JPS6335891A - Production of synthetic leather - Google Patents
Production of synthetic leatherInfo
- Publication number
- JPS6335891A JPS6335891A JP18164286A JP18164286A JPS6335891A JP S6335891 A JPS6335891 A JP S6335891A JP 18164286 A JP18164286 A JP 18164286A JP 18164286 A JP18164286 A JP 18164286A JP S6335891 A JPS6335891 A JP S6335891A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- synthetic leather
- expanded
- layer
- polyvinyl chloride
- 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
Links
- 239000002649 leather substitute Substances 0.000 title claims abstract description 28
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000011347 resin Substances 0.000 claims abstract description 45
- 229920005989 resin Polymers 0.000 claims abstract description 45
- 239000004800 polyvinyl chloride Substances 0.000 claims abstract description 18
- 229920000915 polyvinyl chloride Polymers 0.000 claims abstract description 18
- 239000003094 microcapsule Substances 0.000 claims abstract description 16
- 239000011342 resin composition Substances 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 239000004744 fabric Substances 0.000 claims abstract description 6
- 239000004925 Acrylic resin Substances 0.000 claims abstract description 4
- 229920000178 Acrylic resin Polymers 0.000 claims abstract description 4
- 239000002245 particle Substances 0.000 claims abstract description 4
- 229920002803 thermoplastic polyurethane Polymers 0.000 claims abstract description 4
- 239000006260 foam Substances 0.000 claims description 27
- 210000004027 cell Anatomy 0.000 claims description 11
- 210000000497 foam cell Anatomy 0.000 claims description 8
- 238000000034 method Methods 0.000 abstract description 26
- 239000000203 mixture Substances 0.000 abstract description 6
- 238000005187 foaming Methods 0.000 abstract description 4
- 239000004604 Blowing Agent Substances 0.000 abstract description 3
- 239000000853 adhesive Substances 0.000 abstract description 3
- 230000001070 adhesive effect Effects 0.000 abstract description 3
- 238000009835 boiling Methods 0.000 abstract description 3
- 150000001875 compounds Chemical class 0.000 abstract description 3
- 239000004014 plasticizer Substances 0.000 description 8
- 239000004088 foaming agent Substances 0.000 description 7
- 239000003381 stabilizer Substances 0.000 description 6
- 238000001816 cooling Methods 0.000 description 4
- 239000002562 thickening agent Substances 0.000 description 4
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 3
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 3
- 229920002635 polyurethane Polymers 0.000 description 3
- 239000004814 polyurethane Substances 0.000 description 3
- 230000037303 wrinkles Effects 0.000 description 3
- 239000003963 antioxidant agent Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 206010000060 Abdominal distension Diseases 0.000 description 1
- 239000004156 Azodicarbonamide Substances 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 241000156978 Erebia Species 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 1
- 235000019399 azodicarbonamide Nutrition 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 208000024330 bloating Diseases 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- -1 for example Polymers 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000008029 phthalate plasticizer Substances 0.000 description 1
- 229920006264 polyurethane film Polymers 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
Abstract
Description
【発明の詳細な説明】
童1上(1月差団
本発明は合成皮革の製造方法に関し、詳しくは、軽量で
柔軟な発泡層を有する合成皮革を所謂乾式法にて製造す
る方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing synthetic leather, and more particularly, to a method for producing synthetic leather having a lightweight and flexible foam layer by a so-called dry method.
