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JP2006016711A - Method for dyeing polyester fiber - Google Patents

Method for dyeing polyester fiber Download PDF

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JP2006016711A
JP2006016711A JP2004193092A JP2004193092A JP2006016711A JP 2006016711 A JP2006016711 A JP 2006016711A JP 2004193092 A JP2004193092 A JP 2004193092A JP 2004193092 A JP2004193092 A JP 2004193092A JP 2006016711 A JP2006016711 A JP 2006016711A
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dyeing
carbon dioxide
polyester fiber
supercritical carbon
polyester fibers
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Tomoyuki Horio
智之 堀尾
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Teijin Ltd
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Teijin Techno Products Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for dyeing a polyester fiber, capable of dyeing the polyester fiber as a deep color and in a good efficiency. <P>SOLUTION: This method for dyeing the polyester fiber in supercritical carbon dioxide fluid is provided by adding 0.01-10 mole % mixed liquid of water with at least one polar organic solvent selected from a group consisting of methanol, ethanol, propanol, isopropyl alcohol, butanol, benzyl alcohol, acetone, acetophenone, N-methyl-2-pyrrolidone, methyl ethyl ketone, dimethyl sulfoxide, dimethyl formamide, ethylene glycol and acetonitrile to the supercritical carbon dioxide fluid. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明はポリエステル繊維の染色方法に関するものであり、更に詳しくは、ポリエステル繊維を濃色に、且つ効率良く染色することが可能なポリエステル繊維の染色方法に関するものである。   The present invention relates to a method for dyeing polyester fibers, and more particularly, to a method for dyeing polyester fibers capable of dyeing polyester fibers darkly and efficiently.

ポリエステル繊維の染色加工は、水を大量に使用し、しかも染色後に未着染料や染色助剤などが廃水となって大量に排出されるので、水質汚濁の原因となり、これの浄化が企業の大きな負担となりはじめている。   Polyester fiber dyeing uses a large amount of water, and after dyeing, unattached dyes and dyeing assistants are discharged as waste water and discharged in large quantities. It is starting to become a burden.

このような問題を解決するため、最近、廃液をほとんど出さずにポリエステル繊維を効率よく染色する方法として、超臨界二酸化炭素中で染色を行う方法が提案されている。   In order to solve such problems, recently, a method of dyeing in supercritical carbon dioxide has been proposed as a method of efficiently dyeing polyester fibers with little waste liquid.

例えば、特開平5−132880号公報には、分散染料を用いて疎水性繊維、例えば、ポリエステル、ナイロン、ポリオレフィン等の繊維を高濃度で染色する方法が開示されている。   For example, Japanese Patent Application Laid-Open No. 5-132880 discloses a method of dyeing hydrophobic fibers such as polyester, nylon, polyolefin and the like with a high concentration using a disperse dye.

さらに、特開2002−371483号公報、特開2002−363870号公報には、セルロース繊維を超臨界二酸化炭素中にて染色する方法が開示されているが、該方法を採用した場合、高温度では染料が分解し鮮明な染色ができないし、一方、低圧では染料の溶解度が不十分であるため、実質的に濃度の高い染色物が得られないという問題があった。
特開平5−132880号公報 特開2002−371483号公報 特開2002−363870号公報
Furthermore, JP-A-2002-371383 and JP-A-2002-363870 disclose methods for dyeing cellulose fibers in supercritical carbon dioxide. The dye is decomposed and cannot be dyed clearly. On the other hand, the dye has insufficient solubility at a low pressure, so that there is a problem that a dyed substance having a substantially high concentration cannot be obtained.
JP-A-5-132880 JP 2002-371383 A JP 2002-363870 A

本発明の目的は、上記従来技術の有する問題点を解決し、特に、ポリエステル繊維を濃色に、且つ効率良く染色することが可能なポリエステル繊維の染色方法を提供することにある。   An object of the present invention is to solve the above-mentioned problems of the prior art, and in particular, to provide a method for dyeing polyester fibers capable of dyeing polyester fibers darkly and efficiently.

本発明者らは上記目的を達成するために鋭意検討した結果、超臨界二酸化炭素による染色に際し、極性有機溶媒と水との混合液を共溶媒として併用するとき、所望の濃度が発現することを究明し、本発明に到達した。   As a result of intensive studies to achieve the above object, the present inventors have found that, when dyeing with supercritical carbon dioxide, when using a mixture of a polar organic solvent and water as a cosolvent, a desired concentration is expressed. As a result, the present invention was reached.

