JP2002030577A - Method for producing leathery sheet-like product - Google Patents
Method for producing leathery sheet-like productInfo
- Publication number
- JP2002030577A JP2002030577A JP2001135952A JP2001135952A JP2002030577A JP 2002030577 A JP2002030577 A JP 2002030577A JP 2001135952 A JP2001135952 A JP 2001135952A JP 2001135952 A JP2001135952 A JP 2001135952A JP 2002030577 A JP2002030577 A JP 2002030577A
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- solution
- producing
- leather
- immersion
- 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
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims abstract description 39
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 36
- 239000000835 fiber Substances 0.000 claims abstract description 34
- 239000000243 solution Substances 0.000 claims abstract description 28
- 229920001410 Microfiber Polymers 0.000 claims abstract description 20
- 239000000126 substance Substances 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000839 emulsion Substances 0.000 claims abstract description 5
- 239000002904 solvent Substances 0.000 claims abstract description 5
- 229920000642 polymer Polymers 0.000 claims description 23
- 238000007654 immersion Methods 0.000 claims description 22
- 230000004580 weight loss Effects 0.000 claims description 22
- 239000012744 reinforcing agent Substances 0.000 claims description 20
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 13
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 13
- 239000003513 alkali Substances 0.000 claims description 11
- 239000007864 aqueous solution Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000007127 saponification reaction Methods 0.000 claims description 6
- 229920000728 polyester Polymers 0.000 claims description 4
- 239000003960 organic solvent Substances 0.000 abstract description 8
- 239000013585 weight reducing agent Substances 0.000 abstract description 8
- 239000012670 alkaline solution Substances 0.000 abstract description 4
- 229920001971 elastomer Polymers 0.000 abstract 3
- 239000000806 elastomer Substances 0.000 abstract 3
- 239000004745 nonwoven fabric Substances 0.000 description 16
- -1 bisphenol A compound Chemical class 0.000 description 13
- 238000000034 method Methods 0.000 description 12
- 239000000463 material Substances 0.000 description 6
- 229920000139 polyethylene terephthalate Polymers 0.000 description 6
- 239000005020 polyethylene terephthalate Substances 0.000 description 6
- 238000004090 dissolution Methods 0.000 description 5
- 229920002635 polyurethane Polymers 0.000 description 5
- 239000004814 polyurethane Substances 0.000 description 5
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- 239000004952 Polyamide Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- NZNMSOFKMUBTKW-UHFFFAOYSA-N cyclohexanecarboxylic acid Chemical compound OC(=O)C1CCCCC1 NZNMSOFKMUBTKW-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000000986 disperse dye Substances 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000013013 elastic material Substances 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 238000009987 spinning Methods 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N Bisphenol A Natural products C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 101150000715 DA18 gene Proteins 0.000 description 1
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- RRLWYLINGKISHN-UHFFFAOYSA-N ethoxymethanol Chemical compound CCOCO RRLWYLINGKISHN-UHFFFAOYSA-N 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 239000002649 leather substitute Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Landscapes
- Treatment Of Fiber Materials (AREA)
- Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は皮革様シート状物の
環境に配慮した製造方法に関する。さらに詳しくは、皮
革様シート状物の製造において有機溶媒を使用すること
なく複合繊維の1成分を除去する方法に関する。[0001] The present invention relates to an environment-friendly method for producing a leather-like sheet. More specifically, it relates to a method for removing one component of a conjugate fiber without using an organic solvent in the production of a leather-like sheet.
【0002】[0002]
【従来の技術】繊維からなるシートに高分子弾性体を付
与してなる皮革様シート状物は、衣料用途、資材用途と
もに広く用いられている。特に0.3dtex以下の極細
繊維を用いた皮革様シート状物は天然皮革に似た風合
い、タッチを有しており、近年その使用が拡大してい
る。該極細繊維を得る手段としては、複数の高分子物質
を用いて海島型の複合繊維もしくはポリマーブレンド繊
維を作り、その中の一成分を有機溶媒によって除去する
方法が、得られる繊維が細く、繊維間に適度な空間がで
き柔軟性に優れるため広く採用されている。2. Description of the Related Art A leather-like sheet obtained by providing a polymer sheet with a polymer elastic material is widely used for both clothing and materials. In particular, leather-like sheet materials using ultrafine fibers of 0.3 dtex or less have a texture and touch similar to that of natural leather, and their use has been expanding in recent years. As a means for obtaining the ultrafine fibers, a method of producing a sea-island type composite fiber or a polymer blend fiber using a plurality of polymer substances, and removing one of the components with an organic solvent, the resulting fiber is thin, fiber It has been widely adopted because it has a moderate space between them and has excellent flexibility.
【0003】近年、有機溶媒の使用に対して環境への悪
影響が懸念され、該皮革様シート状物の製造に関しても
有機溶剤を使用することなく製造することが要望される
ようになってきた。例えば、アルカリ水溶液を用いた極
細繊維発現処理が特開平6−316814号公報に示さ
れているが、該処理では補強剤が付与できず、極細繊維
発現処理に有機溶媒を用いたものと比較すると風合いと
品位の劣るものしかできなかった。In recent years, there has been a concern that the use of an organic solvent may adversely affect the environment, and there has been a demand for the production of such a leather-like sheet without using an organic solvent. For example, an ultrafine fiber expression treatment using an alkaline aqueous solution is disclosed in JP-A-6-316814, but in this treatment, a reinforcing agent cannot be added, and compared with a treatment using an organic solvent for the extrafine fiber expression treatment. Only the texture and quality were inferior.
