JPH064931B2 - Method for mercerizing roving yarn - Google Patents
Method for mercerizing roving yarnInfo
- Publication number
- JPH064931B2 JPH064931B2 JP10319889A JP10319889A JPH064931B2 JP H064931 B2 JPH064931 B2 JP H064931B2 JP 10319889 A JP10319889 A JP 10319889A JP 10319889 A JP10319889 A JP 10319889A JP H064931 B2 JPH064931 B2 JP H064931B2
- Authority
- JP
- Japan
- Prior art keywords
- roving
- cheese
- mercerizing
- treatment
- caustic soda
- 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.)
- Expired - Lifetime
Links
Landscapes
- Treatment Of Fiber Materials (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は粗糸のシルケット加工方法に関する。The present invention relates to a method for mercerizing roving yarn.
(従来の技術) 綿および綿混紡の繊維にたいしては、光沢の付与、寸法
安定性の改善、吸湿性の増加および強力の向上等のため
にシルケット加工(マーセライズ加工)が行なわれてい
る。一般にシルケット加工は、織物、編物の状態で行な
われているが、シルケット加工に伴う綿組織の強い収縮
作用によって記事の風合が硬化し、バルキー性や柔軟性
が損なわれるという問題がある。このため、編織前の糸
の階段で処理を行う方法もあるが、糸のシルケット加工
の場合は、張力管理等の問題より、かせ状で行なわれる
ことが多く生産性の問題がある。これを解決せんとし
て、特公昭57−47783号公報の如き提案もある
が、依然生産性は向上されていない。(Prior Art) Cotton and cotton-blended fibers are subjected to mercerizing (mercerizing) in order to impart gloss, improve dimensional stability, increase hygroscopicity and strength. Generally, mercerizing is carried out in the form of woven or knitted fabric, but there is a problem that the texture of articles is hardened due to the strong shrinking action of the cotton structure accompanying mercerizing, and bulkiness and flexibility are impaired. For this reason, there is a method of performing processing at the stairs of the yarn before knitting, but in the case of mercerizing the yarn, it is often carried out in a skein shape because of problems such as tension management, and there is a problem of productivity. As a solution to this problem, there is a proposal such as Japanese Patent Publication No. 57-47783, but the productivity has not been improved yet.
これらの従来技術では、バルキー性があり、染色性・生
産性等も良好な素材の開発は難しく、紡績前工程でのシ
ルケット加工が望まれていた。しかしながら、単に原綿
を高濃度の苛性ソーダ溶液を用いてシルケット加工を行
なった場合は、原綿が固い塊となって解綿が困難にな
り、紡績がほとんど不可能になると共に、仮に紡績し得
たとしても、上記の処理をした後に混打綿工程からコー
マ工程を通過するまでの間に多量の単繊維が屑綿とな
る。With these conventional techniques, it is difficult to develop a material having bulkiness and good dyeability and productivity, and mercerizing in the pre-spinning process has been desired. However, when the raw cotton is simply mercerized by using a high-concentration caustic soda solution, the raw cotton becomes a solid mass, making it difficult to break the cotton, and spinning becomes almost impossible. However, after the above treatment, a large amount of monofilament becomes waste cotton from the mixed-plying step to the passing of the combing step.
このような問題点を解決するために、特公昭62−27
188号公報にはスライバーの状態で連続的にシルケッ
ト加工する方法が開示されている。In order to solve such a problem, Japanese Patent Publication No. 62-27
Japanese Patent No. 188 discloses a method of continuous mercerizing in a sliver state.
(発明が解決しようとする課題) しかしながら、特公昭62−27188号公報に開示さ
れた方法は、設備的な問題や、大量生産向の連続法であ
るために、小量生産には向かないという問題点が存在す
る。(Problems to be Solved by the Invention) However, the method disclosed in Japanese Patent Publication No. 62-27188 is not suitable for small-quantity production because it has a facility problem and is a continuous method for mass production. There are problems.
本発明は、かかる問題点を解決するために、特公昭62
−27188号の対象とするスライバー状態の次の状態
である粗糸の状態に着目し、チーズの状態で、工業的に
有利にアルカリ処理を行う方法を提供するものである。In order to solve such a problem, the present invention discloses a Japanese Patent Publication No.
Focusing on the state of roving, which is the state following the sliver state targeted by No. 27188, the present invention provides a method for industrially advantageously performing alkali treatment in the state of cheese.
