JPH0533000A - Production of organic composition for chrome tanning - Google Patents
Production of organic composition for chrome tanningInfo
- Publication number
- JPH0533000A JPH0533000A JP19325191A JP19325191A JPH0533000A JP H0533000 A JPH0533000 A JP H0533000A JP 19325191 A JP19325191 A JP 19325191A JP 19325191 A JP19325191 A JP 19325191A JP H0533000 A JPH0533000 A JP H0533000A
- Authority
- JP
- Japan
- Prior art keywords
- hair
- keratin
- protein
- water
- acid
- 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
Landscapes
- Treatment And Processing Of Natural Fur Or Leather (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、クロム鞣革製造に於い
て、クロム鞣剤を添加する前に皮を処理するための有機
組成物の製造方法に関するものである。より詳細には、
本発明は、牛皮の脱毛工程において、発生する副産物で
ある体毛を原料としてクロム鞣剤処理に有用な有機組成
物の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an organic composition for treating leather in the production of chrome tanned leather before adding a chrome tanning agent. More specifically,
The present invention relates to a method for producing an organic composition which is useful for treating a chrome tanning agent, using as a raw material body hair, which is a by-product, in the hair removal process of cowhide.
【0002】[0002]
【従来の技術】従来から広く行われている牛皮の脱毛工
程では、牛毛に先ず還元剤、酵素等を加えて牛毛のジス
ルフィド結合を切断し、次に水酸化カルシウムを加えて
牛皮を完全に溶解し、石灰漬処理廃液と一緒に廃液処理
槽に入れて沈殿法または活性汚泥法にて処理している。
この際の石灰漬処理廃液のB.O.Dは、20,000〜24,000 pp
mである。2. Description of the Related Art In the hair removal process of cowhide, which has been widely used in the past, first, a reducing agent, an enzyme, etc. are added to the hair to break the disulfide bond of the hair, and then calcium hydroxide is added to completely dissolve the cowhide. Then, it is placed in a waste liquid treatment tank together with the lime pickling waste liquid and treated by a precipitation method or an activated sludge method.
At this time, the BOD of the lime pickling waste liquid is 20,000 to 24,000 pp.
m.
【0003】また革の鞣工程に使用されるケラチン蛋白
質の可溶化においては、従来のジスルフィド結合を開裂
してから、酵素等の処理によって主鎖のペプチド結合を
切断して水溶性ケラチン溶液を作っているが、この処理
によってケラチンは、アミノ酸段階にまで分解されてい
る。このためこのケラチン加水分解物をクロム鞣剤の皮
への吸着反応に利用した場合、まず分解されたアミノ酸
にクロム鞣剤が先に吸着して、鞣剤の皮内部への浸透お
よびコラーゲン繊維との反応を阻止する可能性がある。
また、ケラチン加水分解物の調製に数日間を要すること、
しかも抽出したケラチン加水分解物(pH 約6.0〜7.0)は
pH 4.5 以下に於いて沈殿を生ずる傾向があるため、クロ
ム鞣剤を先に革に添加した後、従来の塩基度上昇剤の代
わりにケラチン加水分解物を添加している。In the solubilization of the keratin protein used in the leather tanning process, a conventional disulfide bond is cleaved and then a peptide bond in the main chain is cleaved by treatment with an enzyme or the like to prepare a water-soluble keratin solution. However, this treatment decomposes keratin to the amino acid stage. Therefore, when this keratin hydrolyzate is used for the adsorption reaction of the chrome tanning agent on the skin, the chrome tanning agent is first adsorbed on the decomposed amino acid, and the tanning agent penetrates into the skin and collagen fibers May block the reaction of.
Also, it takes several days to prepare the keratin hydrolyzate,
Moreover, the extracted keratin hydrolyzate (pH about 6.0-7.0)
Since chrome tanning agents are added to the leather first, the keratin hydrolyzate is added in place of the conventional basicity increasing agents, since precipitation tends to occur at pH 4.5 and below.
【0004】さらにケラチン加水分解物そのものの pH
が高いため、ケラチン加水分解物は主に、再鞣工程に於
いて用いるクロム鞣剤の吸着反応に用いられている。Furthermore, the pH of the keratin hydrolyzate itself
Therefore, the keratin hydrolyzate is mainly used for the adsorption reaction of the chromium tanning agent used in the retanning process.