【0004】[0004]
【発明が解決しようとする課題】発明者らは、かかる従
来技術の背景に鑑み、鋭意検討の結果、本発明に達し
た。即ち、極細繊維発現型繊維シートに補強剤を付与せ
しめた後、有機溶剤を用いることなくアルカリ水溶液に
より極細繊維を発現し、その後溶液タイプもしくはエマ
ルジョンの高分子弾性体を付与し、補強剤と高分子弾性
体および繊維が風合いを損ねることなく接着を向上さ
せ、風合いと耐久性に優れた皮革様シート状物を環境へ
の負荷を軽減した上で得られることを見出したものであ
る。SUMMARY OF THE INVENTION In view of the background of the prior art, the inventors have made intensive studies and, as a result, have reached the present invention. That is, after applying a reinforcing agent to the ultrafine fiber-expressing fiber sheet, the ultrafine fibers are expressed by an alkaline aqueous solution without using an organic solvent, and thereafter, a polymer elastic body of a solution type or an emulsion is provided, and the reinforcing agent and the reinforcing agent are added. It has been found that the molecular elastic body and the fiber improve the adhesion without impairing the feeling, and that a leather-like sheet having excellent feeling and durability can be obtained while reducing the load on the environment.
【0005】[0005]
【課題を解決するための手段】本発明はかかる従来技術
の問題を解決するために、以下のような構成を有する。
即ち、皮革様シート状物の製造方法であって、 1.アルカリ水溶液に対する溶解性の異なる少なくとも
2種類以上の高分子物質の組み合わせからなる極細繊維
発現型繊維を用いてシートを作成する工程。 2.シートに以下の(1)〜(3)の特性を全て満たす補強剤
を付与する工程。 (1)40℃の10重量%水酸化ナトリウム水溶液中に20分
間浸漬したあとの重量減少率が10%以下。 (2)N,N-ジメチルホルムアミドに60分浸漬したあとの
重量減少率が5%以下。 (3)98℃の熱水中に30分浸漬したあとの重量減少率
が95%以上。 3.シートをアルカリ水溶液で処理して、前記シートの
形態は実質的に保ちつつ極細繊維を発現せしめる工程。 4.シートに高分子弾性体の溶液もしくはエマルジョン
を含浸して高分子弾性体を付与する工程。 5.シート中の補強剤および高分子弾性体の溶媒を一部
あるいは全て除去する工程。 をこの順で行うことを特徴とする皮革様シート状物の製
造方法である。SUMMARY OF THE INVENTION The present invention has the following arrangement in order to solve the problems of the prior art.
That is, a method for producing a leather-like sheet material, A step of forming a sheet using ultrafine fiber-expressing fibers composed of a combination of at least two or more types of polymer substances having different solubility in an aqueous alkali solution. 2. A step of applying a reinforcing agent that satisfies all of the following characteristics (1) to (3) to the sheet. (1) The weight loss rate after immersion in a 10% by weight aqueous sodium hydroxide solution at 40 ° C. for 20 minutes is 10% or less. (2) The weight loss rate after immersion in N, N-dimethylformamide for 60 minutes is 5% or less. (3) The weight loss rate after immersion in hot water of 98 ° C. for 30 minutes is 95% or more. 3. A step of treating the sheet with an aqueous alkali solution to develop ultrafine fibers while substantially maintaining the shape of the sheet. 4. A step of impregnating the sheet with a solution or emulsion of a polymer elastic body to give the polymer elastic body. 5. A step of removing part or all of the solvent for the reinforcing agent and the elastic polymer in the sheet. Are carried out in this order.
【0006】[0006]
【発明の実施の形態】本発明の皮革様シート状物の製造
にあたり、まずアルカリ水溶液に対する溶解性の異なる
2種類以上の高分子物質の組み合わせからなる極細繊維
発現型繊維を用いてシートを作成する工程が必要であ
る。DESCRIPTION OF THE PREFERRED EMBODIMENTS In the production of a leather-like sheet according to the present invention, a sheet is first prepared using ultrafine fiber-expressing fibers comprising a combination of two or more polymer substances having different solubilities in an aqueous alkaline solution. A process is required.
【0007】本発明でいう高分子物質がアルカリ水溶液
に対する溶解性を異にするとは、極細繊維を発現せしめ
る条件下で溶解速度が20倍以上、より好ましくは40
倍以上異なることをいう。In the present invention, a polymer substance having a different solubility in an aqueous alkali solution means that the dissolution rate is at least 20 times, more preferably 40 times or more, under the conditions for developing ultrafine fibers.
It means that it is more than twice different.
