JPH08199420A - Production of highly flexible vegetable fiber - Google Patents

Production of highly flexible vegetable fiber

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Publication number
JPH08199420A
JPH08199420A JP2352295A JP2352295A JPH08199420A JP H08199420 A JPH08199420 A JP H08199420A JP 2352295 A JP2352295 A JP 2352295A JP 2352295 A JP2352295 A JP 2352295A JP H08199420 A JPH08199420 A JP H08199420A
Authority
JP
Japan
Prior art keywords
raw material
fiber
aqueous solution
producing
hydrogen peroxide
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.)
Pending
Application number
JP2352295A
Other languages
Japanese (ja)
Inventor
Akio Onda
昭雄 御田
Yoshiaki Tanaka
良晁 田中
Toshiaki Ikeura
敏明 池浦
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2352295A priority Critical patent/JPH08199420A/en
Publication of JPH08199420A publication Critical patent/JPH08199420A/en
Pending legal-status Critical Current

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  • Paper (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)

Abstract

PURPOSE: To obtain highly flexible continuous fibers useful even for high-grade fabrics, etc., by treating a stock such as fiber bundles extracted from a vegetable raw material in an aqueous solution containing an alkaline substance and hydrogen peroxide under mild conditions. CONSTITUTION: A vegetable stock including fiber bundles or fiber bundles extracted from such stock are treated in an aqueous solution containing an alkaline substance and hydrogen peroxide (generator) under mild conditions (at normal temperatures to 50 deg.C for 2-48h, or at 50 deg.C to the boiling point of the solution for 0.5-24h) The concentrations of the alkaline substance in terms of Na2 O and hydrogen peroxide in terms of H2 O2 in the solution are 0.1-4wt.% and 0.02-3wt.%, respectively.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、繊維束を含む植物系原
料又は該原料から採取された繊維束から、柔軟性に富む
長い植物繊維を製造する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a long flexible plant fiber from a plant-based raw material containing a fiber bundle or a fiber bundle collected from the raw material.

【0002】[0002]

【従来の技術】植物の葉や茎、皮等の部分には、長さ3
〜6mm程度の単繊維がペクチンとリグニンで固められ
た長い繊維束として含まれている。これらの繊維束は植
物から採取され、ロープや袋、織物等の繊維製品を得る
ための原料繊維として利用されている。植物から機械的
に採取された繊維束(以下、繊維とも言う)は、粗剛で
あるため、ロープや、帆布、袋等の製品にしか利用でき
ず、織物用繊維として利用することができない。
2. Description of the Related Art Plant leaves, stems, skins and the like have a length of 3
Single fibers of about 6 mm are included as a long fiber bundle that is hardened with pectin and lignin. These fiber bundles are collected from plants and used as raw fibers for obtaining fiber products such as ropes, bags, and woven fabrics. A fiber bundle mechanically collected from a plant (hereinafter, also referred to as a fiber) is coarse and rigid, and therefore can be used only for products such as ropes, canvas and bags, and cannot be used as textile fibers.

【0003】従来、このような粗剛繊維束から織物等に
使える細繊維を得る方法として、繊維束を数週間発酵処
理する方法が知られている。この方法は、繊維束内のペ
クチンとリグニンを醗酵除去し、これによって細繊維を
得る方法である。しかし、この方法の場合、ペクチン除
去は比較的容易に行うことができるもののリグニン除去
はむつかしく、そのリグニンの除去率には制限があり、
繊維束中に含まれていたリグニン分の3〜7%程度が除
去されるにすぎない。従って、このようにして得られる
繊維にはセルロースとリグニンが濃縮され、リグニン含
有率が上昇するのでその柔軟性と漂白性の点では未だ満
足すべきものではない。また、この方法は発酵処理なの
で比較的生分解され易いリグニン分の少ないものにしか
適用できず、木質化が進んだ繊維束、例えば、パイナッ
プルやバナナの幹等に含まれている繊維束に対して適用
しても、実用性ある繊維を得ることができない。また、
前記方法は発酵処理であることから、その繊維の製造に
長時間を要するためにセルロースまで分解して強度が低
下するという問題もある。
[0003] Conventionally, as a method for obtaining fine fibers that can be used for a woven fabric or the like from such a coarse and rigid fiber bundle, a method of fermenting the fiber bundle for several weeks is known. This method is a method of fermenting and removing pectin and lignin in a fiber bundle to obtain fine fibers. However, in this method, pectin removal can be performed relatively easily, but lignin removal is difficult, and the lignin removal rate is limited,
Only about 3 to 7% of the lignin content contained in the fiber bundle is removed. Therefore, cellulose and lignin are concentrated in the fiber thus obtained, and the lignin content is increased, so that the flexibility and the bleaching property thereof are not yet satisfactory. Further, since this method is a fermentation process, it can be applied only to those with a relatively small amount of lignin that is relatively easily biodegraded, and fiber bundles that have advanced wood conversion, for example, for fiber bundles contained in pineapple and banana trunks, etc. However, it is impossible to obtain a practical fiber. Also,
Since the above method is a fermentation process, it takes a long time to produce the fiber, so that there is also a problem that the cellulose is decomposed and the strength is lowered.