皿米皇弦止
従来、合成皮革の製造方法として、湿式法と乾式法とが
知られている。このうち、乾式法とは、先ず、離型紙丘
に表皮層を形成する樹脂を塗布乾燥させ、その上に樹脂
と発泡剤とを含有する樹脂組成物を塗布し、加熱して、
発泡剤の分解によって発生したガスにて発泡セルを形成
させて、発泡層を形成し、更に、接着剤にて基布を接着
した後、離型紙を剥離することによって製造する方法で
ある。例えば、発泡層を形成する樹脂として、ポリ塩化
ビニルペーストレジンを用いる場合は、レジン100重
量部に対して、可塑剤60〜100重滑部及びアゾシカ
−ボンアミドのような発泡剤2〜5重量部を含む発泡性
樹脂組成物を加熱して、発泡層を形成させる。Conventionally, wet methods and dry methods are known as methods for producing synthetic leather. Among these, the dry method involves first applying and drying a resin to form a skin layer on a release paper mound, then applying a resin composition containing a resin and a foaming agent thereon, and heating it.
This is a manufacturing method in which foam cells are formed using gas generated by decomposition of a foaming agent to form a foam layer, a base fabric is bonded with an adhesive, and a release paper is peeled off. For example, when polyvinyl chloride paste resin is used as the resin forming the foam layer, 60 to 100 parts by weight of a plasticizer and 2 to 5 parts by weight of a foaming agent such as Azocicabonamide are used for 100 parts by weight of the resin. The foamable resin composition containing the above is heated to form a foam layer.
しかし、この乾式法によっては、従来、軽量で且つ柔軟
な発泡層を有する合成皮革を得ることが困難である。特
に、樹脂として、ポリ塩化ビニルペーストレジンを用い
る場合は、その比重が大きいために、得られる合成皮革
が重く、しかも、上記のように、可塑剤を多量に用いる
必要があるために、所謂ぼってりした感触及び外観を有
する。However, conventionally, it has been difficult to obtain synthetic leather having a lightweight and flexible foam layer by this dry method. In particular, when polyvinyl chloride paste resin is used as the resin, its specific gravity is high, so the resulting synthetic leather is heavy, and as mentioned above, it is necessary to use a large amount of plasticizer, resulting in so-called bloating. It has a solid feel and appearance.
他方、発泡層を軽量化するために、発泡セルによる空隙
率を高めるときは、発泡剤の加熱発泡に際して、ガス抜
けが起こって、発泡層が所謂へたりを起こす。On the other hand, when increasing the porosity of the foam cells in order to reduce the weight of the foam layer, gas escape occurs during heating and foaming of the foaming agent, causing the foam layer to sag.
衾肌尤五失旦主立上工至皿用立
そこで、本発明者は、従来の合成皮革における上記した
問題を解決するために鋭意研究した結果、従来の発泡剤
に代えて、熱膨張性マイクロカプセルを含む発泡性樹脂
組成物を用い、これを加熱発泡させることによって、乾
式法にても、湿式法と同等の軽量で且つ柔軟な発泡層を
形成し得ることを見出して、本発明に至ったものである
。Therefore, as a result of intensive research in order to solve the above-mentioned problems with conventional synthetic leather, the inventors of the present invention developed a thermally expandable foaming agent in place of the conventional foaming agent. We have discovered that by using a foamable resin composition containing microcapsules and heating and foaming it, it is possible to form a lightweight and flexible foam layer that is equivalent to the wet method even in a dry method, and has developed the present invention. This is what we have come to.
訓皿立を邂迭達火へq玉役
本発明による合成皮革の製造方法は、基布の上に樹脂発
泡層が積層されてなる合成皮革の製造方法において、樹
脂と平均粒径5〜50μmの熱膨張性マイクロカプセル
とを含む発泡性樹脂組成物を基布上に塗布し、加熱して
、発泡層を形成することを特徴とする。A method for manufacturing synthetic leather according to the present invention is a method for manufacturing synthetic leather in which a resin foam layer is laminated on a base fabric, in which resin and an average particle size of 5 to 50 μm are used. The method is characterized in that a foamable resin composition containing thermally expandable microcapsules is applied onto a base fabric and heated to form a foam layer.