(課題を解決するための手段) 本発明は、セルロース系繊維を含有する短繊維を紡績工
程を通して粗糸となし、これを0.1〜0.5g/cm3の捲
取密度で捲取ってチーズを形成した後、該チーズを密閉
容器内にセットして、760mmHg以下に減圧後、高
濃度苛性ソーダ溶液を注入して、該チーズに対し温度4
0〜60℃の高濃度苛性ソーダ溶液を流動せしめる処理
を施こした後水洗い、中和することを特徴とするもの及
び、セルロース系繊維を含有する短繊維を紡績工程を通
して粗糸となし、これを0.1〜05g/m3の捲取密度で
捲取ってチーズを形成した後、該チーズを密閉容器内に
セットして、760mmHg以下に減圧し、次いで高圧
水蒸気を注入した後、温度40〜60℃の高濃度苛性ソ
ーダ溶液を流動せしめる処理を施こし水洗い、中和する
ことを特徴とするものである。(Means for Solving the Problems) In the present invention, short fibers containing cellulosic fibers are made into roving through a spinning process, and the roving is wound at a winding density of 0.1 to 0.5 g / cm 3 to form cheese. After that, the cheese is set in a closed container, the pressure is reduced to 760 mmHg or less, and a high-concentration caustic soda solution is injected, and the cheese is heated to a temperature of 4
What is characterized by performing a treatment for fluidizing a high-concentration caustic soda solution at 0 to 60 ° C., followed by washing with water and neutralization, and short fibers containing cellulosic fibers are made into roving through a spinning process. After forming cheese by winding at a winding density of 0.1 to 05 g / m 3 , the cheese is set in a closed container, depressurized to 760 mmHg or less, and then high-pressure steam is injected, and then the temperature is 40 to 60 ° C. It is characterized in that it is subjected to a treatment for fluidizing the high concentration caustic soda solution, washed with water and neutralized.
本発明に用いるセルロース系繊維を含有する短繊維と
は、シルケット加工に適した天然セルロース系短繊維で
ある綿糸等であって、綿糸と混紡できる合成繊維、ポリ
アミド系繊維(例えば、ナイロン6、ナイロン6.6)、
ポリアクリロニトリル系繊維(例えばポリエチレンテレ
フタレート)、ポリビニルアルコール系繊維(例えばビ
ニロン)、ポリオレフィン系繊維(例えばポリエチレ
ン)、ポリウレタン系繊維などの混紡短繊維を含む。こ
れらの短繊維は、高知の紡績工程即ち、混打綿・梳綿・
練条等の工程を経てスライバーとなし、更に粗紡工程を
経て粗糸の形態に捲取る。The short fibers containing cellulosic fibers used in the present invention include cotton yarn which is a natural cellulose short fiber suitable for mercerizing, and synthetic fibers that can be mixed with cotton yarn, polyamide fibers (for example, nylon 6, nylon). 6.6),
It includes blended short fibers such as polyacrylonitrile fiber (eg polyethylene terephthalate), polyvinyl alcohol fiber (eg vinylon), polyolefin fiber (eg polyethylene), polyurethane fiber and the like. These short fibers are used in Kochi's spinning process, that is, blended cotton / cardboard /
It is made into a sliver through a process such as kneading, and is further wound into a roving form through a roving process.
本発明で、粗糸とはボビン等に捲取ってチーズの形態に
できるものであれば特に限定はされないが、通常、0.2
〜0.5g/m程度のものを云う。又、粗糸は一般に行な
われている如く、0.5〜2回/inch程度の撚をかけ
ることが好ましい。In the present invention, the roving is not particularly limited as long as it can be wound on a bobbin or the like to form cheese, but usually 0.2
~ 0.5 g / m. Further, it is preferable that the roving is twisted about 0.5 to 2 times / inch as is generally done.