【0005】しかし、上述したいずれの場合において
も、B.O.Dが高く、また重金属を含む工場廃液処理の問題
を改善するための努力はなされていない。However, in any of the above cases, no efforts have been made to improve the problem of treating industrial waste liquid having a high BOD and containing heavy metals.
【0006】[0006]
【発明が解決しようとする課題】本発明は皮革製造分野
において従来使用されている上記牛皮の脱毛工程に於い
て、発生する公害廃棄物である体毛の有効利用と、それに
伴う工場廃液中のB.O.D.を現在の20,000〜24,000から1
0,000台へ減少させることを目的とするものである。DISCLOSURE OF THE INVENTION The present invention relates to the effective use of body hair, which is a pollution waste, which is generated in the hair removal process of cowhide, which has been conventionally used in the field of leather production, and the BOD contained in factory waste liquor. The current 20,000 to 24,000 to 1
The purpose is to reduce the number to 0,000.
【0007】またクロム鞣剤の皮への吸着反応を向上さ
せて、クロム鞣剤の使用量の低減を計り、併せて鞣製後の
皮から出るクロム廃液濃度を従来より著しく減少させ、
鞣工場で使用するクロム鞣剤の減少および排水処理工程
の改善に寄与することを目的とする。Further, by improving the adsorption reaction of the chrome tanning agent on the skin, the amount of the chrome tanning agent used is reduced, and at the same time, the concentration of the chrome waste liquid discharged from the tanned leather is significantly reduced as compared with the conventional one.
The purpose is to contribute to the reduction of chromium tanning agents used in the tanning factory and improvement of wastewater treatment process.
【0008】[0008]
【課題を解決するための手段】本発明では従来工場廃液
中に混入、廃棄されていた牛毛が皮表面から離れ、媒液
に溶解しない状態で回収されるため工場から出る石灰漬
廃液のB.O.D.が減少する。この牛毛を短時間で回収し、
この回収毛を蛋白質部分分解して、水溶性ケラチンを得、
これに有機酸またはその塩類を加えて、皮革鞣工程にお
けるクロム鞣剤の皮への吸着反応を向上させる有機組成
物の製造方法を提供するものである。According to the present invention, BOD of lime waste liquid discharged from a factory is recovered because cow hair, which has been mixed and discarded in a factory waste liquid in the past, is separated from the skin surface and is not dissolved in a liquid medium. Decrease. Collect this cow hair in a short time,
The recovered hair is partially decomposed into proteins to obtain water-soluble keratin,
It is intended to provide a method for producing an organic composition in which an organic acid or a salt thereof is added to improve the adsorption reaction of a chrome tanning agent on the leather in the leather tanning step.
【0009】本発明の主たる観点においては、牛毛をそ
のまま回収し、調製することにより目的有機組成物を製
造する点にある。即ち牛毛の脱毛処理工程で毛根を水酸
化カルシウムで弛緩させてから還元剤(水硫化ソーダ、硫
化ソーダ、メルカプタン類およびアミン類等)を加えて脱
毛する。この牛毛を反応系外に取り出すには、液循環装置
およびパイプを取り付けた太鼓を用いる。液循環装置パ
イプの途中に回転式遠心分離型濾過装置(セメントミキ
サータイプ)を設置して牛毛を系外に押し出すと同時に、
アルカリ処理液は循環パイプを通って再び太鼓内に戻す
ようにする。[0009] A main aspect of the present invention lies in that the target organic composition is produced by collecting and preparing cow hair as it is. That is, hair roots are relaxed with calcium hydroxide in the hair removal process of cow hair, and then a reducing agent (sodium hydrosulfide, sodium sulfide, mercaptans, amines, etc.) is added to remove hair. To take this cow hair out of the reaction system, a drum equipped with a liquid circulation device and a pipe is used. Liquid circulation device A rotary centrifugal separation type filtration device (cement mixer type) was installed in the middle of the pipe to push cow hair out of the system and at the same time,
The alkaline treatment liquid is returned to the drum again through the circulation pipe.
