JPH10317276A - Alkali thinning treatment of polyester fiber fabric - Google Patents

Alkali thinning treatment of polyester fiber fabric

Info

Publication number
JPH10317276A
JPH10317276A JP12528897A JP12528897A JPH10317276A JP H10317276 A JPH10317276 A JP H10317276A JP 12528897 A JP12528897 A JP 12528897A JP 12528897 A JP12528897 A JP 12528897A JP H10317276 A JPH10317276 A JP H10317276A
Authority
JP
Japan
Prior art keywords
alkali
weight
polyester fiber
weight loss
treatment
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
JP12528897A
Other languages
Japanese (ja)
Inventor
Kenichi Kamemaru
賢一 亀丸
Michinori Yamana
道則 山名
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.)
Unitika Ltd
Original Assignee
Unitika Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Unitika Ltd filed Critical Unitika Ltd
Priority to JP12528897A priority Critical patent/JPH10317276A/en
Publication of JPH10317276A publication Critical patent/JPH10317276A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for an alkali thinning treatment of a polyester fiber fabric capable of efficiently hydrolyzing the polyester fiber in high reproducibility even with an alkali of a lower concentration of 0.1-10%. SOLUTION: In a hydrolysis treatment of a polyester fiber fabric with an alkali, the polyester fiber is hydrolyzed using an alkali treating liquid composed of >=60 wt.% of an alkylene glycol or a polyoxyalkylene glycol as the solvent and water as another main solvent. Thus, a polyester fiber fabric is treated for alkali thinning.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は,ポリエステル系繊
維布帛のアルカリ減量処理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 reducing the alkali content of a polyester fiber fabric.

【0002】[0002]

【従来の技術】ポリエステル系繊維は,種々の優れた物
性を有し,主に衣料用途等の分野で活用されている繊維
であるが,これを特に婦人用衣料素材として用いる場合
に,その剛直性が風合の点で大きな欠点になっていた。
この剛直性は,結晶化度の高い繊維の構造に起因してい
るものであり,これを解決するために苛性ソーダや苛性
カリ等の水溶液中で60℃以上の温度で処理し,加水分
解せしめることによる繊維の風合改良を行う,いわゆる
アルカリ減量加工が1949年に英国で開発(英国特許
第652948号)されている。
2. Description of the Related Art Polyester fibers are fibers that have various excellent physical properties and are mainly used in the field of clothing and the like. Sex was a major drawback in terms of hand.
This rigidity is due to the structure of the fiber having a high degree of crystallinity. In order to solve this problem, the fiber is treated in an aqueous solution of caustic soda or potassium hydroxide at a temperature of 60 ° C. or more and hydrolyzed. A so-called alkali weight reduction process for improving the texture of fibers has been developed in the United Kingdom in 1949 (UK Patent No. 652948).

【0003】このアルカリ減量加工は,その目的に応じ
た風合を得るために数%〜50%程度の減量率を必要と
するが,特に20%以上の高減量を行うためには,比較
的高濃度の苛性ソーダ水溶液を必要とし,連続式,バッ
チ式によって条件は異なるが,いずれの方法でも,通常
は生産性を考慮して,20〜50重量%の高濃度の苛性
ソーダを使用するのが一般的である。このように,高濃
度の苛性ソーダ水溶液を使用すると,アルカリ減量加工
時に作業員の危険度が高くなるばかりか,高濃度である
がゆえに,減量速度の管理が難しく,減量斑が発生し,
安定して加工ができない等の問題が多かった。
[0003] In this alkali weight reduction processing, a weight reduction rate of several percent to 50% is required in order to obtain a feeling suitable for the purpose. A high-concentration aqueous solution of caustic soda is required, and the conditions differ depending on the continuous type or batch type. In any case, usually, a high concentration of 20 to 50% by weight of caustic soda is used in consideration of productivity. It is a target. As described above, when a high-concentration aqueous solution of caustic soda is used, not only does the danger of workers increase during alkali weight reduction processing, but also because of the high concentration, it is difficult to control the weight loss rate, and weight loss spots occur.
There were many problems such as inability to stably process.