本発明は、シルケット処理を粗糸の状態に対して行うの
であるが、粗糸の状態に対してシルケット加工や染色等
の液流処理を施すことは甚だ困難を伴なう。その理由
は、前記従来技術にも述べられた如く、原綿や梳綿、練
条スライバー、或は羊毛のトップ染めのように、単繊維
又はそれを平行に単に配列した状態のものを液流処理す
ることは、既に実施されているように、割合簡単であ
る。また、糸染めも糸自体が取扱いの容易な形態に完成
されているから、これも容易であると言える。しかし、
普通、粗糸は、プラスチックボビン又は木管に捲かれて
居り、このまま染色等の液流処理に供する事は出来な
い。又、染色用チューブに捲返すことも強伸度が弱く、
手間も掛るため、実用上かなり無理がある。In the present invention, the mercerizing process is performed on the roving yarn state, but it is extremely difficult to perform the mercerizing process or the liquid flow treatment such as dyeing on the roving state. The reason is, as described in the above-mentioned prior art, a single fiber or a state in which the fibers are simply arranged in parallel, such as raw dyeing, carding, kneading sliver, or wool top dyeing, is subjected to liquid flow treatment. To do is relatively simple, as it has already been done. Further, it can be said that this is also easy for yarn dyeing because the yarn itself is completed in a form that is easy to handle. But,
Usually, the roving is wound around a plastic bobbin or a wood pipe, and cannot be used as it is for liquid flow treatment such as dyeing. Also, the strength and elongation are weak when it is rewound on the dyeing tube,
Since it takes time and effort, it is practically impossible.
本発明では、直接液流処理に供する事のできるボビンに
前記粗糸を捲取り、以下に述べる液流処理を施すことに
よって粗糸の状態でのシルケット加工が可能となるので
ある。かかるボビンとしては第1図に示す如き、金属或
いはプラスチック、又は木管製で周面に小孔を多数穿設
したものであって、粗糸を捲取った後、積層してパッケ
ージ染色機等に載置でき処理液が前記小孔を通じて吐出
できるものであればよい。又、特開昭62−21506
0号公報に開示された形状の染色ボビン(第2図)を粗
糸の捲取りが可能となるよう設計調整して用いれば積層
後の圧縮により、各粗糸が密着し、シルケット加工が効
果的に行なえる。In the present invention, the roving is wound on a bobbin which can be directly subjected to the liquid flow treatment, and the liquid flow treatment described below is performed to enable mercerizing in the state of the roving. Such a bobbin is made of metal, plastic, or wood pipe and has a number of small holes formed on its peripheral surface, as shown in FIG. Any material can be used as long as it can be placed and the processing liquid can be discharged through the small holes. Also, JP-A-62-21506
If the dyeing bobbin (FIG. 2) having the shape disclosed in Japanese Patent Publication No. 0 is designed and adjusted so that the roving can be wound up, each roving will adhere due to compression after lamination, and mercerizing will be effective. You can do it.
かかるボビンに粗糸を捲き取るに際しては、捲取密度が
0.1〜0.5g/cm3となるようソフトに捲取ることが必
要であり、かかる範囲であれば、前記の如き圧縮ボビン
でも使用することができる。捲取密度は前記範囲内であ
れば本発明の効果を得ることができるが、通常用いられ
るワインダーにより0.15g/cm3未満の密度をもって
チーズの形状に捲上げることは難しく、又、0.3g/c
m3を超えると糸切れ等の問題が生じるため0.15〜0.3
g/cm3がより好ましい。更に、0.18g/cm3以上
の捲取密度とすればシルケット加工に共なう粗糸の収縮
も少なく好都合であり、0.24g/cm3以下とすれば、
処理液の流量にもよるが、苛性ソーダが均一に浸透し、
処理斑も極めて少なくなる。When winding the roving on the bobbin, the winding density is
It is necessary to softly wind it up to 0.1 to 0.5 g / cm 3, and the compression bobbin as described above can also be used within this range. If the winding density is within the above range, the effect of the present invention can be obtained, but it is difficult to wind it into a cheese shape with a density of less than 0.15 g / cm 3 by a winder that is usually used, and 0.3 g / cm 3 c
If it exceeds m 3 , problems such as thread breakage occur, so 0.15 to 0.3
g / cm 3 is more preferable. Furthermore, if the winding density is 0.18 g / cm 3 or more, it is convenient because the shrinkage of the roving that accompanies mercerizing is small, and if it is 0.24 g / cm 3 or less,
Depending on the flow rate of the processing liquid, caustic soda penetrates uniformly,
Treatment spots are also extremely small.
