JPH0418341A - Leather powder-contaiing film or sheet and laminate using same - Google Patents

Leather powder-contaiing film or sheet and laminate using same

Info

Publication number
JPH0418341A
JPH0418341A JP12200490A JP12200490A JPH0418341A JP H0418341 A JPH0418341 A JP H0418341A JP 12200490 A JP12200490 A JP 12200490A JP 12200490 A JP12200490 A JP 12200490A JP H0418341 A JPH0418341 A JP H0418341A
Authority
JP
Japan
Prior art keywords
leather
powder
leather powder
less
film
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
Application number
JP12200490A
Other languages
Japanese (ja)
Other versions
JPH07103248B2 (en
Inventor
Yasunori Ikuga
生賀 康則
Nobuo Kusamoto
伸夫 草本
Kazuhisa Kaneda
金田 和久
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP12200490A priority Critical patent/JPH07103248B2/en
Publication of JPH0418341A publication Critical patent/JPH0418341A/en
Publication of JPH07103248B2 publication Critical patent/JPH07103248B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To enhance appearance, the touch and long-term properties while keeping the original hygroscopicity, moisture release properties and moisture permeability of leather by using an ultrafine leather powder reduced in impurity and having a specific particle size. CONSTITUTION:A leather powder-containing film or sheet is constituted of 1 - 90 wt.% of a leather powder with cortex content of 85 wt.% or more, oils and fats content of 2 wt.% or less, the total amount of water extractable Na<+>- and Ca<2+>-ions of 0.5 wt.% or less, and average particle size D50 of 7mum or less and the standard deviation of a particle size of 3mum or less and 99 - 10 wt.% of a synthetic resin. This leather powder-containing film or sheet is constituted as a coating film or laminated to a base material directly or through an adhesive.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は皮革粉含有フィルム又はシート、及びそれを用
いた積層体、特に皮革粉の改良に関し、合成皮革、人工
皮革等としてアパレル、靴、鞄、車両内装材、家具、文
房具等に利用できる。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a leather powder-containing film or sheet and a laminate using the same, particularly to the improvement of leather powder, and is applicable to apparel, shoes, as synthetic leather, artificial leather, etc. It can be used for bags, vehicle interior materials, furniture, stationery, etc.

〔背景技術〕[Background technology]

従来よりアパレル、靴、鞄等の素材として合成皮革や人
工皮革が使用されている。近年は天然皮革様の感触、外
観、吸湿性、放湿性、透湿性等の性能にいっそう近づけ
るため、動物の皮革を原料とした皮革粉を配合したフィ
ルム、合成皮革、人工皮革等も知られている(例えば特
開昭63−233828号、特開平1−314789号
)。これらの用途に使用される皮革粉は、粒径が余り大
きいと、表面がざらついたり、外観が悪くなったり、表
面コート層又は含浸層への添加が困難になる等、製品化
に支障をきたすため、10μm以下の粒径のものが必要
で、できるだけ小さい方が好ましいとされている。
Synthetic leather and artificial leather have traditionally been used as materials for apparel, shoes, bags, etc. In recent years, films containing leather powder made from animal hides, synthetic leathers, and artificial leathers have become known in order to bring them closer to the feel, appearance, moisture absorption, moisture release, and moisture permeability of natural leather. (For example, JP-A-63-233828, JP-A-1-314789). If the particle size of the leather powder used for these purposes is too large, the surface will be rough, the appearance will be poor, and it will be difficult to add it to the surface coating layer or impregnated layer, which will hinder commercialization. Therefore, particles with a particle size of 10 μm or less are required, and it is said that it is preferable to have a particle size as small as possible.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかしながら従来使用されている皮革粉は、例えば特開
昭63−233828号では粒径40μm以下、また特
開平1−314789号では粒径30μm以下と、粒径
10μm以上のものもかなり含むため、フィルムやシー
トへの混入は不適当である。
However, the leather powder used conventionally has a particle size of 40 μm or less in JP-A No. 63-233828, and a particle size of 30 μm or less in JP-A-1-314789. It is inappropriate for it to be mixed in or in sheets.

しかも従来は皮革自体に通常含まれるコラーゲン以外の
不純物の量、種類等について考慮されていないために、
フィルム又はシート、或いは合成皮革、人工皮革等に用
いた場合、長期使用中又は保存中、湿度、熱等の影響に
より表面に不純物が白粉としてブリードアウトして製品
の外観や耐変色性等の性能の劣化を招くという問題があ
る。
Moreover, conventionally, the amount and type of impurities other than collagen normally contained in the leather itself have not been considered.
When used for films, sheets, synthetic leather, artificial leather, etc., impurities may bleed out as white powder on the surface due to the effects of humidity, heat, etc. during long-term use or storage, which may affect the product's appearance and performance such as color fastness. There is a problem in that it causes deterioration.

本発明の目的は皮革本来の吸湿性、放湿性、透湿性等の
優れた特性を維持しながら、外観、感触及び長期性能を
向上した皮革粉含有フィルム又はシート、及びそれを用
いた合成皮革、人工皮革等の積層体を提供することであ
る。
The purpose of the present invention is to provide a leather powder-containing film or sheet that has improved appearance, feel, and long-term performance while maintaining the excellent properties inherent to leather such as moisture absorption, moisture release, and moisture permeability, and synthetic leather using the same. An object of the present invention is to provide a laminate of artificial leather or the like.

〔課題を解決するための手段および作用〕本発明は、皮
革粉を用いた合成皮革、人工皮革等の製品化において、
皮革粉の粒径のみならず、皮革自体に含まれる各種不純
物成分も製品の性能、特に長期性能に重大な影響を及ぼ
すことに着目し・不純物の少ない特定粒径の超微細皮革
粉を用いることにより、前記目的を達成しようとするも
のである。
[Means and effects for solving the problems] The present invention provides a method for producing synthetic leather, artificial leather, etc. using leather powder.
Focusing on the fact that not only the particle size of leather powder but also various impurity components contained in the leather itself have a significant impact on product performance, especially long-term performance, we used ultra-fine leather powder with a specific particle size with few impurities. This aims to achieve the above objective.

即ち本発明の皮革粉含有フィルム又はシートは、皮質分
が85wt%以上、油脂分が2wt%以下、水で抽出可
能なNa+イオンとCa2+イオンとの合計量が0.5
wt%以下、及び平均粒径D50か7μm以下で且つ前
記粒径の標準偏差が3μm以下である皮革粉1〜90w
t%と合成樹脂99〜10wt%とで構成される。
That is, the leather powder-containing film or sheet of the present invention has a cortex content of 85 wt% or more, an oil content of 2 wt% or less, and a total amount of water-extractable Na+ ions and Ca2+ ions of 0.5.
Leather powder 1 to 90 w wt% or less, and an average particle size D50 of 7 μm or less, and a standard deviation of the particle size of 3 μm or less
t% and 99-10wt% of synthetic resin.

本発明の積層体は前記皮革粉含有フィルム又はシートを
、塗膜として、或いは直接又は接着剤を介して基材に積
層して構成される。
The laminate of the present invention is constructed by laminating the above-mentioned leather powder-containing film or sheet on a base material as a coating film, or directly or via an adhesive.