【0004】これらの問題を解決するために,特公昭3
7−3946号公報に見られるごとく,4%以下の苛性
ソーダ水溶液中でアミンを併用してアルカリ減量を促進
させる方法や,米国特許第315577号に見られるご
とく,第4級アンモニウム塩を併用する方法,すなわ
ち,0.5〜5%の水酸化アルカリ金属に0.005〜0.5
%のラウリルジメチルベンジルアンモニウムクロライド
等の第4級アンモニウム塩を添加したアルカリ水溶液で
処理する方法が提案されている。しかしながら,前者の
方法では,苛性ソーダ1%以下の濃度では加水分解促進
効果が薄く,特に20%以上の高減量率を期待する場合
は,生産性が著しく低下することが判明している。ま
た,後者の方法では,使用する第4級アンモニウム塩の
苛性ソーダによる繊維の分解促進効果が激しすぎること
から,実作業上,分解反応速度を一定に管理することが
極めて難しいという問題を有している。
In order to solve these problems, Japanese Patent Publication No. Sho 3
As disclosed in JP-A-7-3946, a method in which an amine is used in combination with an aqueous solution of caustic soda of 4% or less to promote alkali weight reduction, and a method in which a quaternary ammonium salt is used in combination as disclosed in US Pat. That is, 0.005 to 0.5% for 0.5 to 5% of alkali metal hydroxide.
%, A method of treating with an aqueous alkali solution to which a quaternary ammonium salt such as lauryldimethylbenzylammonium chloride is added. However, it has been found that in the former method, the effect of promoting hydrolysis is weak at a concentration of caustic soda of 1% or less, and the productivity is remarkably reduced particularly when a high weight loss rate of 20% or more is expected. Further, the latter method has a problem that it is extremely difficult to control the decomposition reaction rate to a constant level in actual work, because the effect of caustic soda of the quaternary ammonium salt used to promote fiber decomposition is too strong. ing.

【0005】ポリエステル系繊維の減量率を正確に制御
する方法としては,特公昭61−160475号公報に
見られるごとく,ポリエステル系繊維をアルカリ水溶液
中で加水分解させるに当たり,アルカリ加水分解が実質
的に進行する前に装置内の処理浴の量とその濃度を決定
し,決定された処理浴の量および苛性ソーダ濃度,装置
内の織編物の重量並びに予定減量率に基づいて予定減量
率に到達したときの処理浴の苛性ソーダ推定濃度を算出
し,実際の減量物の減量率と比較して統計的に処理を行
い,次回の苛性ソーダ濃度測定値を予測して精度および
再現性を向上させる方法が提案されている。このような
アルカリ減量方法は,近年バッチ式減量機において採用
されているが,苛性ソーダ濃度の滴定装置の精度が極め
て高精度でなければ十分に減量率を管理することができ
ないため,ロット間でバラツキが発生するという問題を
有しており,実用上さらなる精度の向上が必要であっ
た。
As a method of accurately controlling the rate of weight reduction of polyester fibers, as disclosed in JP-B-61-160475, when polyester fibers are hydrolyzed in an aqueous alkali solution, alkali hydrolysis is substantially carried out. Before proceeding, determine the amount of treatment bath in the equipment and its concentration, and when the expected weight loss is reached based on the determined amount of treatment bath and caustic soda concentration, the weight of the woven or knitted fabric in the equipment, and the expected weight loss rate A method has been proposed to calculate the estimated caustic soda concentration of the treatment bath, perform statistical processing by comparing it with the actual weight loss rate, and predict the next measured caustic soda concentration to improve accuracy and reproducibility. ing. Such an alkali weight reduction method has recently been adopted in batch type weight loss machines, but if the accuracy of the titrator for caustic soda concentration is not very high, the weight loss rate cannot be controlled sufficiently, so that there is variation between lots. Therefore, there is a problem that the occurrence of the problem occurs, and it is necessary to further improve the accuracy in practical use.

【0006】一方,バッチ式減量法では生産性が劣るた
め,連続式減量法も提唱され,実用化されている。例え
ば,特開昭57−61766号公報によれば,50℃以
上,100℃未満の乾熱雰囲気中でアルカリ水溶液の均
一付着性を高める目的で,リン酸エステル系,アルキル
サルファイト系等の耐アルカリ性浸透剤を0.1〜3.0%
併用したアルカリ水溶液をマングル等で絞る,いわゆる
パディング法等によって織編物に付与し,短時間内にア
ルカリ加水分解反応を完結せしめる方法が提案されてい
る。しかしながら,連続式の場合には,生産性を考慮し
て減量加工を行うのであるから,一般に高濃度の苛性ソ
ーダ水溶液が必要であり,この方法でも同様に減量の不
均一性や減量率の正確な管理が難しいという問題を有し
ていた。
[0006] On the other hand, since the productivity is inferior in the batch type weight loss method, a continuous type weight loss method has also been proposed and put into practical use. For example, according to Japanese Patent Application Laid-Open No. 57-61766, in order to enhance uniform adhesion of an alkaline aqueous solution in a dry heat atmosphere at a temperature of 50 ° C. or more and less than 100 ° C., a phosphate-based or alkyl-sulfite-based resin is used. 0.1 to 3.0% of alkaline penetrant
A method has been proposed in which the combined aqueous alkali solution is applied to the woven or knitted fabric by a so-called padding method or the like, which is squeezed with a mangle or the like, to complete the alkali hydrolysis reaction in a short time. However, in the case of the continuous type, since the weight reduction process is performed in consideration of the productivity, a high-concentration aqueous solution of caustic soda is generally required. There was a problem that management was difficult.