【0010】本発明の他の観点としては目的組成物の分
子量を制御することにより分子量について均一な組成物
の調製が可能な点にある。即ち系外に取り出された牛毛
は上記水酸化カルシウムでのアルカリ処理により、ケラ
チン分子中のジスルフィド結合(S−S)が部分的にチオエ
ーテル結合(-S-)に変わっている。本発明の特徴は、ジス
ルフィド結合を開裂してチオ-ル基(SH-)にする従来法と
は異なり、ジスルフィド結合を有するシステイン残基
を、チオエーテル結合を有するランチオニン残基に変え
る点にある(特開平2−51533号公報参照)。この反応によ
り生成されるチオエーテル結合は非常に強固であるた
め、アルカリ処理後の蛋白質の部分分解工程において切
断されずにケラチン蛋白質中に残存する。従ってアルカ
リ処理の段階でランチオニン残基の生成を制御すること
により、最終生産物である水溶性ケラチン蛋白質の分子
量を調節することが可能である(特開平2−51533号公報
参照)。Another aspect of the present invention is that a composition having a uniform molecular weight can be prepared by controlling the molecular weight of the target composition. That is, the cattle hair taken out of the system was partially converted from the disulfide bond (S-S) in the keratin molecule into a thioether bond (-S-) by the alkali treatment with calcium hydroxide. A feature of the present invention is that, unlike the conventional method of cleaving a disulfide bond to form a thiol group (SH-), a cysteine residue having a disulfide bond is changed to a lanthionine residue having a thioether bond ( (See JP-A-2-51533). The thioether bond produced by this reaction is so strong that it remains in the keratin protein without being cleaved in the partial decomposition step of the protein after the alkali treatment. Therefore, it is possible to control the molecular weight of the final product, the water-soluble keratin protein, by controlling the production of lanthionine residues during the alkaline treatment (see Japanese Patent Laid-Open No. 2-51533).
【0011】ランチオニン残基生成の制御は、アルカリ
性塩溶液の濃度、アルカリ処理時間および温度等の条件
によって変化し得る。好ましい実施態様においては、牛毛
のアルカリ処理脱毛工程において、牛皮を水酸化カルシ
ウム飽和溶液中で、温度 20℃〜30℃、pH 11〜13 の範囲
で処理した場合、アルカリ処理時間が長ければ牛毛中の
システイン残基からランチオニン残基への変換程度が高
まり、免疫作用が起こって、脱毛処理が完全に行われな
いことはよく知られている。アルカリ処理条件を予め決
定しておき、引き続き行う蛋白質部分分解の条件と組み
合わせれば、最終目的たる水溶性ケラチン蛋白質の分子
量の調節をより適確に行うことができる。The control of the production of lanthionine residue can be changed depending on the conditions such as the concentration of the alkaline salt solution, the alkaline treatment time and the temperature. In a preferred embodiment, when the cowhide is treated in a calcium hydroxide saturated solution at a temperature of 20 ° C to 30 ° C and a pH of 11 to 13 in the alkaline treatment hair removal step of the cow's hair, if the alkali treatment time is long, It is well known that the degree of conversion of the cysteine residue to the lanthionine residue is increased, an immune action occurs, and the hair removal treatment is not completely performed. If the alkaline treatment conditions are determined in advance and combined with the conditions for the subsequent partial decomposition of the protein, the molecular weight of the final water-soluble keratin protein can be adjusted more accurately.
【0012】ここで使用する”免疫作用”と言う用語
は、脱毛工程において水酸化カルシウムを単独使用した
場合、ケラチンのジスルフィド結合(S−S)を開裂し
てチオール基(−SH)を生じるが、そのチオ−ル基が
ケラチン内各種反応基と結合して、ポリペプチ鎖間で二
次的な結合を起こし、再びチオエ−テル結合のアミノ酸
基、例えばランチオニン結合を生成するために脱毛効果
はかえって阻止される現象をいう(神谷 誠著、主婦の
友出版サ−ビスセンタ−版、皮革加工学 第64頁参
照)。アルカリ処理条件としては、アルカリ性塩類とし
て水酸化カルシウムを使用する場合、濃度は0.1重量%
から飽和溶液(3〜4重量%)、pH 11〜13、温度40℃以
下、浸漬処理時間は24時間以内が好ましい。また水酸化
ナトリウムまたは水酸化カリウムの場合は、濃度0.001
〜0.1Nにおいて水酸化カルシウムと同一条件で使用可
能である。As used herein, the term "immunity" refers to the use of calcium hydroxide alone in the hair removal process to cleave the disulfide bond (S-S) of keratin to give a thiol group (-SH). , Its thiol group binds to various reactive groups in keratin to cause a secondary bond between the polypeptide chains, and again produces an amino acid group of a thioether bond, for example, a lanthionine bond, so that the hair removal effect is rather returned. This is a phenomenon that is prevented (see Makoto Kamiya, Shufu no Tomo Shuppan Service Center Edition, Leather Processing Science, page 64). As the alkaline treatment conditions, when calcium hydroxide is used as the alkaline salt, the concentration is 0.1% by weight.