【0008】本発明において、アルカリ水溶液に対する
溶解性の高い高分子物質は特に限定はされないが、アル
カリ溶解速度と紡糸安定性の点から、5-ソディウムスル
ホイソフタル酸、ポリエチレングリコール、ドデシルベ
ンゼンスルホン酸ナトリウム、ビスフェノールA化合
物、イソフタル酸、アジピン酸、ドデカジオン酸、シク
ロヘキシルカルボン酸等を5〜20モル%共重合した共
重合ポリエステルが好ましい。特に耐熱性、弱アルカリ
溶解性の点から5-ソディウムスルホイソフタル酸を5〜2
0モル%共重合したポリエチレンテレフタレート共重合
体を用いることがより好ましい。また、これら共重合体
は2元のみならず3元以上の多元共重合体であってもよ
い。In the present invention, the polymer substance having high solubility in an aqueous alkali solution is not particularly limited, but from the viewpoint of alkali dissolution rate and spinning stability, 5-sodium sulfoisophthalic acid, polyethylene glycol, sodium dodecylbenzenesulfonate. , A bisphenol A compound, isophthalic acid, adipic acid, dodecadionic acid, cyclohexylcarboxylic acid, etc., in a copolymerized polyester of 5 to 20 mol% is preferred. In particular, from the viewpoint of heat resistance and weak alkali solubility, 5-sodium sulfoisophthalic acid is added to 5 to 2
It is more preferable to use a polyethylene terephthalate copolymer copolymerized with 0 mol%. Further, these copolymers may be not only binary but also multi-component copolymers of three or more.
【0009】本発明において、アルカリ水溶液に対する
溶解性の低い高分子物質として、ポリエチレンテレフタ
レート、ポリプロピレンテレフタレート、ポリブチレン
テレフタレート等のポリエステル、共重合ポリエステ
ル、ナイロン−6、ナイロン−6,6等のポリアミド、
共重合ポリアミド等を好ましく用いることができる。In the present invention, as a polymer having low solubility in an aqueous alkali solution, polyesters such as polyethylene terephthalate, polypropylene terephthalate and polybutylene terephthalate, copolymerized polyesters, polyamides such as nylon-6 and nylon-6,6,
Copolyamide and the like can be preferably used.
【0010】本発明は、アルカリ水溶液を用いて極細繊
維を発現せしめることを特徴とするが、そのようなアル
カリ水溶液としては特に限定されることはなく、水酸化
ナトリウム水溶液、水酸化カリウム水溶液、アンモニア
塩等を用いることができる。また、適宜熱を加えながら
処理することは処理の効率を高める上で好ましい。The present invention is characterized in that ultrafine fibers are expressed using an alkaline aqueous solution. Such an alkaline aqueous solution is not particularly limited, and may be an aqueous sodium hydroxide solution, an aqueous potassium hydroxide solution, an aqueous ammonia solution. Salts and the like can be used. Further, it is preferable to perform the treatment while appropriately applying heat in order to increase the efficiency of the treatment.
【0011】極細繊維発現繊維の形態としては、特公昭
48−22126号公報等に示されたような高分子相互
配列体繊維、特公昭51−21041号公報、特公昭6
0−21904号公報等で示された混合紡糸繊維、特開
平9−310230号公報等で示された分割型複合繊維
等、目的に応じて適宜選択して使用することが好まし
い。かかる繊維から得られる極細繊維の繊度は0.3dt
ex以下であることが、柔軟性等の風合いの点から好ま
しい。Examples of the form of the ultrafine fiber-expressing fiber include high molecular mutual alignment fibers as disclosed in JP-B-48-22126, JP-B-51-21041, and JP-B-6-218.
It is preferable to appropriately select and use a mixed spun fiber disclosed in Japanese Patent Application Laid-Open No. 0-21904, a splittable conjugate fiber disclosed in Japanese Patent Application Laid-Open No. 9-310230, or the like according to the purpose. The fineness of the ultrafine fibers obtained from such fibers is 0.3 dt
ex or less is preferred in terms of texture such as flexibility.
【0012】単繊維繊度は0.3dtex以下であるのが
好ましいが、必ずしも不織布に含まれている単繊維全て
が0.3dtex以下である必要はなく、不織布が実質的
に0.3dtex以下の単繊維で構成されている状態とな
ればよい。The single fiber fineness is preferably 0.3 dtex or less, but it is not necessary that all the single fibers contained in the nonwoven fabric be 0.3 dtex or less. What is necessary is just to be in the state where it was done.
【0013】かかる極細繊維発現型繊維をシート化する
にあたりその形態としては、特に限定されることはな
く、織物、編物、不織布等を好ましく用いることができ
るが、柔軟性、質感の点で不織布がより好ましい。かか
る不織布としては特に限定されることはなく、短繊維不
織布、長繊維不織布いずれでも用いることができる。ま
た不織布の製造方法もスパンボンド法、メルトブロー
法、フラッシュ紡糸法、抄紙法、カード法等のいずれで
もよく、必要に応じて、ニードルパンチ法、水流交絡法
等で絡合を施してもよい。[0013] In forming such an ultrafine fiber-expressing fiber into a sheet, the form is not particularly limited, and a woven fabric, a knitted fabric, a nonwoven fabric and the like can be preferably used, but a nonwoven fabric is preferred in terms of flexibility and texture. More preferred. Such a nonwoven fabric is not particularly limited, and any of a short fiber nonwoven fabric and a long fiber nonwoven fabric can be used. The method for producing the nonwoven fabric may be any of a spun bond method, a melt blow method, a flash spinning method, a paper making method, a card method, and the like, and if necessary, may be entangled by a needle punch method, a hydroentanglement method, or the like.
