JP2003336180A - Method for scouring, bleaching and dyeing fiber by one bath - Google Patents
Method for scouring, bleaching and dyeing fiber by one bathInfo
- Publication number
- JP2003336180A JP2003336180A JP2002137629A JP2002137629A JP2003336180A JP 2003336180 A JP2003336180 A JP 2003336180A JP 2002137629 A JP2002137629 A JP 2002137629A JP 2002137629 A JP2002137629 A JP 2002137629A JP 2003336180 A JP2003336180 A JP 2003336180A
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- Prior art keywords
- bath
- hydrogen peroxide
- dyeing
- scouring
- bleaching
- 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.)
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Links
Abstract
Description
【発明の詳細な説明】
【0001】
【発明の属する技術分野】本発明は、セルロース繊維類
の精練・漂白・染色処理を同一浴で行う方法であって、
漂白を過酸化水素により行う一浴精練漂白染色方法に関
する。なお、本発明において繊維とは、糸・布・各種繊
維製品を含む意味で用いられる。
【0002】
【従来技術】セルロース繊維等の繊維の加工において
は、繊維の精練・漂白を同一の浴で処理し、精練及び漂
白を行った浴液を一旦排出した後に染色工程への移行を
行うのが一般的に行われている。この染色工程への移行
に際しては、精練および漂白を行った浴液を一旦排水
し、新たに水を加えて水洗し、この水を排水した後に新
たな水を添加して染色工程を行っている。従って、染色
工程は熱水若しくは温水(40〜100℃)において行
うために、水の取り替えに伴う水の大量消費と加熱によ
るエネルギーの消費がなされていた。
【0003】このような、水及びエネルギーの消費を解
決するために、特開2000−80574は、公知の精
練剤と、漂白剤である過酸化水素を用いて精練と漂白を
同一浴にて行った後に、この同一浴内で金属塩を用いて
前記過酸化水素を分解し、続いてこの同一浴にて染料を
用いて染色を行う一浴精練漂白染色方法を提案してい
る。
【0004】
【発明が解決しようとする課題】しかし、この一浴精練
漂白染色方法は、繊維の精練・漂白と染色とを同一浴で
行い、浴内部を洗浄することなく染色を行うために、繊
維の精練・漂白の際に出た汚れや塵が浴内に残ることか
ら、この浴内に残った汚れや塵が染色時に繊維に付着し
て染色が不均一となる場合もある。従って、一浴精練漂
白染色方法は、精練および漂白を行った浴を一旦排水し
て水洗した後に染色を行う精練・漂白・染色を行う従来
方法に比べ、染色性が未だ十分ではないという問題点を
有していた。一方、この同一浴中における精練、漂白、
染色の一連の工程において、処理される繊維を傷めるこ
とは極力防止しなければならない。
【0005】本発明の目的は、繊維を傷めることなく、
繊維の精練・漂白の際に出た汚れや塵を分解除去するこ
とができ、前記従来方法と比較して可及的に同等の染色
性が得られる一浴精練漂白染色方法を提供するところに
ある。
【0006】