It is preferable that the saturated solution (3 to 4% by weight), pH 11 to 13, temperature of 40 ° C. or less, and immersion treatment time be within 24 hours. In the case of sodium hydroxide or potassium hydroxide, the concentration is 0.001
It can be used under the same conditions as calcium hydroxide at ~ 0.1N.
【0013】また上記アルカリ処理は、システイン残基
およびランチオニン残基以外のアミノ酸残基になんら実
質的な変化を与えないことも周知である(特開平2-5153
3号公報)。It is also well known that the above alkali treatment does not substantially change amino acid residues other than cysteine residue and lanthionine residue (Japanese Patent Laid-Open No. 2-5153).
No. 3 bulletin).
【0014】実際に、牛毛のアルカリ処理の後系外に取
り出された牛毛は、その後蛋白質部分分解が行われる。
この部分分解には、アルカリ加水分解、酸加水分解、酵
素分解、酸化分解または還元分解等の通常法がそのまま
使用できる。従来法ではこの部分分解においてアミノ酸
レベルまで加水分解が進行するが、本発明では前述のラ
ンチオニン基の存在により、分子量1,000から36,000の
ポリペプチドにまでしか分解が進行しない(特開平2-51
533号公報)。アルカリ加水分解による蛋白質の部分分
解においては、0.1〜10%の水酸化ナトリウム水溶液4〜
8Kgに対して牛毛1〜2 Kgの割合で加え、70〜100℃、
1〜24時間分解を行い水溶性ケラチン蛋白質を得る。そ
の他の蛋白質の部分分解についての条件は当業者が実験
的に決定できる。部分分解終了後、濾過、脱色し、その溶
液に有機酸またはその塩類(蟻酸、蓚酸、乳酸、コハク酸、
クエン酸、マロン酸、マレイン酸、フタ-ル酸、アジピン酸、
またはその塩類)を加え、溶液の pH を3.0〜4.5付近に調
節する。上述した有機組成物を鞣革工程における浸酸工
程中、クロム鞣剤添加前に太鼓内に注入し、革への浸透
を行ってからクロム鞣剤を加えて常法により鞣製を行
う。Actually, the cow hair taken out of the system after alkaline treatment of cow hair is subjected to partial protein decomposition.
For this partial decomposition, ordinary methods such as alkali hydrolysis, acid hydrolysis, enzymatic decomposition, oxidative decomposition or reductive decomposition can be used as they are. In the conventional method, hydrolysis proceeds to the amino acid level in this partial decomposition, but in the present invention, due to the presence of the above-mentioned lanthionine group, the decomposition proceeds only to a polypeptide having a molecular weight of 1,000 to 36,000 (JP-A-2-51).
No. 533). In the partial decomposition of proteins by alkaline hydrolysis, 0.1-10% sodium hydroxide aqueous solution 4-
Add 1 to 2 Kg of hair to 8 Kg, 70 to 100 ℃,
Degradation is performed for 1 to 24 hours to obtain a water-soluble keratin protein. Conditions for partial degradation of other proteins can be experimentally determined by those skilled in the art. After the partial decomposition is completed, the solution is filtered and decolorized, and the solution is added with an organic acid or its salts (formic acid, oxalic acid, lactic acid, succinic acid,
Citric acid, malonic acid, maleic acid, phthalic acid, adipic acid,
Or its salts) to adjust the pH of the solution to around 3.0-4.5. During the soaking process in the tanning process, the above-mentioned organic composition is injected into the drum before the addition of the chrome tanning agent to penetrate the leather, and then the chrome tanning agent is added to carry out tanning by a conventional method.