本発明のフィルム又はシート等に使用される皮革粉はこ
のように皮質分等の特性値を限定したものであるが、こ
れらの限定は次のような理由による。
The leather powder used for the film, sheet, etc. of the present invention has the characteristic values such as cortical content limited as described above, and these limitations are due to the following reasons.

I)皮質分85wt%以上: 皮質分の含有量が多いということは、不純物の量が少な
いことを意味すると同時に、レザー、塗料等に混入した
製品の表面状態、タッチ感等を向上させる重要な因子と
なることを意味する。即ち皮質分が多い方が少ない粉末
量で効率的に製品の表面状態等を改善できる。
I) Cortex content of 85 wt% or more: A high content of cortical content means that the amount of impurities is small, and at the same time, it is an important substance that improves the surface condition, touch feeling, etc. of products mixed in leather, paint, etc. It means to be a factor. In other words, the surface condition of the product can be improved more efficiently with a smaller amount of powder when the amount of cortical material is larger.

2)油脂分2wt%以下(好ましくは0.5wt%以下
): 動物皮革に存在する油脂分は熱等で変質し、混合製品の
悪臭、着色及びブリードアウトによる表面風合の悪化(
ベタベタ、ヌルヌル、テカテカ感)の原因となる。従っ
て、油脂分は少ない程、好ましい。
2) Oil and fat content of 2 wt% or less (preferably 0.5 wt% or less): The oil and fat content present in animal leather deteriorates due to heat, etc., resulting in bad odor, coloring, and deterioration of the surface texture of the mixed product due to bleed-out (
(Causes sticky, slimy, shiny feeling). Therefore, the lower the oil and fat content, the better.

3)水で抽出可能な遊離イオン(Na” 、 Ca”)
の合計量0.5wt%以下: 皮革原料に由来する不純物のうち、水で抽出された遊離
イオン量が多いと、製品化した場合、湿度、熱等の影響
を受け、製品表面にその塩(例えばNacl、 Na2
504. CaSO4等)がブリートアウトし、製品外
観の悪化につながる。なお、水で抽出可能な遊離イオン
としてはNa” 、 Ca2+の陽イオンの他に、cl
”−、30,2−の陰イオンが存在するが、ブリードア
ウトしてくるものは、それらイオンの対イオンの塩の形
態でしか生じないため、量の少ない陽イオンであるNa
+とCa2+との合計量で規定した。
3) Free ions extractable with water (Na”, Ca”)
Total amount of 0.5 wt% or less: Among the impurities derived from leather raw materials, if the amount of free ions extracted with water is large, the product will be affected by humidity, heat, etc., and the salts ( For example, Nacl, Na2
504. CaSO4, etc.) bleed out, leading to deterioration of product appearance. In addition to cations such as Na'' and Ca2+, free ions that can be extracted with water include Cl.
``-, 30, 2- anions exist, but the ones that bleed out are only in the form of salts of the counter ions of these ions, so the cation Na, which is a small amount,
It was defined as the total amount of + and Ca2+.

4)平均粒径D5o≦7μmで且つ標準偏差σ≦3μm
 : 粒径は薄肉製品には決定的な因子で、粒径か大きければ
、分散不良による欠陥及び表面風合の悪化(ザラザラ感
、凹凸感)につながる。一方、粒径が小さいほど分散が
良好となり、製品欠陥の少ない(ボイド、糸切れ等)タ
ッチ感の良好な表面状態をもった製品が得られる。また
、標準偏差が小さいことは分布上大きな粒子の混入が少
ないことを意味する。
4) Average particle diameter D5o≦7μm and standard deviation σ≦3μm
: Particle size is a decisive factor for thin-walled products; if the particle size is large, it will lead to defects due to poor dispersion and deterioration of surface texture (roughness, unevenness). On the other hand, the smaller the particle size, the better the dispersion, and a product with less product defects (voids, thread breakage, etc.) and a surface condition with a good touch feel can be obtained. Furthermore, a small standard deviation means that there are few large particles mixed in in the distribution.

上記特性値の測定法は、次の通りである。The method for measuring the above characteristic values is as follows.

A)皮質分及び油脂分: JIS K6550−1976 r皮革試験方法J6.
7及び6.4による。
A) Cortex and oil/fat content: JIS K6550-1976 r Leather Test Method J6.
7 and 6.4.

旧水で抽出可能な遊離イオン(Na” 、 Ca”)の
合計量: 乾燥皮革粉10gを純水1007rLl中で一昼夜攪拌
し、皮革粉中の遊離イオンを抽出する。抽出液中のNa
++ Ca2+を原子吸光法で定量し、皮革粉からの抽
出量として求める。
Total amount of free ions (Na'', Ca'') extractable with old water: 10 g of dry leather powder was stirred in 1007 rL of pure water all day and night to extract free ions in the leather powder. Na in the extract
++ Ca2+ is determined by atomic absorption spectrometry and determined as the amount extracted from leather powder.

C)平均粒径及び標準偏差の分布・ 数十mgの皮革粉を100−のメタノールに分散し、コ
ールタ−カウンター(コールタ−・エレクトロニクス社
製)で粒子の分布を測定し、平均粒径及び標準偏差を求
める。
C) Distribution of average particle size and standard deviation - Disperse several tens of mg of leather powder in 100-methanol, measure the particle distribution with a Coulter Counter (manufactured by Coulter Electronics), and calculate the average particle size and standard deviation. Find the deviation.

なお、皮革粉の密度範囲は通常0.38〜0.43g/
cc(皮革粉を120℃で2時間乾燥後、JIS K6
721に準じて測定)である。密度が大き過ぎると、粒
径が増大して所定の平均粒径7μmを超えるし、方、密
度が小さ過ぎると、皮革粉が繊維状となったり、セン毛
部分が多く出て合成樹脂を均一に分散し難くなることが
あるからである。
Note that the density range of leather powder is usually 0.38 to 0.43 g/
cc (after drying leather powder at 120℃ for 2 hours, JIS K6
721). If the density is too high, the particle size will increase and exceed the predetermined average particle size of 7 μm. On the other hand, if the density is too small, the leather powder will become fibrous or have many loose hairs, making it difficult to uniformly coat the synthetic resin. This is because it may become difficult to disperse.

以上のような本発明に係る皮革粉は、例えば皮革粉原料
に対し粗粉砕、乾燥、溶剤による脱脂、残存溶剤の除去
、水洗、脱水、スチームによる膨潤処理、乾燥、微粉砕
、微粉末と粗粉末との分級の各工程を行った後、更に前
記微粉末を平均粒径D50”7μm以下に再微粉砕する
工程及び前記D5o−7μm以下の微粉末からD50”
2μm以下の微粉末を分級除去する工程を行うことによ
り製造できる。
The leather powder according to the present invention as described above can be produced by, for example, processing the leather powder raw material by coarsely pulverizing, drying, degreasing with a solvent, removing residual solvent, washing with water, dehydration, swelling treatment with steam, drying, finely pulverizing, and converting fine powder into coarse powder. After carrying out each step of classification with the powder, a step of re-pulverizing the fine powder to an average particle size D50" of 7 μm or less, and a step of re-pulverizing the fine powder with an average particle size D50" of 7 μm or less, and a D50"
It can be manufactured by performing a step of classifying and removing fine powder of 2 μm or less.

