl group carbon number: 4 to 8) copolymer, chlorinated polyethylene, or the like. These are used alone or in combination of two or more.

【0009】本発明のフッ素系複合チューブの製造方法
を、製造設備を示す図1に基づいて説明する。第1の押
出成形機1からフッ素系熱可塑性エラストマーをチュー
ブ状に押出す。押し出されたチューブ2を冷却装置3に
より連続的に冷却した後乾燥装置4により連続的に乾燥
する。冷却装置3としては、冷却用の水槽の中をチュー
ブを通過させる方式のもの、冷却水をチューブにシャワ
ーリングする方式のもの等を用いる。乾燥装置4として
は、ヒーターや温風吹付機等を用いる。乾燥したチュー
ブ2を接着剤塗布装置5に送り、チューブの表面に接着
剤を連続的に塗布する。接着剤塗布装置5としては、た
とえば図3に示した如く、スプレーガン9により接着剤
8をチューブ2の表面にスプレーする方式のもの、接着
剤槽の中をチューブを通過させる方式のもの等を用い
る。
A method of manufacturing the fluorine-based composite tube of the present invention will be described with reference to FIG. 1 showing manufacturing equipment. The fluorine-based thermoplastic elastomer is extruded from the first extruder 1 into a tube shape. The extruded tube 2 is continuously cooled by the cooling device 3 and then continuously dried by the drying device 4. As the cooling device 3, a system of passing a tube through a cooling water tank, a system of showering cooling water on the tube, or the like is used. As the drying device 4, a heater, a hot air blowing machine, or the like is used. The dried tube 2 is sent to the adhesive application device 5, and the adhesive is continuously applied to the surface of the tube. As the adhesive application device 5, for example, as shown in FIG. 3, a system of spraying the adhesive 8 onto the surface of the tube 2 by a spray gun 9, a system of passing the tube through an adhesive tank, or the like is used. To use.

【0010】次いで、接着剤を塗布したチューブ2を、
該チューブの進行方向に対して略直角に設置した第2の
押出成形機6のクロスヘッド・ダイ7の中を通過させ、
この第2の押出成形機6により汎用軟質熱可塑性樹脂8
をチューブ2の外周面に押出被覆して複合チューブ10
とする。
Next, the tube 2 coated with the adhesive is
Passing through the crosshead die 7 of the second extruder 6 installed at a substantially right angle to the traveling direction of the tube,
The general-purpose soft thermoplastic resin 8 is made by the second extruder 6.
Of the composite tube 10 by extrusion coating the outer peripheral surface of the tube 2.
And

【0011】上記の如くして、図2に示す如き、フッ素
系熱可塑性エラストマー層11、接着剤層12及び汎用
軟質熱可塑性樹脂層13の順序で積層された複合チュー
ブが得られる。
As described above, as shown in FIG. 2, a composite tube in which the fluorine-based thermoplastic elastomer layer 11, the adhesive layer 12, and the general-purpose soft thermoplastic resin layer 13 are laminated in this order is obtained.

【0012】[0012]