【0015】本発明のさらなる観点においては、工場内
で使用するクロム鞣剤の使用量の減少を図り、人体が高
濃度の重金属化合物にさらされる頻度を減らし、また工
場廃液中の酸化クロム量を減少することによって工場廃
液処理に関する問題の1つを解決することにある。即ちこ
の有機組成物の添加によって、鞣製後の廃液中の残存酸
化クロム量(Cr2O3量)は、90〜200 ppmとなり、通常の鞣
製後の残存酸化クロム量(Cr2O3量)が4,000〜8,000ppmで
あるのに比べると著しく改善されることが判る。この結
果、工場内でのクロム鞣剤の使用量は従来より削減され、
鞣製および革の水絞り工程後の工場廃液中のクロム残存
量は著しく減少し工場廃液処理改善に大きく寄与するも
のと考えられる。 さらに、最近数多く市販されているク
ロム鞣剤の革への高吸着剤を本発明の有機組成物の代替
として使用した場合、最も有効と思われる市販品でもク
ロム鞣製後の廃液中の残存酸化クロム量は 480 ppmであ
った。In a further aspect of the present invention, the amount of chromium tanning agent used in the factory is reduced, the frequency of exposure of the human body to heavy metal compounds of high concentration is reduced, and the amount of chromium oxide in the factory effluent is reduced. The solution is to solve one of the problems associated with the treatment of wastewater from plants. That is, by the addition of this organic composition, the amount of residual chromium oxide in the waste liquid after tanning (Cr 2 O 3 amount) is 90 to 200 ppm, the amount of residual chromium oxide after tanning (Cr 2 O 3 amount) Is 4,000 to 8,000 ppm, which is significantly improved. As a result, the amount of chrome tanning agent used in the factory has been reduced compared to before,
It is considered that the amount of residual chromium in the factory effluent after the water squeezing process for tanned leather and leather is significantly reduced, which will contribute greatly to the improvement of the factory effluent treatment. Furthermore, when a highly adsorbent for leather of a chrome tanning agent, which is commercially available recently, is used as a substitute for the organic composition of the present invention, even the most likely commercial product is the residual chromium oxide in the waste liquid after chrome tanning. The amount was 480 ppm.
【0016】また既述の如くケラチン加水分解物をクロ
ム鞣剤の革への吸着反応に使用している例もあるが、ケ
ラチン加水分解物は分子量分布が2,000〜20,000と広範
囲であり、加水分解物のpHを塩酸で下げてもpH6.5−7.0
の範囲にあり、pH 4.5 以下では沈殿を起こす傾向があ
る。一般にクロム鞣剤の溶液のpHは、約2.6から3.5 位に
なるので、クロム鞣剤を加える前にこのケラチン加水分
解物を加えると革へのクロム鞣剤との反応以前に、この
ケラチン加水分解物とクロム鞣剤とが反応し、沈殿が起
こる可能性が高い。従ってクロム鞣剤を革に加え、クロム
鞣剤を浸透させてからこのケラチン加水分解物を加えて
いる。このケラチン加水分解物の添加法は、従来法のク
ロム鞣製において塩基度上昇剤として一般に広く使用さ
れているアルカリ塩類、(蟻酸ソーダ、重炭酸ソーダ、酢酸
ソーダ、ポリ燐酸ソーダ、炭酸ソーダ等)の添加と同様に、
クロム鞣剤が革表面に吸着偏在する傾向が高く、皮を均
一に鞣すことができない。さらに蛋白質部分分解物の分
子量分布が広いこともクロム鞣剤と反応するアルカリ加
水分解物の革への均一浸透を妨げる原因となっている。There is also an example in which the keratin hydrolyzate is used for the adsorption reaction of the chrome tanning agent on the leather as described above, but the keratin hydrolyzate has a wide molecular weight distribution of 2,000 to 20,000, and the hydrolysis Even if the pH of the product is lowered with hydrochloric acid, the pH is 6.5-7.0.
The pH range is less than 4.5 and precipitation tends to occur at pH 4.5 or below. Generally, the pH of a chrome tanning agent solution is about 2.6 to 3.5, so if this keratin hydrolyzate is added before adding the chrome tanning agent, this keratin hydrolyzing agent will react with the chrome tanning agent before it reacts with the leather. It is highly possible that the substance reacts with the chrome tanning agent to cause precipitation. Therefore, a chrome tanning agent is added to the leather and the chrome tanning agent is allowed to penetrate before the keratin hydrolyzate is added. The addition method of this keratin hydrolyzate is the addition of alkali salts, which are generally widely used as a basicity increasing agent in the conventional chrome tanning method (sodium formate, sodium bicarbonate, sodium acetate, sodium polyphosphate, sodium carbonate, etc.). Similarly,
Chromium tanning agents tend to be unevenly adsorbed on the leather surface, and the leather cannot be tanned uniformly. Further, the wide molecular weight distribution of the partially decomposed protein also hinders the uniform penetration of the alkaline hydrolyzate that reacts with the chrome tanning agent into the leather.