本発明においては、樹脂としては、例えば、ポリ塩化ビ
ニルペーストレジン、ウレタン樹脂、アクリル樹脂等を
用いることができる。樹脂としてポリ塩化ビニルペース
トレジンを用いるときは、発泡性樹脂組成物は、ポリ塩
化ビニルペーストレジン100重量部に対して、可塑剤
50〜100重量部、熱膨張性マイクロカプセル10〜
30重量部及び適宜量の安定剤を含有する。In the present invention, as the resin, for example, polyvinyl chloride paste resin, urethane resin, acrylic resin, etc. can be used. When using polyvinyl chloride paste resin as the resin, the foamable resin composition contains 50 to 100 parts by weight of a plasticizer and 10 to 10 parts by weight of thermally expandable microcapsules based on 100 parts by weight of the polyvinyl chloride paste resin.
Contains 30 parts by weight and an appropriate amount of stabilizer.
可塑剤としては、例えば、フタル酸エステル系可塑剤が
好ましく用いられる。かかる可塑剤の具体例として、例
えば、フタル酸ジブチルやフタル酸ジオクチルを挙げる
ことができる。エポキシ系可塑剤も必要に応じて用いら
れる。安定剤としては、例えば、Ba−Zn系安定剤が
好適であり一1通常、ポリ塩化ビニルベーストレジン1
00重量部に対して1〜3重量部用いられる。As the plasticizer, for example, a phthalate plasticizer is preferably used. Specific examples of such plasticizers include dibutyl phthalate and dioctyl phthalate. Epoxy plasticizers may also be used if necessary. As the stabilizer, for example, a Ba-Zn stabilizer is suitable, and usually a polyvinyl chloride base resin.
1 to 3 parts by weight per 00 parts by weight.
樹脂としてポリ塩化ビニルペーストレジンを含む発泡性
樹脂組成物は、必要に応じて、充填剤、酸化防止剤、増
粘剤、着色剤等の通常の配合剤を適宜量含有していても
よい。The foamable resin composition containing polyvinyl chloride paste resin as the resin may contain appropriate amounts of ordinary compounding agents such as fillers, antioxidants, thickeners, and colorants, as necessary.
また、樹脂としてウレタン樹脂又はアクリル樹脂を含む
発泡性樹脂組成物は、樹脂を10〜30重景%含む樹脂
溶液100重量部に対して、熱膨張性ブイクロカプセル
を10〜30重景部含有する。この場合も、発泡性樹脂
組成物は、必要に応じて、充填剤、酸化防止剤、増粘剤
、着色剤等の通常の配合剤を適宜量含有していてもよい
。In addition, a foamable resin composition containing a urethane resin or an acrylic resin as a resin contains 10 to 30 parts by weight of thermally expandable buiclocapsules per 100 parts by weight of a resin solution containing 10 to 30 parts by weight of the resin. do. In this case as well, the foamable resin composition may contain appropriate amounts of ordinary compounding agents such as fillers, antioxidants, thickeners, and colorants, if necessary.
本発明において用いる熱膨張性マイクロカプセルとは、
熱軟化性樹脂を殻壁とし、内部にブタン等の炭化水素の
ような低沸点有機化合物を含むマイクロカプセルを意味
し、例えば、松本油脂製菓−から「マツモトマイクロス
フェア−」として、平均粒径や殻壁の熱軟化温度の種々
異なるものが市販されている。本発明においては、特に
、平均粒径5〜50μmである熱膨張性マイクロカプセ
ルが好ましく用いられる。更に、用いる樹脂がポリ塩化
ビニルペーストレジンであるときは、殻壁の熱軟化温度
が100〜150℃であるものが好ましい。The thermally expandable microcapsules used in the present invention are:
It refers to microcapsules with a shell wall made of thermoplastic resin and containing a low-boiling organic compound such as a hydrocarbon such as butane inside. Various types of shells with different heat softening temperatures are commercially available. In the present invention, thermally expandable microcapsules having an average particle size of 5 to 50 μm are particularly preferably used. Furthermore, when the resin used is polyvinyl chloride paste resin, it is preferable that the heat softening temperature of the shell wall is 100 to 150°C.