この製造方法をさらに詳しく説明すると、まず後工程の
微粉砕を容易にするため、皮革粉原料をショークラッシ
ャー、カッターミル、ハンマークラッシャー等の粗砕機
で粒径10mm以下程度に粗粉砕する。こうして得られ
る粗砕皮革粉は通常40〜60wt%の水分を含んでい
る。なお皮革粉原料としてはシェービング屑革、床革等
が使用できる。
To explain this manufacturing method in more detail, first, in order to facilitate fine pulverization in the subsequent process, the leather powder raw material is coarsely pulverized to a particle size of about 10 mm or less using a pulverizer such as a show crusher, cutter mill, or hammer crusher. The coarsely crushed leather powder thus obtained usually contains 40 to 60 wt% of water. Note that shaving waste leather, floor leather, etc. can be used as the raw material for the leather powder.

次に後工程での脱脂(油脂分の除去)を容易にするため
、この含水粗粉末を20〜30wt%程度の水分になる
迄、乾燥する。
Next, in order to facilitate degreasing (removal of fats and oils) in a subsequent step, this water-containing coarse powder is dried until the moisture content is approximately 20 to 30 wt%.

次にこの乾燥粗粉末を適当な溶剤を用いて油脂分か2w
t%以下、好ましくは0.5wt%以下になる迄、脱脂
する。ここで脱脂用溶剤としてはn−ヘキサン、ベンジ
ン、メチレンクロライド、アセトン、酢酸エチル、トル
エン等が使用できる。
Next, this dry coarse powder is mixed with an appropriate solvent to dissolve 2w of oil and fat.
Degreasing is performed until the content is t% or less, preferably 0.5wt% or less. Here, n-hexane, benzine, methylene chloride, acetone, ethyl acetate, toluene, etc. can be used as the degreasing solvent.

引続き、粗粉末中の残存溶剤を除去するため、脱脂後の
粗粉末を熱処理する。熱源としては通常、安全上からス
チームか使用されるため、この工程はスチームパージと
も呼ばれる。他の熱源としては加熱窒素、加熱空気等も
使用できる。
Subsequently, in order to remove residual solvent in the coarse powder, the coarse powder after degreasing is heat treated. For safety reasons, steam is usually used as the heat source, so this process is also called steam purging. Other heat sources that can be used include heated nitrogen and heated air.

次に主として皮革中の遊離イオン(Na” 、 Ca2
勺を抽出、除去すると共に、粗粉末に所定の水分を保持
させるため、水洗工程及び脱水工程を行う。この一連の
水洗操作はバッチ式で数回繰り返す方法が効果的で、例
えば溶剤除去後の粗粉末に一定量の水を供給し、所望時
間攪拌及び必要あれば空気によるバブリングを行った後
、脱水する方法を、水の供給量にもよるが、通常数回、
好ましくは3〜4回繰り返す。連続式水洗操作は使用水
量が多くなり、有利とは言えないが、可能である。
Next, free ions (Na”, Ca2
In addition to extracting and removing the strawberry, a water washing process and a dehydration process are performed in order to make the coarse powder retain a predetermined amount of moisture. It is effective to repeat this series of water washing operations several times in a batch manner. For example, a fixed amount of water is supplied to the coarse powder after the solvent has been removed, and after stirring for a desired time and bubbling with air if necessary, dehydration is performed. Depending on the amount of water supplied, it is usually done several times.
Preferably repeat 3 to 4 times. Continuous water washing operation requires a large amount of water and is not advantageous, but it is possible.

脱水は通常、操作の簡便性の点から濾過(水切り又は水
抜き)により行なわれるか、遠心脱水等、他の方法で行
なってもよい。
Dehydration is usually carried out by filtration (draining or draining) for ease of operation, or may be carried out by other methods such as centrifugal dehydration.

水温は、常温でよく、好ましくは30℃以下である。The water temperature may be room temperature, preferably 30°C or lower.

以上のような一連の水洗操作により遊離のNa”イオン
とCa2+イオンとの合計量(乾燥重量換算)が0.5
wt%以下で、水分が通常65〜70%の含水粗粉末が
得られる。この一連の水洗操作により最終的に粗粉末は
通常、所定の水分(65〜70%)を保持することにな
るので、この方法は脱水後の粗粉末の水分の確認だけで
、従来行われているような、溶剤除去後の粗粉末に所定
の水分になる迄、水を補給する調湿工程を事実上廃止で
きるという利点がある。
Through the above series of water washing operations, the total amount of free Na'' ions and Ca2+ ions (dry weight equivalent) was reduced to 0.5.
A water-containing coarse powder having a water content of usually 65 to 70% can be obtained when the amount is less than wt%. As a result of this series of water washing operations, the coarse powder usually retains a predetermined moisture content (65-70%), so this method only requires checking the moisture content of the coarse powder after dehydration, which has not been done in the past. This method has the advantage that the humidity conditioning step of replenishing water until the coarse powder after removing the solvent reaches a predetermined moisture content can be virtually eliminated.

ここで、粗粉末に所定量の水分を保持又は補給するのは
次のような理由による。即ち、乾いた状態では次工程の
スチーム蒸煮後微粉砕を行っても、微粉化が進まない。
Here, the reason why a predetermined amount of water is retained or supplied to the coarse powder is as follows. That is, in a dry state, even if pulverization is performed after steam steaming in the next step, pulverization will not proceed.

しかし水分を含み、従って膨潤した粗粉末をスチーム蒸
煮すると、一部熱変性し、乾燥すると、締まって固くな
り、粉砕、微粉化し易くなるからである。
However, when steam-cooked coarse powder that contains water and is swollen, it is partially denatured by heat, and when dried, it becomes compact and hard, making it easier to crush and pulverize.

次に後工程の微粉砕を容易にするため、脱水後の粗砕皮
革粉を攪拌しなからスチームにより膨潤処理(スチーム
蒸煮)を行う。
Next, in order to facilitate fine pulverization in the subsequent process, the coarsely crushed leather powder after dehydration is stirred and then subjected to a swelling treatment (steam cooking) using steam.

引続き、後工程の微粉砕を容易にするため、膨潤処理後
の粗砕皮革粉を水分3wt%以下程度になる迄、乾燥す
る。この乾燥工程は通常、ドライヤーによる予備乾燥及
び真空乾燥機による本乾燥を組み合わせて行われる。
Subsequently, in order to facilitate fine pulverization in the subsequent step, the coarsely crushed leather powder after the swelling treatment is dried until the moisture content is approximately 3 wt % or less. This drying step is usually performed by combining preliminary drying using a dryer and main drying using a vacuum dryer.

次に後工程の再微粉砕を容易にするため、乾燥後の粗砕
皮革粉をビクトリーミル、ボールミル、コロイドミル、
ジェットミル、ローラーミル、ハンマーミル等の乾式粉
砕機で平均粒径50μm程度になる迄、微粉砕する。
Next, in order to facilitate re-pulverization in the subsequent process, the coarsely crushed leather powder after drying is processed using a Victory mill, ball mill, colloid mill, etc.
Finely pulverize using a dry pulverizer such as a jet mill, roller mill, or hammer mill until the average particle size is approximately 50 μm.