【0004】[0004]

【発明が解決しようとする課題】本発明は、繊維束を含
む植物系原料又は該原料から採取された繊維束から、柔
軟性に富む長い繊維を効率よく製造する方法を提供する
ことをその課題とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for efficiently producing long flexible fibers from a plant-based raw material containing a fiber bundle or a fiber bundle collected from the raw material. And

【0005】[0005]

【課題を解決するための手段】本発明者らは、前記課題
を解決すべく鋭意研究を重ねた結果、本発明を完成する
に至った。すなわち、本発明によれば、繊維束を含む植
物系原料又は該原料から採取された繊維束を原料とし、
これをアルカリ性物質と過酸化水素又は過酸化水素発生
剤を含む水溶液中で温和に処理して柔軟性に富む長い繊
維を得ることを特徴とする植物繊維の製造方法が提供さ
れる。
Means for Solving the Problems The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, have completed the present invention. That is, according to the present invention, a plant-based raw material containing a fiber bundle or a fiber bundle collected from the raw material is used as a raw material,
There is provided a method for producing plant fibers, characterized by gently treating this in an aqueous solution containing an alkaline substance and hydrogen peroxide or a hydrogen peroxide generator to obtain long fibers having a high flexibility.

【0006】本発明で使用する原料は繊維束を含む植物
又はそれから採取された繊維束である。具体的には、バ
ナナ、アバカ(マニラ麻)、パイナップル、サイザル
麻、竜舌蘭等の葉、葉柄、幹又はそれらから得られる繊
維束;ジュート(インド麻)、ケナフ(ボンベイ麻)、
こうぞ、みつまた、桑、雁皮等の靭皮又は該靭皮類から
得られる繊維束等である。なお、植物の葉や靭皮等より
繊維束の方が取扱い容易なので、原料としては繊維束の
方が好ましい。植物からの繊維束採取は従来公知の方法
で行うことができる。この場合、機械力だけでなく微生
物及び/又は酵素を使う生分解処理を併用するのが好ま
しい。
The raw material used in the present invention is a plant containing fiber bundles or fiber bundles collected therefrom. Specifically, banana, abaca (manila hemp), pineapple, sisal, orchid orchid leaves, petioles, stems or fiber bundles obtained from them; jute (indian hemp), kenaf (Bombay hemp),
Kozo, Mitsumata, bast such as mulberry and goose bark, and fiber bundles obtained from the bast. Since the fiber bundle is easier to handle than plant leaves or bast, the fiber bundle is preferable as a raw material. Collection of fiber bundles from plants can be performed by a conventionally known method. In this case, it is preferable to use not only mechanical force but also biodegradation treatment using microorganisms and / or enzymes.

【0007】本発明において、繊維束や繊維束が含まれ
ている植物系原料を処理する処理液は、アルカリ性物質
と過酸化水素を含む水溶液である。アルカリ性物質とし
ては、ナトリウム又はカリウムの水酸化物、炭酸塩及び
重炭酸塩等が使われる。このアルカリ性物質は脱リグニ
ン作用を示す。そして、水酸化物はアルカリ性が強いこ
とから、木質化が比較的進んだリグニン含有量の多い原
料から柔軟性植物繊維を製造する場合に好適である。し
かし、通常の原料から植物繊維を製造する場合には、水
酸化物と炭酸塩の混合物や炭酸塩を単独で使うのが好ま
しい。木質化が軽度の原料を使う場合は、炭酸塩と重炭
酸塩の混合物や重炭酸塩の単独使用が好ましく、繊維を
損傷しないで収率良く柔軟性繊維を得ることができる。
アルカリ性物質の使用量は、絶乾原料に対してNa2O
換算で2〜10重量%、好ましくは5〜10重量%であ
る。
In the present invention, the treatment liquid for treating the fiber bundle or the plant-based raw material containing the fiber bundle is an aqueous solution containing an alkaline substance and hydrogen peroxide. As the alkaline substance, hydroxides, carbonates and bicarbonates of sodium or potassium are used. This alkaline substance exhibits a delignification action. And since hydroxide has strong alkalinity, it is suitable when manufacturing a flexible vegetable fiber from a raw material with a relatively large amount of lignin that has been relatively woody. However, in the case of producing plant fibers from ordinary raw materials, it is preferable to use a mixture of hydroxide and carbonate or a carbonate alone. When using a raw material that is lightly woody, it is preferable to use a mixture of carbonate and bicarbonate or bicarbonate alone, and flexible fibers can be obtained in good yield without damaging the fibers.
The amount of alkaline substances used is Na 2 O
It is 2 to 10% by weight, preferably 5 to 10% by weight in terms of conversion.