【課題を解決するための手段】そこで、本発明者らは、
繊維、特にセルロース繊維の精練・漂白・染色を同一の
浴で行う方法において、浴中に過酸化水素量4〜21g
/Lの過酸化水素水を添加することにより漂白が行われ
た後に、前記浴中に過酸化水素の分解促進剤を添加する
工程を行い、次いで前記浴中に染料を添加して染色を行
う一浴精練漂白染色方法であれば、過酸化水素により繊
維の漂白とともに塵が分解されて浴内の繊維に由来する
塵を取り除くことができ、精練および漂白を行った浴液
を一旦排水し、水洗した後に染色を行う精練・漂白・染
色を行う方法と同等の染色性を確保することができる。
しかも、浴中に過酸化水素量4〜21g/Lの過酸化水
素水の添加であれば、当該繊維を過酸化水素によって脆
化させて繊維を傷めることなく、セルロース繊維を漂白
することができる。さらに、過酸化水素分解促進剤を添
加することにより、漂白処理後残留する過酸化物により
分解等される染料も用いることも可能となる。
【0007】本発明は、セルロース繊維の精練・漂白・
染色を同一の浴で行う方法において、浴中に過酸化水素
量4〜21g/Lの過酸化水素水を添加することにより
漂白が行われた後に、前記浴中に過酸化水素の分解促進
剤を添加し、次いで前記浴中に染料を添加して染色を行
うことを特徴とする一浴精練漂白染色方法である。な
お、本発明では、浴中に過酸化水素量4〜21g/Lの
過酸化水素水を添加することにより漂白しているが、こ
れは精練時濃度を基準とした添加量を示している。な
お、過酸化水素量4〜21g/Lの過酸化水素水として
は、たとえば濃度35重量%過酸化水素水を10〜50
ml/L調整することにより得られるが、これに限定さ
れない。
【0008】
【発明の実施の態様】本発明は、セルロース繊維の精練
・漂白・染色を同一の浴で行う方法において、精練及び
漂白を同一浴で行うに際して、当該漂白剤として浴中に
過酸化水素量4〜21g/Lの過酸化水素水を添加する
ことにより漂白された後に、前記浴中に過酸化水素の分
解促進剤を添加する工程を行い、次いで前記浴中に染料
を添加して染色を行う一浴精練漂白染色方法である。こ
の一浴精練漂白染色方法は、前記セルロース繊維につい
ての精練、漂白、過酸化水素の分解及び染色が同一の浴
内において行われる方法であり、浴内の水が新たな水に
置換されることがない方法である。
【0009】本発明において、セルロース繊維の漂白剤
は、過酸化酸素により行われるものであるが、具体的に
は、過酸化水素量4〜21g/Lの過酸化水素水(たと
えば、35重量%の過酸化水素水10〜50ml/L)
が添加された浴液にセルロース繊維を浸漬することによ
り行われる。前記漂白工程は、セルロースを精練する精
練工程と同一の浴内で行われるものであるが、精練工程
の後に漂白工程を行っても良いが、工程時間の短縮のた
めに、精練工程と漂白工程とを同時に行うことが好まし
い。精練工程と漂白工程を同時に行う場合には、同一浴
内の水に、精練剤、漂白剤である過酸化水素水及びアル
カリ剤を添加し、さらに必要に応じて芒硝を添加して、
浴中にセルロース繊維を浸漬することにより行われる。
前記精練剤としては、後の染色時に影響を与えず精練性
を有するものであれば特に限定されるものではなく、例
えばミグノールSD−77、ウェットソフターD−57
8、ウェットソフターLZ(以上、一方社油脂工業
(株))などの精練性を有する染色助剤を用いても良
い。また、前記アルカリ剤としては、公知のアルカリ剤
としてソーダ灰や液体アルカリ剤を用いることができる
が、ソーダ灰の場合精練工程から持ち込まれる残留アル
カリ量の調整(部分中和)等が必要であるため、液体ア
ルカリ剤を用いることが好ましい。
【0010】本発明の漂白工程は、浴中に過酸化水素量
4〜21g/Lの過酸化水素水、たとえば濃度35重量