次に同様な理由から、得られた微粉砕皮革粉を重力式分
級機;慣性式分級機;サイクロン、ミクロンセパレータ
ー等の遠心式分級機:ふるい分は機等により微粉末(例
えば平均粒径D50=30μm以下のもの)と粗粉末(
例えばD50=60μm以上)とに分級する。なお粗粉
末は必要に応じて微粉砕工程に循環することかできる。
Next, for the same reason, the obtained finely pulverized leather powder is passed through a gravity classifier; an inertial classifier; a centrifugal classifier such as a cyclone or a micron separator; = 30 μm or less) and coarse powder (
For example, D50=60 μm or more). Incidentally, the coarse powder can be recycled to the pulverization step if necessary.

引き続き、前記微粉末をD5o−7μmJJ下になる迄
、再微粉砕した後、前記D50=7μm以下の微粉末か
らり、。=2μm以下の微粉末を分級除去する工程を行
う。再微粉砕工程は前述のような乾式粉砕機のうち、微
粉化に適したシェツトミル、コロイドミル等の粉砕機に
よって実施できる。また、分級工程は前述のような分級
機により実施できる。
Subsequently, the fine powder is re-pulverized until it becomes D5o-7 μm JJ or less, and then the fine powder with D50=7 μm or less is obtained. A process of classifying and removing fine powder of 2 μm or less is performed. The re-pulverization step can be carried out using a dry pulverizer suitable for pulverization, such as a shet mill or a colloid mill, among the dry pulverizers mentioned above. Further, the classification step can be carried out using a classifier as described above.

以上の方法では、一連の水洗操作を脱脂工程の後で行っ
たが、この水洗操作は脱脂の前あるいは微粉化後でも可
能である。
In the above method, a series of water washing operations were performed after the degreasing step, but this water washing operation can also be performed before degreasing or after pulverization.

以上のようにして得られる皮革粉と併用される合成樹脂
としては熱可塑性のものでも、熱硬化性のものでもよい
。代表的な熱可塑性樹脂としては塩化ビニル樹脂、酢酸
ビニル樹脂、ポリスチレン、ABS樹脂、アクリル樹脂
、ポリエチレン、ポリプロピレン、フッ素樹脂、ポリア
ミド樹脂、アセタール樹脂、ポリカーボネート、ウレタ
ン系、エステル系等の熱可塑性エラストマー、セルロー
ス系プラスチック等がある。代表的な熱硬化性樹脂とし
てはフェノール樹脂、ユリア樹脂、メラミン樹脂、不飽
和ポリエステル脂、エポキシ樹脂、ジアリルフタレート
樹脂、熱硬化性ポリウレタン樹脂、ケイ素樹脂等がある
The synthetic resin used in combination with the leather powder obtained as described above may be thermoplastic or thermosetting. Typical thermoplastic resins include vinyl chloride resin, vinyl acetate resin, polystyrene, ABS resin, acrylic resin, polyethylene, polypropylene, fluororesin, polyamide resin, acetal resin, polycarbonate, urethane resin, thermoplastic elastomer such as ester resin, There are cellulose plastics, etc. Typical thermosetting resins include phenol resin, urea resin, melamine resin, unsaturated polyester resin, epoxy resin, diallyl phthalate resin, thermosetting polyurethane resin, and silicone resin.

本発明の組成物には、品質の安定化等の目的や使用環境
に応じて、この分野で通常使用される添加剤、例えば繊
維、抗酸化剤、紫外線吸収剤の他、可塑剤、安定剤、潤
滑剤等の加工性改良剤;充填剤;染料、顔料等の着色剤
等を必要量添加することができる。
The composition of the present invention may contain additives commonly used in this field, such as fibers, antioxidants, ultraviolet absorbers, plasticizers, stabilizers, etc., depending on the purpose of quality stabilization and the usage environment. , processability improvers such as lubricants; fillers; coloring agents such as dyes and pigments, etc. can be added in necessary amounts.

ここで繊維としては綿、麻、絹、毛等の天然繊維やレー
ヨン、キュプラ、ポリエステル、ポリエチレン、ポリピ
レン、ポリウレタン、ビニロン、アクリル、ナイロン、
アセテート、ポリ塩化ビニル等の化学繊維が挙げられる
Fibers include natural fibers such as cotton, linen, silk, wool, rayon, cupro, polyester, polyethylene, polypyrene, polyurethane, vinylon, acrylic, nylon, etc.
Examples include chemical fibers such as acetate and polyvinyl chloride.

酸化防止剤としてはアルキルフェノール、アルキレン・
ビスフェノール、アルキルフェノールゆチオエーテル、
β、β′−チオプロピオン酸エステル、有機亜リン酸エ
ステル、芳香族アミン、フェノール・ニッケル複合体等
かある。
As antioxidants, alkylphenols, alkylenes,
Bisphenol, alkylphenol thioether,
Examples include β, β'-thiopropionate, organic phosphite, aromatic amine, and phenol/nickel complex.

紫外線吸収剤としてはフェニルサリチレートのようなサ
リチル酸エステル系、2−ヒドロキシヘンシトリアール
のようなヒドロキシベンゾフェノン系:2−ヒドロキシ
ヘンシフエノン、2−ヒドロキシ−4−メトキシヘンシ
フエノン、2−ヒドロキシ−4−オクトキシベンゾフェ
ノン、2,2−ジヒドロキジー4−メトキシヘンシフエ
ノン等のヒドロキシヘンシフエノン系等がある。
As ultraviolet absorbers, salicylic acid esters such as phenyl salicylate, hydroxybenzophenones such as 2-hydroxyhensitrial: 2-hydroxyhensiphenone, 2-hydroxy-4-methoxyhensiphenone, 2-hydroxy Hydroxyhensiphenones such as -4-octoxybenzophenone and 2,2-dihydroxydi-4-methoxyhensiphenone are available.

加工性改良剤としては、塩化ビニル用にはフタル酸ジオ
クチル、フタル酸ジブチル、リン酸トリクレジル、リン
酸トリオクチル等の可塑剤や、三塩基性硫酸鉛、ステア
リン酸鉛、二塩基性亜リン酸鉛等の安定剤、及びステア
リン酸、ステアリン酸鉛、カルナウバワックス等の潤滑
剤があり、ポリウレタン用にはジメチルホルムアミド、
メチルエチルケトン、インプロピルアルコール等の溶剤
がある。
Processability improvers for vinyl chloride include plasticizers such as dioctyl phthalate, dibutyl phthalate, tricresyl phosphate, trioctyl phosphate, tribasic lead sulfate, lead stearate, and dibasic lead phosphite. and lubricants such as stearic acid, lead stearate, and carnauba wax.For polyurethane, dimethylformamide,
Solvents include methyl ethyl ketone and inpropyl alcohol.

充填剤としては炭酸カルシウム、チタン白、クレー、雲
母等がある。
Examples of fillers include calcium carbonate, titanium white, clay, and mica.