【実施例】以下、本発明を実施例に基づき更に詳しく説
明するが、本発明はこれらに限定されるものではない。 実施例1 第1の40mmφ押出成形機(池貝鉄工株式会社製、FS
40)のシリンダー温度を230〜280℃に設定し、
該押出成形機のホッパーに、ソフトセグメントとしての
フッ化ビニリデン−ヘキサフルオロプロピレンランダム
共重合体とハードセグメントとしてのテトラフルオロエ
チレン−エチレンランダム共重合体とをブロック共重合
させた比重1.89(ASTM D792)、融点22
0℃(ASTM D3418)のフッ素系熱可塑性エラ
ストマーを投入して、内径44mm、外径46mmのチュー
ブを押出成形し、このチューブを冷却水のシャワーリン
グにより連続的に冷却した後、温風を吹き付けて連続的
に乾燥させ、次いで予め主剤と硬化剤とを1:1の重量
比で均一になるまで充分に混合した接着剤(セメダイン
株式会社製、EP−001)を図3に示す塗布器により
該チューブ表面に連続的に塗布して、該チューブの進行
方向に直角に設置した第2の50mmφ押出成形機(池貝
鉄工株式会社製、FS50)のクロスヘッド・ダイの中
を通過させた。
The present invention will be described in more detail based on the following examples, but the invention is not intended to be limited thereto. Example 1 First 40 mmφ extruder (FS manufactured by Ikegai Tekko KK
Set the cylinder temperature of 40) to 230-280 ° C,
In the hopper of the extruder, a vinylidene fluoride-hexafluoropropylene random copolymer as a soft segment and a tetrafluoroethylene-ethylene random copolymer as a hard segment were block-copolymerized with a specific gravity of 1.89 (ASTM). D792), melting point 22
A 0 ° C (ASTM D3418) thermoplastic fluorinated elastomer is added to extrude a tube having an inner diameter of 44 mm and an outer diameter of 46 mm, and the tube is continuously cooled by a shower ring of cooling water and then blown with hot air. And continuously dried, and then an adhesive (EP-001, manufactured by Cemedine Co., Ltd.) in which the main agent and the curing agent were sufficiently mixed in advance in a weight ratio of 1: 1 to be uniform was applied by an applicator shown in FIG. The coating was continuously applied to the surface of the tube and passed through a crosshead die of a second 50 mmφ extrusion molding machine (FS50 manufactured by Ikegai Tekko KK) installed at a right angle to the traveling direction of the tube.

【0013】一方、第2の押出成形機のシリンダー温度
を155〜185℃に設定し、該押出成形機のホッパー
に鉛系熱安定剤(堺化学工業株式会社製、トリベースT
L7000)を配合した平均重合度1250(JIS
K6721)の塩化ビニル樹脂(鐘淵化学工業株式会社
製、カネビニールS1003)100重量部に対し、ジ
−2−エチルヘキシルフタレート80重量部及び炭酸カ
ルシウム20重量部を配合した軟質塩化ビニル樹脂組成
物を投入して押出し、クロスヘッド・ダイを通過してい
る接着剤を表面に塗布された該フッ素系熱可塑性エラス
トマーのチューブの外周面に該軟質塩化ビニル樹脂組成
物を約2mmの肉厚に接着させて押出成形し、内径44m
m、外径50mmの複合チューブを得た。
On the other hand, the cylinder temperature of the second extruder is set to 155 to 185 ° C., and the hopper of the extruder is charged with a lead-based heat stabilizer (Tribase T manufactured by Sakai Chemical Industry Co., Ltd.).
L7000) blended with an average degree of polymerization of 1250 (JIS
K6721) vinyl chloride resin (Kanefuchi Chemical Co., Ltd., Kanevinyl S1003) 100 parts by weight of di-2-ethylhexyl phthalate 80 parts by weight and calcium carbonate 20 parts by weight of a soft vinyl chloride resin composition. The flexible vinyl chloride resin composition is adhered to the outer peripheral surface of the fluorothermoplastic elastomer tube whose surface is coated with the adhesive passing through the crosshead die and having a thickness of about 2 mm. Extrusion molding, inner diameter 44m
A composite tube with m and an outer diameter of 50 mm was obtained.

【0014】実施例2 実施例1で使用した設備を使用して、第1の押出成形機
のシリンダー温度を230〜280℃に設定し、該押出
成形機のホッパーに、実施例1で使用したものと同一の
フッ素系熱可塑性エラストマーを投入して、内径44m
m、外径46mmのチューブを押出成形し、このチューブ
を冷却水のシャワーリングにより連続的に冷却した後、
温風を吹き付けて連続的に乾燥させ、次いで実施例1で
使用した接着剤と同一の接着剤を塗布器によりチューブ
表面に連続的に塗布して、該チューブの進行方向に直角
に設置した第2の押出成形機のクロスヘッド・ダイの中
を通過させた。
Example 2 Using the equipment used in Example 1, the cylinder temperature of the first extruder was set to 230-280 ° C., and the hopper of the extruder was used in Example 1. The same fluorine-based thermoplastic elastomer as that used is added, and the inner diameter is 44 m.
After extruding a tube with m and an outer diameter of 46 mm and continuously cooling this tube with a shower ring of cooling water,
Hot air was blown to dry continuously, and then the same adhesive as that used in Example 1 was continuously applied to the tube surface by an applicator, and the tube was placed at right angles to the traveling direction of the tube. It was passed through the crosshead die of a No. 2 extruder.