【0017】本発明は、更に以下の実施例によって具体
的に説明するが、本発明の範囲は、実施例のみに限定さ
れるものではない。The present invention will be further described with reference to the following examples, but the scope of the present invention is not limited to the examples.
【0018】[0018]
【実施例1】牛毛は、アメリカ産ステアー・フレッシュ
アンドトリムド重量61/63ポンドの原皮を使用した。Example 1 Cow's hair was made of American Steer Fresh and Trimmed raw leather having a weight of 61/63 pounds.
【0019】使用した太鼓は、液循環タイプで循環途中
に牛毛回収装置を取り付けた。The drum used was a liquid circulation type and a cow hair recovery device was attached during circulation.
【0020】 予備水漬 施塩して約45%の水分を有する原皮の重量を100%とし
て、これを秤量基準として以下の薬品量を計算した。25
℃、200%重量の水に活性剤として0.2%のポリオキシエ
チレンアルキルフェニルエーテルを加え、太鼓を使用し
て(以下同様)周速度 30 m/分(以下同様)にて5分
間回転した後、60分間停止、30分間回転、60分間停止、3
0分間回転を行った後、排水した。約400l/分の流水で6
0分水洗し排水後フレッシング(皮の表面についている脂
肪および結締組織を取り除く操作)を行った。Preliminary soaking was carried out, and the weight of the bark having a water content of about 45% was defined as 100%, and the following chemical amounts were calculated based on this as a basis of weighing. twenty five
After adding 0.2% polyoxyethylene alkylphenyl ether as an activator to 200% water by weight at ℃, and using a drum (hereinafter the same) and rotating at a peripheral speed of 30 m / min (the same below) for 5 minutes, Stop for 60 minutes, Rotate for 30 minutes, Stop for 60 minutes, 3
After rotating for 0 minutes, it was drained. 6 with running water of about 400 l / min
After washing with water for 0 minutes and draining, it was subjected to freshening (an operation of removing fat and tightening tissue attached to the surface of the skin).
【0021】 水漬 予備水洗した原皮を以下の水溶液に浸け下記の操作を行
った。Preliminary water rinsing The rawhide that had been prewashed with water was immersed in the following aqueous solution, and the following operation was performed.
【0022】 25℃、200重量%の水 0.1% Busan 30L (ブックマンラボラトリー社製: Buckman Labratories Inc. ) 0.1% ポリオキシエチレンアルキルフェニルエ−テル 0.1% 水酸化ナトリウム 180分間回転した後、再び上記水溶液に漬け込み、10分
間回転90分間停止を7回繰り返した。翌朝10分間回転し
排水した。次に25℃の水200重量%で10分間回転、排水
しさらに27℃の水200重量%で10分間回転し排水した。25%, 200% by weight of water 0.1% Busan 30L (manufactured by Bookman Laboratories Inc .: Buckman Labratories Inc.) 0.1% polyoxyethylene alkylphenyl ether 0.1% sodium hydroxide After rotating for 180 minutes, the above aqueous solution was again used. It was soaked in, and rotated for 10 minutes and stopped for 90 minutes was repeated 7 times. The next morning, it was rotated for 10 minutes and drained. Next, it was rotated and drained with 200% by weight of water at 25 ° C. for 10 minutes, and further drained by rotating with 200% by weight of water at 27 ° C. for 10 minutes.
【0023】 アルカリ処理(脱毛) 施塩して約 45% の水分を有する原皮の重量を100%と
して、これを秤量基準として以下の薬品量を計算した。Alkali treatment (depilation) The weight of the bark having a water content of about 45% after salting was set to 100%, and the following chemical amount was calculated based on this as the basis of weighing.
【0024】上記で得た水漬原皮を27℃、150重量%
の水および 0.1%ポリオキシエチレンアルキルフェニル
エーテルの水溶液に浸け20分間回転し、10分間停止させ
た。次に3.0%の水酸化カルシウムを加え、5分間回転2
0分間停止を2回繰り返しさらに5分間回転した。次に2.
5%の水硫化ソーダを加え、10分間回転20分間停止を2
回繰り返した。さらに0.8%の炭酸ソーダを加え、10分
間回転および20分間停止を2回繰り返した後、10分間回転
し停止させた。最後に27℃、150重量%の水を加え20分間
回転し、牛毛を回収した後排水した。[0024] The above-prepared raw hide is heated at 27 ° C and 150% by weight.