かくして本発明によれば、超臨界二酸化炭素流体中で、ポリエステル繊維を染色するに際し、該超臨界二酸化炭素流体に、メタノール、エタノール、プロパノール、イソプロピルアルコール、ブタノール、ベンジルアルコール、アセトン、アセトフェノン、N−メチル−2−ピロリドン、メチルエチルケトン、ジメチルスルフォキシド、ジメチルフォルムアミド、エチレングリコール、アセトニトリルからなる群から選ばれた少なくとも一種の極性有機溶媒と水との混合液を0.01〜10モル%添加することを特徴とするポリエステル繊維の染色方法が提供される。   Thus, according to the present invention, when polyester fibers are dyed in a supercritical carbon dioxide fluid, methanol, ethanol, propanol, isopropyl alcohol, butanol, benzyl alcohol, acetone, acetophenone, N- 0.01 to 10 mol% of a mixed liquid of at least one polar organic solvent selected from the group consisting of methyl-2-pyrrolidone, methyl ethyl ketone, dimethyl sulfoxide, dimethyl formamide, ethylene glycol, and acetonitrile and water is added. A method for dyeing polyester fibers is provided.

本発明によれば、廃液をほとんど出さずに、ポリエステル繊維を濃色に、且つ効率良く染色することが可能なポリエステル繊維の染色方法が提供されるので、ポリエステル繊維の染色加工に広く使用することができる。   According to the present invention, a polyester fiber dyeing method capable of efficiently dyeing polyester fibers in a dark color with little waste liquid is provided, so that it can be widely used for dyeing polyester fibers. Can do.

以下、本発明を詳細に説明する。本発明で使用するポリエステル繊維とは、エチレンテレフタレートを主たる繰り返し成分とするものが好ましく、繰り返し単位の90モル%以上がエチレンテレフタレートであるものがより好ましく、さらに繰り返し単位の95モル%以上がエチレンテレフタレートであるものが好ましい。   Hereinafter, the present invention will be described in detail. The polyester fiber used in the present invention is preferably one having ethylene terephthalate as the main repeating component, more preferably 90 mol% or more of the repeating unit is ethylene terephthalate, and more preferably 95 mol% or more of the repeating unit of ethylene terephthalate. Are preferred.

尚、該ポリエステルには、少量の共重合成分が共重合されていても良く、具体的には、イソフタル酸、5−ナトリウムスルホイソフタル酸、ナフタレンジカルボン酸などの芳香族ジカルボン酸、アジピン酸、セバシン酸などの脂肪族ジカルボン酸、テトラメチレングリコール、ヘキサメチレングリコールなどの脂肪族ジオールなどが例示される。更に該ポリエステル繊維は、本範囲の目的を損なわない範囲内で、安定剤、酸化防止剤、帯電防止剤、蛍光増白剤、触媒、着色剤などを添加したものでもよい。   The polyester may be copolymerized with a small amount of a copolymer component, specifically, aromatic dicarboxylic acids such as isophthalic acid, 5-sodium sulfoisophthalic acid, naphthalenedicarboxylic acid, adipic acid, sebacin. Examples include aliphatic dicarboxylic acids such as acids, and aliphatic diols such as tetramethylene glycol and hexamethylene glycol. Further, the polyester fiber may be added with a stabilizer, an antioxidant, an antistatic agent, a fluorescent brightening agent, a catalyst, a colorant, and the like within a range not impairing the purpose of this range.

本発明においては、上記ポリエステル繊維を、超臨界二酸化炭素流体中で染色するに際し、該超臨界二酸化炭素流体に、メタノール、エタノール、プロパノール、イソプロピルアルコール、ブタノール、ベンジルアルコール、アセトン、アセトフェノン、N−メチル−2−ピロリドン、メチルエチルケトン、ジメチルスルフォキシド、ジメチルフォルムアミド、エチレングリコール、アセトニトリルからなる群から選ばれた少なくとも一種の極性有機溶媒と水との混合液を共溶媒として添加する。   In the present invention, when the polyester fiber is dyed in a supercritical carbon dioxide fluid, methanol, ethanol, propanol, isopropyl alcohol, butanol, benzyl alcohol, acetone, acetophenone, N-methyl is added to the supercritical carbon dioxide fluid. A mixture of at least one polar organic solvent selected from the group consisting of -2-pyrrolidone, methyl ethyl ketone, dimethyl sulfoxide, dimethyl formamide, ethylene glycol, and acetonitrile and water is added as a co-solvent.

