Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH042717B2 - - Google Patents
[go: Go Back, main page]

JPH042717B2 - - Google Patents

Info

Publication number
JPH042717B2
JPH042717B2 JP14217384A JP14217384A JPH042717B2 JP H042717 B2 JPH042717 B2 JP H042717B2 JP 14217384 A JP14217384 A JP 14217384A JP 14217384 A JP14217384 A JP 14217384A JP H042717 B2 JPH042717 B2 JP H042717B2
Authority
JP
Japan
Prior art keywords
aluminum hydroxide
synthetic leather
parts
weight
foam
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
JP14217384A
Other languages
Japanese (ja)
Other versions
JPS6128079A (en
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 filed Critical
Priority to JP14217384A priority Critical patent/JPS6128079A/en
Publication of JPS6128079A publication Critical patent/JPS6128079A/en
Publication of JPH042717B2 publication Critical patent/JPH042717B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
  • Laminated Bodies (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明は、ウレタン樹脂発泡体を中間層とする
合成皮革の製造方法に関するものである。 従来の技術 従来、合成皮革において中間層として用いられ
る樹脂を発泡させる方法として、(1)ガス球体を樹
脂中に分散させ、加熱により破球させ発泡させる
方法、(2)ジメチルホルムアミド(DMF)等の親
水性有機溶剤の溶液に対して行なわれる湿式凝固
法、(3)エマルジヨン樹脂を機械的に発泡させる機
械発泡法、(4)熱分解性の発泡剤を樹脂中に分散さ
せて、発生するガスにより発泡させる発泡剤法、
(5)イソシアネート基と水との反応により発生する
ガスを利用するイソシアネート反応法などが公知
である。 発明が解決しようとする問題点 これらのうち、湿式凝固法は、有機溶剤を使用
するため、排水処理の問題がある。機械発泡法
は、高性能ミキサー等の微細な気泡を得るための
発泡装置が必要であり、かつ、エマルジヨン樹脂
により得た発泡体では樹脂が機械的強度に欠けた
り、気泡剤が合成皮革表面へしみ出したりする等
の問題が残る。ガス球体や発泡剤を用いる方法で
は、発泡温度のコントロールが困難であり、また
発泡体の形態については気泡径が大きく、気泡密
度が小さいという問題がある。イソシアネート基
と水との反応では、加工時の湿度や温度の影響を
受けやすく、発泡体の形態もガス球体や発泡剤を
用いる方法と同様に悪い。 このような現状に鑑み、本発明者らは、イソシ
アネート反応法において従来問題となつている点
について改良すべく研究を重ねた結果、本発明に
到つたものである。 問題点を解決するための手段 すなわち、本発明は、合成皮革の製造に用いる
発泡性接着剤として、ポリマー末端基にイソシア
ネート基を有するポリエステル型もしくはポリエ
ーテル型ウレタン、水含有マイクロカプセル、及
び触媒からなる発泡性組成物を用い、これに水酸
化アルミニウムを添加することを特徴とする合成
皮革の製造方法を提供するものである。 従来、ウレタン樹脂発泡体を得る方法として、
ポリマー末端基としてイソシアネート基を有する
ポリマー、水を包接した熱分解性のマイクロカプ
セル及び触媒の存在下に、加熱発泡する方法が工
業的に実施されている。しかし、従来方法では、
発泡形態が球形で、発泡工程が安全性のないもの
であつた。また、増量剤として炭酸カルシウム等
の使用がなされているが、これは単なる増量剤で
しかなかつた。 しかして、本発明者らは、上記組成物中に水酸
化アルミニウムを添加することによつて、発泡形
態を従来の球形独立発泡(気泡径:約100μ)か
ら、微細でち密な偏平状の独立気泡を有する発泡
体(気泡径:50μ以下)に変化せしめると共に、
これに付随した種々の利点を見出したものであ
る。すなわち、水酸化アルミニウムを添加するこ
との第1の利点は、その反応促進作用により、加
熱発泡に要する時間を著しく短縮できる点であ
り、大巾な生産性の向上が得られる。これに加え
て安価な水酸化アルミニウムの充填効果と発泡層
の厚みが増加することなどによるウレタンの節減
効果が得られる。また微細な発泡構造による風合
の柔軟化も本発明の主な利点である。 水酸化アルミニウムの種類としては、平均粒子
径1〜30μの範囲のものが適当であり、粒子径が
30μ以上では塗工ムラや塗工スジが発生するので
好ましくない。添加量としては、ポリウレタン
100重量部に対して15部〜50重量部の範囲が適当
であり、15重量部以下では加熱発泡時間の短縮効
果が得られず、50重量部以上では基布との接着力
が低下する欠点がある。 実施例 以下、実施例によつて本発明を更に説明する。 離型紙上に、下記処方の表皮層ポリウレタン樹
脂塗料を100g/m2となる様に塗布し、これを120
℃にて2分間乾燥し、表皮層を形成させた。次
に、この表面層上に下記処方の発泡層ポリウレタ
ン樹脂塗料を200g/m2となる様に塗布した。こ
れを140℃にて30秒間加熱発泡させ、直ちに基布
を貼り合せた後、120℃で2分間熱処理した。冷
却後、あるいは60℃にて12時間熟成後、離型紙を
剥離し、合成皮革を得た。 表皮層樹脂組成 ラツクスキンU−2216〔セイコー化成(株):ウレタ
ンポリマー〕 ……100重量部 メチルエチルケトン ……30重量部 顔 料 ……14重量部 発泡層樹脂組成 エコール−7100〔東洋ポリマー(株):ウレタンポリ
マー〕 ……100重量部 EP−620〔東洋ポリマー(株):マイクロカプセル〕
……4重量部 AD−D−14G〔東洋ポリマー(株):触媒〕
……1重量部 C−308〔住友アルミニウム(株):水酸化アルミニウ
ム〕 ……30重量部 メチルエチルケトン ……2重量部 水酸化アルミニウムの平均粒径は8μであつた。 比較例として、上記発泡層樹脂組成から水酸化
アルミニウムを除いたものを比較例1とし、また
水酸化アルミニウムの代わりに炭酸カルシウム
(平均粒径5μ)を用いたものを比較例2として合
成皮革を作製した。 本発明例と比較例の合成皮革の物性を測定し、
その結果を第1表に示す。
INDUSTRIAL APPLICATION FIELD The present invention relates to a method for producing synthetic leather using a urethane resin foam as an intermediate layer. Conventional technology Conventionally, methods for foaming resin used as an intermediate layer in synthetic leather include (1) a method in which gas spheres are dispersed in the resin and the spheres are broken and foamed by heating, (2) dimethylformamide (DMF), etc. Wet coagulation is carried out on a solution of a hydrophilic organic solvent, (3) mechanical foaming is carried out by mechanically foaming the emulsion resin, and (4) thermally decomposable blowing agent is dispersed in the resin. Foaming agent method that uses gas to foam;
(5) Isocyanate reaction methods that utilize gas generated by the reaction between isocyanate groups and water are well known. Problems to be Solved by the Invention Among these, the wet coagulation method uses an organic solvent, so there is a problem in wastewater treatment. The mechanical foaming method requires a foaming device such as a high-performance mixer to obtain fine bubbles, and foams obtained from emulsion resins may lack mechanical strength or the foaming agent may reach the surface of the synthetic leather. Problems such as seepage remain. In the method using gas spheres or a foaming agent, it is difficult to control the foaming temperature, and there are also problems