【0014】本発明において、上述の不織布に補強剤と
して特定の高分子物質を付与する。In the present invention, a specific polymer substance is added to the above-mentioned nonwoven fabric as a reinforcing agent.
【0015】かかる高分子物質としては、 (1)40℃の10重量%水酸化ナトリウム水溶液中に20分
間浸漬したあとの重量減少率が10%以下。 (2)N,N-ジメチルホルムアミドに60分浸漬したあとの
重量減少率が5%以下。 (3)98℃の熱水中に30分浸漬したあとの重量減少率が
95%以上。なる特性を全て満たす必要がある。[0015] As such a polymer substance, (1) the weight reduction rate after immersion in a 10% by weight aqueous sodium hydroxide solution at 40 ° C for 20 minutes is 10% or less. (2) The weight loss rate after immersion in N, N-dimethylformamide for 60 minutes is 5% or less. (3) Weight loss rate after immersion in hot water of 98 ° C for 30 minutes
95% or more. It is necessary to satisfy all the characteristics.
【0016】(1)の重量減少率は5%以下が好まし
く、3%以下であればより好ましい。また、(2)の重
量減少率は3%以下が好ましい。さらに(3)の重量減
少率は97%以上が好ましく、100%であればより好
ましい。The weight reduction rate of (1) is preferably 5% or less, more preferably 3% or less. Further, the weight reduction rate of (2) is preferably 3% or less. Further, the weight reduction rate of (3) is preferably 97% or more, and more preferably 100%.
【0017】かかる特性を有することにより、極細繊維
発現処理時のフェルト形態および機能保持、ポリウレタ
ンとの接着性をコントロールできることから品位、風合
い、物性を目的に応じて任意に制御することができる。
かかる高分子物質としてはポリビニルアルコール、ある
いはその誘導体、水溶性でんぷん、カルボキシメチルセ
ルロース、アクリル酸エステル部分ケン化物、ポリアク
リルアミド、酢酸セルロース等の有機物質が好ましい。
鹸化度が90%未満のポリビニルアルコールを補強剤と
して用いた場合アルカリ水溶液に溶出してフェルト形態
および機能保持の効果が不十分となるため、本発明にお
いては特に鹸化度が90%以上のポリビニルアルコールが
好ましく、鹸化度が95%以上のポリビニルアルコールで
あればさらに好ましい。By having such properties, it is possible to control the form of the felt and the function retention during the process of developing ultrafine fibers, and to control the adhesiveness with polyurethane, so that the quality, texture and physical properties can be arbitrarily controlled according to the purpose.
As such a high molecular substance, an organic substance such as polyvinyl alcohol or a derivative thereof, water-soluble starch, carboxymethyl cellulose, partially saponified acrylate, polyacrylamide, and cellulose acetate is preferable.
When polyvinyl alcohol having a saponification degree of less than 90% is used as a reinforcing agent, it is eluted into an aqueous alkali solution and the effect of maintaining the form and function of the felt becomes insufficient. Is preferable, and polyvinyl alcohol having a saponification degree of 95% or more is more preferable.
【0018】また、アルカリ水溶液への溶解性を下げる
目的で、これらの補強剤を不織布に付与した後、熱処理
することが極めて効果的であるので好ましい。この熱処
理の温度は、130℃以上が好ましく、130℃〜195℃であ
ればより好ましい。130℃未満であれば効果が不十分で
あるので好ましくなく、195℃を越えると不溶化し、除
去できなくなる場合があるので好ましくない。このよう
な補強剤の除去処理における易制御性の点から、熱処理
の温度は、150℃〜190℃であればさらに好ましい。処理
時間はシートの形態、熱処理装置の性能により、状況、
目的に応じて適宜決めることができる。In order to reduce the solubility in an aqueous alkali solution, it is preferable to apply a heat treatment after applying these reinforcing agents to the nonwoven fabric, since it is extremely effective. The temperature of this heat treatment is preferably 130 ° C. or higher, more preferably 130 ° C. to 195 ° C. If the temperature is lower than 130 ° C., the effect is insufficient, so that it is not preferable. If the temperature is higher than 195 ° C., it may be insoluble and may not be removed. The temperature of the heat treatment is more preferably 150 ° C. to 190 ° C. from the viewpoint of easy control in the removal treatment of the reinforcing agent. The processing time depends on the form of the sheet and the performance of the heat treatment equipment,
It can be determined appropriately according to the purpose.
【0019】本発明において、極細繊維発現処理する際
の除去溶媒としては、アルカリ水溶液を用い、必要に応
じて加熱、攪拌、絞液等の操作を行い、補強剤の付与さ
れた不織布中の繊維の易溶解性成分を除去する。この
際、より溶解性の低い高分子物質が一部溶解してもかま
わないが、この処理中にシートの形態、機能を実質的に
維持し続ける条件下で行うことが必要である。In the present invention, an aqueous alkaline solution is used as a solvent to be removed during the ultrafine fiber development treatment, and if necessary, operations such as heating, stirring, and squeezing are performed to obtain fibers in the nonwoven fabric to which a reinforcing agent has been added. The easily soluble components of are removed. At this time, a polymer material having lower solubility may be partially dissolved, but it is necessary to carry out the treatment under the condition that the shape and function of the sheet are substantially maintained during the treatment.