【0008】過酸化水素は、アルカリ性物質と共存時に
脱リグニンを容易にすると共に製品の白色度向上効果が
あり、この効果は過酸化水素の代りに反応系で過酸化水
素を発生する化合物を使っても発現する。従って、水溶
性有機過酸やその水溶性塩、水溶性無機過酸やその水溶
性塩、過酸化水素と無機化合物との水溶性付加体等の過
酸化水素発生剤を過酸化水素の代りに加えても良い。こ
れらの使用量は、H2O2として絶乾原料の1〜30重量
%、好ましくは3〜10重量%である。以上のほか、処
理液中には必要に応じて種々の添加剤を加えることがで
きる。例えば、キレート化剤、アントラキノン系化合物
及びマグネシウム化合物を添加することができる。ま
た、みつまたやジュートの靭皮や粗繊維等のようにリグ
ニン分が少ない原料の使用時には、処理液中にシュ酸又
はその水溶性塩を加えると、除去すべきリグニンとペク
チンの溶解除去がほぼ同時に終了し、そのために繊維束
の柔軟化や漂白が迅速で効果的に行われる。ここで添加
されるシュウ酸量は、処理液中の全アルカリ金属の5〜
80%、好ましくは15〜50%がシュウ酸塩に転換す
る量である。
Hydrogen peroxide has the effect of facilitating delignification when coexisting with an alkaline substance and improving the whiteness of the product. This effect uses a compound that generates hydrogen peroxide in the reaction system instead of hydrogen peroxide. Will be expressed. Therefore, a hydrogen peroxide generator such as a water-soluble organic peracid or a water-soluble salt thereof, a water-soluble inorganic peracid or a water-soluble salt thereof, or a water-soluble adduct of hydrogen peroxide and an inorganic compound is used instead of hydrogen peroxide. You may add. The amount of these used as H 2 O 2 is 1 to 30% by weight, preferably 3 to 10% by weight of the absolutely dry raw material. In addition to the above, various additives can be added to the treatment liquid as needed. For example, chelating agents, anthraquinone compounds and magnesium compounds can be added. In addition, when using raw materials with a low lignin content such as mitsumata or jute bast or crude fiber, adding oxalic acid or its water-soluble salt to the treatment liquid almost eliminates the dissolution and removal of lignin and pectin to be removed. At the same time, the fiber bundles are softened and bleached quickly and effectively. The amount of oxalic acid added here is 5 to 5 of all the alkali metals in the treatment liquid.
80%, preferably 15-50%, is the amount converted to oxalate.

【0009】キレート化剤は、処理液や原料中に含まれ
ている重金属イオンを不活性化させる。過酸化水素は重
金属イオンで速やかに分解するが、キレート化剤の添加
により過酸化水素の分解を防ぐことができる。また、キ
レート化剤の添加により得られる植物繊維の白色度が向
上する。このような効果を持つキレート化剤としては公
知品が全部使えるが、クエン酸、EDTA(エチレンジ
アミン四酢酸)、DTPA(ジエチレントリアミン五酢
酸)、ジフォスフォン酸等が好ましく、下記一般式
(1)で示されるジフォスフォン酸又はその水溶性塩が
特に好ましい。
The chelating agent inactivates the heavy metal ions contained in the processing liquid and the raw material. Hydrogen peroxide decomposes rapidly with heavy metal ions, but the addition of a chelating agent can prevent the decomposition of hydrogen peroxide. Further, the whiteness of the plant fiber obtained by adding the chelating agent is improved. As the chelating agent having such an effect, all known products can be used, but citric acid, EDTA (ethylenediaminetetraacetic acid), DTPA (diethylenetriaminepentaacetic acid), diphosphonic acid and the like are preferable and represented by the following general formula (1). Diphosphonic acid or its water-soluble salts are particularly preferred.

【化1】 (但し、Rは炭素数1〜11のアルキル基を表してい
る)
Embedded image (However, R represents an alkyl group having 1 to 11 carbon atoms)

【0010】ジフォスフォン酸やその塩は処理液に溶解
して効果を示すことから、ジフォスフォン酸塩としては
ナトリウム塩やカリウム塩等の水溶性塩が好ましい。ジ
フォスフォン酸又はその塩を添加すると前記キレート化
剤としての効果を示すと共に、アントラキノン系化合物
の使用量低下及び水不溶なマグネシウム化合物等を水溶
性にする効果がある。従って、水に不溶又は難溶なマグ
ネシウム化合物を処理液に添加する場合は、該マグネシ
ウム化合物をジフォスフォン酸含有水中で加熱する等の
方法で水溶性とし、これを処理液に添加するのが好まし
い。また、ジフォスフォン酸が存在するとキレート化剤
やマグネシウム化合物を水溶性にすることができるか
ら、該化合物の存在時には処理液に添加するキレート化
剤やマグネシウム化合物を溶解性と無関係に自由に選択
することができる。キレート化剤は1種又は2種以上を
混合して処理液に添加すれば良く、その添加量は絶乾原
料の0.03〜5重量%、好ましくは0.2〜2重量%
である。
Since diphosphonic acid and its salts are dissolved in the treatment solution and show effects, water-soluble salts such as sodium salts and potassium salts are preferable as the diphosphonate. Addition of diphosphonic acid or a salt thereof has the effect as the chelating agent, and also has the effects of reducing the amount of anthraquinone compound used and making water-insoluble magnesium compounds and the like water-soluble. Therefore, when a magnesium compound which is insoluble or hardly soluble in water is added to the treatment liquid, it is preferable that the magnesium compound is made water-soluble by a method such as heating in water containing diphosphonic acid and then added to the treatment liquid. In addition, since the chelating agent and the magnesium compound can be made water-soluble in the presence of diphosphonic acid, the chelating agent and the magnesium compound to be added to the treatment liquid in the presence of the compound can be freely selected regardless of the solubility. You can The chelating agent may be added singly or in combination of two or more kinds to the treatment liquid, and the addition amount thereof is 0.03 to 5% by weight, preferably 0.2 to 2% by weight of the absolutely dried raw material.
Is.