本発明の皮革粉含有フィルム又はシートを作るには、ペ
レット状、パウダー状、ブロック状又はペースト状の樹
脂を用いた場合、予め加熱混合あるいは混練時の発泡及
び粉末の加水分解防止のため、皮革粉の水分量を0.5
wt%とし、この乾燥皮革粉と樹脂と必要であれば添加
剤とを加熱下に混合又は混練し、例えばペレット状、粉
体状等に加工した後、フィルム又はシート状に成形する
。また、いったん液状組成物としてもよく、この場合は
樹脂を適当な溶剤に溶解又は分散し、これに前記皮革粉
及び必要あれば添加剤を加え、攪拌、混合した後、フィ
ルム又はシート状に成形する。いずれの場合も皮革粉と
合成樹脂との混合割合は合成樹脂10〜99wt%に対
し、皮革粉90〜1wt%の範囲である。皮革粉の割合
が90wt%を超えると、フィルム又はシートに脆化が
現れ、また1wt%未満ではその添加効果かない。ただ
し合成樹脂中の皮革粉含有量はフィルムの場合は5〜1
0wt%が好ましく、またシートの場合は10〜60w
t%が好ましい。
In order to make the leather powder-containing film or sheet of the present invention, when pellet-shaped, powder-shaped, block-shaped or paste-shaped resin is used, in order to prevent foaming and powder hydrolysis during heating and mixing or kneading, Reduce the moisture content of the flour to 0.5
wt%, and the dried leather powder, resin, and additives if necessary are mixed or kneaded under heating, processed into pellets, powder, etc., and then formed into a film or sheet. Alternatively, it may be made into a liquid composition. In this case, the resin is dissolved or dispersed in a suitable solvent, the leather powder and additives are added thereto if necessary, stirred and mixed, and then formed into a film or sheet. do. In either case, the mixing ratio of leather powder and synthetic resin is in the range of 90 to 1 wt% of leather powder to 10 to 99 wt% of synthetic resin. If the proportion of leather powder exceeds 90 wt%, the film or sheet will become brittle, and if it is less than 1 wt%, the addition effect will be ineffective. However, the leather powder content in the synthetic resin is 5 to 1 in the case of film.
0 wt% is preferable, and in the case of a sheet, 10 to 60 w
t% is preferred.

フィルム又はシートの厚さは5μm以上か適当で、皮革
粉は均一に分散していることか好ましい。
The thickness of the film or sheet is suitably at least 5 μm, and the leather powder is preferably uniformly dispersed.

また皮革粉か表面に露出していてもよく、この場合はさ
らにタッチ感や温感の向上に役立つ。
In addition, leather powder may be exposed on the surface, and in this case, it is useful to further improve the touch feeling and the sense of warmth.

成形方法としては乾式製膜、湿式製膜、カレンダー成形
、インフレーション成形、Tダイ成形、プレス成形等が
利用できる。
As a forming method, dry film forming, wet film forming, calendar molding, inflation molding, T-die molding, press molding, etc. can be used.

以上のような皮革粉含有フィルム又はシートはそれ自体
で使用することかできるが、基材に、後述するような方
法で積層して各種用途に供することもできる。また、必
要に応じてパフかけ、エンボスロール加工等により表面
仕上げを施すこともできる。ここで使用される基材とし
ては前述のような天然又は化学繊維よりなる織布、編布
又は不織布の他、合成樹脂フィルム又はシート、他の皮
革粉含有フィルム又はシート、紙等が挙げられる。
The above-described leather powder-containing film or sheet can be used by itself, but it can also be used for various purposes by laminating it on a base material by the method described below. In addition, surface finishing can be performed by puffing, embossing roll processing, etc., if necessary. Examples of the base material used here include woven fabrics, knitted fabrics, and nonwoven fabrics made of natural or chemical fibers as described above, as well as synthetic resin films or sheets, other leather powder-containing films or sheets, and paper.

積層法としては、ポリウレタン樹脂を使用する場合は、
基材に皮革粉含有樹脂溶液を含浸する方法、基材に前記
溶液を塗布する湿式法、或いは前記溶液等で皮革粉、含
有フィルム又はシートを作り、これを直接又は接着剤を
介して基材に積層する乾式法か挙げられる。またポリ塩
化ビニル樹脂の場合は、皮革粉含有加熱溶融樹脂を押出
成形やカレンダー成形によりフィルム又はシートを製造
し、これを予め接着剤を塗布、乾燥させた基材に積層す
る方法か挙げられる。
When using polyurethane resin as a lamination method,
A method of impregnating a base material with a resin solution containing leather powder, a wet method of applying the solution to the base material, or a method of making a leather powder-containing film or sheet with the solution etc. and applying it directly or through an adhesive to the base material. One example is the dry method of laminating layers. In the case of polyvinyl chloride resin, a method may be used in which a film or sheet is produced by extrusion molding or calendar molding from a heat-melted resin containing leather powder, and the film or sheet is laminated onto a base material that has been previously coated with an adhesive and dried.

具体的な積層装置を第1〜3図に示す。第1図は乾式コ
ーティング装置で離型紙l上の皮革粉含有樹脂溶液より
なる乾式コーテイング液2はナイフロール3によって所
望の厚さに塗布され、乾燥機4内で乾燥された後、冷却
ロール5によって冷却され、皮革粉含有フィルム又はシ
ートとなる。
A specific laminating apparatus is shown in FIGS. 1 to 3. FIG. 1 shows a dry coating device in which a dry coating liquid 2 consisting of a resin solution containing leather powder is coated on a release paper l to a desired thickness by a knife roll 3, dried in a dryer 4, and then cooled by a cooling roll 5. The leather powder is then cooled to form a leather powder-containing film or sheet.

次いてこのフィルム又はシートの表面に接着剤6が塗布
された後、ニップロール8において、別途に供給される
基材7(含浸性でも非含浸性でもよい)と積層され、乾
燥機9内で乾燥され、更に冷却ロール10によって冷却
されて積層体11となる。
Next, after an adhesive 6 is applied to the surface of this film or sheet, it is laminated with a separately supplied base material 7 (which may be impregnable or non-impregnable) in a nip roll 8, and dried in a dryer 9. It is further cooled by a cooling roll 10 to form a laminate 11.

第2図は含浸コーティング装置で、含浸性基材20は含
浸槽2内に導入され、ここで皮革粉含有溶液よりなる含
浸コーテイング液22が含浸され、引き続き、マングル
23によって余剰の液が絞られた後、凝固兼水洗槽24
内に導入され、ここで水25によって凝固、水洗され、
更に乾燥機26によって乾燥されて積層体27となる。
FIG. 2 shows an impregnating coating apparatus, in which an impregnable substrate 20 is introduced into an impregnating tank 2, where it is impregnated with an impregnating coating liquid 22 made of a leather powder-containing solution, and then the excess liquid is squeezed out by a mangle 23. After that, the coagulation and washing tank 24
is introduced into the interior, where it is coagulated and washed with water 25,
It is further dried by a dryer 26 to form a laminate 27.

第3図は第2図の装置と類似した湿式コーティング装置
で、基材30はコーティングロール31によって皮革粉
含有溶液よりなる湿式コーテイング液32が塗布された
後、凝固兼水洗槽33,34.35に順次導入され、水
36,37.38によって凝固、水洗され、更に乾燥機
39によって乾燥されて積層体40となる。
FIG. 3 shows a wet coating device similar to the device shown in FIG. The laminate 40 is sequentially introduced into a laminate 40, solidified and washed with water 36, 37, and 38, and further dried in a drier 39 to form a laminate 40.

以上のような本発明に係るフィルム又はシート、及び積
層体の製造工程を第4図にまとめて示した。
The manufacturing process of the film or sheet and laminate according to the present invention as described above is summarized in FIG. 4.