【0020】次に、高分子弾性体の溶液もしくはエマル
ジョンの付与処理については含浸法、スプレー法、コー
ティング法等を施したものを熱による乾式凝固法、水等
による湿式凝固法、適宜スチーム処理等の常法で処理す
ることができる。Next, the treatment for applying the solution or emulsion of the elastic polymer is performed by impregnation, spraying, coating or the like, followed by dry coagulation with heat, wet coagulation with water, steam treatment as appropriate, etc. Can be processed in the usual manner.
【0021】本発明において、高分子弾性体としてはポ
リウレタン、スチレンブタジエンゴム、ブタジエンゴ
ム、ニトリルゴム、天然ゴム、ポリ塩化ビニル、ポリア
ミド、ポリアミノ酸、ポリアクリル酸エステル等を好ま
しく用いることができるが、風合いを柔軟にする点でポ
リウレタンがより好ましい。In the present invention, polyurethane, styrene-butadiene rubber, butadiene rubber, nitrile rubber, natural rubber, polyvinyl chloride, polyamide, polyamino acid, polyacrylic acid ester and the like can be preferably used as the polymer elastic body. Polyurethane is more preferable in terms of softening the texture.
【0022】本発明において、高分子弾性体の溶媒とし
ては、ジメチルホルムアミド、メチルエチルケトン、ト
ルエン、イソプロピルアルコール、酢酸エチル、メチレ
ングリコールモノエチルエーテル等を好ましく用いるこ
とができる。In the present invention, dimethylformamide, methyl ethyl ketone, toluene, isopropyl alcohol, ethyl acetate, methylene glycol monoethyl ether and the like can be preferably used as the solvent for the polymer elastic material.
【0023】高分子弾性体の総付与量はシート構成繊維
に対し20〜120重量%付与するのが好ましい。The total amount of the elastic polymer is preferably 20 to 120% by weight based on the fiber constituting the sheet.
【0024】本発明において、高分子弾性体溶液を付与
した後、凝固し温水中に漬け、補強剤を除去した後、常
法により必要に応じ、スライス、バフィングして目的と
する銀付用基材もしくはスエード用基材を得ることがで
きる。この基材は適宜の後処理加工に供することができ
る。In the present invention, the polymer elastic solution is applied, coagulated and immersed in warm water to remove the reinforcing agent, and then sliced and buffed as necessary by a conventional method to obtain the desired silver-attaching base. A material or a substrate for suede can be obtained. This substrate can be subjected to appropriate post-processing.
【0025】[0025]
【実施例】本発明を下記の実施例により説明する。実施
例中における部とは重量部のことを指す。本発明におけ
る溶解速度、重量減少率は以下の方法により測定した。 (1)溶解速度 JIS K6911の耐薬品性試験に準じて処理時間を
1時間として得た重量比より求めた。 (2)重量減少率 (a)補強剤をポリプロピレンの不織布2gに対して合
計重量がほぼ5gとなるように含浸して付与したものを
W0gとし、このものを恒温槽で液温40℃に保たれた
10重量%水酸化ナトリウム水溶液300mL中に20
分間浸漬した後の重量をW1gとして、次式により求め
た。 重量減少率=(W0−W1)/(W0−2)×100
(%) (b)補強剤をポリプロピレンの不織布2gに対して合
計重量がほぼ5gとなるように含浸して付与したものを
W0gとし、このものを20℃のN,N-ジメチルホルムア
ミド300mL中に60分間浸漬した後の重量をW2gと
して、次式により求めた。 重量減少率=(W0−W2)/(W0−2)×100
(%) (c)補強剤をポリプロピレンの不織布2gに対して合
計重量がほぼ5gとなるように含浸して付与したものを
W0gとし、このものを恒温槽で98℃に保たれた熱水
中に30分間浸漬した後の重量をW3gとして、次式によ
り求めた。 重量減少率=(W0−W3)/(W0−2)×100
(%) 実施例1 5-ソディウムスルホイソフタル酸を8モル%共重合した
ポリエチレンテレフタレートを海成分として30部、島成
分としてポリエチレンテレフタレートが70部からなる割
合で1フィラメント中に島成分が36島含まれる形態であ
り、平均繊度が、3.8dtexの海島型繊維のステープ
ルを用いてカード、クロスラッパーを通してウェブを形
成し、しかる後、ニードルパンチを施し、不織布を作成
した。The present invention will be described by the following examples. Parts in Examples refer to parts by weight. The dissolution rate and weight reduction rate in the present invention were measured by the following methods. (1) Dissolution rate The dissolution rate was determined from the weight ratio obtained by treating the treatment time as 1 hour according to the chemical resistance test of JIS K6911. (2) Weight loss rate (a) W 0 g was obtained by impregnating a reinforcing agent with 2 g of polypropylene non-woven fabric so that the total weight was about 5 g, and this was W 0 g. In 300 mL of a 10% by weight aqueous sodium hydroxide solution
The weight after immersion for one minute was defined as W 1 g and was determined by the following equation. Weight loss rate = (W 0 −W 1 ) / (W 0 −2) × 100
(%) (B) W 0 g obtained by impregnating a reinforcing agent with 2 g of polypropylene non-woven fabric so that the total weight becomes approximately 5 g, and prepare W 0 g, and this is 300 mL of N, N-dimethylformamide at 20 ° C. The weight after immersion in the steel for 60 minutes was defined as W 2 g by the following equation. Weight loss rate = (W 0 −W 2 ) / (W 0 −2) × 100
(%) (C) W 0 g was obtained by impregnating a reinforcing agent with 2 g of polypropylene non-woven fabric so that the total weight was approximately 5 g, and this was W 0 g, and this was kept at 98 ° C. in a thermostat. The weight after immersion in water for 30 minutes was defined as W 3 g according to the following equation. Weight loss rate = (W 0 −W 3 ) / (W 0 −2) × 100
Example 1 30 parts of polyethylene terephthalate obtained by copolymerizing 8 mol% of 5-sodium sulfoisophthalic acid as a sea component and 70 parts of polyethylene terephthalate as an island component contained 36 island island components in one filament. A staple of sea-island type fiber having an average fineness of 3.8 dtex was used to form a web through a card and a cross wrapper, and then a needle punch was performed to prepare a nonwoven fabric.