このように準備されたソフト捲きのチーズは、公知のチ
ーズ染色機等の密閉容器にセットして760mmHg以
下好ましくは500mmHg以下に減圧した後、以下の
二法の何れかにより、後述の苛性ソーダ溶液を粗糸に迅
速且つ均一に浸透せしめる。即ち第1法は減圧後、直ち
に苛性ソーダ溶液を注入する方法である。又、第2法
は、減圧後、高圧水蒸気を注入して粗糸をスチームセッ
トした後、苛性ソーダ溶液を注入する方法である。第2
法の場合、高圧水蒸気は102℃以上、760mmHg
以上のものが好ましく、ヒートセットは1〜10分間程
度行うのがよい。The soft-rolled cheese thus prepared is set in a closed container such as a known cheese dyeing machine and depressurized to 760 mmHg or less, preferably 500 mmHg or less, and then by one of the following two methods, the caustic soda solution described below is used. Quickly and uniformly penetrate the roving. That is, the first method is a method of injecting a caustic soda solution immediately after decompression. The second method is a method of injecting high-pressure steam after depressurizing to steam set the roving, and then injecting a caustic soda solution. Second
In the case of the method, high pressure steam is 102 ° C or higher, 760 mmHg
The above is preferable, and heat setting is preferably performed for about 1 to 10 minutes.
これら両方法で用いる苛性ソーダ溶液は、高濃度即ち、
苛性ソーダ量が18〜30重量%程度のもので、かかる
範囲より被処理物の種類や処理の適度により適宜選択す
る。又、苛性ソーダ溶液の処理温度は、40〜60℃の
範囲で選ぶことができるが、40℃以下では、処理の均
一性に問題があり、60℃以上では、粗糸の強力が低下
し紡績性に問題が起こる。The caustic soda solution used in both of these methods has a high concentration, that is,
The amount of caustic soda is about 18 to 30% by weight, and is appropriately selected from the range depending on the type of the object to be treated and the suitability of the treatment. The treatment temperature of the caustic soda solution can be selected in the range of 40 to 60 ° C, but if it is 40 ° C or lower, there is a problem in the uniformity of treatment, and if it is 60 ° C or higher, the tenacity of the roving is reduced and the spinnability is reduced. Problems occur.
更に、苛性ソーダ溶液には、他にアニオン系界面活性剤
を添加するとよい。アニオン系界面活性剤は、市販のシ
ルケット加工用の浸透剤の中から選ぶことができる。ア
ニオン系界面活性剤としては、ポリエチレングリコール
エーテル硫酸エステル塩系・オレフィン類硫酸エステル
塩系・アミド結合硫酸エステル塩系・エステル結合硫酸
エステル塩系・エステル結合スルホン酸塩系・アミド結
合スルホン酸塩系・エーテル結合スルホン酸塩系・アル
キルアリルスルホン酸塩系・エーテル結合アルキルスル
ホン酸塩系・エステル結合アルキルアリルスルホン酸塩
系・アミド結合アルキルアリルスルホン酸塩系などが挙
げられる。このような界面活性剤の中から1種もしくは
2種以上を前記濃度の範囲で添加するのが良いが、特に
望ましくは浸透力の大きい高級アルコールサルフェート
系界面活性剤が良い。又、濃度は0.1%〜1%(ow
f)程度の間で被処理物の巻き密度等により選択する。
かかるアニオン系界面活性剤は十分にチーズに脱気、浸
透効果を与える作用をする。又、苛性ソーダ容器にはテ
トラクロルエチレンなどの溶剤を適宜添加しても良い。Further, an anionic surfactant may be added to the caustic soda solution. The anionic surfactant can be selected from commercially available penetrants for mercerizing. As anionic surfactants, polyethylene glycol ether sulfate ester-based, olefins sulfate ester-based, amide-bound sulfate ester-based, ester-bound sulfate ester-based, ester-bound sulfonate-amide-bound sulfonate -Ether bond sulfonic acid salt system-Alkyl allyl sulfonate salt system-Ether bond alkyl sulfonate salt system-Ester bond alkyl allyl sulfonate salt system-Amid bond alkyl allyl sulfonate salt system etc. are mentioned. It is preferable to add one or two or more of these surfactants within the above concentration range, and it is particularly preferable to use a higher alcohol sulfate surfactant having a high penetrating power. The concentration is 0.1% to 1% (ow
It is selected according to the winding density of the object to be processed, etc. between about f).
Such an anionic surfactant has a function of sufficiently giving deaeration and penetration effects to cheese. Further, a solvent such as tetrachloroethylene may be appropriately added to the caustic soda container.