【0007】このように,苛性ソーダ等のアルカリ加水
分解によるポリエステル系繊維の分解は,それ自体の減
量機構も理論的にかなり確立されたものであり,かつバ
ッチ式,連続式のいずれの方法においても実用化されて
いる公知のポリエステル系繊維布帛の風合改良法である
が,いずれの方法も,高濃度の苛性ソーダ水溶液を必要
としたり,低濃度であっても,第4級アンモニウム塩を
併用するとアルカリ加水分解反応が激しすぎて減量速度
の正確な管理が難しい等の問題が多く,近年これらの問
題を解消する抜本的なポリエステル系繊維布帛のアルカ
リ減量法の提案は見受けられない。
As described above, the decomposition of polyester fibers by alkali hydrolysis of caustic soda, etc., has its weight-reduction mechanism well established theoretically, and can be carried out by any of the batch method and the continuous method. It is a well-known method of improving the feel of polyester fiber fabrics that has been put into practical use, and any of these methods requires a high-concentration aqueous solution of caustic soda or a low-concentration quaternary ammonium salt. There are many problems such as that the alkali hydrolysis reaction is so intense that it is difficult to accurately control the rate of weight loss, and in recent years there has been no proposal for a drastic alkali weight reduction method for polyester-based fiber cloth which solves these problems.

【0008】[0008]

【発明が解決しようとする課題】本発明は,このような
現状に鑑みて行われたもので,0.1〜10%の低濃度の
アルカリでも,ポリエステル系繊維を効率よく,再現性
よく加水分解することができるポリエステル系繊維布帛
のアルカリ減量処理方法を得ることを目的とするもので
ある。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above-mentioned circumstances, and is effective in reproducing polyester fibers efficiently and reproducibly even with an alkali having a low concentration of 0.1 to 10%. An object of the present invention is to provide a method for treating an alkali weight loss of a polyester fiber fabric that can be decomposed.

【0009】[0009]

【課題を解決するための手段】本発明は,上記目的を達
成するもので,次の構成よりなるものである。すなわ
ち,本発明は,「ポリエステル系繊維布帛のアルカリに
よる加水分解処理に際して,その溶媒としてアルキレン
グリコールおよび/またはポリオキシアルキレングリコ
ールを60重量%以上含み,その他の主たる溶媒として
水を用いてなるアルカリ処理液を用いてポリエステル系
繊維を加水分解処理することを特徴とするポリエステル
系繊維布帛のアルカリ減量処理方法」を要旨とするもの
である。ここで“および/または”なる語句は,両者の
うちのいずれか一方または双方を意味するものとする。
The present invention attains the above object and has the following constitution. That is, the present invention relates to an alkali-treated polyester fiber cloth which contains at least 60% by weight of alkylene glycol and / or polyoxyalkylene glycol as a solvent and water as a main solvent during the hydrolysis treatment of the polyester fiber cloth with an alkali. And subjecting the polyester fibers to hydrolysis treatment using a liquid. Here, the phrase "and / or" means either one or both.

【0010】[0010]