with the form of the foam, such as large cell diameters and low cell density. The reaction between isocyanate groups and water is easily affected by humidity and temperature during processing, and the morphology of the foam is also poor, similar to methods using gas spheres or blowing agents. In view of the current situation, the present inventors conducted repeated research to improve the conventional problems in the isocyanate reaction method, and as a result, they arrived at the present invention. Means for Solving the Problems That is, the present invention provides a foamable adhesive for use in the production of synthetic leather made from polyester or polyether urethane having an isocyanate group at the polymer terminal group, water-containing microcapsules, and a catalyst. The present invention provides a method for producing synthetic leather, which is characterized by using a foamable composition and adding aluminum hydroxide thereto. Conventionally, as a method for obtaining urethane resin foam,
A method of heating and foaming in the presence of a polymer having an isocyanate group as a polymer terminal group, a thermally decomposable microcapsule containing water, and a catalyst has been carried out industrially. However, in the conventional method,
The foamed form was spherical and the foaming process was unsafe. In addition, calcium carbonate and the like have been used as a bulking agent, but this is nothing more than a bulking agent. By adding aluminum hydroxide to the above composition, the present inventors changed the foam form from the conventional spherical closed foam (cell diameter: approximately 100μ) to fine, dense, flat, independent foam. In addition to changing it into a foam with bubbles (cell diameter: 50μ or less),
We have discovered various advantages associated with this. That is, the first advantage of adding aluminum hydroxide is that the time required for heating and foaming can be significantly shortened due to its reaction promoting effect, resulting in a significant improvement in productivity. In addition, the filling effect of inexpensive aluminum hydroxide and the effect of saving urethane can be obtained by increasing the thickness of the foam layer. Furthermore, the softening of the texture due to the fine foam structure is also a major advantage of the present invention. The suitable type of aluminum hydroxide is one with an average particle size of 1 to 30μ;
If it is 30μ or more, coating unevenness and coating streaks will occur, which is not preferable. As for the amount added, polyurethane
A range of 15 to 50 parts by weight per 100 parts by weight is appropriate; if it is less than 15 parts by weight, the effect of shortening the heat foaming time cannot be obtained, and if it is more than 50 parts by weight, the adhesive strength with the base fabric will decrease. There is. Examples Hereinafter, the present invention will be further explained with reference to Examples. On the release paper, apply a skin layer polyurethane resin paint with the following formulation to 100g/ m2 , and
It was dried at ℃ for 2 minutes to form a skin layer. Next, a foam layer polyurethane resin paint having the following formulation was applied onto this surface layer at a coating weight of 200 g/m 2 . This was heat-foamed at 140°C for 30 seconds, a base fabric was immediately attached, and then heat treated at 120°C for 2 minutes. After cooling or aging at 60°C for 12 hours, the release paper was peeled off to obtain synthetic leather. Skin layer resin composition Luxkin U-2216 [Seiko Kasei Co., Ltd.: Urethane polymer] ...100 parts by weight Methyl ethyl ketone ...30 parts by weight Pigment ...14 parts by weight Foam layer resin composition Ecole-7100 [Toyo Polymer Co., Ltd.: Urethane polymer] ...100 parts by weight EP-620 [Toyo Polymer Co., Ltd.: Microcapsule]
...4 parts by weight AD-D-14G [Toyo Polymer Co., Ltd.: Catalyst]
...1 part by weight C-308 [Sumitomo Aluminum Co., Ltd.: Aluminum hydroxide] ...30 parts by weight Methyl ethyl ketone ...2 parts by weight The average particle size of the aluminum hydroxide was 8 μm. As comparative examples, synthetic leather was prepared by removing aluminum hydroxide from the above foam layer resin composition as Comparative Example 1, and using calcium carbonate (average particle size 5μ) instead of aluminum hydroxide as Comparative Example 2. Created. Measuring the physical properties of the synthetic leather of the present invention example and comparative example,
The results are shown in Table 1.