【0011】アントラキノン系化合物は、アントラキノ
ン、アルキルアントラキノン、ジヒドロキシアントラセ
ン及びアルキルジヒドロキシアントラセン等である。前
記アントラキノン系化合物をアルカリ性過酸化水素水溶
液を主剤とする処理液に添加すると、セルロースと共存
するリグニンとヘミセルロースとの酸化還元触媒として
作用し、顕蓄な脱リグニン効果が得られる。この効果
は、分子内に炭素数1〜12、特に2〜5のアルキル基
を1個持つ場合に顕著である。また、アルキル基の置換
部位はβ位が好ましい。アントラキノン系化合物は、前
記の中から選ばれる一種又は2種以上を混合して使えば
良く、その添加量は絶乾原料の0.01〜2重量%、好
ましくは0.03〜0.3重量%である。
The anthraquinone compounds include anthraquinone, alkyl anthraquinone, dihydroxy anthracene and alkyl dihydroxy anthracene. When the above-mentioned anthraquinone compound is added to a treatment liquid containing an alkaline hydrogen peroxide aqueous solution as a main component, it acts as a redox catalyst for lignin and hemicellulose that coexist with cellulose, and a remarkable delignification effect is obtained. This effect is remarkable when one alkyl group having 1 to 12 carbon atoms, particularly 2 to 5 carbon atoms is contained in the molecule. Further, the substitution position of the alkyl group is preferably β-position. The anthraquinone compound may be used alone or as a mixture of two or more selected from the above, and the addition amount thereof is 0.01 to 2% by weight, preferably 0.03 to 0.3% by weight of the absolutely dry raw material. %.

【0012】マグネシウム化合物はセルロースの分解を
防止する効果を持ち、処理液中に添加すると得られる繊
維の品質を向上させることができる。この効果は、マグ
ネシウム化合物がアルカリ性過酸化水素水溶液によるセ
ルロースの崩壊を防ぐ効果によるものと推定される。ま
た、本発明で使用するマグネシウム化合物は水溶性であ
ることが好ましいが、水不溶性の場合はジフォスフォン
酸又はその塩で処理して水溶性にすれば良いから、水溶
性化合物に限定されない。従って、マグネシウム化合物
は酸化物、炭酸塩、硫酸塩、塩化物、乳酸塩、酢酸塩等
の中から選ばれる1種又は2種以上混合物として添加す
れば良い。なお、マグネシウム化合物を有機酸塩として
添加すると処理液中に塩素や硫黄等の公害性元素が蓄積
しないから、処理後の液からアルカリ性物質等を回収再
利用する際に好ましい。マグネシウム化合物の添加量
は、絶乾原料に対してMgOとして0.02〜1重量
%、好ましくは0.1〜0.5重量%である。
The magnesium compound has the effect of preventing the decomposition of cellulose and can improve the quality of the fiber obtained by adding it to the treatment liquid. This effect is presumed to be due to the effect of the magnesium compound to prevent the collapse of cellulose by the alkaline hydrogen peroxide solution. Further, the magnesium compound used in the present invention is preferably water-soluble, but when it is insoluble in water, it may be treated with diphosphonic acid or a salt thereof to make it water-soluble, and is not limited to a water-soluble compound. Therefore, the magnesium compound may be added as one kind or a mixture of two or more kinds selected from oxides, carbonates, sulfates, chlorides, lactates, acetates and the like. It should be noted that the addition of a magnesium compound as an organic acid salt is preferable when recovering and reusing an alkaline substance or the like from the liquid after the treatment, since polluting elements such as chlorine and sulfur do not accumulate in the treatment liquid. The addition amount of the magnesium compound is 0.02 to 1% by weight, preferably 0.1 to 0.5% by weight as MgO with respect to the absolutely dried raw material.

【0013】本発明では、原料中のリグニンとペクチン
を処理液に溶解除去して柔軟性に富む長繊維を得る。本
発明の場合、原料を温和に処理することが重要であり、
過酷に処理すると繊維束が短繊維化されるので好ましく
ない。本発明の原料処理温度は特に制約されないが、一
般的には常温又は常圧下の処理液の沸点以下である。そ
の処理時間は、常温〜50℃で処理する場合は2〜48
時間、好ましくは6〜24時間であり、50℃〜処理水
の沸点で処理する場合は0.5〜24時間、好ましくは
2〜8時間である。処理液中のアルカリ性物質の濃度
は、Na2Oとして0.1〜4重量%、好ましくは0.
2〜2重量%とするのが良い。また、過酸化水素の濃度
は、H2O2として0.02〜3重量%、好ましくは0.
1〜0.8重量%とするのが良い。
In the present invention, lignin and pectin in the raw material are dissolved and removed in the treatment liquid to obtain long fibers having a high flexibility. In the case of the present invention, it is important to treat the raw material gently,
Severe treatment shortens the fiber bundle, which is not preferable. The raw material treatment temperature of the present invention is not particularly limited, but is generally not higher than the boiling point of the treatment liquid at room temperature or atmospheric pressure. The treatment time is 2 to 48 when treated at room temperature to 50 ° C.
The time is preferably 6 to 24 hours, and is 0.5 to 24 hours, preferably 2 to 8 hours when treated at 50 ° C to the boiling point of the treated water. The concentration of the alkaline substance in the treatment liquid is 0.1 to 4% by weight as Na 2 O, preferably 0.1.
It is preferable to be 2 to 2% by weight. Further, the concentration of hydrogen peroxide is 0.02 to 3% by weight as H 2 O 2 , preferably 0.1.
It is preferable to set it to 1 to 0.8% by weight.