【0026】このシートに鹸化度98%のポリビニルア
ルコール水溶液を島繊維に対して30部含浸し、乾燥し
た後150℃で熱処理を施した。上述のポリビニルアル
コールの40℃の10重量%水酸化ナトリウム水溶液中に20
分間浸漬したあとの重量減少率は3%、N,N-ジメチルホ
ルムアミドに60分浸漬したあとの重量減少率は3%、9
8℃の熱水中に30分浸漬したあとの重量減少率は100
%であった。次に、このシートを60℃に加熱した10%水
酸化ナトリウム水溶液を用いて海成分を除去した。この
処理後のシートにポリウレタンのジメチルホルムアミド
溶液を島繊維に対して40部含浸付与し、湿式凝固し、9
0℃の熱水を用いて脱ポリビニルアルコール(同時に脱
ジメチルホルムアミド)処理を施した。The sheet was impregnated with 30 parts of an aqueous solution of polyvinyl alcohol having a saponification degree of 98% with respect to the island fiber, dried, and then heat-treated at 150 ° C. 20% by weight of the above-mentioned polyvinyl alcohol in a 10% by weight aqueous solution of sodium hydroxide at 40 ° C.
The weight loss after immersion in N, N-dimethylformamide for 3 minutes was 3%, and the weight loss after immersion for 3 minutes was 3%.
Weight loss rate after immersion in hot water at 8 ° C for 30 minutes is 100
%Met. Next, sea components were removed from this sheet using a 10% aqueous sodium hydroxide solution heated to 60 ° C. The sheet after this treatment was impregnated with 40 parts of a dimethylformamide solution of polyurethane with respect to the island fiber, wet-coagulated, and
Polyvinyl alcohol (and simultaneously dimethylformamide) treatment was performed using hot water at 0 ° C.
【0027】次にこのシートをスライス、バフィングし
た後、サーキュラー染色機において分散染料で染色を施
した。Next, this sheet was sliced and buffed, and then dyed with a disperse dye in a circular dyeing machine.
【0028】得られた皮革様シート状物は、耐久性に富
み、良好な物性を有するものであった。 比較例1 実施例1と同様にして得た不織布に鹸化度88%のポリ
ビニルアルコール水溶液を島繊維に対して30部含浸し
乾燥した後は実施例1と同様に極細繊維発現処理以降の
処理を施した。上述のポリビニルアルコールの40℃の10
重量%水酸化ナトリウム水溶液中に20分間浸漬したあと
の重量減少率は20%、N,N-ジメチルホルムアミドに60
分浸漬したあとの重量減少率は3%、98℃の熱水中に
30分浸漬したあとの重量減少率は100%であった。The obtained leather-like sheet material was rich in durability and had good physical properties. Comparative Example 1 The nonwoven fabric obtained in the same manner as in Example 1 was impregnated with 30 parts of an aqueous solution of polyvinyl alcohol having a saponification degree of 88% with respect to the island fiber, and dried. gave. 10 of 40 ° C of the above polyvinyl alcohol
The weight loss after immersion in a 20 wt% aqueous sodium hydroxide solution for 20 minutes is 20%, and 60% in N, N-dimethylformamide.
3% weight loss after immersion in hot water at 98 ° C
The weight loss rate after immersion for 30 minutes was 100%.
【0029】得られた皮革様シート状物は極細繊維発現
処理中にポリビニルアルコールの溶出が見られ、柔軟性
がなくペーパーライクなものになった。 比較例2 5-ソディウムスルホイソフタル酸を8モル%共重合した
ポリエチレンテレフタレートを海成分として30部、島成
分としてポリエチレンテレフタレートが70部からなる割
合で1フィラメント中に島成分が36島含まれる形態であ
り、平均繊度が、3.8dtexの海島型繊維のステープ
ルを用いてカード、クロスラッパーを通してウェブを形
成し、しかる後、ニードルパンチを施し、不織布を作成
した。In the obtained leather-like sheet, polyvinyl alcohol was eluted during the ultrafine fiber development treatment, and it became paper-like without flexibility. Comparative Example 2 30 parts of polyethylene terephthalate obtained by copolymerizing 8 mol% of 5-sodium sulfoisophthalic acid as a sea component and 70 parts of polyethylene terephthalate as an island component in a ratio of 36 islands in one filament. Yes, a web was formed through a card and a cross wrapper using staples of sea-island type fibers having an average fineness of 3.8 dtex, and then a needle punch was performed to prepare a nonwoven fabric.