【発明の実施の形態】以下,本発明について詳細に説明
する。本発明で用いられるポリエステル系繊維布帛とし
ては,ポリエチレンテレフタレート,ポリブチレンテレ
フタレート等のポリエステル繊維を主体とした織物,編
物,不織布等や,上記ポリエステル繊維と改質ポリエス
テル繊維,ポリアミド繊維,ポリウレタン繊維や綿,ウ
ール等の天然繊維との混繊糸,交絡糸,複合混紡糸から
なる交編織織編物等を挙げることができる。上述の繊維
布帛に本発明方法ではアルカリによる加水分解処理を行
うが,ここで用いるアルカリとしては,苛性ソーダ,苛
性カリ,炭酸ソーダ,炭酸カリ等を適宜選択して使用す
ることができる。一般的には,苛性ソーダを用いる方が
現状の加工場の設備の点から見て有利である。アルカリ
加水分解剤の濃度は,通常0.1〜10重量%が適当であ
るが,目標とする減量率に応じて適宜決定することがで
きる。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. Examples of the polyester fiber fabric used in the present invention include woven fabrics, knitted fabrics, and nonwoven fabrics mainly composed of polyester fibers such as polyethylene terephthalate and polybutylene terephthalate, and the above polyester fibers and modified polyester fibers, polyamide fibers, polyurethane fibers, and cotton. And knitted and woven knitted fabrics composed of mixed yarns, entangled yarns, and composite mixed yarns with natural fibers such as wool and wool. In the method of the present invention, the above-mentioned fiber cloth is subjected to hydrolysis treatment with an alkali. As the alkali used here, caustic soda, caustic potash, sodium carbonate, potash carbonate, or the like can be appropriately selected and used. In general, the use of caustic soda is advantageous from the viewpoint of the existing processing plant equipment. Usually, the concentration of the alkali hydrolyzing agent is suitably from 0.1 to 10% by weight, but can be appropriately determined according to the target weight loss rate.

【0011】本発明では,アルカリによる加水分解処理
に際して,その溶媒としてアルキレングリコールおよび
/またはポリオキシアルキレングリコールを60重量%
以上含み,その他の主たる溶媒として水を用いてなるア
ルカリ処理液を用いる。ここで用いるアルキレングリコ
ールの代表的な例としては,エチレングリコール,プロ
ピレングリコール等が挙げられる。また,ポリオキシア
ルキレングリコールとしては,ポリエチレングリコー
ル,ポリプロピレングリコール等が挙げられるが,使用
上の簡便さから,分子量100〜1000程度のポリエ
チレングリコールが好ましく用いられる。さらに好まし
くは,分子量400程度の常温で液体状態のポリエチレ
ングリコールが用いられる。アルキレングリコールおよ
び/またはポリオキシアルキレングリコールの溶媒中の
含有量は,60重量%以上であることが好ましく,特に
好ましくは,80重量%以上が望ましい。アルキレング
リコールおよび/またはポリオキシアルキレングリコー
ルの含有量が60重量%未満であると,アルカリ減量の
促進効果が乏しく,通常の水系のアルカリ減量に比べて
際立った効果が望めない。
According to the present invention, in the hydrolysis treatment with alkali, alkylene glycol and / or polyoxyalkylene glycol are used as a solvent in an amount of 60% by weight.
An alkaline treatment liquid containing water as described above and using water as another main solvent is used. Representative examples of the alkylene glycol used here include ethylene glycol and propylene glycol. Examples of the polyoxyalkylene glycol include polyethylene glycol and polypropylene glycol, and polyethylene glycol having a molecular weight of about 100 to 1,000 is preferably used from the viewpoint of simplicity in use. More preferably, polyethylene glycol in a liquid state at room temperature with a molecular weight of about 400 is used. The content of the alkylene glycol and / or the polyoxyalkylene glycol in the solvent is preferably at least 60% by weight, particularly preferably at least 80% by weight. When the content of the alkylene glycol and / or the polyoxyalkylene glycol is less than 60% by weight, the effect of promoting the alkali weight reduction is poor, and a remarkable effect cannot be expected as compared with the ordinary water-based alkali weight reduction.

