JPS6052950B2 - Method for manufacturing laminate - Google Patents

Method for manufacturing laminate

Info

Publication number
JPS6052950B2
JPS6052950B2 JP54133292A JP13329279A JPS6052950B2 JP S6052950 B2 JPS6052950 B2 JP S6052950B2 JP 54133292 A JP54133292 A JP 54133292A JP 13329279 A JP13329279 A JP 13329279A JP S6052950 B2 JPS6052950 B2 JP S6052950B2
Authority
JP
Japan
Prior art keywords
resin
elastomer
layer
base material
coating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP54133292A
Other languages
Japanese (ja)
Other versions
JPS5656846A (en
Inventor
信義 福田
優治 小宮
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.)
Toppan Inc
Original Assignee
Toppan Printing 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 Toppan Printing Co Ltd filed Critical Toppan Printing Co Ltd
Priority to JP54133292A priority Critical patent/JPS6052950B2/en
Publication of JPS5656846A publication Critical patent/JPS5656846A/en
Publication of JPS6052950B2 publication Critical patent/JPS6052950B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C66/00General aspects of processes or apparatus for joining preformed parts
    • B29C66/70General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material
    • B29C66/71General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material characterised by the composition of the plastics material of the parts to be joined

Description

【発明の詳細な説明】 本発明は、布、不織布等へのポリマー防水ライニング
処理に係るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to polymer waterproof lining treatments for fabrics, nonwovens, and the like.

従来これらの素材に対し防水性の付与表面物性の向上を
目的とする樹脂のライニング処理は、ポリマー溶液によ
るコーティング、又は含浸さらにはポリマーフィルムを
該基材へ接着剤又は熱プレス等の手段によるラミネート
法などにより行われているが、これらの方法によつて布
、不織布等多孔質基材にコーティングする場合、基材に
対する溶液の浸透が大きく、均一なライニング皮膜を得
る為には過大な塗布量を施さねばならず、基材のもつ風
合及び通気性を著しくそこねるばかりでなく、不要な溶
剤を乾燥させる乾燥設備と溶剤回収装置が必要である等
製造コストが大きい。防火災等安全上の問題さらに製品
に溶剤が残留しやすい等の問題があつた。又熱可塑性エ
ラストマーをシリコーン剥離紙等に塗布乾燥後、フィル
ムとし、該基材にラミネートする手法も提案されている
が、やはり前記の如き問題がさけ難く、又剥離紙が高価
である為コストの高いものとなる。さらに熱可塑性エラ
ストマーを該基材に溶融押出コーティングを行う手法も
考えられるが、エラストマー単層で押出しコーティング
を行つた場合、薄層化が困難である為やはり基材の風合
、通気性がそこなわれる等製品物性上の問題、樹脂目付
量(単位布帛当りの塗布量)が大きい為製造コストが大
きくなる。さらに単層押出しコーティングでは膜厚20
μ程度が限度であるが、薄くコーティングを行つた場合
溶融樹脂のもつ熱量が小さくなる為、冷却ロールと圧着
ロールとの接触により瞬時に冷却される為基材のくい込
みが小さく強力な接着が得にくい。又熱可塑性エラスト
マーは、金属の冷却ロールにブロッキングしやすい為作
業性を著しくそこねる等の問題があつた。 本発明は、
布、不織布、紙等の基材上に共押出しコーティング法に
より熱可塑性エラストマーとこのエラストマーに剥離性
を有する樹脂の少くとも2層以上の積層溶融皮膜をコー
ティングを行い、しかる後前記樹脂を剥離する事により
熱可塑性エラストマーライニング皮膜を得るものである
Conventionally, resin lining treatments for the purpose of imparting waterproof properties to these materials and improving surface properties have included coating or impregnation with a polymer solution, and lamination of a polymer film onto the base material using adhesives, heat pressing, or other means. However, when coating porous substrates such as cloth and nonwoven fabrics using these methods, the solution penetrates into the substrate greatly, and an excessive coating amount is required to obtain a uniform lining film. This not only significantly impairs the texture and air permeability of the base material, but also requires drying equipment and solvent recovery equipment to dry unnecessary solvents, resulting in high production costs. There were safety issues such as fire prevention, as well as problems such as the tendency for solvents to remain in the product. A method has also been proposed in which a thermoplastic elastomer is coated on a silicone release paper or the like, dried, formed into a film, and then laminated to the base material. However, the same problems as mentioned above are unavoidable, and the cost is low because the release paper is expensive. It will be expensive. Another option is to melt-extrude coat the base material with a thermoplastic elastomer, but if you extrude coat a single layer of elastomer, it is difficult to make the layer thinner, so the texture and breathability of the base material will be affected. Problems with physical properties of the product, such as sagging, and high resin weight (coating amount per unit fabric) increase manufacturing costs. In addition, for single-layer extrusion coating, the film thickness is 20
The limit is approximately μ, but when coating thinly, the amount of heat held by the molten resin becomes smaller, and as it is instantly cooled by contact between the cooling roll and the pressure roll, strong adhesion is achieved with less penetration into the base material. Hateful. Further, thermoplastic elastomers have problems such as being prone to blocking on metal cooling rolls, which significantly impairs workability. The present invention
Coating a laminated molten film of at least two layers of a thermoplastic elastomer and a resin that has releasability to the elastomer by a coextrusion coating method on a base material such as cloth, nonwoven fabric, or paper, and then peeling off the resin. As a result, a thermoplastic elastomer lining film is obtained.