本発明の方法によれば、合成皮革の製造工程において、
かかる熱膨張性マイクロカプセルを含む発泡性樹脂組成
物を離型紙上に塗布し、乾燥し、加熱するとき、熱膨張
性マイクロカプセルの殻壁が熱軟化すると共に、内部の
低沸点化合物が膨張し、次いで、冷却される過程で殻壁
が再凝固して、微細な独立セルからなる均質な発泡層が
形成される。According to the method of the present invention, in the synthetic leather manufacturing process,
When a foamable resin composition containing such thermally expandable microcapsules is applied onto a release paper, dried, and heated, the shell wall of the thermally expandable microcapsules is thermally softened, and the low boiling point compound inside expands. Then, during the cooling process, the shell wall re-solidifies to form a homogeneous foam layer consisting of fine closed cells.
例えば、従来のポリ塩化ビニルペーストレジンを樹脂と
して用いる乾式法によれば、発泡剤を分解して生じるガ
スを樹脂のマトリックス内に内包させることによって、
発泡層を形成する。従って、マトリックスとしての樹脂
は、これを比較的多量に用いることが必要とされるので
、前述したように、発泡層の密度は、通常、0.3〜0
.5 g 7cm3であって、湿式法で得られる発泡層
の密度0.1〜0゜3g/cm3に比べて著しく大きい
。For example, according to the dry method using conventional polyvinyl chloride paste resin as the resin, the gas generated by decomposing the blowing agent is encapsulated within the resin matrix.
Form a foam layer. Therefore, it is necessary to use a relatively large amount of resin as a matrix, so as mentioned above, the density of the foam layer is usually 0.3 to 0.
.. 5 g 7 cm 3 , which is significantly larger than the density of the foamed layer obtained by the wet method, which is 0.1 to 0.3 g/cm 3 .
しかしながら、本発明の方法によれば、発泡性樹脂組成
物を加熱することによって、熱膨張性マイクロカプセル
の殻壁が軟化膨張し、相互に融着し、冷却の過程で殻壁
が凝固して、発泡層を形成するので、樹脂は、膨張した
マイクロカプセルを相互に接合するバインダーとしての
量があれば足りることとなり、従って、本発明の方法に
よれば、従来の乾式法に比べて、用いる樹脂量を大幅に
低減することができる。更に、発泡セルは、膨張したマ
イクロカプセルによって形成されるから、かかる発泡セ
ルは、独立した微細な球状であり、月つ、均質であり、
その結果、従来、乾式法によっては得ることが困難であ
った軽量な発泡層を得ることができる。However, according to the method of the present invention, by heating the foamable resin composition, the shell walls of the thermally expandable microcapsules soften and expand, fuse together, and solidify during the cooling process. , since a foamed layer is formed, the amount of resin is sufficient as a binder to bond the expanded microcapsules to each other. Therefore, according to the method of the present invention, compared to the conventional dry method, The amount of resin can be significantly reduced. Furthermore, since the foamed cells are formed by expanded microcapsules, such foamed cells are independent, finely spherical, round, and homogeneous;
As a result, it is possible to obtain a lightweight foam layer, which has conventionally been difficult to obtain by dry methods.
本発明によれば、通常11発泡セル径が実質的に30〜
100.Ijmであり、セル密度が80〜90%である
軽量で柔軟な発泡層を有する合成皮革を得ることができ
る。尚、ここに、セル密度とは、発泡構造の断面におい
て、発泡セルが占める面積の割合をいう。特に、樹脂と
してポリ塩化ビニルベーストレジンを用いる場合は、密
度0.30〜0゜37 g7cm)の発泡層を得ること
ができ、更に、樹脂量の減少に伴って、必要な可塑剤量
も少量でよいので発泡層には前記した所謂ぼってり怒も
ない。According to the present invention, the normally 11 foam cell diameter is substantially 30 to 30.