【0012】上述の溶媒の他の主たる溶媒としては水が
用いられ,40重量%未満の範囲で用いられる。本発明
方法では,処理温度並びに処理時間については,目標と
する風合に適した減量率により適宜調節を行うことがで
きる。特に処理温度に関しては,常圧で処理する場合,
アルキレングリコールおよび/またはポリオキシアルキ
レングリコールの含有比率によって条件が異なる。これ
らグリコールの含有比率が60〜90重量%の場合の処
理温度は60〜100℃であり,好ましくは80〜10
0℃である。この範囲の含有比率では,溶媒中の水分が
影響して,実用上短時間で100℃以上に温度を上げる
ことは困難である。一方,加圧によって処理できる場合
はこの限りではないが,処理装置が大がかりになるとい
う問題が生じる。上述のアルキレングリコールおよび/
またはポリオキシアルキレングリコールの含有比率が9
0重量%以上の場合の処理温度は60〜180℃程度で
あり,特に好ましくは80〜140℃である。80℃未
満では,効果的にアルカリ減量を促進させる効果に乏し
く,140℃以上では,処理時間が長くなると繊維の融
解が起こり,極端に強度低下を引き起こす可能性がある
ので注意を要する。
Water is used as another main solvent of the above-mentioned solvents, and is used in an amount of less than 40% by weight. In the method of the present invention, the processing temperature and the processing time can be appropriately adjusted by a weight reduction rate suitable for a target feeling. Especially regarding the processing temperature, when processing at normal pressure,
Conditions vary depending on the content ratio of alkylene glycol and / or polyoxyalkylene glycol. When the content ratio of these glycols is 60 to 90% by weight, the treatment temperature is 60 to 100 ° C, preferably 80 to 100 ° C.
0 ° C. At a content ratio in this range, it is difficult to raise the temperature to 100 ° C. or more in a short period of time due to the influence of moisture in the solvent. On the other hand, the case where the processing can be performed by pressurization is not limited to this, but there is a problem that the processing apparatus becomes large-scale. The above-mentioned alkylene glycol and / or
Or when the content ratio of the polyoxyalkylene glycol is 9
When the content is 0% by weight or more, the processing temperature is about 60 to 180 ° C, and particularly preferably 80 to 140 ° C. If the temperature is lower than 80 ° C., the effect of effectively promoting the alkali weight loss is poor, and if the temperature is 140 ° C. or higher, if the treatment time is prolonged, the fibers may be melted and the strength may be extremely lowered, so care must be taken.

【0013】本発明において特に推奨される処理条件
は,分子量100〜400程度のポリエチレングリコー
ルが95重量%以上,水5重量%未満の混合溶媒で,浴
比1:20〜30程度,処理温度80〜140℃,処理
時間5〜30分程度が目安となる。処理装置としては,
連続式,バッチ式のいずれも採用することが可能であ
る。連続式の場合,通常の公知の連続式減量機を使用す
ることができ,水系のアルカリ減量と同様に,処理液を
パッダーにてパッドした後のエージング工程,つまり滞
留槽での滞留時間の調節が重要である。一方,バッチ式
の場合も,通常の公知の液流型染色機やバッチ式減量機
を使用することができるが,ポリオキシアルキレングリ
コールが特にポリエチレングリコールであって,その溶
媒中の含有率が95重量%以上の場合には,常圧で10
0℃以上の処理が可能であるため,開放型の処理機が採
用可能である。
The processing conditions particularly recommended in the present invention are as follows: a mixed solvent of 95% by weight or more and less than 5% by weight of polyethylene glycol having a molecular weight of about 100 to 400, a bath ratio of about 1:20 to 30 and a processing temperature of 80%. As a guide, a temperature of about 140 ° C. and a processing time of about 5 to 30 minutes are guidelines. As a processing device,
Both a continuous type and a batch type can be adopted. In the case of the continuous type, an ordinary known continuous type weight loss machine can be used, and similarly to the water-based alkali weight reduction, the aging step after padding the processing liquid with a padder, that is, the adjustment of the residence time in the retention tank. is important. On the other hand, in the case of the batch type, an ordinary known liquid jet dyeing machine or a batch type weight loss machine can be used. However, the polyoxyalkylene glycol is particularly polyethylene glycol, and the content in the solvent is 95%. If it is more than 10% by weight, 10
Since processing at 0 ° C. or higher is possible, an open type processing machine can be adopted.

【0014】[0014]

【作用】本発明のポリエステル系繊維のアルキレングリ
コールおよび/またはポリオキシアルキレングリコール
溶液におけるアルカリ加水分解は,その反応機構が明確
に解明できてはいないが,従来法のアルカリ減量と比べ
て低濃度のアルカリ溶液で反応促進効果が高く,短時間
でアルカリ剤を消費できるため,ほぼ理論減量率に近い
減量率を効率よく得ることができることから,これらグ
リコールがポリエステル系繊維と親和性が高いことによ
る膨潤効果等により,アルカリ剤が効率よく繊維分子を
分解するものと推測している。また低濃度であるがゆ
え,実作業上の危険性も少なく,アルカリ加水分解反応
の制御も容易であり再現性も高く,従来法とは異なった
新規な風合を有するポリエステル系繊維を得ることがで
きる。
The alkali hydrolysis of the polyester fiber of the present invention in an alkylene glycol and / or polyoxyalkylene glycol solution has not been clearly elucidated, but its concentration is lower than that of the conventional method. Alkali solution has a high reaction promoting effect and can consume alkaline agent in a short time, so that a weight loss rate close to the theoretical weight loss rate can be obtained efficiently, and swelling due to the high affinity of these glycols with polyester fibers. It is presumed that the alkali agent efficiently decomposes fiber molecules due to effects and the like. In addition, because of the low concentration, there is little danger in actual work, easy control of alkali hydrolysis reaction, high reproducibility, and obtaining a polyester fiber with a new feeling different from the conventional method. Can be.