共押出しコーティング法とは、2個以上の押出機より押
出された樹脂がコンバイニングアダプター或いはブラッ
クボックスと呼ばれる樹脂合流部を経て積層化された樹
脂を、Tダイより押出すタイプ、又は2個以上の押出機
より押出された樹脂がTダイ内部で積層化され押出され
るマルチマニホールドタイプさらにダイ外で積層化され
るマルチスロットタイプ等の押出機−Tダイより押出さ
れた積層樹脂を冷却ロールと圧着ロールとにより基材上
へ圧着固化されるものであるが、共押出し法を利用する
事により溶融膜の保持及び引取性が改善され、単層に於
いては不可能な薄層エラストマーコーティングが可能と
なる。この時前記樹脂層はコーティング完了後剥離され
、基地へのエラストマーライニング皮膜を得る為エラス
トマーと樹脂の層間強度は、これを容易に剥し得る必要
がある。この様に二層以上の積層された溶融皮膜をコー
ティングすることは、樹脂層によつて溶融膜の保持が出
来るため、エラストマー層を非常に薄くする事が可能で
あり、従来単層では不可能とされていた1〜20μ程度
の薄層コーティングが可能となる。
The coextrusion coating method is a type in which the resin extruded from two or more extruders passes through a resin confluence part called a combining adapter or black box, and then the laminated resin is extruded from a T die, or two or more extruders. Multi-manifold type extruders, in which the resin extruded from the T-die is laminated inside the T-die and extruded, and multi-slot type extruders, in which the resin is laminated outside the die. The molten film is pressed and solidified onto the base material using a pressure roll, but by using the coextrusion method, the retention and take-up properties of the molten film are improved, and thin-layer elastomer coating, which is impossible with a single layer, is possible. It becomes possible. At this time, the resin layer is peeled off after coating is completed, and in order to obtain an elastomer lining film on the base, the interlayer strength between the elastomer and the resin must be such that it can be easily peeled off. Coating with a laminated molten film of two or more layers in this way allows the elastomer layer to be made extremely thin because the molten film can be held by the resin layer, which was previously impossible with a single layer. Thin layer coating of about 1 to 20 μm, which was previously thought to be possible, is now possible.