【0015】一方、第2の押出成形機のシリンダー温度
を130〜145℃に設定し、該押出成形機のホッパー
にメルトインデックス(190℃、10Kg/cm2)30g
/10分、酢酸ビニル含量33重量%のEVAを投入し
て押出し、クロスヘッド・ダイを通過している接着剤を
表面に塗布された該フッ素系熱可塑性エラストマーのチ
ューブの外周面に該EVAを約2mmの肉厚に接着させて
押出成形し、内径44mm、外径50mmの複合チューブを
得た。
On the other hand, the cylinder temperature of the second extruder is set to 130 to 145 ° C. and the melt index (190 ° C., 10 Kg / cm 2 ) 30 g is set in the hopper of the extruder.
/ 10 minutes, EVA having a vinyl acetate content of 33% by weight is charged and extruded, and the EVA that has passed through the crosshead die is applied to the outer peripheral surface of the tube of the fluorine-based thermoplastic elastomer coated on the surface. A composite tube having an inner diameter of 44 mm and an outer diameter of 50 mm was obtained by adhering to a wall thickness of about 2 mm and extruding.

【0016】比較例1 2機の押出成形機と1基の共通のヘッド・ダイよりなる
設備を使用して、第1の40mmφ押出成形機(池貝鉄工
株式会社製、FS40)のシリンダー温度を210〜2
40℃に設定し、該押出成形機のホッパーに、実施例1
で使用したものと同一のフッ素系熱可塑性エラストマー
100重量部に対し、メタクリル酸メチルを主成分とす
る共重合体であって、該共重合体0.4gを含む100
mlのトルエン溶液の30℃で測定した比粘度が1.4で
ある共重合体(鐘淵化学工業株式会社製、カネエース
PA−20)を20重量部配合したフッ素系熱可塑性エ
ラストマー組成物を投入して押出し、同時に第2の50
mmφ押出成形機(池貝鉄工株式会社製、FS50)のシ
リンダー温度を155〜185℃に設定し、該押出成形
機のホッパーに、実施例1で使用したものと同一の軟質
塩化ビニル樹脂組成物を投入して押出し、これらの押出
物を共通のヘッド・ダイ(設定温度:240℃)に導入
して第1の押出成形機による押出物が内周面層として1
mmの肉厚に、第2の押出成形機による押出物が外周面層
として2mmの肉厚に形成された内径44mm、外径50mm
の複合チューブを得た。
COMPARATIVE EXAMPLE 1 A first 40 mmφ extruder (FS40 manufactured by Ikegai Tekko KK) was operated at a cylinder temperature of 210 by using an equipment consisting of two extruders and a common head die. ~ 2
Example 1 was set in the hopper of the extruder set at 40 ° C.
100 parts by weight of the same fluorine-based thermoplastic elastomer as used in 1., which is a copolymer containing methyl methacrylate as a main component and containing 0.4 g of the copolymer.
A copolymer having a specific viscosity of 1.4 in ml of a toluene solution measured at 30 ° C. (Kaneace Chemical Co., Ltd.
PA-20) was mixed with 20 parts by weight of a fluorine-containing thermoplastic elastomer composition and extruded, and at the same time, the second 50
A cylinder temperature of an mmφ extruder (FS50, manufactured by Ikegai Tekko Co., Ltd.) was set to 155 to 185 ° C., and the same soft vinyl chloride resin composition as that used in Example 1 was placed in the hopper of the extruder. After being charged and extruded, these extrudates are introduced into a common head die (set temperature: 240 ° C.), and the extrudate produced by the first extruder is used as an inner peripheral surface layer.
The inner diameter is 44 mm and the outer diameter is 50 mm, and the extrudate produced by the second extruder has a thickness of 2 mm and has a thickness of 2 mm as the outer peripheral surface layer.
A composite tube of