〔実施例〕〔Example〕

以下に本発明を実施例によってさらに詳しく説明する。 The present invention will be explained in more detail below with reference to Examples.

実JL例」よ(皮革粉含有フィルム) 皮革粉の製造: クロムなめしした牛皮屑革(シエービンク革)の塊12
00kgを解砕機(ホソカワミクロン社製)で、元のシ
ェービング屑革の形状(max  : l am幅×1
2 cm長)にほぐした後、粗砕機(オダテ社製)1ン
マーミル:能力600kg/Hr )に順次送り込み、
粒径約10mm以下の粗砕皮革粉とする。この粗粉末の
水分は40〜60wt%であった。
Actual JL Example (Leather powder-containing film) Production of leather powder: Lump 12 of chrome-tanned cowhide waste leather (schiebink leather)
00kg is crushed using a crusher (manufactured by Hosokawa Micron) to the original shape of the shaving waste leather (max: lam width x 1
After loosening it into pieces (2 cm long), they were sequentially fed into a coarse crusher (manufactured by Odate Co., Ltd., 1 mm mill: capacity 600 kg/Hr),
Crushed leather powder with a particle size of about 10 mm or less. The moisture content of this coarse powder was 40 to 60 wt%.

次に、この湿潤粗砕皮革粉350kgを真空乾燥機に入
れ、水分が20〜30wt%になる迄、乾燥する。引続
き、この乾燥粗砕皮革粉270kgを脱脂機に投入し、
n−ヘキサンを100f /minをフィードしながら
1時間15分攪拌、抽出を行って脱脂後、濾過する。得
られた脱脂粗粉末中の残存油脂分CtO,5wt%以下
であった。
Next, 350 kg of this wet coarsely crushed leather powder is placed in a vacuum dryer and dried until the moisture content becomes 20 to 30 wt%. Subsequently, 270 kg of this dry coarsely crushed leather powder was put into a degreasing machine,
While feeding n-hexane at 100 f/min, the mixture was stirred for 1 hour and 15 minutes, extracted, defatted, and filtered. The residual fat and oil content CtO in the obtained coarse defatted powder was 5 wt% or less.

次に、この脱脂粗砕皮革粉中の残存溶剤を130’C、
2kg / crl Gの蒸気で溶剤(ヘキサン)臭力
くなくなるまでパージする。
Next, the remaining solvent in this defatted coarsely crushed leather powder was heated at 130'C.
Purge with 2 kg/crl G steam until the solvent (hexane) odor disappears.

同脱脂機に常温の水2rn’を補給し30分攪拌後、濾
過により水切りする。このノ<・ソチ水洗操作を計4回
行って屑革中の金属イオン等の遊離イオン及び水溶性成
分を除去する。a過、水切り後の粗砕皮革粉は65〜7
0wt%の水分を含んでいた。
The same degreasing machine was replenished with 2rn' of water at room temperature, and after stirring for 30 minutes, the water was drained by filtration. This water washing operation is carried out a total of four times to remove free ions such as metal ions and water-soluble components in the waste leather. Crushed leather powder after a filtration and draining is 65-7
It contained 0 wt% water.

次に、これを調湿することなく、スチーム蒸煮機に移し
、攪拌しなから130°C、2kg / crjGの蒸
気で45分間蒸煮する。
Next, this is transferred to a steam steamer without adjusting the humidity, and is steamed for 45 minutes at 130°C with 2 kg/crjG steam without stirring.

次に蒸煮後の粗砕皮革粉を、90°Cに保持されたドラ
イヤーで30〜40wt%の水分になるまで3時間予備
乾燥した後、真空乾燥機で45℃、8時間乾燥し、水分
1wt%以下の乾燥粗砕皮革粉190kgを得る。
Next, the coarsely crushed leather powder after steaming was pre-dried in a dryer maintained at 90°C for 3 hours until the moisture content was 30-40wt%, and then dried in a vacuum dryer at 45°C for 8 hours to reduce the moisture content to 1wt%. Obtain 190 kg of dry coarsely crushed leather powder.

次に、これをファインビクトリーミル(ホソカワミクロ
ン社製)で2時間1700rpmで微粉砕する。
Next, this was pulverized using a Fine Victory Mill (manufactured by Hosokawa Micron Corporation) at 1700 rpm for 2 hours.

引続き、これをサイクロン式分級機で分級し、平均粒径
I)50−約30μmの微細皮革粉35kg及びり、。
Subsequently, this was classified using a cyclone classifier to obtain 35 kg of fine leather powder with an average particle size of I) 50 to about 30 μm.

−約60μmの粗大皮革粉155kgを得る。- 155 kg of coarse leather powder of approximately 60 μm are obtained.

なお、D50”約60μmの粗大皮革粉は前記微粉砕工
程に循環した。
Incidentally, the coarse leather powder having a D50'' of about 60 μm was circulated to the above-mentioned pulverization step.

更に、このD50−約30μmの皮革粉35kgをシェ
ツトミル(セイシン企業社製)により、空気圧8 kg
 / cnf G 、風量10 rn’/mim、処理
量20kg/Hrの条件で全量がD50≦7μmになる
迄、再微粉砕する。
Furthermore, 35 kg of this leather powder with a D50 of about 30 μm was milled in a shet mill (manufactured by Seishin Enterprise Co., Ltd.) at an air pressure of 8 kg.
/cnf G , air flow rate of 10 rn'/mim, and throughput of 20 kg/Hr until the total amount becomes D50≦7 μm.

最後に、これをサイクロン(セイシン企業社製)で分級
してD5゜≦7μmの超微細皮革粉33゜25kg及び
り、。−2μm以下の超微細皮革粉(ノヘグフィルター
中) 1.75kgを得る。
Finally, this was classified using a cyclone (manufactured by Seishin Enterprise Co., Ltd.) to yield 33° and 25 kg of ultrafine leather powder with D5°≦7μm. - 1.75 kg of ultrafine leather powder (in Noheg filter) of less than 2 μm is obtained.

皮革粉含有フィルムの製造 こうして得られたり、。≦7μmの超微細皮革粉(以下
皮革粉Aという)の性状を後記表−1(こ示す。
The production of leather powder-containing films is thus obtained. The properties of ultra-fine leather powder (hereinafter referred to as leather powder A) with a particle size of ≦7 μm are shown in Table 1 below.

次に合成皮革用ポリウレタン溶液(大日精化社製しザミ
ンME−3612LP)の固形分90wt%に対し乾燥
皮革粉Aが10wt%になるように、両者を混合した樹
脂溶液(樹脂固形分20wt%)を離型紙上にコーター
で塗布し、70℃乾燥して30μm厚のフィルムを作製
する。
Next, a polyurethane solution for synthetic leather (Zamine ME-3612LP manufactured by Dainichiseika Chemical Co., Ltd.) was mixed with a resin solution (resin solid content 20 wt%) so that the dry leather powder A was 10 wt% with respect to the solid content of 90 wt%. ) is applied onto release paper using a coater and dried at 70°C to produce a 30 μm thick film.

LLLL(皮革粉含有フィルム) ポリウレタン溶液の固形分70wt%に対し乾燥皮革粉
Aが30wt%になるように混合した他は、実施例1と
同じフィルム作製法でフィルムを作製する。
LLLL (Leather powder-containing film) A film is produced using the same film production method as in Example 1, except that the dry leather powder A is mixed at 30 wt% with respect to the solid content of 70 wt% of the polyurethane solution.