かかる苛性ソーダ溶液による処理は、減圧に用いたチー
ズ染色機等の密閉容器中で連続して行うと能率的であ
り、チーズ染色機を用いた場合、浴比1:5〜1:10
程度で処理するとよく、又、苛性ソーダ溶液も予めサブ
タンクに用意しておくとよい。この場合、処理は、前記
の如きボビンを用いて溶液をボビンの小孔を通じて流量
5〜30/分・kg程度で流動させつつ20〜40分
間程度行う。溶液の流動方向はボビン内から粗糸側へ吐
出するIN−OUTでも、粗糸側からボビン内へ吸引す
るOUT−INでもよいが、シリケット加工の場合IN
−OUTの方が均一なアルカリ処理が行なえる点で好ま
しい。The treatment with the caustic soda solution is efficient when continuously performed in a closed container such as a cheese dyeing machine used for depressurization. When using the cheese dyeing machine, the bath ratio is 1: 5 to 1:10.
It is better to treat the solution in a degree, and a caustic soda solution may be prepared in the sub tank in advance. In this case, the treatment is performed for about 20 to 40 minutes while using the bobbin as described above to flow the solution through the small holes of the bobbin at a flow rate of about 5 to 30 / min · kg. The flow direction of the solution may be IN-OUT discharged from the bobbin to the roving yarn side or OUT-IN sucked from the roving yarn side to the bobbin side.
-OUT is preferable because uniform alkali treatment can be performed.
かかる処理後の被処理物は、さらに十分に湯洗され、水
洗された後、中和され油剤処理を施して後、脱水、乾燥
される。乾燥方法も特に限定はされないが、チーズ染色
法で好適に用いられる高周波減圧乾燥機等を用いると均
一な乾燥状態と、風合いのよい仕上りが得られる。The object to be treated after such treatment is further sufficiently washed with hot water, washed with water, neutralized, treated with an oil agent, dehydrated and dried. The drying method is also not particularly limited, but a uniform dry state and a finish with a good texture can be obtained by using a high-frequency vacuum dryer that is preferably used in the cheese dyeing method.
このようにして得られるシリケット処理粗糸は、シルケ
ット処理時の収縮により風合が硬く感じられるが、紡績
機の仕掛りさらに、ドラフトによって解繊されるので、
その結果得られる糸条の柔軟性は回復し、しかも通常の
紡績糸にはない光沢を備えている。The sikette-treated roving obtained in this way feels hard due to shrinkage during mercerizing, but since the work of the spinning machine further disentangles it by draft,
As a result, the flexibility of the yarn is restored, and it has a luster that is not present in ordinary spun yarn.
(実施例) 実施例中の数値の基本となる試験方法は、次の通りであ
る。(Example) The test method which is the basis of the numerical values in the examples is as follows.
綿繊維膨潤度 電子顕微鏡写真にて観察 バリウム活性数 シルケットの程度を測る価であり、木綿繊維の水酸化バ
リウムの吸収程度により次式によって計算した。Cotton fiber swelling degree Observed by electron micrograph Barium activity number It is the value to measure the degree of mercerized, and it was calculated by the following formula based on the absorption degree of barium hydroxide in cotton fiber.
No=水酸化バリウム規定数10ccにたいするN/1
0HClの滴定数 Nm=シルケット綿を浸したときの母液10ccにたい
するN/10HClの滴定数 Nu=未処理綿を浸したときの母液10ccにたいする
N/10HClの滴定数 風合 曲げ KES−FB風合測定システムのKES−FB2純曲げ
試験機にて測定した。 No = N / 1 for a barium hydroxide standard number of 10 cc
Droplet constant of 0HCl Nm = Drop constant of N / 10HCl in mother liquor 10cc when immersed in mercerized cotton Nu = Drop constant of N / 10HCl in mother liquor 10cc when immersed in untreated cotton Feeling Bending KES-FB Feeling measurement It was measured with a KES-FB2 pure bending tester of the system.
風合 圧縮 KES−FB風合測定システムのKES−FB3圧縮試
験機にて測定した。Feeling compression Measured with a KES-FB3 compression tester of a KES-FB texture measuring system.