100. It is possible to obtain synthetic leather having a lightweight and flexible foam layer with Ijm and a cell density of 80 to 90%. Here, the cell density refers to the ratio of the area occupied by foam cells in the cross section of the foam structure. In particular, when polyvinyl chloride-based resin is used as the resin, it is possible to obtain a foamed layer with a density of 0.30 to 0.37 g (7 cm), and furthermore, as the amount of resin is reduced, the amount of plasticizer required is also small. Therefore, the foam layer does not have the above-mentioned so-called bubbly.
又肌■匹玉
以上のよ・うに、本発明の方法によれば、従来の乾式法
による合成皮革の製造に比べて、用いる樹脂量を大幅に
低減できるので、従来、乾式法によっては得ることが困
難であった軽量な発泡層を存する合成皮革を製造するこ
とができる。しかも、本発明の方法によって得られる発
泡セルは、独立した微細な球状であり、且・つ、均質で
あるので、風合にもすぐれる。Also, as described above, according to the method of the present invention, the amount of resin used can be significantly reduced compared to the production of synthetic leather using the conventional dry method. It is possible to produce synthetic leather with a lightweight foam layer, which has been difficult to produce. In addition, the foamed cells obtained by the method of the present invention have an independent fine spherical shape and are homogeneous, so they have excellent texture.
特に、本発明の方法においで、樹脂として、ポリ塩化ビ
ニルベーストレジンを用いる場合は、湿式法による場合
と同等の密度0.1〜0.3 g 7cm3の軽量な発
泡層を得ることができ、しかも、用いる樹脂量の減少に
伴って必要な可塑剤量も減少するので、発泡層は、所謂
ぼってり感もない。In particular, in the method of the present invention, when polyvinyl chloride-based resin is used as the resin, it is possible to obtain a lightweight foam layer with a density of 0.1 to 0.3 g 7 cm3, which is equivalent to the wet method. Moreover, as the amount of resin used decreases, the amount of plasticizer required also decreases, so the foamed layer does not have a so-called bulky feel.
夫施炭 下記の配合物を用いて、合成皮革を製造;7た。Husband Charcoal Synthetic leather was manufactured using the following formulation; 7.
尚、部数は重量部を示す。Note that the number of parts indicates parts by weight.
ポリ塩化ビニルベーストレジン(重合
度 1650) ioo部ジオクチル
フタレート 80部Ba−Zn系安定剤
FL54 (アデカ・アーガス化学■製)
2部熱膨張性マイクロカプセルF80D
(松本油脂製薬側型、殻壁軟化温度140〜
145℃) 20部増粘剤(白石工
業■製) 4部からなる組成物を用いて
、合成皮革を製造した。Polyvinyl chloride base resin (degree of polymerization 1650) Ioo part Dioctyl phthalate 80 parts Ba-Zn stabilizer FL54 (manufactured by Adeka Argus Chemical ■)
Two-part thermally expandable microcapsule F80D
(Matsumoto Yushi Pharmaceutical side type, shell wall softening temperature 140 to 145°C) Synthetic leather was produced using a composition consisting of 20 parts thickener (manufactured by Shiraishi Kogyo ■) and 4 parts.