実施例3(皮革粉含有フィルム) ポリウレタン溶液の固形分50wt%に対し乾燥皮革粉
Aか50wt%になるように混合した他は、実施例1と
同しフィルム作製法でフィルムを作製する。
Example 3 (Leather powder-containing film) A film was produced in the same manner as in Example 1, except that dry leather powder A was mixed to a solid content of 50 wt % in the polyurethane solution so that the dry leather powder A became 50 wt %.

実施例4(皮革粉含有シート) 軟質塩化ヒニル樹脂(信越ポリマー社製、可塑剤38w
t%含有、重合度平均3000) 80 wt%に対し
乾燥皮革粉Aを20wt%混合し、これを160°Cに
加熱混練してシート状に加工後、ペレット化した。次に
このペレットをプレス成形機で厚さ400μmのシート
に成形した。
Example 4 (Leather powder-containing sheet) Soft hinyl chloride resin (manufactured by Shin-Etsu Polymer Co., Ltd., plasticizer 38w)
(containing t%, average degree of polymerization 3000) 80 wt%, 20 wt% of dried leather powder A was mixed therein, heated and kneaded at 160°C, processed into a sheet, and pelletized. Next, this pellet was molded into a sheet with a thickness of 400 μm using a press molding machine.

実JLガ」−(乾式合成皮革) 第1図の乾式コーティング装置を用いて、離型紙上に、
乾式コーテイング液として、乾燥皮革粉Aを固型分基準
で6wt%配合した乾式用ポリウレタン樹脂溶液に助剤
を少量添加した液を塗布し、130℃で乾燥して20μ
m厚の皮革粉含有ポリウレタンフィルムを形成し、これ
を、接着剤とじて乾燥皮革粉Aを固型分基準で5wt%
配合したポリウレタン系接着剤を用いて1デニール、目
付70g/m′のポリエステル不織布よりなる基材に接
着し、140°Cで乾燥して40μm厚の皮革粉含有ポ
リウレタン樹脂層を有する乾式合成皮革を製造した。
JL-(Dry synthetic leather) Using the dry coating device shown in Figure 1, coat it on the release paper.
As a dry coating liquid, a dry coating polyurethane resin solution containing 6 wt% of dry leather powder A on a solid basis, with a small amount of auxiliary agent added, was applied, and dried at 130°C to form a coating of 20 μm.
A polyurethane film containing leather powder with a thickness of
Using a blended polyurethane adhesive, it was adhered to a base material made of polyester nonwoven fabric of 1 denier and a basis weight of 70 g/m', and dried at 140°C to produce dry synthetic leather having a 40 μm thick layer of polyurethane resin containing leather powder. Manufactured.

実施例6(湿式合成皮革) ナイロン50%とテトロン50%との混紡繊維の織布よ
りなる基材に、湿式コーテイング液として、乾燥皮革粉
Aを固形分基準で30wt%配合した湿式用ポリウレタ
ン樹脂溶液に充填剤を少量添加した液を、第3図の湿式
コーティング装置で塗布し、140℃で乾燥して0.7
mm厚の皮革粉含有エステル系ポリウレタン樹脂層を有
する湿式合成皮革を製造した。
Example 6 (Wet-processed synthetic leather) Wet-processed polyurethane resin in which 30 wt% of dry leather powder A was mixed on a solid basis as a wet-processed coating liquid to a base material made of a woven fabric of blended fibers of 50% nylon and 50% Tetron. A small amount of filler added to the solution was applied using the wet coating device shown in Figure 3, and dried at 140°C to give a coating of 0.7
A wet synthetic leather having a layer of leather powder-containing ester-based polyurethane resin having a thickness of mm was produced.

実JL剋7(人工皮革) 2デニール、目付70g/mのポリエステル不織布より
なる基材に、含浸コーテイング液として、乾燥皮革粉A
を固形分基準で25wt%配合したエステル系ポリウレ
タン樹脂溶液(樹脂固形分15wt%)に充填剤を3部
添加した液を、第2図の含浸コーティング装置を用いて
乾燥重量で30 g、’m含浸し 130℃で乾燥した
Real JL 剋7 (artificial leather) Dry leather powder A is applied as an impregnating coating liquid to a base material made of polyester nonwoven fabric with a 2 denier and a basis weight of 70 g/m.
A solution prepared by adding 3 parts of a filler to an ester-based polyurethane resin solution (resin solid content 15 wt%) containing 25 wt% of the solid content of It was impregnated and dried at 130°C.

次にこの含浸処理基材に、湿式コーチインク液として、
乾燥皮革粉Aを固形分基準で30wt%配合したエステ
ル系ポリウレタン樹脂溶液(樹脂固形分15wt%)に
前記と同し充填剤と発砲剤を添加した液を、第3図の湿
式コーチインク装置で塗布し、130℃で乾燥して0.
4+nm厚の多孔質ポリウレタン樹脂層を有する人工皮
革を製造した。
Next, a wet coach ink liquid is applied to this impregnated base material.
The same filler and foaming agent as above were added to an ester-based polyurethane resin solution (resin solid content 15 wt%) containing 30 wt% dry leather powder A on a solid basis, and the liquid was added using the wet coach ink device shown in Figure 3. Coating and drying at 130°C until 0.
An artificial leather with a porous polyurethane resin layer 4+nm thick was produced.

比較例1 皮革粉Aを用いなかった他は実施例1と同しフィルム作
製法に従ってフィルムを作製した。
Comparative Example 1 A film was produced in the same manner as in Example 1 except that leather powder A was not used.

比較例2 スチームパージ後の粗砕皮革粉を、水洗操作を行わずに
、そのまま蒸煮機に移し、この粗粉末に水分が65〜7
0wt%になる迄、水を補給、調湿した後、蒸煮を行っ
た他は実施例1と同し皮革粉の製造方法を繰り返し、D
sa≦7μmの超微細皮革粉(以下、皮革粉Bという)
を製造した。皮革粉Bの性状を後記表−1に示す。
Comparative Example 2 Crushed leather powder after steam purging was directly transferred to a steamer without washing with water, and the moisture content of this coarse powder was 65 to 7.
D
Ultrafine leather powder with sa≦7μm (hereinafter referred to as leather powder B)
was manufactured. The properties of leather powder B are shown in Table 1 below.

次に乾燥皮革粉Aの代わりに乾燥皮革粉Bを用いて実施
例1のフィルム作製法と同様にしてフィルムを作製する
Next, a film is produced in the same manner as in Example 1 using dried leather powder B instead of dried leather powder A.

比較例3 再微粉砕工程及びその後の分級工程を行わなかった他は
実施例1と同じ皮革粉製造法に従ってD5o−約30μ
mの皮革粉(以下、皮革粉Cという)を製造した。皮革
粉Cの性状を後記表−1に示す。
Comparative Example 3 D5o-approximately 30μ was produced according to the same leather powder production method as in Example 1, except that the re-pulverization step and the subsequent classification step were not performed.
Leather powder of m (hereinafter referred to as leather powder C) was produced. The properties of leather powder C are shown in Table 1 below.