【0014】本発明によれば、原料中のペクチンは勿
論、リグニンも容易に除去することができる。本発明の
場合、リグニン分は原料中の全リグニンの30〜100
重量%、好ましくは60〜90重量%を除去するように
処理するのがよい。本発明で得られる長繊維において、
そのリグニン含有率は7重量%以下、好ましくは3重量
%以下であり、その下限値は特に制約されないが、通常
0.5〜3重量%程度である。リグニン含有率の下限値
がこれより低くなると、繊維の強度が著しく損なわれる
ようになるので好ましくない。また、ペクチンの含有率
は5重量%以下、好ましくは2重量%以下であり、その
下限値は特に制約されないが、通常0.3〜2重量%程
度である。ペクチン含有率がこれより低くなると、繊維
の強度が著しく損われるようになるので好ましくない。
また、本発明の繊維は一般に120〜350のヤング率
を有する。本発明において原料に使われる繊維の長さは
30cm以上、好ましくは100cm以上であり、その
繊維の太さ(直径)は通常500μm以下、好ましくは
50〜200μmである。
According to the present invention, not only pectin in the raw material but also lignin can be easily removed. In the case of the present invention, the lignin content is 30 to 100 of the total lignin in the raw material.
It may be treated so as to remove wt.%, Preferably 60 to 90 wt.%. In the long fiber obtained in the present invention,
The lignin content is 7% by weight or less, preferably 3% by weight or less, and the lower limit value is not particularly limited, but is usually about 0.5 to 3% by weight. If the lower limit of the lignin content is lower than this value, the strength of the fiber will be significantly impaired, which is not preferable. The pectin content is 5% by weight or less, preferably 2% by weight or less, and the lower limit thereof is not particularly limited, but is usually about 0.3 to 2% by weight. If the pectin content is lower than this range, the strength of the fiber is significantly impaired, which is not preferable.
Also, the fibers of the present invention generally have a Young's modulus of 120-350. The length of the fiber used as a raw material in the present invention is 30 cm or more, preferably 100 cm or more, and the thickness (diameter) of the fiber is usually 500 μm or less, preferably 50 to 200 μm.

【0015】本発明では、繊維束や繊維束を含む植物系
原料の処理容器に過酸化水素の分解を促進する重金属イ
オンが溶出する重金属容器、或いはアルカリ性物質に弱
いアルミニウム製やほうろう鉄器製等を避けるのが好ま
しい。従って、ステンレス製容器やステンレスで内張り
した容器を使うのが好ましい。また。原料処理時には原
料中のリグニンやペクチンが処理液中の薬品で水溶性と
なって除かれるから、原料を処理液中に浸漬すると共に
該処理液に振動や渦流を与え、これによって原料と新鮮
な処理液との接触を良くするのが好ましい。そのため、
処理液を強制循環したり超音波発生装置からの高周波振
動を処理液に与えるのが望ましく、高周波振動を与える
場合の振動数は105〜107ヘルツ、好ましくは(5〜
50)×105ヘルツが良い。このような方法で、繊維
束の長さを保ったまま該繊維束をばらばらにほぐして柔
軟にすることができるが、処理液による処理中又は処理
後に繊維束を横方向から叩く等の方法によって、該繊維
束に横方向から機械的圧縮と弛緩とを繰り返して与える
と更に好ましい。そして、この方法によれば極めて繊細
で柔軟な高品質の植物繊維を得ることができる。
In the present invention, a container for processing fiber bundles or plant-based raw materials containing fiber bundles is made of a heavy metal container in which heavy metal ions that promote the decomposition of hydrogen peroxide are eluted, or a container made of aluminum or enamel ironware which is weak against alkaline substances. It is preferable to avoid it. Therefore, it is preferable to use a stainless steel container or a container lined with stainless steel. Also. During the processing of the raw material, lignin and pectin in the raw material become water-soluble and are removed by the chemicals in the processing liquid, so that the raw material and the fresh material are vibrated and swirled while being immersed in the processing liquid. It is preferable to improve contact with the processing liquid. for that reason,
It is desirable to forcibly circulate the treatment liquid or to give high-frequency vibration from the ultrasonic generator to the treatment liquid. The frequency of high-frequency vibration is 10 5 to 10 7 hertz, preferably (5 to 5 Hz).
50) × 10 5 Hertz is good. By such a method, the fiber bundle can be loosened and made flexible while keeping the length of the fiber bundle, but by a method such as tapping the fiber bundle from the lateral direction during or after the treatment with the treatment liquid. More preferably, the fiber bundle is repeatedly subjected to mechanical compression and relaxation from the lateral direction. And, according to this method, extremely delicate and flexible high-quality plant fibers can be obtained.

【0016】本発明においては、原料の繊維束が単繊維
化して単繊維や単繊維の結束繊維が副生する。この副生
は従来法で麻を製造する場合にも起るが、従来法では副
生する単繊維や結束繊維中にリグニン分が多いのでパル
プ等に利用するのが困難であった。しかしながら、本発
明法で副生する単繊維や結束繊維中のリグニン分は少な
く、しかも白色度が高いことから、これらを目的とする
柔軟性で長い植物繊維から分離すれば、そのままパルプ
として用いることができる。本発明で発生する廃液は、
これを固形分50〜70重量%程度まで濃縮後に燃焼す
れば熱としてエネルギーを回収することができ、エネル
ギー回収後の灰から水溶性成分を分離回収すれば、アル
カリ金属を炭酸塩として回収することができる。また、
処理液中にシュウ酸が含まれている場合は、処理液中に
カルシウム塩を加えることでシュウ酸をカルシウム塩の
沈殿として回収することができる。
In the present invention, the raw material fiber bundle is made into a single fiber, and a single fiber or a bundle of single fibers is produced as a by-product. Although this by-product also occurs when hemp is produced by the conventional method, it is difficult to use it for pulp or the like because the conventional method has a large amount of lignin in the by-produced monofilament or binding fiber. However, since the amount of lignin in the single fiber or the binding fiber produced as a by-product in the method of the present invention is small and the whiteness is high, if they are separated from the desired flexible and long plant fibers, they can be directly used as pulp. You can The waste liquid generated in the present invention is
Energy can be recovered as heat by concentrating this to a solid content of about 50 to 70% by weight and burning, and if a water-soluble component is separated and recovered from the ash after energy recovery, an alkali metal can be recovered as a carbonate. You can Also,
When oxalic acid is contained in the treatment liquid, oxalic acid can be recovered as a calcium salt precipitate by adding a calcium salt to the treatment liquid.