【0015】[0015]

【実施例】次に,本発明を実施例によってさらに具体的
に説明するが,実施例におけるポリエステル系繊維の減
量率の測定評価は,下記の方法で行った。 (1)減量率 温度25℃,相対湿度60%の条件下で2時間調湿した
減量前のサンプル重量(S)を秤量し,次に,アルカリ
減量加工を行った後,減量前と同条件にて調湿を行い,
減量後の重量(W)を測定し,次式によって計算した。 減量率(%)=(S−W)/S×100
EXAMPLES Next, the present invention will be described in more detail with reference to examples. The measurement and evaluation of the weight loss rate of polyester fibers in the examples were performed by the following methods. (1) Weight loss rate The weight (S) of the sample before weight loss, which was conditioned for 2 hours at a temperature of 25 ° C. and a relative humidity of 60%, was weighed, and then subjected to alkali weight loss processing, and then under the same conditions as before weight loss. We perform humidity control in
The weight (W) after weight loss was measured and calculated by the following equation. Weight loss rate (%) = (S−W) / S × 100

【0016】実施例1 ポリエステル100%の極細糸使いの平織物に公知の方
法で精練,プレセットを行い,減量処理前の織物を得
た。次にこの織物を約7gにカットし,12色ポット染
色試験機(テクサム技研製,MINI−COROUR
12S)を用いて下記処方1の処理液200g中で処理
温度80℃,100℃,130℃の3条件にてそれぞれ
5,10,15,20,25分間のアルカリ減量処理を
行った。 処方1 ポリエチレングリコール 95.0重量% (分子量 400 ) 水 4.9重量% 苛性ソーダ 0.1重量% 続いて,80℃にて5分間の湯洗を行った後,通常のタ
ンブル乾燥(60℃,20分)を行うことにより,本発
明方法によるアルカリ減量加工織物を得た。
Example 1 A plain fabric made of 100% polyester with ultrafine yarn was scoured and preset by a known method to obtain a fabric before weight reduction. Next, this woven fabric was cut into about 7 g, and a 12-color pot dyeing tester (manufactured by Texam Giken, MINI-COLOUR)
Using 12S), alkali reduction treatment was performed in 200 g of a treatment liquid having the following formulation 1 under three conditions of treatment temperatures of 80 ° C., 100 ° C., and 130 ° C. for 5, 10, 15, 20, and 25 minutes, respectively. Formulation 1 Polyethylene glycol 95.0% by weight (molecular weight 400) Water 4.9% by weight Caustic soda 0.1% by weight Then, after washing with hot water at 80 ° C. for 5 minutes, ordinary tumble drying (60 ° C., 20 minutes) to obtain a fabric with a reduced alkali content according to the method of the present invention.

【0017】本発明との比較のため,本実施例で用いた
処方1に代えて従来の水系減量処方2を用いるほかは,
本実施例とまったく同一の条件にてアルカリ減量処理を
行った。 処方2 水 99.9重量% 苛性ソーダ 0.1重量% 本発明および比較用の加工織物の減量率を測定し,その
結果を合わせて表1に示した。
For comparison with the present invention, a conventional water-based weight-loss formula 2 was used in place of the formula 1 used in this example.
The alkali weight reduction treatment was performed under exactly the same conditions as in this example. Formulation 2 Water 99.9% by weight Caustic soda 0.1% by weight The weight loss of the processed fabric of the present invention and the comparative sample was measured, and the results are shown in Table 1.

【0018】[0018]

【表1】 [Table 1]

【0019】表1より明らかなごとく,本発明のアルカ
リ減量法によると,通常の水系減量法より著しく減量速
度が速く,短時間でアルカリ加水分解反応が完了するた
め,減量率の制御が容易で,しかも再現性が高いことが
分かる。本発明方法による減量加工織物は,しっとりと
したドレープ性のよい風合の織物であった。
As is evident from Table 1, according to the alkali weight loss method of the present invention, the weight loss rate is remarkably faster than that of the ordinary aqueous weight loss method, and the alkali hydrolysis reaction is completed in a short time. Further, it can be seen that the reproducibility is high. The weight-reduced woven fabric according to the method of the present invention was a moist woven fabric having a good drape property.