【表】 水酸化アルミニウムの添加により、発泡所要時
間の短縮、発泡層の厚み増加、風合の柔軟化など
の効果が得られ、比較例に比較してより優れた合
成皮革が得られた。 尚、上記の実施例で得られた合成皮革の断面構
造を第1図に、また比較例1で得られた合成皮革
の断面構造を第2図に示す。
[Table] By adding aluminum hydroxide, effects such as shortening the foaming time, increasing the thickness of the foam layer, and softening the texture were obtained, and better synthetic leather was obtained than in the comparative example. The cross-sectional structure of the synthetic leather obtained in the above example is shown in FIG. 1, and the cross-sectional structure of the synthetic leather obtained in Comparative Example 1 is shown in FIG.

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

第1図は、本発明の水酸化アルミニウム添加で
得られた合成皮革の断面構造を示す模式図であ
り、第2図は、水酸化アルミニウムの添加のない
(比較例1)場合の合成皮革の断面模式図である。 1:表皮層、2:気泡、3:発泡層、4:基
布。
Figure 1 is a schematic diagram showing the cross-sectional structure of synthetic leather obtained by adding aluminum hydroxide according to the present invention, and Figure 2 is a schematic diagram showing the cross-sectional structure of synthetic leather obtained by adding aluminum hydroxide. It is a cross-sectional schematic diagram. 1: skin layer, 2: bubbles, 3: foam layer, 4: base fabric.