【0017】比較例2 比較例1で使用した設備を使用して、第1の押出成形機
のシリンダー温度を230〜280℃に設定し、該押出
成形機のホッパーに、実施例1で使用したものと同一の
フッ素系熱可塑性エラストマーを投入して押出し、同時
に第2の押出成形機のシリンダー温度を155〜185
℃に設定し、該押出成形機のホッパーに、実施例1で使
用したものと同一の軟質塩化ビニル樹脂組成物100重
量部に対し、比較例1で使用したものと同一のメタクリ
ル酸メチル系共重合体を20重量部配合した軟質塩化ビ
ニル樹脂組成物を投入して押出し、これらの押出物を共
通のヘッド・ダイ(設定温度:250℃)に導入して第
1の押出成形機による押出物が内周面層として1mmの肉
厚に、第2の押出成形機による押出物が外周面層として
2mmの肉厚に形成された内径44mm、外径複合50mmの
複合チューブを得た。
Comparative Example 2 Using the equipment used in Comparative Example 1, the cylinder temperature of the first extruder was set to 230-280 ° C. and the hopper of the extruder was used in Example 1. The same fluoro-thermoplastic elastomer as that used is charged and extruded, and at the same time, the cylinder temperature of the second extruder is set to 155 to 185.
C. and 100 parts by weight of the same soft vinyl chloride resin composition as used in Example 1 was added to the hopper of the extruder, and the same methyl methacrylate-based copolymer as used in Comparative Example 1 was used. A soft vinyl chloride resin composition containing 20 parts by weight of a polymer is charged and extruded, and these extrudates are introduced into a common head die (set temperature: 250 ° C.) and extruded by a first extruder. To obtain a composite tube having an inner diameter of 44 mm and an outer diameter of 50 mm, in which the inner peripheral surface layer was 1 mm thick and the extruded product from the second extruder was formed as the outer peripheral surface layer having a thickness of 2 mm.

【0018】実施例1、2及び比較例1、2で得た複合
チューブを切削して内周面層と外周面層との接着面の引
張剪断強度を測定するための試験片を図4に示す形状に
準じて各実施例及び比較例毎に5個ずつ作製し、これら
を23℃の恒温室中に48時間放置後23℃において5
00mm/分の速度で引張り、オートグラフにより接着層
の破壊時の強度を測定し、得られたそれぞれ5個の測定
値の平均値を算出した。測定結果を表1に示す。
FIG. 4 shows a test piece for cutting the composite tubes obtained in Examples 1 and 2 and Comparative Examples 1 and 2 and measuring the tensile shear strength of the bonding surface between the inner peripheral surface layer and the outer peripheral surface layer. Five pieces were prepared for each of the examples and comparative examples according to the shape shown, and these were left in a thermostatic chamber at 23 ° C. for 48 hours and then at 5 ° C.
Tensile at a speed of 00 mm / min, the strength at the time of breaking the adhesive layer was measured by an autograph, and the average value of the obtained five measured values was calculated. The measurement results are shown in Table 1.