%の過酸化水素水10〜50ml/Lを添加することに
より行われるが、前記過酸化水素量5〜17g/Lの過
酸化水素水(例えば濃度35重量%の過酸化水素であれ
ば12〜40ml/L)で行われることが好ましく、過酸
化水素量6〜13g/Lの過酸化水素水(例えば濃度3
5重量%の過酸化水素であれば15〜30ml/L)で行
われることがより好ましい。前記過酸化水素水の添加量
が4g/L(例えば濃度35重量%の過酸化水素であれ
ば10ml/L)未満の場合には、浴内の汚れ等を十分に
分解することができず、染色性が十分ではない。前記過
酸化水素水の添加量が21g/L(例えば濃度35重量
%の過酸化水素であれば50ml/L)より多い場合に
は、繊維が酸化されるために脆化し、繊維を傷めてしま
う。
【0011】また、前記セルロース繊維としては、セル
ロースを主骨格とした繊維であれば、特に限定されるも
のではないが、例えば綿、レーヨン、テンセル、リヨセ
ルが代表的に挙げることができる。なお、セルロース繊
維は、通常、浴比1:5〜1:50で浸漬して精練及び
漂白を行うことができる。
【0012】本発明の一浴精練漂白染色方法において、
芒硝を繊維と染料との親和性向上のために用いることが
できる。前記芒硝は、精練時から添加しても良く、精練
剤の種類により精練性を阻害する場合には精練工程終了
後であって染色の際までのどの段階に添加しても良い。
【0013】本発明の一浴精練漂白染色方法では、精練
及び漂白の後であって染色前に、前記浴中に過酸化水素
の分解促進剤を添加する工程を行い、過酸化水素を分解
する。前記過酸化水素分解促進剤は、特に限定されるも
のではなく、チオ硫酸ナトリウムやハイドロサルファイ
ト等の還元剤、カタラーゼに代表される過酸化水素分解
酵素や遷移金属塩を用いることができる。中でも、過酸
化水素と当量添加する必要が無い金属塩、特にコバルト
塩、鉄塩、ルビジウム塩が少量で過酸化水素の分解促進
効果を示すために好ましい。本発明で用いられる過酸化
水素分解剤は、コバルト塩、鉄塩及びルビジウム塩のう
ち少なくとも1種以上の金属塩が好ましい。たとえば、
前記コバルト塩としては、具体的には、酢酸コバルト
(II),(III)、炭酸コバルト(II),(III)、酸化
コバルト(II),(III)、硫酸コバルト(II),(II
I)、塩化コバルト(II),(III),(IV)、臭化コバ
ルト(II)、沃化コバルト(II)などを用いることがで
きるが、酢酸コバルト、硫酸コバルト、特に酢酸コバル
トが好ましい。また前記鉄塩としては、具体的には、酢
酸鉄(II),(III)、炭酸鉄(II)、酸化鉄(II),
(III)、硫酸鉄(II),(III)、塩化鉄(II),(II
I)、臭化鉄(II),(III)、沃化鉄(II)などを用い
ることができるが、酸化鉄(II),(III)、塩化鉄(I
I),(III)、特に酸化鉄(II),(III)が好まし
い。また、前記ルビジウム塩としては、具体的には、酢
酸ルビジウム(II),(III)、炭酸ルビジウム(I
I)、酸化ルビジウム(II),(III)、硫酸ルビジウム
(II),(III)、塩化ルビジウム(II),(III)、臭
化ルビジウム(II),(III)などを用いることができ
るが、炭酸ルビジウム、酸化ルビジウムが好ましく、特
に酸化ルビジウムが好ましい。なお、過酸化水素分解効
果の点から酢酸コバルトを用いることが好ましい。前記
金属塩の添加量、特にコバルト塩、鉄塩及びルビジウム
塩のうち少なくとも1種以上の金属塩は、1〜1000
ppmであることが好ましく、1〜200ppmである
ことがより好ましい。
【0014】本発明の一浴精練漂白染色方法に用いられ
る染料は、染色前に過酸化水素が分解されることから、
特に限定されるものではなく、反応染料や直接染料の何
れも使用可能である。反応染料としてはHot型、V.