ここで、添加する混合液の量は0.01〜10モル%、好ましくは0.1〜5モル%である。該添加量が0.01モル%より少ない場合は、本発明の効果が充分に発現せず、一方、該添加量が10モル%を越える場合は、染色性が低下するばかりでなく、処理後の繊維布帛などに溶媒が残存し、溶媒除去の後処理が必要となるので好ましくない。   Here, the amount of the mixed solution to be added is 0.01 to 10 mol%, preferably 0.1 to 5 mol%. When the added amount is less than 0.01 mol%, the effect of the present invention is not sufficiently exhibited. On the other hand, when the added amount exceeds 10 mol%, not only the dyeability is lowered but also after the treatment. This is not preferable because the solvent remains in the fiber fabric and the like, and a post-treatment after removing the solvent is required.

次いで、本発明においては、上記混合液を添加した超臨界二酸化炭素流体中に染料を添加し、7〜35MPaの圧力、及び40〜200℃の温度で染色する。   Next, in the present invention, a dye is added to the supercritical carbon dioxide fluid to which the above mixed solution is added, and dyeing is performed at a pressure of 7 to 35 MPa and a temperature of 40 to 200 ° C.

ここで用いる染料としては、水に難溶か又は不溶性の分散染料が使用可能で、その例としては、ニトロ染料、メチン染料、キノリン染料、アミノナフトキノン染料、クマリン染料、好ましくはアントラキノン染料、トリシアノビニル染料、アゾ染料、ジニトロジフェニルアミン、など公知の分散染料が使用できる。   As the dye used here, disperse dyes that are sparingly soluble or insoluble in water can be used. Examples thereof include nitro dyes, methine dyes, quinoline dyes, aminonaphthoquinone dyes, coumarin dyes, preferably anthraquinone dyes, tricyano dyes. Known disperse dyes such as vinyl dyes, azo dyes and dinitrodiphenylamine can be used.

染料の添加量は、合成繊維の重量に対し0.01〜10重量部(%owf)であることが好ましい。該添加量が0.01%owfよりも少ない場合には所望の色相に染色できない場合がある。一方、該添加量が20%owfを超える場合には超臨界処理機械の中に染料が多く残存し、洗浄に手間がかかる。   The addition amount of the dye is preferably 0.01 to 10 parts by weight (% owf) with respect to the weight of the synthetic fiber. If the amount added is less than 0.01% owf, the desired hue may not be dyed. On the other hand, when the addition amount exceeds 20% owf, a large amount of dye remains in the supercritical processing machine, and it takes time and effort for cleaning.

本発明の染色方法における超臨界二酸化炭素流体中での圧力は、7〜35MPaであることが好ましい。該圧力が7MPa未満の場合は、染料が繊維に充分に染着されず、本発明の効果が発現しにくくなる。一方、圧力が35MPaを超えると装置が大掛かりになって、加工に要するエネルギーも多くなってしまう。   The pressure in the supercritical carbon dioxide fluid in the dyeing method of the present invention is preferably 7 to 35 MPa. When the pressure is less than 7 MPa, the dye is not sufficiently dyed on the fiber, and the effect of the present invention is hardly exhibited. On the other hand, if the pressure exceeds 35 MPa, the apparatus becomes large and the energy required for processing increases.

また、本発明の染色方法における温度は40〜200℃が好ましい。該温度が40℃未満の場合は染色時間が長くなり過ぎ、本発明の効果が発現しにくくなる。一方、染色温度が200℃を超えると、繊維や染料が劣化する場合があり、染色に要するエネルギーも大きくなる。より好適には150℃以下で良い。   The temperature in the dyeing method of the present invention is preferably 40 to 200 ° C. When the temperature is lower than 40 ° C., the dyeing time becomes too long, and the effect of the present invention is hardly exhibited. On the other hand, if the dyeing temperature exceeds 200 ° C., fibers and dyes may deteriorate, and the energy required for dyeing also increases. More preferably, it may be 150 ° C. or lower.

染色に要する時間は、使用する染料の種類によっても異なるが、通常5〜90分が好ましい。90分を超えると作業効率の点から好ましくない場合が多い。より好適には60分以内が良い。一方、5分未満の時間では、所望の色相が得られない場合が多いし、繊維への付着ムラも発生しやすくなる。より好適には15分以上が良い。   The time required for dyeing varies depending on the type of dye used, but is usually preferably from 5 to 90 minutes. If it exceeds 90 minutes, it is often not preferable from the viewpoint of work efficiency. More preferably, it is within 60 minutes. On the other hand, in a time of less than 5 minutes, a desired hue is often not obtained, and uneven adhesion to the fiber is likely to occur. More preferably, 15 minutes or more is good.