【0030】このシートを60℃に加熱した10%水酸化ナ
トリウム水溶液を用いて海成分を除去した。Sea components were removed from the sheet using a 10% aqueous sodium hydroxide solution heated to 60 ° C.
【0031】このシートに鹸化度98%のポリビニルア
ルコール水溶液を島繊維に対して30部含浸し、乾燥し
た後150℃で熱処理を施した。上述のポリビニルアル
コールの40℃の10重量%水酸化ナトリウム水溶液中に20
分間浸漬したあとの重量減少率は3%、N,N-ジメチルホ
ルムアミドに60分浸漬したあとの重量減少率は3%、9
8℃の熱水中に30分浸漬したあとの重量減少率は100
%であった。次に、この処理後のシートにポリウレタン
のジメチルホルムアミド溶液を島繊維に対して40部含浸
付与し、湿式凝固し、90℃の熱水を用いて脱ポリビニ
ルアルコール(同時に脱ジメチルホルムアミド)処理を
施した。The sheet was impregnated with 30 parts of an aqueous solution of polyvinyl alcohol having a saponification degree of 98% with respect to the island fiber, dried and then heat-treated at 150 ° C. 20% by weight of the above-mentioned polyvinyl alcohol in a 10% by weight aqueous solution of sodium hydroxide at 40 ° C.
The weight loss after immersion in N, N-dimethylformamide for 3 minutes was 3%, and the weight loss after immersion for 3 minutes was 3%.
Weight loss rate after immersion in hot water at 8 ° C for 30 minutes is 100
%Met. Next, the sheet after the treatment is impregnated with 40 parts of a dimethylformamide solution of polyurethane with respect to the island fiber, wet coagulated, and subjected to a treatment for removing polyvinyl alcohol (and simultaneously removing dimethylformamide) using hot water at 90 ° C. did.
【0032】次にこのシートをスライス、バフィングし
た後、サーキュラー染色機において分散染料で染色を施
した。Next, this sheet was sliced and buffed, and then dyed with a disperse dye in a circular dyeing machine.
【0033】得られた皮革様シート状物は、品位が粗
く、風合いはペーパーライクなものになった。The obtained leather-like sheet-like material had a coarse quality and a paper-like texture.
【0034】[0034]
【発明の効果】本発明の製造方法によれば、有機溶媒を
使用することなく複合繊維の少なくとも1成分を除去す
るため、環境に対する負荷を低減でき、かつ良好な品位
と風合いを有する人工皮革を製造することができる。According to the production method of the present invention, since at least one component of the conjugate fiber is removed without using an organic solvent, it is possible to reduce the burden on the environment and to produce artificial leather having good quality and texture. Can be manufactured.
───────────────────────────────────────────────────── 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) D06M 15/333 D06M 15/564 15/564 101:32 // D06M 101:32 5/02 F Fターム(参考) 3B154 AA07 AA17 AB20 BA12 BA25 BB12 BB32 BD17 BE05 BF01 BF07 DA18 DA19 DA28 4F055 AA02 BA11 DA07 DA09 EA04 EA12 EA24 EA34 FA15 GA02 HA04 HA22 4L031 AA18 AB11 AB34 BA11 CA01 4L033 AA07 AB07 AC11 AC15 CA29 CA50 4L047 AA21 BA03 CA05 CB10 CC01 DA00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) D06M 15/333 D06M 15/564 15/564 101: 32 // D06M 101: 32 5/02 F F term ( Reference) 3B154 AA07 AA17 AB20 BA12 BA25 BB12 BB32 BD17 BE05 BF01 BF07 DA18 DA19 DA28 4F055 AA02 BA11 DA07 DA09 EA04 EA12 EA24 EA34 FA15 GA02 HA04 HA22 4L031 AA18 AB11 AB34 BA11 CA01 4L033 AA07 CA07 AC07
Claims (5)
2種類以上の高分子物質の組み合わせからなる極細繊維
発現型繊維を用いてシートを作成する工程。 2.シートに以下の(1)〜(3)の特性を全て満たす補強剤
を付与する工程。 (1)40℃の10重量%水酸化ナトリウム水溶液中に20分
間浸漬したあとの重量減少率が10%以下。 (2)N,N-ジメチルホルムアミドに60分浸漬したあとの
重量減少率が5%以下。 (3)98℃の熱水中に30分浸漬したあとの重量減少率
が95%以上。 3.シートをアルカリ水溶液で処理して、前記シートの
形態は実質的に保ちつつ極細繊維を発現せしめる工程。 4.シートに高分子弾性体の溶液もしくはエマルジョン
を含浸して高分子弾性体を付与する工程。 5.シート中の補強剤および高分子弾性体の溶媒を一部
あるいは全て除去する工程。 をこの順で行うことを特徴とする皮革様シート状物の製
造方法。1. A method for producing a leather-like sheet, comprising: A step of forming a sheet using ultrafine fiber-expressing fibers composed of a combination of at least two or more types of polymer substances having different solubility in an aqueous alkali solution. 2. A step of applying a reinforcing agent that satisfies all of the following characteristics (1) to (3) to the sheet. (1) The weight loss rate after immersion in a 10% by weight aqueous sodium hydroxide solution at 40 ° C. for 20 minutes is 10% or less. (2) The weight loss rate after immersion in N, N-dimethylformamide for 60 minutes is 5% or less. (3) The weight loss rate after immersion in hot water of 98 ° C. for 30 minutes is 95% or more. 3. A step of treating the sheet with an aqueous alkali solution to develop ultrafine fibers while substantially maintaining the shape of the sheet. 4. A step of impregnating the sheet with a solution or emulsion of a polymer elastic body to give the polymer elastic body. 5. A step of removing part or all of the solvent for the reinforcing agent and the elastic polymer in the sheet. Are carried out in this order.