S.型、Supra型のいずれも使用することが可能で
ある。但し、直接染料を使用する場合には、染色の際に
浴内のアルカリ量の調整(部分中和)をする必要があ
る。
【0015】
【実施例】以下、本発明の実施例及び比較例を示すが、
本発明は下記に限定されるものではない。
【0016】(実施例及び比較例)図1に示す作業条件
に従って、精練、漂白、染色処理の各工程を行い、一浴
精練漂白染色方法を行った。すなわち、浴内の水に精練
剤、NaOH、過酸化水素、珪酸ソーダ、芒硝を投入
し、図1に示す浴比にて試験布を浸漬し、浴の温度を1
00℃まで加熱し、60分間保持しながら精練及び漂白
を行った。その後、図1に示す浴比にて過酸化水素分解
促進剤を添加し、30分間保持した後、20分かけて浴
温を60℃とした。60℃となった浴を浴温60℃で5
分間保持した後に、浴中に染料を添加し、5分後にアル
カリ剤を添加して30分間保持した後に室温に戻すこと
により染色を行った。
【0017】この一浴精練漂白染色方法において用いた
薬剤、試験布等の原料・組成は、下記のとおりであり、
その使用量は表1のとおりである。なお、使用量につい
ては、精練剤、NaOH、過酸化水素水及び珪酸ソーダ
の使用量については精練時濃度であり、分解促進剤につ
いては過酸化水素分解時濃度であり、芒硝、染料及びア
ルカリ剤については、最終染色時濃度である。
【0018】精練剤:商品名「ミグノールSD−7
7」、一方社油脂工業(株)社製
NaOH:試薬
過酸化水素水:35重量%過酸化水素水(試薬)
試験布:市販の綿ニット生地
過酸化水素分解促進剤:酢酸コバルト(II)
【0019】染料:次の3種混合染料
C.I.Reactive Yellow 17 :1%
o.w.f
C.I.Reactive Red 21:1% o.w.f
C.I.Reactive Blue 19:1% o.w.f
アルカリ剤:商品名「エスポロンA501」、一方社油
脂工業(株)社製
【0020】
【表1】
【0021】〔評価〕実施例1〜4並びに比較例1及び
2の一浴精練漂白染色工程により染色した染色布につい
て、染色性と脆性について評価した。
(染色性)実施例1〜4並びに比較例1及び2の一浴精
練漂白染色工程により染色した染色布を、精練及び漂白
とは別に染色した染色布と比較して目視により比較して
下記の評価基準により評価した。
◎:精練及び漂白とは別に染色した染色布と同等であ
る。
〇:塵等による若干の染色ムラが認められるが実用上問
題ない。
×:染色ムラが容易に認められる。
【0022】なお、精練及び漂白とは別に染色した染色
布は以下の方法により調製した。市販の精練漂白布を図
2に示す作業条件により染色をした。なお、芒硝、染料
及びアルカリ剤は、実施例1〜4並びに比較例1及び2
と同じ原料、使用量で用いた。
【0023】(脆性)実施例1〜4並びに比較例1及び
2の一浴精練漂白染色工程により染色した染色布を、目
視により下記の評価基準により評価した。
◎:全く脆化が認められない
〇:若干の脆化が認められるが実用上強度に問題がな
い。
×:耐脆化が容易に認められ、繊維の強度の低下が認め
られる。
【0024】(結果)表1より、実施例1は浴中に濃度3
5重量%の過酸化水素水を10〜50ml/L(過酸化水
素量4〜21g/L)添加することにより漂白した実施
例1〜4は、繊維を傷めることなく、染色性が良好であ
る。なお、実施例1は過酸化水素水の添加量が比較的少
量であったために、塵等の分解除去が完全ではなく、若
干の染色ムラが認められたが実用上問題はなく、また脆
化が認められなく、良好な染色布が得られた。実施例4
は、過酸化水素水の添加量が比較的多量であったため、
若干の脆化が認められたが実用上問題はなく、染色ムラ
は認められず、良好な染色布が得られた。実施例3及び
4については、染色性、脆性ともに良好で、優れた染色
布が得られた。
【0025】これに対して、比較例1については過酸化
水素水の添加量が少なすぎるために、染色性が不良であ
り、比較例2は過酸化水素水の添加量が多すぎるために
脆性が不良であった。
【0026】
【発明の効果】本発明の一浴精練漂白染色方法は、セル
ロース繊維に用いた場合に、浴中に過酸化水素量4〜2
1g/Lの過酸化水素水を添加することにより漂白が行
われるため、繊維を脆化させて傷めることなく浴内の塵
が分解除去されるので、染色性が良好であり、セルロー
ス繊維の良好な染色布を得ることができる。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for performing scouring, bleaching and dyeing treatments on cellulose fibers in the same bath,
The present invention relates to a one-bath scouring bleach-dyeing method in which bleaching is performed with hydrogen peroxide. In addition, in this invention, a fiber is used in the meaning including a yarn, cloth, and various fiber products. [0002] In the processing of fibers such as cellulose fibers, scouring and bleaching of the fibers are performed in the same bath, and after the scouring and bleaching bath is once discharged, the process proceeds to a dyeing process. This is commonly done. At the time of transition to the dyeing step, the bath liquid subjected to scouring and bleaching is once drained, freshly added and washed with water, and after draining this water, new water is added to perform the dyeing step. . Therefore, since the dyeing process is performed in hot water or hot water (40 to 100 ° C.), a large amount of water is consumed in replacing the water and energy is consumed by heating. In order to solve such consumption of water and energy, Japanese Patent Application Laid-Open No. 2000-80574 discloses a method in which scouring and bleaching are performed in the same bath using a known scouring agent and hydrogen peroxide as a bleaching agent. After that, a one-bath scouring bleach-dyeing method is proposed in which the