【0017】[0017]

【実施例】次に本発明を実施例によって更に具体的に説
明するが、本発明はこの実施例によって限定されるもの
ではない。また、以下に記す%はいずれも重量%であ
る。
EXAMPLES The present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. In addition, all% described below are% by weight.

【0018】実施例1 パイナップルの古い株から切り離した葉2000kgを
原料とし、これを2枚刃からなる繊維採取器に掛けて紐
状繊維を採取した。これを天日で乾燥して、リグニン含
有率10.4%の粗繊維55.6kgを取得した。この
粗繊維を内容積600リットルのステンレスで内張りし
た平釜に仕込み、これに下記組成の処理液を556リッ
トル加えて90℃で10時間処理した。 処理液中の薬品量(対風乾原料) NaOH(Na2Oとして) 8% H2O2 3% アントラキノン 0.05% EDTA 0.5% MgO 0.1% 前記処理後の繊維を水洗してから柔軟性長繊維と単繊維
とを分離すると、白色度(ハンター)73.8%でリグ
ニン含有率4.7%の柔軟性繊維34.2kg(収率6
1.5%)と、カッパー価20.1の単繊維5.7kg
(収率10.3%)が得られた。この単繊維は高品質パ
ルプとして利用し得るものであった。
Example 1 2000 kg of leaves separated from an old strain of pineapple were used as a raw material, and this was hung on a fiber extractor consisting of two blades to collect cord fibers. This was dried in the sun to obtain 55.6 kg of crude fiber having a lignin content of 10.4%. The crude fiber was charged into a flat kettle lined with stainless steel having an internal volume of 600 liters, to which 556 liters of a treatment liquid having the following composition was added and treated at 90 ° C. for 10 hours. Amount of chemicals in treatment liquid (vs. air-dried raw material) NaOH (as Na 2 O) 8% H 2 O 2 3% Anthraquinone 0.05% EDTA 0.5% MgO 0.1% After washing the fibers after treatment When the flexible long fiber and the single fiber are separated from the above, 34.2 kg (yield 6%) of the flexible fiber having a whiteness (hunter) of 73.8% and a lignin content of 4.7%.
1.5%) and 5.7 kg of monofilament with a Kappa number of 20.1.
(Yield 10.3%) was obtained. This single fiber could be used as a high quality pulp.

【0019】実施例2 バナナの果実を採取した古い幹200kgを切倒し、こ
れをローラーの間に挟んで圧搾脱汁した。脱汁後の幹は
100℃の蒸気で30分間処理してから、内容積300
リットルのステンレス製容器に仕込み、これに水200
リットルとペクチナーゼ200gとアミラーゼ50gを
加え、60℃で8時間保持後に水洗するとリグニン含有
率12.9%の粗繊維の束11.5kgが得られた。前
記粗繊維の束を、1メガヘルツの超音波発生装置を取り
付けた内容積200リットルのステンレス製平釜に入
れ、これに下記組成の処理液を115リットル加え、液
に超音波をあてながら90℃で5時間処理した。処理
後、水洗乾燥した繊維の束を板の上に乗せて木槌で叩い
たところ、ブライトネスがGE83.2%でリグニン含
有率が5.3%の柔軟性長繊維5.8kgが得られ(粗
繊維からの収率50.5%、古幹からの収率2.6
%)、同時にカッパー価12.6の単繊維0.66kg
(粗繊維からの収率5.7%)が得られた。 処理液中の薬品量(対風乾原料) KOH(Na2Oモル換算) 4% K2CO3(Na2Oモル換算) 6% H2O2 7% β−アミルアントラキノン 0.1% 一般式(1)で表され、Rがデシル基のジフォスフォン酸 1.0% MgO 0.1%
Example 2 200 kg of an old trunk from which a banana fruit was collected was cut down and sandwiched between rollers to squeeze and squeeze. After the juice is removed, the stem is treated with steam at 100 ° C for 30 minutes, and then the internal volume of 300
Charge into a liter stainless steel container and add water to it.
Liter, 200 g of pectinase and 50 g of amylase were added, and the mixture was kept at 60 ° C. for 8 hours and then washed with water to obtain 11.5 kg of a crude fiber bundle having a lignin content of 12.9%. The bundle of crude fibers was placed in a stainless steel pot having an internal volume of 200 liters equipped with an ultrasonic generator of 1 megahertz, and 115 liters of a treating solution having the following composition was added thereto, and 90 ° C. while applying ultrasonic waves to the solution. Treated for 5 hours. After the treatment, a bundle of fibers washed with water and dried was placed on a plate and beaten with a mallet to obtain 5.8 kg of flexible long fibers having a brightness of GE83.2% and a lignin content of 5.3% ( 50.5% yield from crude fiber, 2.6 yield from old trunk
%), And 0.66 kg of monofilament with a Kappa number of 12.6 at the same time.
(Yield from crude fiber 5.7%) was obtained. Drug content in the treatment liquid (Taikazeinui material) KOH (Na 2 O molar basis) 4% K 2 CO 3 ( Na 2 O molar basis) 6% H 2 O 2 7 % β- amylanthraquinone 0.1% Formula Represented by (1), R is a decyl diphosphonic acid 1.0% MgO 0.1%