【0019】実施例1、2及び比較例1、2で得た複合
チューブを切断して長さ15cmのチューブをそれぞれ3
本作製し、クリーンルーム内で以下の操作を行なって超
純水に対する汚染性を評価した。まず、これらチューブ
の内面を全有機炭素濃度(以下、TOCという)が8pp
b である超純水を使用してよく拭き洗いした後、チュー
ブ内に液体洗浄剤(第一クリーンケミカル株式会社製、
商品名:スキャット20X−PF5%溶液)を150ml
入れてチューブの両端を封じ、振盪機で4時間振盪し
た。次いでチューブ内面を該超純水をオーバーフローさ
せながら2時間洗浄した後、チューブ内に超純水を15
0ml充填して両端を封じ60℃で24時間振盪した。こ
れらのチューブ内の超純水のTOCをJIS K055
1の方法により測定し、得られたそれぞれ3個の測定値
の平均値を算出した。参考として、市販の塩化ビニル樹
脂製パイプのTOCも測定した。これらの分析結果を表
1に示す。
The composite tubes obtained in Examples 1 and 2 and Comparative Examples 1 and 2 were cut into tubes each having a length of 15 cm.
This was produced and the following operations were performed in a clean room to evaluate the contamination with ultrapure water. First, the total organic carbon concentration (hereinafter referred to as TOC) is 8 pp on the inner surface of these tubes.
After wiping well with ultrapure water which is b, liquid cleaner (Daiichi Clean Chemical Co., Ltd.,
Product name: Scat 20X-PF5% solution) 150ml
The tube was put in, both ends of the tube were sealed, and the tube was shaken for 4 hours on a shaker. Then, the inner surface of the tube was washed for 2 hours while allowing the ultrapure water to overflow, and then the ultrapure water was placed in the tube for 15 hours.
It was filled with 0 ml, sealed at both ends, and shaken at 60 ° C. for 24 hours. The TOC of ultrapure water in these tubes is specified by JIS K055.
The measurement was performed by the method 1 and the average value of the obtained three measured values was calculated. As a reference, the TOC of a commercially available vinyl chloride resin pipe was also measured. The results of these analyzes are shown in Table 1.

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【発明の効果】以上に述べた通り、本発明の方法によ
り、フッ素系熱可塑性エラストマーからなる内周面層
と、汎用軟質熱可塑性樹脂からなる外周面層との間に接
着剤層を設けた複合チューブは、柔軟性を有し曲線部の
敷設工事の施工が容易であるので超純水等を移送する器
材として好適に使用でき工業的に価値が高い。
As described above, according to the method of the present invention, the adhesive layer is provided between the inner peripheral surface layer composed of the fluorine-based thermoplastic elastomer and the outer peripheral surface layer composed of the general-purpose soft thermoplastic resin. The composite tube has flexibility and is easy to lay a curved portion, so that it can be suitably used as a device for transferring ultrapure water or the like, and is industrially valuable.

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

【図1】本発明に用いる製造設備の一例を示す概略図で
ある。
FIG. 1 is a schematic view showing an example of manufacturing equipment used in the present invention.

【図2】本発明のフッ素系複合チューブの概略断面図で
ある。
FIG. 2 is a schematic sectional view of a fluorine-based composite tube of the present invention.

【図3】実施例1及び2で用いた接着剤塗布器の概略図
である。
FIG. 3 is a schematic view of an adhesive applicator used in Examples 1 and 2.

【図4】フッ素系複合チューブの接着部分の引張剪断強
度測定用試験片の形状を示す概略図である。
FIG. 4 is a schematic view showing the shape of a test piece for measuring tensile shear strength of an adhesive portion of a fluorine-based composite tube.

【符号の説明】[Explanation of symbols]

1 第1押出成形機 2 チューブ 3 冷却装置 4 乾燥装置 5 接着剤塗布装置 6 第2押出成形機 7 クロスヘッド・ダイ 8 接着剤 9 スプレーガン 10 複合チューブ 11 フッ素系熱可塑性エラストマー層 12 接着剤層 13 汎用軟質熱可
塑性樹脂層
DESCRIPTION OF SYMBOLS 1 1st extrusion molding machine 2 Tube 3 Cooling apparatus 4 Drying apparatus 5 Adhesive application apparatus 6 2nd extrusion molding machine 7 Crosshead die 8 Adhesive 9 Spray gun 10 Composite tube 11 Fluorine-based thermoplastic elastomer layer 12 Adhesive layer 13 General-purpose soft thermoplastic resin layer

───────────────────────────────────────────────────── 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 19:00 4F ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location // B29K 19:00 4F