hydrogen peroxide is decomposed using a metal salt in the same bath, and then dyeing is performed using a dye in the same bath. [0004] However, this single-bath scouring bleach-dyeing method involves refining, bleaching and dyeing of fibers in the same bath and dyeing without washing the inside of the bath. Since the dirt and dust generated during the scouring and bleaching of the fibers remain in the bath, the dirt and dust remaining in the bath may adhere to the fibers during dyeing, resulting in uneven dyeing. Accordingly, the single-bath scouring / bleaching / dyeing method has a problem that the dyeability is still insufficient compared with the conventional method of performing scouring / bleaching / dyeing after draining and washing the bath after scouring and bleaching once and washing with water. Had. On the other hand, scouring, bleaching,
In the course of the dyeing process, damage to the treated fibers must be minimized. [0005] It is an object of the present invention to provide a fiber without damaging the fiber.
To provide a one-bath scouring bleach-dyeing method capable of decomposing and removing dirt and dust generated at the time of fiber scouring / bleaching and obtaining the same dyeability as possible as compared with the conventional method. is there. Means for Solving the Problems Accordingly, the present inventors have
In a method in which scouring, bleaching and dyeing of fibers, especially cellulose fibers, are performed in the same bath, the amount of hydrogen peroxide in the bath is 4 to 21 g.
/ L hydrogen peroxide solution is added to the solution to perform bleaching, and then a step of adding a hydrogen peroxide decomposition accelerator to the bath is performed, and then a dye is added to the bath to perform dyeing. If the single-bath scouring bleach dyeing method, the dust is decomposed along with the bleaching of the fibers by hydrogen peroxide and the dust derived from the fibers in the bath can be removed, and the scouring and bleaching bath liquid is once drained, Dyeability equivalent to the method of scouring / bleaching / dyeing after washing with water can be secured.
Moreover, if hydrogen peroxide having an amount of 4 to 21 g / L of hydrogen peroxide is added to the bath, the cellulose fibers can be bleached without embrittlement of the fibers by hydrogen peroxide and damaging the fibers. . Further, by adding a hydrogen peroxide decomposition accelerator, it is also possible to use a dye which is decomposed by peroxide remaining after the bleaching treatment. [0007] The present invention provides a method for scouring, bleaching,
In a method in which dyeing is performed in the same bath, bleaching is performed by adding a hydrogen peroxide solution having an amount of hydrogen peroxide of 4 to 21 g / L to the bath, and then a hydrogen peroxide decomposition accelerator is added to the bath. , Followed by dyeing in the bath for dyeing. In the present invention, bleaching is performed by adding a hydrogen peroxide solution having a hydrogen peroxide amount of 4 to 21 g / L to the bath, but this indicates the amount added based on the concentration at the time of scouring. In addition, as the hydrogen peroxide solution having an amount of hydrogen peroxide of 4 to 21 g / L, for example, a hydrogen peroxide solution having a concentration of 35% by weight is used.