【0020】実施例3 ジュートの皮を剥ぎ取り、これを風乾量として30kg
となる量だけ内容積300リットルのステンレス製容器
に仕込み、これに水200リットルとペクチナーゼ25
0gを加えて加温し、60℃で8時間処理後に水洗する
とリグニン含有率18.2%の粗繊維の束21.3kg
が得られた。前記粗繊維の束を、外部に熱交換器と液の
強制循環機を備えた内容積300リットルのステンレス
製反応装置に仕込み、下記組成の処理液を213リット
ル加えて液を強制循環しながら98℃で4時間処理し
た。処理後、水洗乾燥した繊維の束を板の上に乗せて木
槌で叩いたところ、ブライトネスがGE68.1%でリ
グニン含有率が8.7%、ペクチン含有率が0.3%の
麻13.4kg(粗繊維からの収率63.1%)が得ら
れると共に、カッパー価28.1の単繊維が0.83k
g得られた。 処理液中の薬品量(対風乾原料) Na2CO3(Na2Oとして) 8% NaHCO3(Na2Oとして) 10% H2O2 7% 9,10−ジヒドロキシアンスラセン 0.1% 一般式(1)で表され、Rがオクチル基のジフォスフォン酸 1.0% MgO 0.1%
Example 3 The skin of jute was peeled off, and the air-dried amount was 30 kg.
Into a stainless steel container with an internal volume of 300 liters, add 200 liters of water and 25 pectinase.
When 0 g was added and the mixture was heated and treated at 60 ° C. for 8 hours and then washed with water, a bundle of crude fibers having a lignin content of 18.2% 21.3 kg
was gotten. The crude fiber bundle was charged into a stainless steel reactor having an internal volume of 300 liters equipped with a heat exchanger and a forced circulation device for liquid, and 213 liters of a treatment liquid having the following composition was added to the reactor while forcibly circulating the liquid. It was treated at 4 ° C. for 4 hours. After the treatment, a bundle of fibers washed and dried was placed on a board and beaten with a mallet. Hemp 13 with a brightness of GE 68.1%, a lignin content of 8.7% and a pectin content of 0.3% .4 kg (yield from crude fiber 63.1%) is obtained, and single fiber with a kappa number of 28.1 is 0.83 k.
g was obtained. Amount of chemicals in treatment liquid (air-drying raw material) Na 2 CO 3 (as Na 2 O) 8% NaHCO 3 (as Na 2 O) 10% H 2 O 2 7% 9,10-dihydroxyanthracene 0.1% Represented by the general formula (1), R is an octyl-based diphosphonic acid 1.0% MgO 0.1%

【0021】実施例4 表皮を除去したこうぞを冷水にさらし、これを乾燥して
いわゆる白皮5.2kgを得た。該こうぞの白皮を内容
積100リットルのステンレス製平釜に仕込み、これに
下記組成の処理液を52リットル加え、1メガヘルツの
超音波を処理液にあてながら90℃で3時間処理した。
前記処理後の繊維を水洗後に柔軟性長繊維と単繊維とを
分離すると、リグニン5.3%とペクチン4.1%を含
み、ブライトネスがGE89.6%の柔軟性長繊維65
kg(対白皮収率70.1%)を得ると共に、カッパー
価8.2の単繊維0.39kg(収率7.5%)を得
た。 処理液中の薬品量(対風乾原料) 過炭酸ナトリウム(Na2Oとして) 9% シュウ酸ナトリウム(Na2Oとして) 6% β−アミルアントラキノン 0.3% 一般式(1)で表され、Rがオクチル基のジフォスフォン酸 1.0% MgCl2(MgOとして) 0.1%
Example 4 A groove having the skin removed was exposed to cold water and dried to obtain so-called white skin of 5.2 kg. The white skin of the groove was placed in a stainless steel flat pot having an internal volume of 100 liters, and 52 liters of a treatment liquid having the following composition was added thereto, and treated at 90 ° C. for 3 hours while applying ultrasonic waves of 1 MHz to the treatment liquid.
When the flexible filaments and the monofilaments are separated after washing the treated fibers with water, the flexible filaments containing 5.3% lignin and 4.1% pectin and having a brightness of GE89.6% 65.
In addition to obtaining kg (yield 70.1% based on the peel), 0.39 kg (yield 7.5%) of single fiber having a kappa number of 8.2 was obtained. Amount of chemicals in treatment liquid (air-dried raw material) Sodium percarbonate (as Na 2 O) 9% Sodium oxalate (as Na 2 O) 6% β-amylanthraquinone 0.3% Represented by the general formula (1), R is an octyl diphosphonic acid 1.0% MgCl 2 (as MgO) 0.1%

【0022】[0022]