Was soaked in water and an aqueous solution of 0.1% polyoxyethylene alkyl phenyl ether, rotated for 20 minutes, and stopped for 10 minutes. Then add 3.0% calcium hydroxide and spin for 5 minutes 2
The stop for 0 minutes was repeated twice, and the rotation was continued for another 5 minutes. Then 2.
Add 5% sodium hydrosulfide, rotate for 10 minutes, stop for 20 minutes 2
Repeated times. Further, 0.8% sodium carbonate was added, and rotation for 10 minutes and stop for 20 minutes were repeated twice, and then rotation for 10 minutes was stopped. Finally, water at 27 ° C and 150% by weight was added, and the mixture was rotated for 20 minutes to collect cow hair and then drain it.
【0025】ここで得られた牛皮は従来法により、再石
灰漬、戻し、浸酸および鞣製が行なわれた。The cowhide obtained here was recalcified, rehydrated, soaked and tanned by a conventional method.
【0026】[0026]
【実施例2】牛毛からの有機組成物の製造方法 実施例1で回収した牛毛を反応器に入れて、30℃の流水
(100l/分)で60分間水洗を行い、排水後もう一度同
一条件で水洗を行う。このアルカリ処理牛毛を使用し
て、本発明の有機組成物を製造した。すなわちまずアル
カリ処理牛毛1kgを反応器に入れ、さらに1規定の水酸
化ナトリウム水溶液を8リットルを加え、80℃で24時間撹
拌しながら加熱し、ケラチン蛋白質水溶液を得た。この
蛋白質の分子量はゲル濾過法で約 9,000であった。Example 2 Method for Producing Organic Composition from Cow Hair The cow hair collected in Example 1 was placed in a reactor and rinsed with running water (100 l / min) at 30 ° C. for 60 minutes, and after draining under the same conditions again. Wash with water. The alkali-treated cow hair was used to produce the organic composition of the present invention. That is, first, 1 kg of alkali-treated cow hair was placed in a reactor, 8 liters of 1N sodium hydroxide aqueous solution was further added, and the mixture was heated at 80 ° C. for 24 hours with stirring to obtain an aqueous keratin protein solution. The molecular weight of this protein was about 9,000 by gel filtration.
【0027】反応液を冷却し1日静置した。翌日40℃に反
応液を加熱した後、濾過し濾液を脱色後、2.8 kgの乳酸
を撹拌しながら加えてpHを3.0〜3.5に調整した。The reaction solution was cooled and allowed to stand for 1 day. The next day, the reaction solution was heated to 40 ° C., filtered, and the filtrate was decolorized. Then, 2.8 kg of lactic acid was added with stirring to adjust the pH to 3.0 to 3.5.
【0028】[0028]
【実施例3】本発明の有機組成物を使用したクロム鞣製 原皮はキップスキン(アメリカ産)17ポンドを使用し
た。なお、3.0 mmの厚さにすいた皮の重量を100%として
これを秤量基準として以下の薬品量を計算した。水漬、
石灰浸漬、すき(3.0mm)および戻しの工程は、従来どお
りの方法で行った。Example 3 Kip skin (American) 17 pounds was used as the chrome-tanned raw hide using the organic composition of the present invention . The amount of the chemicals below was calculated with the weight of the skin thinned to a thickness of 3.0 mm as 100% and the basis of the weight. Pickled,
The steps of lime dipping, plow (3.0 mm) and returning were carried out in the conventional manner.
【0029】浸酸 25℃、50重量%の水、8%の食
塩水溶液中で10分間回転した。0.5%の蟻酸を含む5重
量%の水をさらに加え15分間回転した。1.0%の硫酸を
含む10%重量水を20分毎に4回に分けて加え、本発明の
有機組成物を2.0重量%加え60分回転した。最後に35℃の
20重量%水を加えて7時間回転した後、60分毎に10分間
回転を繰り返した。翌朝、10分間回転後、防黴剤を入れ
てさらに10分間回転した後、革を取り出し平に広げた。Immersion of acid In a 25 ° C., 50% by weight water, 8% saline solution, rotation was carried out for 10 minutes. 5% by weight of water containing 0.5% formic acid was further added and the mixture was rotated for 15 minutes. 10% weight water containing 1.0% sulfuric acid was added every 20 minutes in four portions, 2.0% by weight of the organic composition of the present invention was added, and the mixture was rotated for 60 minutes. Finally at 35 ℃
After adding 20% by weight of water and rotating for 7 hours, rotation was repeated every 60 minutes for 10 minutes. The next morning, after rotating for 10 minutes, a mildew proofing agent was added, and after rotating for another 10 minutes, the leather was taken out and spread flat.