It is obtained by adjusting the ml / L, but is not limited to this. DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for scouring, bleaching and dyeing cellulose fibers in the same bath. In performing scouring and bleaching in the same bath, peroxide is used as the bleaching agent in the bath. After bleaching by adding a hydrogen peroxide solution having a hydrogen amount of 4 to 21 g / L, a step of adding a hydrogen peroxide decomposition accelerator to the bath is performed, and then a dye is added to the bath. This is a one-bath scouring bleach dyeing method for dyeing. This one-bath scouring bleach-dyeing method is a method in which scouring, bleaching, decomposition of hydrogen peroxide and dyeing of the cellulose fiber are performed in the same bath, and the water in the bath is replaced with new water. There is no way. In the present invention, the bleaching agent for cellulose fibers is carried out with oxygen peroxide. Specifically, a hydrogen peroxide solution having an amount of hydrogen peroxide of 4 to 21 g / L (for example, 35% by weight) Hydrogen peroxide solution of 10 to 50 ml / L)
Is carried out by immersing the cellulose fibers in a bath solution to which is added. The bleaching step is performed in the same bath as the refining step of refining cellulose, but the bleaching step may be performed after the refining step. Are preferably performed simultaneously. When performing the scouring step and the bleaching step at the same time, to the water in the same bath, add a scouring agent, a hydrogen peroxide solution that is a bleaching agent and an alkali agent, and further add sodium sulfate as needed,
This is performed by immersing the cellulose fibers in the bath.
The scouring agent is not particularly limited as long as it has scouring properties without affecting the subsequent dyeing. For example, Mignol SD-77, wet softer D-57
8. A dyeing aid having a refining property such as wet softer LZ (above, on the other hand, Ongaku Yushi Kogyo Co., Ltd.) may be used. As the alkaline agent, soda ash or a liquid alkaline agent can be used as a known alkaline agent, but in the case of soda ash, adjustment (partial neutralization) of the amount of residual alkali introduced from the scouring step is required. Therefore, it is preferable to use a liquid alkaline agent. The bleaching step of the present invention is carried out by adding a hydrogen peroxide solution having a hydrogen peroxide amount of 4 to 21 g / L, for example, a hydrogen peroxide solution having a concentration of 35% by weight, to 50 to 50 ml / L, in a bath. Is preferably performed with the above-mentioned aqueous hydrogen peroxide having a hydrogen peroxide amount of 5 to 17 g / L (for example, 12 to 40 ml / L for a hydrogen peroxide having a concentration of 35% by weight), and a hydrogen peroxide amount of 6 to 13 g. / L hydrogen peroxide solution (for example, concentration 3
More preferably, the reaction is performed at 15 to 30 ml / L for 5% by weight of hydrogen peroxide. When the addition amount of the hydrogen peroxide solution is less than 4 g / L (for example, 10 ml / L for a hydrogen peroxide having a concentration of 35% by weight), dirt and the like in the bath cannot be sufficiently decomposed, Insufficient dyeability. If the amount of the hydrogen peroxide solution is more than 21 g / L (for example, 50 ml / L for a hydrogen peroxide having a concentration of 35% by weight), the fibers are oxidized and thus become brittle and damage the fibers. . The cellulose fiber is not particularly limited as long as it is a fiber having cellulose as a main skeleton, and examples thereof include cotton, rayon, Tencel, and lyocell. The cellulose fibers can be scoured and bleached by immersing them in a bath ratio of 1: 5 to 1:50. In the one-bath scouring bleach-dyeing method of the present invention,
Glauber's salt can be used to improve the affinity between the fiber and the dye. Glauber's salt may be added from the time of refining, and when the refining is inhibited depending on the type of refining agent, it may be added at any stage after the refining process but before dyeing. In the one-bath scouring bleach-dyeing method of the present invention, after scouring and bleaching and before dyeing, a step of adding a hydrogen peroxide decomposition accelerator to the bath is performed to decompose the hydrogen peroxide. . The hydrogen peroxide decomposition promoter is not particularly limited, and a reducing agent such as sodium thiosulfate or hydrosulfite, a hydrogen peroxide decomposition enzyme represented by catalase, or a transition metal salt can be used. Among them, metal salts that do not need to be added in an equivalent amount to hydrogen peroxide, particularly cobalt salts, iron salts, and rubidium salts, are preferable because they exhibit a small amount of hydrogen peroxide decomposition promoting effect. The hydrogen peroxide decomposer used in the present invention is preferably a metal salt of at least one of a cobalt salt, an iron salt and a rubidium salt. For example,
Specific examples of the cobalt salt include cobalt acetates (II) and (III), cobalt carbonates (II) and (III), cobalt oxides (II) and (III), cobalt sulfates (II) and (II).