【発明の効果】本発明によれば、これまで高級布地等の
原料用繊維原料として使われていなかった農産廃棄物等
から、繊細で柔軟性に富む長い繊維を効率よく製造する
ことができる。また、本発明で副生する単繊維はパルプ
として利用することができる。
Industrial Applicability According to the present invention, delicate and flexible long fibers can be efficiently produced from agricultural wastes which have not been used as raw materials for raw materials such as high-grade fabrics. Further, the single fiber produced as a by-product in the present invention can be used as pulp.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 繊維束を含む植物系原料又は該原料から
採取された繊維束を原料とし、これをアルカリ性物質と
過酸化水素又は過酸化水素発生剤を含む水溶液中で温和
に処理して柔軟性に富む長い繊維を得ることを特徴とす
る植物繊維の製造方法。
1. A plant-based raw material containing a fiber bundle or a fiber bundle collected from the raw material is used as a raw material, which is mildly treated in an aqueous solution containing an alkaline substance and hydrogen peroxide or a hydrogen peroxide generator to provide flexibility. A method for producing a plant fiber, which comprises obtaining a long fiber rich in nature.
【請求項2】 水溶液中にキレート化剤とアントラキノ
ン系化合物が含まれていることを特徴とする請求項1に
記載した植物繊維の製造方法。
2. The method for producing a plant fiber according to claim 1, wherein the aqueous solution contains a chelating agent and an anthraquinone compound.
【請求項3】 水溶液中にマグネシウム化合物が含まれ
ていることを特徴とする請求項1又は2に記載した植物
繊維の製造方法。
3. The method for producing plant fiber according to claim 1, wherein the aqueous solution contains a magnesium compound.
【請求項4】 水溶液中にシュウ酸又はその水溶性塩が
含まれていることを特徴とする請求項1〜3のいずれか
に記載した植物繊維の製造方法。
4. The method for producing a plant fiber according to claim 1, wherein the aqueous solution contains oxalic acid or a water-soluble salt thereof.
【請求項5】 キレート化剤の少なくとも一部が下記一
般式(1)で表されるジフォスフォン酸であることを特
徴とする請求項2〜4のいずれかに記載した植物繊維の
製造方法。 【化1】 (但し、Rは炭素数1〜11のアルキル基を表してい
る)
5. The method for producing a plant fiber according to claim 2, wherein at least a part of the chelating agent is diphosphonic acid represented by the following general formula (1). Embedded image (However, R represents an alkyl group having 1 to 11 carbon atoms)
【請求項6】 水溶液に渦流及び/又は振動を与えるこ
とを特徴とする請求項1〜5のいずれかに記載した植物
繊維の製造方法。
6. The method for producing a plant fiber according to claim 1, wherein the aqueous solution is swirled and / or vibrated.
【請求項7】 水溶液に高周波振動を与えることを特徴
とする請求項1〜5のいずれかに記載した植物繊維の製
造方法。
7. The method for producing a vegetable fiber according to claim 1, wherein the aqueous solution is subjected to high frequency vibration.
JP2352295A 1995-01-18 1995-01-18 Production of highly flexible vegetable fiber Pending JPH08199420A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2352295A JPH08199420A (en) 1995-01-18 1995-01-18 Production of highly flexible vegetable fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2352295A JPH08199420A (en) 1995-01-18 1995-01-18 Production of highly flexible vegetable fiber

Publications (1)

Publication Number Publication Date
JPH08199420A true JPH08199420A (en) 1996-08-06

Family

ID=12112789

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2352295A Pending JPH08199420A (en) 1995-01-18 1995-01-18 Production of highly flexible vegetable fiber

Country Status (1)

Country Link
JP (1) JPH08199420A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005070952A1 (en) * 2004-01-23 2005-08-04 Mcs Micro Carrier Systems Gmbh Lipid- derivatized bisphosphonic acid
JP2007126809A (en) * 2005-11-01 2007-05-24 Meirong Xu Process for extraction and preparation of bast fibers, bast fibers obtained from this process, and use of these bast fibers
JP2010095805A (en) * 2008-10-14 2010-04-30 Nisshinbo Holdings Inc Method for producing banana fibers and blended yarn and fiber structure using banana fibers
CN104630908A (en) * 2015-02-15 2015-05-20 东华大学 Method for preparing flax fiber by combined process of mucor circinelloides DK1 strain and hydrogen peroxide
CN104630909A (en) * 2015-02-15 2015-05-20 东华大学 Method for preparing flax fiber by ultrasonic combination of mucor circinelloides DK1 strain and hydrogen peroxide
JP2023523935A (en) * 2020-04-21 2023-06-08 ユニバーシティ オブ メリーランド, カレッジ パーク Method for extracting delignified cellulosic fibers from natural plant material and materials using such fibers

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005070952A1 (en) * 2004-01-23 2005-08-04 Mcs Micro Carrier Systems Gmbh Lipid- derivatized bisphosphonic acid
JP2007126809A (en) * 2005-11-01 2007-05-24 Meirong Xu Process for extraction and preparation of bast fibers, bast fibers obtained from this process, and use of these bast fibers
JP2010095805A (en) * 2008-10-14 2010-04-30 Nisshinbo Holdings Inc Method for producing banana fibers and blended yarn and fiber structure using banana fibers
CN104630908A (en) * 2015-02-15 2015-05-20 东华大学 Method for preparing flax fiber by combined process of mucor circinelloides DK1 strain and hydrogen peroxide
CN104630909A (en) * 2015-02-15 2015-05-20 东华大学 Method for preparing flax fiber by ultrasonic combination of mucor circinelloides DK1 strain and hydrogen peroxide
JP2023523935A (en) * 2020-04-21 2023-06-08 ユニバーシティ オブ メリーランド, カレッジ パーク Method for extracting delignified cellulosic fibers from natural plant material and materials using such fibers

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