また、染色浴はオートクレーブを用いることが好ましく、浴比は1:5〜100が好ましい。   The dyeing bath is preferably an autoclave, and the bath ratio is preferably 1: 5 to 100.

以下、実施例を挙げて本発明の構成および効果をさらに詳細に説明する。尚、実施例における各物性は以下の方法により求めたものである。   Hereinafter, an example is given and the composition and effect of the present invention are explained in detail. In addition, each physical property in an Example is calculated | required with the following method.

(1)染色性
マクベス・カラーアイ(Macbeth COLOR-EYE)モデルCE−3100を用い、繊維構造物の明度指数L*で表現した。ここで、明度指数L*とは、JIS Z 8701(2度視野XYZ系による色の表示方法)、又はJIS Z 8728(10度視野XYZ系による色の表示方法)に規定する三刺激値のYを用いて求められるものであり、明度指数L*の数値が小さい程、濃染化されていることを示す。
(1) Dyeability Using a Macbeth COLOR-EYE model CE-3100, it was expressed by a lightness index L * of the fiber structure. Here, the lightness index L * is a tristimulus value Y defined in JIS Z 8701 (a method for displaying colors by a 2-degree visual field XYZ system) or JIS Z 8728 (a method for displaying colors by a 10-degree visual field XYZ system). The smaller the value of the lightness index L *, the deeper the dyeing.

[実施例1]
44dtex/20fのポリエステル繊維を経糸及び緯糸に配して得た、平織物を常法にて精練し、100℃で1分乾燥した後、180℃で30秒プレセットし、目付50g/mの平織物を得た。
[Example 1]
A plain fabric obtained by arranging 44 dtex / 20f polyester fiber on warp and weft is scoured by a conventional method, dried at 100 ° C. for 1 minute, pre-set at 180 ° C. for 30 seconds, and has a basis weight of 50 g / m 2. A plain woven fabric was obtained.

次に、容積800ccの小型オートクレーブ内に上記織物と、精製した分散染料(CI.Disperse Blue56)を6%owfを入れ、更に共溶媒として水(二酸化炭素重量に対し1モル%)とメタノール(二酸化炭素重量に対し5モル%)を入れ、オートクレーブを封入した。   Next, the above-mentioned fabric and 6% owf of the purified disperse dye (CI. Disperse Blue 56) are placed in a small autoclave having a capacity of 800 cc, and water (1 mol% based on the weight of carbon dioxide) and methanol (dioxide dioxide) are used as cosolvents. 5 mol% relative to the weight of carbon) was added, and an autoclave was enclosed.

次に二酸化炭素ガズボンベから、オートクレーブ内に二酸化炭素を注入し、昇温速度2℃/分にて昇温を行った。オートクレーブ内部の温度が135℃、圧力20.0MPaになったことを確認して30分間温度と圧力を保持し、染色を行った。   Next, carbon dioxide was injected into the autoclave from the carbon dioxide gas pants, and the temperature was raised at a rate of temperature rise of 2 ° C./min. After confirming that the temperature inside the autoclave was 135 ° C. and the pressure was 20.0 MPa, the temperature and pressure were maintained for 30 minutes, and dyeing was performed.

染色後、80℃まで温度を下げ、オートクレーブの圧力を0.5MPa/分で減圧を行い5MPaまで減圧した後、オートクレーブ内部圧力を大気圧まで開放した。   After dyeing, the temperature was lowered to 80 ° C., and the pressure of the autoclave was reduced to 0.5 MPa to reduce the pressure to 5 MPa, and then the internal pressure of the autoclave was released to atmospheric pressure.

得られた被染物は濃い青色に均一に染色されていた。得られた被染物を常法にて還元洗浄、湯洗した後、乾燥した。   The obtained article to be dyed was uniformly dyed dark blue. The obtained article to be dyed was subjected to reduction washing and hot water washing by a conventional method and then dried.

超臨界二酸化炭素中での処理条件と、得られた織物のL*値を表1に示す。   Table 1 shows the treatment conditions in supercritical carbon dioxide and the L * value of the resulting fabric.