次に乾燥皮革粉Aの代わりに乾燥皮革粉Bを用いて実施
例1のフィルム作製法と同様にしてフィルムを作製する
Next, a film is produced in the same manner as in Example 1 using dried leather powder B instead of dried leather powder A.

几Ve引上ごj− 皮革粉Aを用いなかった他は実施例4〜7に従って夫々
シート又は積層体を製造した。
Sheets or laminates were produced according to Examples 4 to 7, respectively, except that leather powder A was not used.

次に以上のようにして得られたフィルム、シート及び積
層体について透湿度、吸湿量等の性能を試験した。その
結果を表−2及び表−3に示す。
Next, the films, sheets, and laminates obtained as described above were tested for performance such as moisture permeability and moisture absorption. The results are shown in Table-2 and Table-3.

試験方法は次の通りである。The test method is as follows.

(1)透湿度 JIS K6549に準じる。(1) Moisture permeability According to JIS K6549.

(2)吸湿量 23℃、30%RHで平衡状態に達した試料の片面(単
層の場合はとちらかの面でも構わないか、2層以上で構
成される試料では基材とは反対の面)を23℃、80%
RHの環境下に置いた時の重量増を測定する。
(2) Moisture absorption One side of the sample that has reached an equilibrium state at 23°C and 30% RH (in the case of a single layer, either side is fine, or in the case of a sample composed of two or more layers, the opposite side to the substrate) surface) at 23℃, 80%
Measure the weight increase when placed in an RH environment.

(3)放湿量 23℃、80%RHで平衡状態に達した試料の片面(測
定綿は吸湿量の場合と同し)を23℃、30%RHの環
境下に置いた時の重量減を測定する。
(3) Weight loss when one side of the sample that reached equilibrium at 23°C and 80% RH (the measuring cotton was the same as for the moisture absorption) was placed in an environment of 23°C and 30% RH. Measure.

(4)タッチ感 表面を手で触れて比較する。(4) Touch feeling Compare by touching the surface.

(5)耐湿テスト 30℃、95%RH環境下に24時間さらした後の表面
の変化を観察する。
(5) Humidity test Observe changes in the surface after being exposed to an environment of 30° C. and 95% RH for 24 hours.

表 表 表−2 〔発明の効果〕 以上のような本発明によれば、皮革本来の吸湿性、放湿
性、透湿性等の優れた特性を維持しなから、外観、触感
及び長期性能を向上した皮革粉含有フィルム又はシート
及びそれを用いた合成皮革、人工皮革等の積層体を提供
することかできる。
Table 2 [Effects of the Invention] According to the present invention as described above, the appearance, feel, and long-term performance are improved while maintaining the excellent properties inherent to leather such as moisture absorption, moisture release, and moisture permeability. It is possible to provide a film or sheet containing leather powder and a laminate of synthetic leather, artificial leather, etc. using the same.

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

第1〜3図は夫々、本発明の積層体を製造するための一
例の乾式コーティング装置、含浸コーティング装置及び
湿式コーティング装置を#ン!4た第4図は本発明に係
る皮革粉フィルム又はシート、及び積層体の一例の製造
工程図である。 ■・・・離型紙、2,22.33・・・コーテイング液
又は皮革粉含有樹脂溶液、3・・・ナイフロール、4゜
26.39−・・乾燥機、5.10−・・冷却ロール、
7゜20.30・・・基材、11. 27. 40・・
・積層体、22・・・含浸槽、24,33,34.35
・・・凝固兼水洗槽、25,36,37.38・・・水
。 第 図
Figures 1 to 3 show examples of a dry coating device, an impregnation coating device, and a wet coating device, respectively, for manufacturing the laminate of the present invention. FIG. 4 is a manufacturing process diagram of an example of a leather powder film or sheet and a laminate according to the present invention. ■...Release paper, 2,22.33...Coating liquid or leather powder-containing resin solution, 3...Knife roll, 4゜26.39-...Dryer, 5.10-...Cooling roll ,
7°20.30...Base material, 11. 27. 40...
・Laminated body, 22... Impregnation tank, 24, 33, 34.35
...Coagulation and washing tank, 25, 36, 37. 38...Water. Diagram

Claims (2)

【特許請求の範囲】[Claims] (1)皮質分が85wt%以上、油脂分が2wt%以下
、水で抽出可能なNa^+イオンとCa^2^+イオン
との合計量が0.5wt%以下、及び平均粒径D_5_
0が7μm以下で且つ前記粒径の標準偏差が3μm以下
である皮革粉1〜90wt%と合成樹脂99〜10wt
%とからなることを特徴とする皮革粉含有フィルム又は
シート。
(1) Cortex content is 85 wt% or more, oil content is 2 wt% or less, total amount of water-extractable Na^+ ions and Ca^2^+ ions is 0.5 wt% or less, and average particle size D_5_
1 to 90 wt% of leather powder whose diameter is 7 μm or less and the standard deviation of the particle size is 3 μm or less, and 99 to 10 wt% of a synthetic resin.
A film or sheet containing leather powder, characterized in that it consists of %.
(2)請求項(1)の皮革粉含有フィルム又はシートを
、塗膜として、或いは直接又は接着剤を介して基材に積
層してなる積層体。
(2) A laminate obtained by laminating the leather powder-containing film or sheet of claim (1) on a base material as a coating, or directly or via an adhesive.
JP12200490A 1990-05-11 1990-05-11 Leather powder-containing film or sheet, and laminate using the same Expired - Lifetime JPH07103248B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12200490A JPH07103248B2 (en) 1990-05-11 1990-05-11 Leather powder-containing film or sheet, and laminate using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12200490A JPH07103248B2 (en) 1990-05-11 1990-05-11 Leather powder-containing film or sheet, and laminate using the same

Publications (2)

Publication Number Publication Date
JPH0418341A true JPH0418341A (en) 1992-01-22
JPH07103248B2 JPH07103248B2 (en) 1995-11-08

Family

ID=14825186

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12200490A Expired - Lifetime JPH07103248B2 (en) 1990-05-11 1990-05-11 Leather powder-containing film or sheet, and laminate using the same

Country Status (1)

Country Link
JP (1) JPH07103248B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0665397A (en) * 1992-08-25 1994-03-08 Kyodo Giken Kagaku Kk Dispersion sheet or tape, aerobic and/or hydrophilic self-adhesive sheet or tape, aerobic and/or hydrophilic resin film sheet or tape, and production thereof
ITVI20100181A1 (en) * 2010-06-29 2011-12-30 Texim Srl REGENERATED LEATHER AND A METHOD OF REALIZING SUCH A REGENERATED LEATHER.

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0665397A (en) * 1992-08-25 1994-03-08 Kyodo Giken Kagaku Kk Dispersion sheet or tape, aerobic and/or hydrophilic self-adhesive sheet or tape, aerobic and/or hydrophilic resin film sheet or tape, and production thereof
ITVI20100181A1 (en) * 2010-06-29 2011-12-30 Texim Srl REGENERATED LEATHER AND A METHOD OF REALIZING SUCH A REGENERATED LEATHER.
WO2012001490A1 (en) * 2010-06-29 2012-01-05 Texim Srl Regenerated bonded leather and method for making it

Also Published As

Publication number Publication date
JPH07103248B2 (en) 1995-11-08

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