【0020】実施例2 上記実施例1と同一の7gにカットされた減量処理前の
織物を用いて,下記処方3の処理液200g中で130
℃,10分間のアルカリ減量処理を行った。 処方3 ポリエチレングリコール 100重量% (分子量 400 ) 水 5.0重量% 苛性ソーダ 0.5, 1, 2, 3, 5, 10重量%の6水準
Example 2 Using the same fabric as in Example 1 but cut into 7 g before the weight reduction treatment, 130 g
An alkali reduction treatment was performed at 10 ° C. for 10 minutes. Formulation 3 Polyethylene glycol 100% by weight (molecular weight 400) Water 5.0% by weight Caustic soda 0.5, 1, 2, 3, 5, 10% by weight 6 levels

【0021】本発明との比較のため,本実施例で用いた
処方3に代えて従来の水系減量処方4を用いるほかは,
本実施例とまったく同一の条件にてアルカリ減量処理を
行った。 処方4 水 100重量% 苛性ソーダ 0.5,1,2,3,5,10重量%の6水準 本発明および比較用の加工織物の減量率を測定し,その
結果を合わせて表2に示した。参考までに理論減量率を
次式によって計算し,同様に表2に示した。 理論減量率(%)=192/80×(苛性ソーダ重量
g)/(生地重量g)×100
For comparison with the present invention, a conventional water-based weight-loss formula 4 was used in place of the formula 3 used in the present example.
The alkali weight reduction treatment was performed under exactly the same conditions as in this example. Formulation 4 Water 100% by weight Caustic soda 0.5, 1, 2, 3, 5, 10% by weight 6 levels The weight loss rate of the present invention and the processed fabric for comparison was measured, and the results are shown in Table 2 together. . For reference, the theoretical weight loss rate was calculated by the following equation, and is shown in Table 2. Theoretical weight loss (%) = 192/80 × (weight of caustic soda) / (weight of dough) × 100

【0022】[0022]

【表2】 [Table 2]

【0023】表2より明らかなごとく,本発明のアルカ
リ減量法は,通常の水系減量法に比べて低濃度のアルカ
リ溶液で著しく減量反応が促進され,しかもほぼ理論減
量率に近い減量率を得ることができることから,効率の
よいアルカリ減量処理が可能であることが分かる。
As is clear from Table 2, in the alkali weight reduction method of the present invention, the weight loss reaction is remarkably accelerated with a low-concentration alkaline solution as compared with the ordinary aqueous weight loss method, and a weight loss rate almost close to the theoretical weight loss rate is obtained. This shows that efficient alkali weight reduction treatment is possible.

【0024】[0024]

【発明の効果】本発明のごとく,アルキレングリコール
やポリオキシアルキレングリコール溶液におけるポリエ
ステル系繊維のアルカリ加水分解は,低濃度のアルカリ
溶液でも反応促進効果が高いため,効率よく再現性の高
い減量加工が可能である。このことにより,実作業にお
いて減量斑の問題やロット間の減量率のバラツキが減少
し,安定した加工を行うことができる。さらに,各実施
例に示した95%以上のポリエチレングリコール溶媒の
場合,処理温度が100℃未満の低温処理でもアルカリ
加水分解反応が著しく促進されるため,省エネ効果が期
待できる。また100℃以上の条件の場合においても,
本発明方法では常圧下で処理することができるため,簡
便な装置で加工が可能である。本発明方法では,分解反
応がより短時間で促進され,アルカリ剤の濃度を理論減
量率から計算することにより,再現性よくアルカリ加水
分解を行うことができるので,非常に効率のよい減量加
工が可能である。
As described in the present invention, the alkali hydrolysis of polyester fibers in an alkylene glycol or polyoxyalkylene glycol solution has a high reaction promoting effect even in a low-concentration alkaline solution, so that a weight-reducing process with high reproducibility can be performed efficiently. It is possible. As a result, in actual work, the problem of uneven weight loss and the variation in the weight loss rate between lots are reduced, and stable processing can be performed. Further, in the case of the polyethylene glycol solvent of 95% or more shown in each of the examples, even at a low temperature treatment at a treatment temperature of less than 100 ° C., the alkali hydrolysis reaction is remarkably promoted, so that an energy saving effect can be expected. In addition, even under the condition of 100 ° C or more,
In the method of the present invention, processing can be performed under normal pressure, so that processing can be performed with a simple apparatus. In the method of the present invention, the decomposition reaction is accelerated in a shorter time, and the alkali hydrolysis can be carried out with good reproducibility by calculating the concentration of the alkali agent from the theoretical weight loss rate. It is possible.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポリエステル系繊維布帛のアルカリによ
る加水分解処理に際して,その溶媒としてアルキレング
リコールおよび/またはポリオキシアルキレングリコー
ルを60重量%以上含み,その他の主たる溶媒として水
を用いてなるアルカリ処理液を用いてポリエステル系繊
維を加水分解処理することを特徴とするポリエステル系
繊維布帛のアルカリ減量処理方法。
1. An alkaline treatment liquid comprising 60% by weight or more of an alkylene glycol and / or a polyoxyalkylene glycol as a solvent and water as a main solvent when the polyester fiber cloth is hydrolyzed with an alkali. A method for reducing the alkali content of a polyester fiber cloth, comprising subjecting the polyester fiber to a hydrolysis treatment.
JP12528897A 1997-05-15 1997-05-15 Alkali thinning treatment of polyester fiber fabric Pending JPH10317276A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12528897A JPH10317276A (en) 1997-05-15 1997-05-15 Alkali thinning treatment of polyester fiber fabric