[実施例2〜3、比較例1〜6]
実施例1において、使用する極性溶媒と水の量、及び超臨界二酸化炭素中での染色条件を表1に示す如く変更した以外は実施例1と同様に実施した。
[Examples 2-3, Comparative Examples 1-6]
In Example 1, it carried out like Example 1 except having changed the amount of the polar solvent and water to be used, and the dyeing conditions in supercritical carbon dioxide as shown in Table 1.

超臨界二酸化炭素中での処理条件と、得られた織物のL*値を表1に示す。   Table 1 shows the treatment conditions in supercritical carbon dioxide and the L * value of the resulting fabric.

Figure 2006016711
Figure 2006016711

本発明によれば、廃液をほとんど出さずに、ポリエステル繊維を濃色に、且つ効率良く染色することが可能なポリエステル繊維の染色方法が提供されるので、ポリエステル繊維の染色加工に広く使用することができる。   According to the present invention, a polyester fiber dyeing method capable of efficiently dyeing polyester fibers in a dark color with little waste liquid is provided, so that it can be widely used for dyeing polyester fibers. Can do.

Claims (3)

超臨界二酸化炭素流体中で、ポリエステル繊維を染色するに際し、該超臨界二酸化炭素流体に、メタノール、エタノール、プロパノール、イソプロピルアルコール、ブタノール、ベンジルアルコール、アセトン、アセトフェノン、N−メチル−2−ピロリドン、メチルエチルケトン、ジメチルスルフォキシド、ジメチルフォルムアミド、エチレングリコール、アセトニトリルからなる群から選ばれた少なくとも一種の極性有機溶媒と水との混合液を0.01〜10モル%添加することを特徴とするポリエステル繊維の染色方法。   When dyeing polyester fibers in a supercritical carbon dioxide fluid, the supercritical carbon dioxide fluid is mixed with methanol, ethanol, propanol, isopropyl alcohol, butanol, benzyl alcohol, acetone, acetophenone, N-methyl-2-pyrrolidone, methyl ethyl ketone. Polyester fiber characterized by adding 0.01 to 10 mol% of a mixed liquid of at least one polar organic solvent selected from the group consisting of dimethylsulfoxide, dimethylformamide, ethylene glycol and acetonitrile. Dyeing method. 染料の添加量が0.01〜20%owfである請求項1記載のポリエステル繊維の染色方法。   The method for dyeing polyester fibers according to claim 1, wherein the amount of the dye added is 0.01 to 20% owf. 染色処理が、7〜35MPaの圧力、及び40〜200℃の温度下で実施される請求項1記載のポリエステル繊維の染色方法。   The method for dyeing polyester fibers according to claim 1, wherein the dyeing treatment is performed under a pressure of 7 to 35 MPa and a temperature of 40 to 200 ° C.
JP2004193092A 2004-06-30 2004-06-30 Method for dyeing polyester fiber Withdrawn JP2006016711A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006045702A (en) * 2004-08-02 2006-02-16 Teijin Techno Products Ltd Method for dyeing meta-type wholly aromatic polyamide fibers
JP2013535587A (en) * 2010-08-03 2013-09-12 キュービック テック コーポレイション Transfer of color and other physical properties to laminate materials
WO2020077665A1 (en) * 2018-10-16 2020-04-23 苏州大学 Anhydrous fiber dyeing method for mixed fluid medium
CN114592365A (en) * 2022-03-25 2022-06-07 青岛即发集团股份有限公司 A kind of supercritical carbon dioxide fluid dyeing method with high dyeing rate of disperse dyes

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006045702A (en) * 2004-08-02 2006-02-16 Teijin Techno Products Ltd Method for dyeing meta-type wholly aromatic polyamide fibers
JP2013535587A (en) * 2010-08-03 2013-09-12 キュービック テック コーポレイション Transfer of color and other physical properties to laminate materials
WO2020077665A1 (en) * 2018-10-16 2020-04-23 苏州大学 Anhydrous fiber dyeing method for mixed fluid medium
US11560669B2 (en) 2018-10-16 2023-01-24 Soochow University Fiber dyeing method using mixed fluid medium
CN114592365A (en) * 2022-03-25 2022-06-07 青岛即发集团股份有限公司 A kind of supercritical carbon dioxide fluid dyeing method with high dyeing rate of disperse dyes
CN114592365B (en) * 2022-03-25 2023-04-07 青岛即发集团股份有限公司 Supercritical carbon dioxide fluid dyeing method with high disperse dye uptake
WO2023179106A1 (en) * 2022-03-25 2023-09-28 青岛即发集团股份有限公司 Supercritical carbon dioxide fluid dyeing method featuring high dye uptake of disperse dye

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