離型紙上にポリウレタン溶液(大日精化住萄、■/ザミ
ン2825LP)を塗布、乾燥して、厚さ30μmのポ
リウレタン被膜を形成させた。この上に上記ポリ塩化ビ
ュルゾル配合物を4008/m”の割合にて塗布し、熱
風炉にて170℃で1分間加熱発泡させた。冷却し7た
後、この発泡体層のトにポリウレタン系接着側(大日精
化α岩、17ザミンUD603)を40g/m2の割合
にて塗布し、直ちに起毛布の起毛面をその上に貼り合わ
せ、加圧した後、120℃で2分間加熱乾燥させた。冷
却後、40℃で2日間熟成した後、離型紙を剥離し、厚
さl、 2mmの合成皮革を得た。A polyurethane solution (Dainichisei Kashuo, ■/Zamine 2825LP) was applied onto the release paper and dried to form a polyurethane film with a thickness of 30 μm. The above-mentioned polychlorinated Bursol compound was applied on top of this at a rate of 4008/m'' and heated and foamed in a hot air oven at 170°C for 1 minute. After cooling, the foam layer was coated with polyurethane. Apply adhesive side (Dainichiseika α Rock, 17 Zamin UD603) at a rate of 40 g/m2, immediately paste the raised side of the raised fabric on top, pressurize, and heat dry at 120°C for 2 minutes. After cooling and aging at 40°C for 2 days, the release paper was peeled off to obtain synthetic leather with a thickness of 1 and 2 mm.
得られた合成皮革は、発泡セル径70μm、セル密度8
0%、発泡層の密度0.13 g/cm1であって、極
めて軽量柔軟であり、天然皮革にみられる小じわを有し
、風合にもすぐれるものであった。The obtained synthetic leather has a foam cell diameter of 70 μm and a cell density of 8.
0%, the density of the foam layer was 0.13 g/cm1, it was extremely lightweight and flexible, had fine wrinkles found in natural leather, and had an excellent texture.
比較例1
ポリ塩化ビニルベーストレジン(重合
度 1650) 100
部ジオクチルフタレート 80部Ba
−Zn系安定剤PL54 2部発泡剤
(アゾシカ−ボンアミド) 3部セル調整剤
1部増粘剤
4部からなる組成物を用いた以外は
、実施例1と同様にして、厚さ1.2Hの合成皮革を製
造した。Comparative Example 1 Polyvinyl chloride base resin (degree of polymerization 1650) 100
Part dioctyl phthalate 80 parts Ba
-Zn stabilizer PL54 2 parts Foaming agent (Azosicabonamide) 3 parts Cell conditioner
1 part thickener
Synthetic leather with a thickness of 1.2H was produced in the same manner as in Example 1, except that a composition consisting of 4 parts was used.
得られた合成皮革は、発泡セル径160μm、セル密度
85%、発泡層の密度0.37 g/cm3であって、
重く、硬く、大しわを有していた。The obtained synthetic leather had a foam cell diameter of 160 μm, a cell density of 85%, and a foam layer density of 0.37 g/cm3,
It was heavy, hard, and had large wrinkles.
比較例
ポリウレタン溶液 100部発泡剤(
アゾジカルボンアミド) 5部架橋剤
2部整泡剤
1部からなる配合物を前記ポリ塩化ビ
ニルゾルに代えて用い、加熱発泡温度を140℃とした
以外は、実施例と同様にして、厚さ1.2寵の合成皮革
を製造した。Comparative example polyurethane solution 100 parts blowing agent (
Azodicarbonamide) 5-part crosslinking agent
2-part foam stabilizer
Synthetic leather with a thickness of 1.2 cm was produced in the same manner as in the example except that a mixture consisting of 1 part of polyvinyl chloride sol was used in place of the polyvinyl chloride sol and the heating and foaming temperature was 140°C.
得られた合成皮革は、発泡セル径210μm、セル密度
80%、発泡層の密度0.41 g/cts”であって
、重く、硬く、大じわを有していた。The obtained synthetic leather had a foam cell diameter of 210 μm, a cell density of 80%, and a foam layer density of 0.41 g/cts, and was heavy, hard, and had large wrinkles.
Claims (4)
る合成皮革の製造方法において、樹脂と平均粒径5〜5
0μmの熱膨張性マイクロカプセルとを含む発泡性樹脂
組成物を加熱して、発泡層を形成することを特徴とする
合成皮革の製造方法。(1) In a method for producing synthetic leather in which a resin foam layer and a skin layer are laminated on a base fabric, a resin and an average particle size of 5 to 5
A method for producing synthetic leather, which comprises heating a foamable resin composition containing thermally expandable microcapsules of 0 μm to form a foam layer.