破壊強力 JIS L−1096 A法(ミューレン法) 処理の均一性及染色濃度 アルカリ処理粗糸をもちいた編地を、Remazol
BLACK B 5% owfにて染色し、その染色濃
度及染 色面の良否を判定した。Destructive strength JIS L-1096 A method (Mullen method) Uniformity of treatment and dyeing density Knitted fabric using alkali treated roving is Remazol
It was dyed with BLACK B 5% owf, and the dyeing density and the quality of the dyed surface were evaluated.
実施例1 綿繊維とポリエステル繊維を3:1の重量比で混綿した
原綿を通常の紡績工程を通して粗紡あがりの粗糸0.4g
/mとなし、これを第1図に示したボビンに0.2g/cm
3の捲き密度で捲き取ってチーズを形成した。次に該チ
ーズ50個(粗糸重量50kg)をチーズ染色機(LL
C−50/60型 日阪製作所(株)製)に入れ、真空
ポンプを用いて500mmHgまで減圧した。サブタン
クに苛性ソーダ濃度21%、アニオン系界面活性剤(シ
ルピットP−25 一方社油脂(株)製)0.2%の水溶
液を調整し、真空ポンプを止めた後、注入した。該水溶
液が完全に注入された後、In−Outの流れ方向で、
流量10/分・kgに設定し、50℃で30分間処理
をおこなった。処理後、水洗を20分間、湯洗を80℃
で10分間、中和を80℃で10分間行ない、40℃で
10分間紡績油剤による柔軟処理を行なった。得られた
アルカリ処理粗糸は、脱水、乾燥され、精紡機に仕掛り
さらに、ドラフトによって解繊され、30番手の紡績糸
を得た。得られた紡績糸を32ゲージの両面丸編機にイ
ンターロック組織に編みあげ、通常公知の方法にて晒、
染色、仕上げ剤付与、乾燥仕上げセットを行なった。Example 1 0.4 g of roving yarn after roving was obtained by subjecting a raw cotton obtained by mixing cotton fiber and polyester fiber in a weight ratio of 3: 1 through a usual spinning process.
/ M, which is 0.2g / cm on the bobbin shown in Fig. 1.
The cheese was rolled up at a winding density of 3 . Next, the cheese dyeing machine (LL
It was put in a C-50 / 60 type HISAKA MFG. CO., LTD. And the pressure was reduced to 500 mmHg using a vacuum pump. An aqueous solution having a caustic soda concentration of 21% and an anionic surfactant (Silpit P-25, manufactured by Yushisha Co., Ltd.) of 0.2% was prepared in a sub tank, and after the vacuum pump was stopped, it was injected. After the aqueous solution is completely injected, in the In-Out flow direction,
The flow rate was set to 10 / min · kg and the treatment was performed at 50 ° C for 30 minutes. After treatment, rinse with water for 20 minutes and rinse with hot water at 80 ° C
For 10 minutes, neutralization was carried out at 80 ° C. for 10 minutes, and softening treatment with a spinning oil was carried out at 40 ° C. for 10 minutes. The obtained alkali-treated roving was dehydrated, dried, set in a spinning machine, and then defibrated by a draft to obtain a spun yarn of No. 30. The spun yarn obtained was knitted on a 32-gauge double-sided circular knitting machine into an interlock structure and exposed by a commonly known method.
Dyeing, application of finishing agent, and dry finishing set were performed.
実施例2 実施例1と同じチーズを通常公知の高圧チーズ染色機に
入れ、真空ポンプを用いて700mmHgまで減圧し
た。真空ポンプを止めた後、高圧水蒸気を導き入れスチ
ームセットを行なった。サブタンクに苛性ソーダ濃度2
1%、アニオン系界面活性剤(シルピットP−25 一
方社油脂(株)製)0.2%の水溶液を調整し、真空ポ
ンプを止めた後、注入した。該水溶液が完全に注入され
た後、In−Outの流れ方向で、流量10/分・k
gに設定し、50℃で30分間処理をおこなった。処理
後、水洗を20分間、湯洗を80℃で10分間、中和を
80℃で10分間行ない、40℃で10分間紡績油剤に
よる柔軟処理を行なった。得られたアルカリ処理粗糸
は、実施例1と同様に紡績され編み立てられ、同様の方
法で、晒、染色、仕上げ剤付与、乾燥仕上げセットを行
なった。Example 2 The same cheese as in Example 1 was placed in a commonly known high-pressure cheese dyeing machine, and the pressure was reduced to 700 mmHg using a vacuum pump. After stopping the vacuum pump, high-pressure steam was introduced to perform steam setting. Caustic soda concentration 2 in the sub tank
An aqueous solution containing 1% and 0.2% of an anionic surfactant (Silpit P-25, manufactured by Yushisha Co., Ltd.) was prepared, and the vacuum pump was stopped and then injected. After the aqueous solution is completely injected, the flow rate is 10 / min · k in the In-Out flow direction.