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12528897A JPH10317276A (en) 1997-05-15 1997-05-15 Alkali thinning treatment of polyester fiber fabric

Publications (1)

Publication Number Publication Date
JPH10317276A true JPH10317276A (en) 1998-12-02

Family

ID=14906376

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12528897A Pending JPH10317276A (en) 1997-05-15 1997-05-15 Alkali thinning treatment of polyester fiber fabric

Country Status (1)

Country Link
JP (1) JPH10317276A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001288675A (en) * 2000-03-31 2001-10-19 Teijin Ltd Method for caustic reduction of polyalkylene terephthalate-based fiber
KR100822283B1 (en) * 2002-10-30 2008-04-16 주식회사 코오롱 A method of extracting sea component from woven or knitted fabric with sea-island type composite fiber
US10494741B2 (en) 2013-11-25 2019-12-03 Asahi Kasei Fibers Corporation Absorbent fabric

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001288675A (en) * 2000-03-31 2001-10-19 Teijin Ltd Method for caustic reduction of polyalkylene terephthalate-based fiber
KR100822283B1 (en) * 2002-10-30 2008-04-16 주식회사 코오롱 A method of extracting sea component from woven or knitted fabric with sea-island type composite fiber
US10494741B2 (en) 2013-11-25 2019-12-03 Asahi Kasei Fibers Corporation Absorbent fabric

Similar Documents

Publication Publication Date Title
CN109306619A (en) The cold dome open-width desizing technique of chemical fiber plus material
US1741637A (en) Vegetable textile material and process for producing same
JPH08502789A (en) Wool treatment method
JPH10317276A (en) Alkali thinning treatment of polyester fiber fabric
US4269602A (en) Buffered non-formaldehyde durable press textile treatment
JPH08503741A (en) Wool treatment method
CN108951142A (en) Fiber woolen fabric and preparation method thereof with cashmere feel and gloss
JP2000282377A (en) Erosion removal processing for fiber textile
JPS6228483A (en) Treatment of fiber
JP2003253575A (en) Dyeing process for fiber structure and dyed fiber structure
JPH0219235B2 (en)
JP2851282B2 (en) Desizing scouring and bleaching method for cotton fabric
JPH02216282A (en) Method for weight reduction processing of cellulosic fiber structure
US2457033A (en) Treatment of wool to impart shrinkage resistance thereto
US2702228A (en) Method of modifying cellulose fibers with alkali solutions of copper or nickel biuret
JP3730733B2 (en) Elongated animal hair fiber and production method thereof
US3397942A (en) Antifelting process for keratinous materials
US4225312A (en) Treatment of textiles
KR930008699B1 (en) Manufacturing method for textile softening and silk touch
JPH0657628A (en) Modification process for animal hair fiber structures
JPH02251674A (en) Mercerization of roving
JP2006052480A (en) Method for processing cellulosic fiber-containing cloth and the cellulosic fiber-containing cloth
JPH02289168A (en) Mercerization of roving
JP2002317344A (en) Woven fabric
JP2002115175A (en) Method of manufacturing polyester based fabric containing cellulose based fiber