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 2機の押出成形機を使用して、第1の押
出成形機によりフッ素系熱可塑性エラストマーを連続的
にチューブ状に押出成形し該チューブを連続的に冷却し
乾燥させた後、、該チューブ表面に接着剤を連続的に塗
布して該チューブの進行方向にほぼ直角に設置した第2
の押出成形機のクロスヘッド・ダイの中を通過させ、第
2の押出成形機により汎用軟質熱可塑性樹脂を該チュー
ブの外周面に押出成形させることを特徴とするフッ素系
複合チューブの製造方法。
1. A fluoroplastic elastomer is continuously extruded into a tube shape by a first extruder using two extruders, and the tube is continuously cooled and dried. , The adhesive is continuously applied to the surface of the tube, and the adhesive is installed at a right angle to the traveling direction of the tube.
Of the extrusion molding machine, and a general-purpose soft thermoplastic resin is extruded on the outer peripheral surface of the tube by a second extrusion molding machine.
【請求項2】 フッ素系熱可塑性エラストマーがフッ素
系ソフトセグメントとフッ素系ハードセグメントとのブ
ロック共重合体である請求項1記載の製造方法。
2. The production method according to claim 1, wherein the fluorinated thermoplastic elastomer is a block copolymer of a fluorinated soft segment and a fluorinated hard segment.
【請求項3】 汎用軟質熱可塑性樹脂が軟質塩化ビニル
系樹脂組成物及びオレフィン系樹脂からなる群より選択
される少なくとも1種である請求項1又は2記載の製造
方法。
3. The method according to claim 1, wherein the general-purpose soft thermoplastic resin is at least one selected from the group consisting of a soft vinyl chloride resin composition and an olefin resin.
JP3290660A 1991-10-09 1991-10-09 Manufacture of composite tube of fluoroelastomer Withdrawn JPH0596599A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3290660A JPH0596599A (en) 1991-10-09 1991-10-09 Manufacture of composite tube of fluoroelastomer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3290660A JPH0596599A (en) 1991-10-09 1991-10-09 Manufacture of composite tube of fluoroelastomer

Publications (1)

Publication Number Publication Date
JPH0596599A true JPH0596599A (en) 1993-04-20

Family

ID=17758848

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3290660A Withdrawn JPH0596599A (en) 1991-10-09 1991-10-09 Manufacture of composite tube of fluoroelastomer

Country Status (1)

Country Link
JP (1) JPH0596599A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995011940A1 (en) * 1993-10-29 1995-05-04 Daikin Industries, Ltd. Thermoplastic resin composition and laminate made therefrom
JP2004506548A (en) * 2000-08-23 2004-03-04 スリーエム イノベイティブ プロパティズ カンパニー Method for producing multilayer product having fluororesin layer and elastomer layer
JP2009061401A (en) * 2007-09-06 2009-03-26 Gunze Ltd Fiber structure for filtration filter and method for manufacturing the same
CN114728486A (en) * 2019-11-15 2022-07-08 美国圣戈班性能塑料公司 Multilayer pipe and method for producing same

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995011940A1 (en) * 1993-10-29 1995-05-04 Daikin Industries, Ltd. Thermoplastic resin composition and laminate made therefrom
US5891538A (en) * 1993-10-29 1999-04-06 Baikin Industries, Ltd. Thermoplastic resin composition and laminate comprising the same
JP2004506548A (en) * 2000-08-23 2004-03-04 スリーエム イノベイティブ プロパティズ カンパニー Method for producing multilayer product having fluororesin layer and elastomer layer
JP2009061401A (en) * 2007-09-06 2009-03-26 Gunze Ltd Fiber structure for filtration filter and method for manufacturing the same
CN114728486A (en) * 2019-11-15 2022-07-08 美国圣戈班性能塑料公司 Multilayer pipe and method for producing same
JP2023502379A (en) * 2019-11-15 2023-01-24 サン-ゴバン パフォーマンス プラスティックス コーポレイション Multilayer pipe and its manufacturing method

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