アルコールであることを特徴とする請求項1に記載の皮
革様シート状物の製造方法。2. The method for producing a leather-like sheet according to claim 1, wherein the reinforcing agent is polyvinyl alcohol having a saponification degree of 90% or more.
温度に加熱することによって40℃の10重量%水酸化ナト
リウム水溶液中に20分間浸漬したあとの重量減少率を5
%以下とすることを特徴とする請求項1または2に記載
の皮革様シート状物の製造方法。3. A sheet provided with a reinforcing agent is heated to a temperature of 130 ° C. or higher to reduce the weight loss after immersion in a 10% by weight aqueous sodium hydroxide solution at 40 ° C. for 20 minutes.
% Or less, the method for producing a leather-like sheet according to claim 1 or 2.
る極細繊維が繊度0.3dtex以下のポリエステル繊維
であることを特徴とする請求項1〜3のいずれかに記載
の皮革様シート状物の製造方法。4. The method for producing a leather-like sheet according to claim 1, wherein the ultrafine fibers produced by the treatment with the alkaline aqueous solution are polyester fibers having a fineness of 0.3 dtex or less.
95℃未満の温度に加熱することを特徴とする請求項1
または3に記載の皮革様シート状物の製造方法。5. A sheet provided with a reinforcing agent at 150 ° C. or higher
2. Heating to a temperature of less than 95 [deg.] C.
Or the method for producing a leather-like sheet according to item 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001135952A JP4644971B2 (en) | 2000-05-10 | 2001-05-07 | Method for producing leather-like sheet |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000136754 | 2000-05-10 | ||
| JP2000-136754 | 2000-05-10 | ||
| JP2001135952A JP4644971B2 (en) | 2000-05-10 | 2001-05-07 | Method for producing leather-like sheet |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002030577A true JP2002030577A (en) | 2002-01-31 |
| JP4644971B2 JP4644971B2 (en) | 2011-03-09 |
Family
ID=26591588
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001135952A Expired - Fee Related JP4644971B2 (en) | 2000-05-10 | 2001-05-07 | Method for producing leather-like sheet |
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| Country | Link |
|---|---|
| JP (1) | JP4644971B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008085307A2 (en) | 2007-01-03 | 2008-07-17 | Eastman Chemical Company | Water-dispersible and multicomponent fibers from sulfopolyesters |
| WO2014084253A1 (en) * | 2012-11-30 | 2014-06-05 | 東レ株式会社 | Sheet-shaped object and process for producing said sheet-shaped object |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54147276A (en) * | 1978-05-09 | 1979-11-17 | Asahi Chemical Ind | Nonnwoven fabric and production |
| JPS616376A (en) * | 1984-05-23 | 1986-01-13 | 株式会社 コ−ロン | Production of suede like artificial leather |
| JPS61215782A (en) * | 1985-03-15 | 1986-09-25 | Toray Ind Inc | Production of artificial leather sheet |
| JPS6477688A (en) * | 1988-07-28 | 1989-03-23 | Toray Industries | Production of leathery sheetlike material |
| JPH0533256A (en) * | 1991-07-23 | 1993-02-09 | Kuraray Co Ltd | Method for manufacturing fibrous sheet |
| JPH11140770A (en) * | 1997-11-07 | 1999-05-25 | Toray Ind Inc | Production of napped sheet |
-
2001
- 2001-05-07 JP JP2001135952A patent/JP4644971B2/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54147276A (en) * | 1978-05-09 | 1979-11-17 | Asahi Chemical Ind | Nonnwoven fabric and production |
| JPS616376A (en) * | 1984-05-23 | 1986-01-13 | 株式会社 コ−ロン | Production of suede like artificial leather |
| JPS61215782A (en) * | 1985-03-15 | 1986-09-25 | Toray Ind Inc | Production of artificial leather sheet |
| JPS6477688A (en) * | 1988-07-28 | 1989-03-23 | Toray Industries | Production of leathery sheetlike material |
| JPH0533256A (en) * | 1991-07-23 | 1993-02-09 | Kuraray Co Ltd | Method for manufacturing fibrous sheet |
| JPH11140770A (en) * | 1997-11-07 | 1999-05-25 | Toray Ind Inc | Production of napped sheet |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008085307A2 (en) | 2007-01-03 | 2008-07-17 | Eastman Chemical Company | Water-dispersible and multicomponent fibers from sulfopolyesters |
| WO2014084253A1 (en) * | 2012-11-30 | 2014-06-05 | 東レ株式会社 | Sheet-shaped object and process for producing said sheet-shaped object |
| CN104838063A (en) * | 2012-11-30 | 2015-08-12 | 东丽株式会社 | Sheet-shaped object and process for producing the sheet-shaped object |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4644971B2 (en) | 2011-03-09 |
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