【0030】最終的に得られた革のpHは4.5、酸化クロム
吸着量は3.8%(皮の水分14%の時の重量を100%とし
た)、熱収縮温度98−102℃、鞣製後の廃液中の残存酸化
クロム量は 97 ppmであり、廃液の色は殆ど無色であった
(従来法での廃液は濃緑青色)。 この革は、従来法により
染色、加脂、水絞り、真空乾燥、熟成、味取り、ステーキン
グ、トグル張およびトリミングを行って仕上げした革の
官能仕上がり検査では、従来法と比較してシボ、銀立ちに
おいて同一、革の弾力性は従来法のものが5段階評価に
て4であるのに対し、本発明の組成物で処理した革は4.
5〜5.0を示していた。The pH of the finally obtained leather is 4.5, the adsorption amount of chromium oxide is 3.8% (the weight when the skin moisture is 14% is 100%), the heat shrink temperature is 98-102 ° C., and the leather is made after tanning. The amount of residual chromium oxide in the waste liquid was 97 ppm, and the color of the waste liquid was almost colorless.
(The waste liquid from the conventional method is dark green blue). This leather is finished by dyeing, greasing, water squeezing, vacuum drying, aging, taste picking, staking, toggling and trimming according to the conventional method, and in the sensory finish inspection of the leather, it is grainy compared with the conventional method. The same in silver standing, the elasticity of the leather is 4 in the 5-point evaluation in the conventional method, whereas the leather treated with the composition of the present invention is 4.
It showed 5 to 5.0.
Claims (1)
へ吸着反応する効果を高める有機組成物の製造方法であ
って; (a)牛皮の脱毛工程に於いて生じる牛毛を、アルカリ
処理し; (b)処理済み牛毛の構成主成分である硬蛋白質ケラチ
ンを、蛋白質部分分解することにより平均分子量が約1,
000〜36,000の範囲内にある水溶性ケラチン蛋白質をつ
くり;そして (c)該水溶性ケラチン蛋白質に有機酸またはその塩類
を加え、pHを3.0〜4.5の間に調整する、ことから成る
クロム鞣用有機組成物の製造方法。Claim: What is claimed is: 1. A method for producing an organic composition that enhances the effect of a chrome tanning agent adsorbing to leather in the chrome tanning step; (a) Cow hair produced in the hair removal step of cowhide. (B) The average molecular weight of the hard protein keratin, which is the main constituent of the treated cow's hair, is about 1 by partially decomposing the protein.
Producing a water-soluble keratin protein in the range of 000 to 36,000; and (c) adding an organic acid or a salt thereof to the water-soluble keratin protein and adjusting the pH to 3.0 to 4.5. Method for producing organic composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03193251A JP3081677B2 (en) | 1991-08-01 | 1991-08-01 | Method for producing organic composition for chrome tanning |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03193251A JP3081677B2 (en) | 1991-08-01 | 1991-08-01 | Method for producing organic composition for chrome tanning |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0533000A true JPH0533000A (en) | 1993-02-09 |
JP3081677B2 JP3081677B2 (en) | 2000-08-28 |
Family
ID=16304851
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03193251A Expired - Fee Related JP3081677B2 (en) | 1991-08-01 | 1991-08-01 | Method for producing organic composition for chrome tanning |
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JP (1) | JP3081677B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007091864A (en) * | 2005-09-28 | 2007-04-12 | Tokyo Univ Of Agriculture & Technology | Leather modifier |
CN104988250A (en) * | 2015-06-23 | 2015-10-21 | 兴业皮革科技股份有限公司 | Cattle instep leather less chrome tanning method based on zirconium-aluminum-titanium matched tanning agent |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0634285U (en) * | 1992-10-07 | 1994-05-06 | 株式会社三岡電機製作所 | Printed wiring board |
-
1991
- 1991-08-01 JP JP03193251A patent/JP3081677B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007091864A (en) * | 2005-09-28 | 2007-04-12 | Tokyo Univ Of Agriculture & Technology | Leather modifier |
CN104988250A (en) * | 2015-06-23 | 2015-10-21 | 兴业皮革科技股份有限公司 | Cattle instep leather less chrome tanning method based on zirconium-aluminum-titanium matched tanning agent |
Also Published As
Publication number | Publication date |
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JP3081677B2 (en) | 2000-08-28 |
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