さらに溶融樹脂の熱が全層に蓄積されている為一方の層
即ちエラストマー層を十分に薄層化しても溶融皮膜全体
の熱量は大きいものとなり、冷却ロール及び圧着ロール
による基材への圧着時、基材への投錨効果によるくい込
みも大きいものとなり接着も秀れたものが得られる。さ
らにエラストマー皮膜はコーティング時に於いては樹脂
層に皮覆されているため、冷却ロールとの接触によるブ
ロッキングも防止でき、作業性も大きく向上する。本発
明に使用できる熱可塑性エラストマーとは、例えば、2
官能ポリオール、グリコールとジイソシアネートをNC
O/0H=0.95〜1.1の割合により反応せしめる
事により製造される、熱可塑性、ポリウレタン樹脂、結
晶性ハードセグメントのポリエステルと非晶性ソフトセ
グメントのポリエーテルブロック共重合より成る熱可塑
性ポリエ.ステルエラストマー、1−2ポリブタジエン
、スチレン−ブタジエンブロック共重合樹脂(SBS)
、スチレン−イソプレンブロック共重合樹脂(SIS)
等であるがコーティング皮膜の表面物性、さらにポリオ
レフィンとの剥離の容易性等を−考慮するとポリウレタ
ン、ポリエステル系エラストマーが好適である。
Furthermore, since the heat of the molten resin is accumulated in all layers, even if one layer, that is, the elastomer layer, is made sufficiently thin, the amount of heat in the entire molten film is large, and when it is pressed onto the base material by the cooling roll and pressure roll. , the penetration into the base material due to the anchoring effect is large, and excellent adhesion can be obtained. Furthermore, since the elastomer film is covered with a resin layer during coating, blocking due to contact with the cooling roll can be prevented, and workability is greatly improved. The thermoplastic elastomer that can be used in the present invention includes, for example, 2
NC functional polyols, glycols and diisocyanates
Thermoplastic, polyurethane resin, manufactured by reacting at a ratio of O/0H = 0.95 to 1.1, consisting of a polyester block copolymerization of a crystalline hard segment polyester and an amorphous soft segment Polie. Stell elastomer, 1-2 polybutadiene, styrene-butadiene block copolymer resin (SBS)
, styrene-isoprene block copolymer resin (SIS)
However, polyurethane and polyester elastomers are preferred in consideration of the surface physical properties of the coating film and the ease of peeling from polyolefin.

樹脂層としては、例えばポリオレフィンを用いることが
でき、例えば高圧法ポリエチレン(LDPE)、中低圧
法ポリエチレン(MDPE,HDPE)、ポリプロピレ
ン、ポリメチルペンテン、ポリブテン、ポリスチレン、
ポリ塩化ビニル及びそれらの共重合樹脂である。
As the resin layer, for example, polyolefin can be used, such as high pressure polyethylene (LDPE), medium and low pressure polyethylene (MDPE, HDPE), polypropylene, polymethylpentene, polybutene, polystyrene,
Polyvinyl chloride and their copolymer resins.

尚本発明の製造に供する装置は、前述の共押出コーティ
ング装置を用いるが、薄層化が容易に出来るコンバイニ
ングアダプター方式又はマルチマニホールド方式が特に
有効である。
Although the above-mentioned coextrusion coating apparatus is used for the production of the present invention, a combining adapter system or a multi-manifold system that can easily form a thin layer is particularly effective.

この様にして製造されるエラストマーライニン・グ皮膜
は、最低膜厚、おおよそ1μ程度まで可能であり、全厚
15〜20μ以上の範囲内でエラストマー層厚みは任意
にコントロールできる。
The elastomer lining film produced in this way can have a minimum thickness of approximately 1 μm, and the elastomer layer thickness can be controlled as desired within the range of a total thickness of 15 to 20 μm or more.

さらにこの時基材に対する接着をより高める目的でポリ
ウレタン系、イソシアネート系、ポリアミド系、ゴム系
、等の接着剤もしくはアンカー剤により基材への表面処
理を行つてもよいが、この場合あくまで基材のもつ風合
及び通気性をそこなわない範囲の塗布量にとどめるべき
である。本発明の手法により得られるエラストマーライ
ニング皮膜は、前述の如く薄層化が可能で、しかも基材
への含浸が少ない事が特徴であり、従つて冒頭に述べた
他の製法に較べ、基材のもつ通気性、風合等は維持しや
すいが、さらに通気性、風合、外観等を改良する為にエ
ラストマー層の全部又は一部に発泡処理を加えてもよい
Furthermore, at this time, the surface of the base material may be treated with a polyurethane-based, isocyanate-based, polyamide-based, rubber-based, etc. adhesive or anchor agent in order to further increase the adhesion to the base material. The amount of application should be kept within a range that does not impair the texture and breathability of the product. The elastomer lining film obtained by the method of the present invention can be made into a thin layer as described above, and is characterized by less impregnation into the base material. The air permeability, texture, etc. of the elastomer layer can be easily maintained, but in order to further improve the air permeability, texture, appearance, etc., all or part of the elastomer layer may be subjected to foaming treatment.