であり、セル密度が80〜90%であることを特徴とす
る特許請求の範囲第1項記載の合成皮革の製造方法。(2) In the foam layer, the foam cell diameter is 30 to 100 μm
The method for producing synthetic leather according to claim 1, wherein the synthetic leather has a cell density of 80 to 90%.
樹脂又はアクリル樹脂であることを特徴とする特許請求
の範囲第1項記載の合成皮革の製造方法。(3) The method for producing synthetic leather according to claim 1, wherein the resin is polyvinyl chloride paste resin, urethane resin, or acrylic resin.
発泡性樹脂組成物を用いて、密度0.1〜0.3g/c
m^3の発泡層を形成することを特徴とする特許請求の
範囲第1項記載の合成皮革の製造方法。(4) Using a foamable resin composition containing polyvinyl chloride paste resin as a resin, the density is 0.1 to 0.3 g/c.
The method for producing synthetic leather according to claim 1, characterized in that a foamed layer of m^3 is formed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61181642A JPH086262B2 (en) | 1986-07-31 | 1986-07-31 | Synthetic leather manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61181642A JPH086262B2 (en) | 1986-07-31 | 1986-07-31 | Synthetic leather manufacturing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6335891A true JPS6335891A (en) | 1988-02-16 |
JPH086262B2 JPH086262B2 (en) | 1996-01-24 |
Family
ID=16104321
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61181642A Expired - Lifetime JPH086262B2 (en) | 1986-07-31 | 1986-07-31 | Synthetic leather manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH086262B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009526117A (en) * | 2006-02-10 | 2009-07-16 | アクゾ ノーベル ナムローゼ フェンノートシャップ | Microsphere |
JP2009540047A (en) * | 2006-06-08 | 2009-11-19 | アクゾ ノーベル ナムローゼ フェンノートシャップ | Microsphere |
CN103375003A (en) * | 2013-07-17 | 2013-10-30 | 成恵民 | Multifunctional soft wall base material production process and formula |
US9062170B2 (en) | 2006-02-10 | 2015-06-23 | Akzo Nobel N.V. | Microspheres |
CN104790222A (en) * | 2014-01-16 | 2015-07-22 | 辛俊兴 | Plush imitating synthetic leather and manufacturing method thereof |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105544235B (en) * | 2015-12-02 | 2017-12-08 | 昆山阿基里斯人造皮有限公司 | A kind of artificial polyvinyl chloride leather production method |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6059180A (en) * | 1983-09-09 | 1985-04-05 | Sunstar Giken Kk | Manufacture of leathery sheet |
JPS6128079A (en) * | 1984-07-11 | 1986-02-07 | Komatsu Seiren Kk | Manufacture of synthetic leather |
-
1986
- 1986-07-31 JP JP61181642A patent/JPH086262B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6059180A (en) * | 1983-09-09 | 1985-04-05 | Sunstar Giken Kk | Manufacture of leathery sheet |
JPS6128079A (en) * | 1984-07-11 | 1986-02-07 | Komatsu Seiren Kk | Manufacture of synthetic leather |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009526117A (en) * | 2006-02-10 | 2009-07-16 | アクゾ ノーベル ナムローゼ フェンノートシャップ | Microsphere |
US9062170B2 (en) | 2006-02-10 | 2015-06-23 | Akzo Nobel N.V. | Microspheres |
JP2009540047A (en) * | 2006-06-08 | 2009-11-19 | アクゾ ノーベル ナムローゼ フェンノートシャップ | Microsphere |
CN103375003A (en) * | 2013-07-17 | 2013-10-30 | 成恵民 | Multifunctional soft wall base material production process and formula |
CN104790222A (en) * | 2014-01-16 | 2015-07-22 | 辛俊兴 | Plush imitating synthetic leather and manufacturing method thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH086262B2 (en) | 1996-01-24 |
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