I), cobalt (II) chloride, (III), (IV), cobalt (II) bromide, cobalt (II) iodide and the like can be used, but cobalt acetate, cobalt sulfate, particularly cobalt acetate is preferred. Specific examples of the iron salt include iron acetate (II), (III), iron carbonate (II), iron oxide (II),
(III), iron (II) sulfate, (III), iron (II) chloride, (II)
I), iron (II), (III) bromide, iron (II) iodide and the like can be used, but iron oxide (II), (III), iron chloride (I
I) and (III), particularly iron oxides (II) and (III) are preferred. Further, as the rubidium salt, specifically, rubidium acetate (II), (III), rubidium carbonate (I
I), rubidium oxides (II) and (III), rubidium sulfates (II) and (III), rubidium chlorides (II) and (III), and rubidium bromide (II) and (III) can be used. , Rubidium carbonate and rubidium oxide are preferable, and rubidium oxide is particularly preferable. Note that it is preferable to use cobalt acetate from the viewpoint of the hydrogen peroxide decomposition effect. The amount of the metal salt added, in particular, at least one or more of the cobalt salt, the iron salt and the rubidium salt is 1 to 1000
ppm, more preferably 1 to 200 ppm. The dye used in the one-bath scouring bleach-dyeing method of the present invention is characterized in that hydrogen peroxide is decomposed before dyeing.
There is no particular limitation, and any of reactive dyes and direct dyes can be used. Hot dyes, V.I.
S. Type or Supra type can be used. However, when a direct dye is used, it is necessary to adjust the amount of alkali in the bath (partial neutralization) at the time of dyeing. EXAMPLES Examples of the present invention and comparative examples will be shown below.
The present invention is not limited to the following. (Examples and Comparative Examples) Each step of scouring, bleaching and dyeing treatments was carried out according to the working conditions shown in FIG. That is, a scouring agent, NaOH, hydrogen peroxide, sodium silicate, and sodium sulfate were added to water in a bath, and a test cloth was immersed at a bath ratio shown in FIG.
The mixture was heated to 00 ° C., and scouring and bleaching were performed while holding the mixture for 60 minutes. Thereafter, a hydrogen peroxide decomposition accelerator was added at the bath ratio shown in FIG. 1, and after maintaining for 30 minutes, the bath temperature was set to 60 ° C. over 20 minutes. The bath that has reached 60 ° C has a bath temperature of 60 ° C for 5
After holding for 1 minute, the dye was added to the bath, and after 5 minutes, an alkali agent was added, and the solution was held for 30 minutes, and then returned to room temperature for dyeing. The raw materials and compositions of the chemicals, test cloths and the like used in this one-bath scouring bleach-dyeing method are as follows:
The amounts used are as shown in Table 1. The amounts used are the concentrations during scouring for the amounts of scouring agent, NaOH, aqueous hydrogen peroxide and sodium silicate, and the concentrations at the time of decomposition of hydrogen peroxide for the decomposition accelerators. Is the final staining concentration. Scouring agent: trade name "Mignol SD-7"
7 ", on the other hand, NaOH: Reagent hydrogen peroxide solution: 35% by weight hydrogen peroxide solution (reagent) Test cloth: Commercial cotton knit fabric Hydrogen peroxide decomposition accelerator: Cobalt acetate (II) Dye: The following three kinds of mixed dyes CI Reactive Yellow 17: 1%
owf CI Reactive Red 21: 1% owf CI Reactive Blue 19: 1% owf Alkaline agent: trade name "Esporon A501", manufactured by Yushi Yushi Kogyo Co., Ltd. [Evaluation] The dyeing properties and brittleness of the dyed fabrics dyed by the one-bath scouring bleach dyeing process of Examples 1 to 4 and Comparative Examples 1 and 2 were evaluated. (Dyeing properties) The dyed fabrics dyed by the one-bath scouring bleach dyeing process of Examples 1 to 4 and Comparative Examples 1 and 2 were compared visually with dyed fabrics dyed separately from scouring and bleaching. The evaluation was based on evaluation criteria. A: Equivalent to a dyed cloth dyed separately from scouring and bleaching. 〇: Slight staining unevenness due to dust or the like is observed, but there is no practical problem. X: Uneven dyeing is easily recognized. A dyed fabric dyed separately from scouring and bleaching was prepared by the following method. A commercially available scouring bleached cloth was dyed under the working conditions shown in FIG. The sodium sulfate, the dye and the alkali agent were used in Examples 1 to 4 and Comparative Examples 1 and 2.