発泡処理はアゾジカーボンアミド、アゾイソブチロニト
リル、ジニトロペンタメチレンテトラミン、バラトルエ
ンスルホニルヒドラジド、4,4″オキシヒースベンゼ
ンスルホニルヒドラジド等の有機発泡剤、重炭酸ナトリ
ウム、炭酸アンモニウム、重炭酸アンモニウム等の無機
系発泡剤等を原料のエラストマー中に加えることにより
行う事が出来るが、押出しと同時に発泡させる一次発泡
、発泡剤分解温度より低温度で押出し、コーティング後
加熱処理、又は水、溶剤等により発泡剤を洗い流して行
う2次発泡何れも可能であるが、発泡させた気泡の方向
性のない事、気泡の均一性が良い事等2次発泡処理の方
が秀れている。この様に本発明は、既に公知の手法によ
るライニングとは異なり、共押出しコーティング法を適
用している為、薄層コーティングが容易であり、通気性
、風合等物性上秀れたものであるばかりでなく、基本的
には無溶剤加工である為製品の残留溶剤の懸念がなく、
乾燥装置、溶剤コストの削減が可能である。
Foaming treatment uses organic blowing agents such as azodicarbonamide, azoisobutyronitrile, dinitropentamethylenetetramine, valatoluenesulfonyl hydrazide, 4,4'' oxyheath benzenesulfonyl hydrazide, sodium bicarbonate, ammonium carbonate, ammonium bicarbonate, etc. This can be done by adding an inorganic blowing agent, etc. to the raw elastomer, but it can be done by primary foaming at the same time as extrusion, extrusion at a temperature lower than the blowing agent decomposition temperature, heat treatment after coating, or by using water, solvent, etc. Although secondary foaming is possible by washing away the foaming agent, secondary foaming is superior because the foamed bubbles are not directional and the bubbles are more uniform. Unlike lining methods that are already known, the present invention uses a coextrusion coating method, so it is easy to coat a thin layer, and it not only has excellent physical properties such as breathability and texture. Since it is basically a solvent-free process, there is no concern about residual solvent in the product.
Drying equipment and solvent costs can be reduced.

又、シリコーン剥離紙等高価な剥離紙を使用せず、安価
なポリオレフィン等の樹脂を用いる上、剥離後の樹脂は
再生して再使用することが可能であり、製造及び材料コ
ストも安価なものとなる。以下、実施例により本発明を
説明する。〈実施例1〉 ポリエステル不織布を基材1とし、第1図の説明図に示
す方法により、この基材1上に熱可塑性ポリウレタンエ
ラストマー(日本ポリウレタン(株)社製、バラプレン
22S)2とメルトインデックス16のポリプロピレン
(三菱油化(株)社製、ノーブレンFL−25F′)3
を積層する。
In addition, it does not use expensive release paper such as silicone release paper, but instead uses inexpensive resin such as polyolefin, and the resin after release can be recycled and reused, resulting in low manufacturing and material costs. becomes. The present invention will be explained below with reference to Examples. <Example 1> A polyester nonwoven fabric was used as the base material 1, and a thermoplastic polyurethane elastomer (Baraprene 22S, manufactured by Nippon Polyurethane Co., Ltd.) 2 and a melt index were coated on this base material 1 by the method shown in the explanatory diagram of FIG. 16 polypropylene (manufactured by Mitsubishi Yuka Co., Ltd., Noblen FL-25F') 3
Laminate.