Claims (1)

【特許請求の範囲】 1 表皮層、発泡接着剤層、及び基布より構成さ
れる合成皮革において、発泡性接着剤としてポリ
マー末端基にイソシアネート基を有するポリエス
テル型もしくはポリエーテル型ポリウレタン、水
含有マイクロカプセル、及び触媒からなる発泡性
組成物を用い、これに水酸化アルミニウムを添加
することを特徴とする合成皮革の製造方法。 2 添加する水酸化アルミニウムの粒子径が1〜
30μであることを特徴とする特許請求範囲第1項
記載の方法。 3 水酸化アルミニウムの添加量がポリウレタン
100重量部に対して15〜50重量部であることを特
徴とする特許請求範囲第1項記載の方法。
[Scope of Claims] 1. Synthetic leather consisting of a skin layer, a foam adhesive layer, and a base fabric, in which a polyester or polyether polyurethane having an isocyanate group at the polymer end group, a water-containing micro A method for producing synthetic leather, which comprises using a foamable composition comprising a capsule and a catalyst, and adding aluminum hydroxide thereto. 2 The particle size of the aluminum hydroxide to be added is 1~
30μ. The method according to claim 1, wherein 3 The amount of aluminum hydroxide added to polyurethane
The method according to claim 1, characterized in that the amount is 15 to 50 parts by weight per 100 parts by weight.
JP14217384A 1984-07-11 1984-07-11 Manufacture of synthetic leather Granted JPS6128079A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14217384A JPS6128079A (en) 1984-07-11 1984-07-11 Manufacture of synthetic leather

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14217384A JPS6128079A (en) 1984-07-11 1984-07-11 Manufacture of synthetic leather

Publications (2)

Publication Number Publication Date
JPS6128079A JPS6128079A (en) 1986-02-07
JPH042717B2 true JPH042717B2 (en) 1992-01-20

Family

ID=15309053

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14217384A Granted JPS6128079A (en) 1984-07-11 1984-07-11 Manufacture of synthetic leather

Country Status (1)

Country Link
JP (1) JPS6128079A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH086262B2 (en) * 1986-07-31 1996-01-24 バンドー化学株式会社 Synthetic leather manufacturing method
JP6433423B2 (en) * 2013-05-27 2018-12-05 アキレス株式会社 Synthetic leather
KR102286926B1 (en) 2017-02-17 2021-08-06 현대자동차주식회사 Flame retardant polyurethane artificial leather and manufacturing method thereof

Also Published As

Publication number Publication date
JPS6128079A (en) 1986-02-07

Similar Documents

Publication Publication Date Title
US2138081A (en) Process for the production of sponge rubber from aqueous rubber dispersions
JP3274071B2 (en) Method for producing closed-cell sponge rubber
JPS6387286A (en) Sublimation transfer recording paper
CN112227076A (en) A preparation method of crease-free ultrafine fiber synthetic leather based on heat-expandable microspheres
JPH042717B2 (en)
US3582393A (en) Method of producing porous sheet material
US3705118A (en) Process for forming a microporous cellular polyimide
US2604664A (en) Preparation of sponge rubber from foamed latex
US3714307A (en) Aqueous coagulation of salt containing polyurethane to form porous sheet
JPS6335891A (en) Synthetic leather manufacturing method
WO2024082209A1 (en) Novel pickering foam templating-based method for preparing wpu synthetic leather foaming layer
JP3482275B2 (en) Resin composition
JPS60255837A (en) Production of porous body
JPH0345787A (en) Synthetic leather
JPS5926458B2 (en) Method for manufacturing polyolefin foam sheet with polyurethane film
JPS63198970A (en) calcium phosphate hollow sphere
JPS6247454B2 (en)
JPH0218329B2 (en)
JPS63277006A (en) Cosmetics applicator for liquid foundation
JPS5636531A (en) Production of microporous product by wet process
JPS6235516B2 (en)
JPS648088A (en) Production of thermal recording material
JPS635425B2 (en)
JPH0354618B2 (en)
JPS599574B2 (en) Manufacturing method for flexible sheet materials