The same raw materials and the amounts used were used. (Brittleness) The dyed fabrics dyed by the one-bath scouring bleach dyeing process of Examples 1 to 4 and Comparative Examples 1 and 2 were visually evaluated according to the following evaluation criteria. :: No embrittlement is observed at all〇: Slight embrittlement is observed, but there is no problem in practical strength. X: Embrittlement resistance was easily recognized, and a decrease in fiber strength was observed. (Results) From Table 1, it was found that Example 1 had a concentration of 3 in the bath.
In Examples 1 to 4 which were bleached by adding 5% by weight of aqueous hydrogen peroxide to 10 to 50 ml / L (the amount of hydrogen peroxide was 4 to 21 g / L), the dyeability was good without damaging the fibers. . In Example 1, since the amount of hydrogen peroxide added was relatively small, decomposition and removal of dust and the like were not complete, and slight dyeing unevenness was observed. Was not observed, and a good dyed cloth was obtained. Example 4
Is because the amount of hydrogen peroxide added was relatively large,
Although slight embrittlement was observed, there was no practical problem, no uneven dyeing was observed, and a good dyed cloth was obtained. In Examples 3 and 4, both dyeability and brittleness were good, and excellent dyed cloths were obtained. On the other hand, the dyeability of Comparative Example 1 was poor because the amount of hydrogen peroxide added was too small, and the brittleness of Comparative Example 2 was too large because the amount of hydrogen peroxide added was too large. Was bad. According to the single-bath scouring bleach-dyeing method of the present invention, when used for cellulose fiber, the amount of hydrogen peroxide in the bath is 4 to 2%.
Bleaching is performed by adding 1 g / L of hydrogen peroxide solution, so that dust in the bath is decomposed and removed without embrittlement and damage to the fibers, so that the dyeability is good and the cellulose fibers are good. A dyed cloth can be obtained.
【図面の簡単な説明】 【図1】 本発明の作業条件の図 【図2】 評価用染色布の染色作業条件の図[Brief description of the drawings] FIG. 1 is a diagram of the working conditions of the present invention. FIG. 2 is a diagram of dyeing operation conditions of a dyed cloth for evaluation.
Claims (1)
一の浴で行う方法において、浴中に過酸化水素量4〜2
1g/Lの過酸化水素水を添加することにより行われた
後に、前記浴中に過酸化水素の分解促進剤を添加し、次
いで前記浴中に染料を添加して染色を行うことを特徴と
する一浴精練漂白染色方法。Claims: 1. A method for refining, bleaching and dyeing cellulose fibers in the same bath, wherein the amount of hydrogen peroxide is 4 to 2 in the bath.
After performing by adding 1 g / L of hydrogen peroxide, a hydrogen peroxide decomposition accelerator is added to the bath, and then a dye is added to the bath to perform dyeing. One bath scouring bleach dyeing method.
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CN104213398A (en) * | 2014-08-14 | 2014-12-17 | 浙江航民股份有限公司 | Production method for polyester cotton oxygen bleaching and disperse dyestuff dyeing one bath process |
CN112342779A (en) * | 2020-11-11 | 2021-02-09 | 河南省沈丘县三闸纺织有限公司 | Process for combining deoxidation and acidification in yarn barrel dyeing |
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CN104213398A (en) * | 2014-08-14 | 2014-12-17 | 浙江航民股份有限公司 | Production method for polyester cotton oxygen bleaching and disperse dyestuff dyeing one bath process |
CN112342779A (en) * | 2020-11-11 | 2021-02-09 | 河南省沈丘县三闸纺织有限公司 | Process for combining deoxidation and acidification in yarn barrel dyeing |
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