エラストマー2及び樹脂3は各押出機4,4″から20
0℃の樹脂温度で押出され、ダイ5中で積層された後、
基材1上に施され、冷却ロール6及び圧着ロール7の間
で圧着される。この後、ポリプロピレン皮膜3を剥離し
た。
Elastomer 2 and resin 3 are each extruder 4,4"
After being extruded at a resin temperature of 0°C and laminated in die 5,
It is applied onto the base material 1 and crimped between a cooling roll 6 and a pressure roll 7. After this, the polypropylene film 3 was peeled off.

この時、ポリウレタン層2として10μのものが可能で
あり、ポリプロピレン層3は35μであつた。〈実施例
2〉 ポリエステルー綿混紡布を基材1とし、熱可塑性ポリエ
ステルエラストマー(東洋紡績(株)社製、ベルプレン
P−70B)をエラストマー2とし、ポリプロピレンを
樹脂3として、第1図の方法によりエラストマー2を基
材1に積層した。
At this time, the polyurethane layer 2 could have a thickness of 10μ, and the polypropylene layer 3 had a thickness of 35μ. <Example 2> The method shown in Fig. 1 was carried out using a polyester-cotton blend fabric as the base material 1, a thermoplastic polyester elastomer (manufactured by Toyobo Co., Ltd., Belprene P-70B) as the elastomer 2, and polypropylene as the resin 3. The elastomer 2 was laminated on the base material 1 by the following steps.

エラストマー層2の厚みは5μ、ポリプロピレン層の厚
みは40μであつた。
The thickness of the elastomer layer 2 was 5μ, and the thickness of the polypropylene layer was 40μ.

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

図面は本発明の実施例を示し、第1図はその説明図であ
る。 1・・・・・・基材、2・・・・・・エラストマー、3
・・・・・・エラストマーに剥離性を有する樹脂、4,
4″・・・・・・押出機、5・・・・・・ダイ、6・・
・・・・冷却ロール、7・・・・・・圧着ロール。
The drawings show an embodiment of the present invention, and FIG. 1 is an explanatory diagram thereof. 1... Base material, 2... Elastomer, 3
...Resin with releasability to elastomer, 4,
4″...Extruder, 5...Die, 6...
...Cooling roll, 7...Crimping roll.

Claims (1)

【特許請求の範囲】 1 布、不織布等の多孔質基材上に、熱可塑性エラスト
マーと、このエラストマーに剥離性を有する樹脂とを共
押出法により溶融押出コーティングし、この後前記樹脂
を剥離することを特徴とする積層体の製造方法。 2 樹脂がポリオレフィンであることを特徴とする前記
第1項記載の方法。 3 熱可塑性エラストマーが発泡剤を含んでいることを
特徴とする前記第1項又は第2項記載の方法。
[Claims] 1. Melt extrusion coating a thermoplastic elastomer and a resin that has release properties on this elastomer on a porous substrate such as cloth or nonwoven fabric using a coextrusion method, and then peeling off the resin. A method for manufacturing a laminate, characterized by: 2. The method according to item 1 above, wherein the resin is a polyolefin. 3. The method according to item 1 or 2 above, wherein the thermoplastic elastomer contains a blowing agent.
JP54133292A 1979-10-16 1979-10-16 Method for manufacturing laminate Expired JPS6052950B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54133292A JPS6052950B2 (en) 1979-10-16 1979-10-16 Method for manufacturing laminate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54133292A JPS6052950B2 (en) 1979-10-16 1979-10-16 Method for manufacturing laminate

Publications (2)

Publication Number Publication Date
JPS5656846A JPS5656846A (en) 1981-05-19
JPS6052950B2 true JPS6052950B2 (en) 1985-11-22

Family

ID=15101235

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54133292A Expired JPS6052950B2 (en) 1979-10-16 1979-10-16 Method for manufacturing laminate

Country Status (1)

Country Link
JP (1) JPS6052950B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS581520A (en) * 1981-06-26 1983-01-06 Toppan Printing Co Ltd Method for lining treatment
DE60045339D1 (en) * 1999-09-27 2011-01-20 Du Pont EXTRUSION COATING PROCESS

Also Published As

Publication number Publication date
JPS5656846A (en) 1981-05-19

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