It was set to g and treated at 50 ° C. for 30 minutes. After the treatment, washing with water was carried out for 20 minutes, washing with hot water at 80 ° C for 10 minutes, neutralization at 80 ° C for 10 minutes, and softening treatment with a spinning oil at 40 ° C for 10 minutes. The obtained alkali-treated roving was spun and knitted in the same manner as in Example 1, and subjected to bleaching, dyeing, application of a finishing agent, and dry finishing set in the same manner.
比較例1 実施例1で使用した粗糸と同じものを使用し、アルカリ
処理をしないほかは、全て同一に処理した。Comparative Example 1 The same roving as that used in Example 1 was used, and the same treatment was performed except that the alkali treatment was not performed.
比較例2 実施例1で使用した粗糸と同じものを使用し、粗糸の状
態でのアルカリ処理はせず、編地の状態で晒の後に、シ
ルケット加工を加えた他は、全て同一に処理した。Comparative Example 2 All were the same except that the same roving as that used in Example 1 was used, alkali treatment was not performed in the state of the roving, and mercerizing was added after bleaching in the state of the knitted fabric. Processed.
比較例3 実施例1で使用した粗糸と同じものを使用し、アルカリ
処理をしないほかは実施例2と全て同様に処理した。Comparative Example 3 The same roving as that used in Example 1 was used, and the same treatment as in Example 2 was carried out except that no alkali treatment was performed.
上記、実施例および比較例にて得られた結果を第1表に
示す。The results obtained in the above Examples and Comparative Examples are shown in Table 1.
第1表に示すように、実施例は、比較例1、3に比べれ
ば染色濃度及染色ムラについて有利であり、編地でシル
ケット加工した比較例2は、風合が硬くバルキー性につ
いて劣ることを示している。 As shown in Table 1, the examples are more advantageous in dyeing density and uneven dyeing than the comparative examples 1 and 3, and the comparative example 2 mercerized in the knitted fabric is hard in texture and poor in bulkiness. Is shown.
(発明の効果) 本発明は、粗糸の状態でシルケット処理を行うことによ
り、非常にバルキー性のある風合を持ち、染色性も良好
な素材を工業的に有利に得ることができ、その応用範囲
は著しく拡大されたものになる。(Effects of the Invention) The present invention can industrially obtain a material having a very bulky texture and good dyeability by performing mercerizing treatment in the state of roving. The range of applications will be significantly expanded.
第1図及び第2図は本発明を実施するに用いて好適なボ
ビンの説明図である。1 and 2 are explanatory views of a bobbin suitable for use in carrying out the present invention.
Claims (2)
工程を通して粗糸となし、これを0.1〜0.5g/cm3の
捲取密度で捲取ってチーズを形成した後、該チーズを密
閉容器内にセットして、760mmHg以下に減圧後、
高濃度苛性ソーダ溶液を注入して、該チーズに対し温度
40〜60℃の高濃度苛性ソーダ溶液を流動せしめる処
理を施こした後水洗い、中和することを特徴とする粗糸
のシルケット加工方法。1. A short fiber containing a cellulosic fiber is made into a roving through a spinning process, and this is wound at a winding density of 0.1 to 0.5 g / cm 3 to form cheese, and the cheese is then hermetically sealed. Set inside, and after reducing the pressure to 760 mmHg or less,
A method for mercerizing roving yarn, which comprises injecting a high-concentration caustic soda solution, subjecting the cheese to a flow of the high-concentration caustic soda solution at a temperature of 40 to 60 ° C., then washing with water and neutralizing.
工程を通して粗糸となし、これを0.1〜0.5g/m3の捲
取密度で捲取ってチーズを形成した後、該チーズを密閉
容器内にセットして、760mmHg以下に減圧し、次
いで高圧水蒸気を注入した後、温度40〜60℃の高濃
度苛性ソーダ溶液を流動せしめる処理を施こし水洗い、
中和することを特徴とする粗糸のシルケット加工方法。2. Short fibers containing cellulosic fibers are made into roving yarn through a spinning process, and this is wound at a winding density of 0.1 to 0.5 g / m 3 to form cheese, and the cheese is then hermetically sealed. Inside, and after decompressing to 760 mmHg or less, and then injecting high-pressure steam, a treatment for fluidizing a high-concentration caustic soda solution at a temperature of 40 to 60 ° C. is applied and washed with water,
A method for mercerizing roving yarn, characterized by neutralizing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10319889A JPH064931B2 (en) | 1989-04-22 | 1989-04-22 | Method for mercerizing roving yarn |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10319889A JPH064931B2 (en) | 1989-04-22 | 1989-04-22 | Method for mercerizing roving yarn |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02289168A JPH02289168A (en) | 1990-11-29 |
JPH064931B2 true JPH064931B2 (en) | 1994-01-19 |
Family
ID=14347823
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10319889A Expired - Lifetime JPH064931B2 (en) | 1989-04-22 | 1989-04-22 | Method for mercerizing roving yarn |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH064931B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102758285A (en) * | 2012-07-26 | 2012-10-31 | 广东溢达纺织有限公司 | Manufacturing method for colored spun yarn blended with mercerized fiber |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005115173A (en) * | 2003-10-09 | 2005-04-28 | Tsuchiya Tsco Co Ltd | Velour material for electrophotographic apparatus |
CN102776639B (en) * | 2012-07-26 | 2015-09-16 | 广东溢达纺织有限公司 | Fancy Yarns and method for making thereof |
CN102747571B (en) * | 2012-07-26 | 2014-05-07 | 广东溢达纺织有限公司 | Roving bobbin for fiber mercerization and method of fiber mercerization |
CN104120572A (en) * | 2014-07-03 | 2014-10-29 | 鲁泰纺织股份有限公司 | Dyeing method of rough yarn used for purified cotton |
-
1989
- 1989-04-22 JP JP10319889A patent/JPH064931B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102758285A (en) * | 2012-07-26 | 2012-10-31 | 广东溢达纺织有限公司 | Manufacturing method for colored spun yarn blended with mercerized fiber |
Also Published As
Publication number | Publication date |
---|---|
JPH02289168A (en) | 1990-11-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE69322170T2 (en) | FIBER TREATMENT | |
JPH10504858A (en) | Lyocell fiber and method for producing the same | |
JP3205962B2 (en) | Cellulose multifilament yarn and fabric comprising the same | |
JPH064931B2 (en) | Method for mercerizing roving yarn | |
KR100587474B1 (en) | Natural fabric for bed having less nappy property and enforced tensile strength | |
JPH02251674A (en) | Mercerization of roving | |
JPH064930B2 (en) | Method for mercerizing roving yarn | |
TWI250238B (en) | Process for producing a dyed and finished lyocell fabric | |
US6652598B1 (en) | Process for the treatment of weft knitted fabrics | |
JP3304934B2 (en) | Hemp yarn processing method and hemp knitted fabric using the processed hemp yarn | |
KR100954822B1 (en) | Densification method of textile fabric | |
US2586106A (en) | Finishing of textile fabrics | |
JPH08291461A (en) | Cellulosic fiber and treatment of fabric comprising the same with alkali | |
JP4312337B2 (en) | Method for modifying cellulosic fibers | |
CN110373758B (en) | Flax spun yarn spinning process based on short flax raw material | |
JP3114823B2 (en) | Modified cotton yarn and method for producing the same | |
EA006660B1 (en) | Process for fabric production | |
JPH05230742A (en) | Knit fabric containing cotton and its production | |
JPH11256471A (en) | Production of durable bulky yarn | |
JPH0696823B2 (en) | Method for producing fiber structure containing cellulosic fiber and fibrillated composite fiber | |
JPH10317276A (en) | Alkali thinning treatment of polyester fiber fabric | |
DE102023104197A1 (en) | MULTI-LAYER TOWEL WITH EXCELLENT ABSORBENCE FOR DOUBLE DYEING IN ONE BATH | |
JP2001234465A (en) | Method of shape-stabilizing processing for cellulosic fiber | |
JP2004211273A (en) | Processing method for forming japanese paper yarn into clothing | |
JPS5887363A (en) | Refining of fiber product |