JPH07109062B2 - Oligomer removing agent and oligomer removing method - Google Patents
Oligomer removing agent and oligomer removing methodInfo
- Publication number
- JPH07109062B2 JPH07109062B2 JP60188515A JP18851585A JPH07109062B2 JP H07109062 B2 JPH07109062 B2 JP H07109062B2 JP 60188515 A JP60188515 A JP 60188515A JP 18851585 A JP18851585 A JP 18851585A JP H07109062 B2 JPH07109062 B2 JP H07109062B2
- Authority
- JP
- Japan
- Prior art keywords
- oligomer
- dyeing
- sulfonic acid
- polyester
- agent
- 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 - Fee Related
Links
Landscapes
- Chemical Or Physical Treatment Of Fibers (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Description
【発明の詳細な説明】 「産業上の利用分野」 本発明はポリエステル繊維から発生するオリゴマーの除
去剤及びオリゴマー除去法に関する。The present invention relates to a removing agent for oligomers generated from polyester fibers and a method for removing oligomers.
「従来の技術」 高分子を構成する単量体が2〜5個重合したものは通常
オリゴマーといわれる。このものは該高分子の成形物
(例えば繊維等)自体にその成形時から付着していたり
成形後の製品化の為の処理工程でその高分子の分解等に
より生成するものである。そしてそのオリゴマーは該高
分子成形物を乾燥状態又は湿潤状態で処理するさいに離
脱して処理機器に付着したり、高分子成形物そのものに
再度樹脂状に付着して種々の障害をもたらす。"Prior Art" A polymer obtained by polymerizing 2 to 5 monomers constituting a polymer is usually called an oligomer. This is attached to the polymer molded product (for example, fiber) itself from the time of molding, or is generated by decomposition of the polymer in a treatment step for commercialization after molding. When the polymer molded product is treated in a dry state or a wet state, the oligomer is detached and attached to the processing equipment, or reattached to the polymer molded product itself like a resin to cause various obstacles.
ポリエステルの成形物であるポリエステル繊維はその染
色時において酸性浴で染色されることが多いのでポリエ
ステル繊維中のエステル基の加水分解に基づくオリゴマ
ーの発生が多く、これらのオリゴマーは染色操作あるい
は染色結果に種々悪い影響を与える。例えばポリエステ
ル繊維の場合これをその染色法の中で最も多用される高
温染色法(例えば染浴pH4〜5、染色温度125〜135℃、
染色時間30〜60分というような条件)で分散染料を用い
て染色を行った場合ポリエステル繊維に対して凡そ0.5
%(重量比)のオリゴマー(主として三量体)が発生す
るといわれている。更にオリゴマーの発生率は分散染料
の濃度、染色時の分散均染剤の有無、染色用水の硬度等
にも影響されることが経験的に知られており、発生した
オリゴマーが繊維や染色機に付着すると不均一な染色を
起したり染色物の風合を損うなどのトラブルを招きやす
い。又オリゴマーは染色を数多く繰り返えした場合に染
色機の内部に蓄積(特に染色機の熱交換器部分への蓄積
が大きい)する性質を有しておりその除去は非常に困難
である。ポリエステル繊維の染色において多用される多
環系エステル型非イオン界面活性剤を主体とした均染剤
が発生したオリゴマーの繊維、染色機への付着をより大
きくするというような傾向もみられる。Since polyester fibers, which are molded polyester, are often dyed in an acid bath during dyeing, oligomers are often generated due to hydrolysis of ester groups in the polyester fibers. It has various bad effects. For example, in the case of polyester fiber, this is the most frequently used high temperature dyeing method (for example, dyeing bath pH 4 to 5, dyeing temperature 125 to 135 ° C,
When dyeing with a disperse dye under conditions such as a dyeing time of 30 to 60 minutes)
% (Weight ratio) of oligomers (mainly trimers) are said to occur. Furthermore, it is empirically known that the generation rate of oligomers is affected by the concentration of disperse dyes, the presence or absence of a disperse dyeing agent at the time of dyeing, and the hardness of dyeing water. If adhered, problems such as uneven dyeing or damage to the texture of the dyed product are likely to occur. Further, the oligomer has a property of accumulating inside the dyeing machine (especially large accumulation in the heat exchanger part of the dyeing machine) when dyeing is repeated many times, and its removal is very difficult. There is also a tendency to increase the adhesion of oligomers generated from a leveling agent mainly composed of a polycyclic ester type nonionic surfactant, which is frequently used in dyeing polyester fibers, to fibers and dyeing machines.
繊維や染色機に付着したオリゴマーはポリエステル繊維
染色物の後処理剤であるアルカリ剤と還元剤からなる還
元洗滌液等では除去出来ず、1,2−ジクロルエタン等の
特殊な溶剤によつて溶解、除去するより方法がない。こ
の溶剤は高価であり、更に人体に対して有害であること
からこの方法は工業的方法としては採用しがたいもので
ある。又付着したオリゴマーの前記以外の除去法として
は例えば水酸化ナトリウムのようなアルカリの存在下で
第4級アンモニウム塩を触媒としてオリゴマーの加水分
解を促進する方法があるがこの方法は付着したオリゴマ
ーをその表面より徐々に加水分解して可溶化するという
ものでありオリゴマーが厚く付着してしまつたような場
合には充分な効果が得られない。なおこの方法において
は触媒として使用する第4級アンモニウム塩がカチオン
性物質である為に染色機内部に残留した場合以後のアニ
オン性物質を使用しての染色に悪い影響を及ぼすおそれ
がありオリゴマーを除去する為のすぐれた方法とは言い
がたい。The oligomer attached to the fiber or the dyeing machine cannot be removed with a reducing washing solution composed of an alkaline agent and a reducing agent, which is a post-treatment agent for dyeing polyester fiber, and dissolved by a special solvent such as 1,2-dichloroethane. There is no better way than removing it. Since this solvent is expensive and harmful to the human body, this method is difficult to adopt as an industrial method. As a method of removing the attached oligomer other than the above, there is a method of promoting the hydrolysis of the oligomer using a quaternary ammonium salt as a catalyst in the presence of an alkali such as sodium hydroxide. It is that it is gradually hydrolyzed and solubilized from the surface, and when the oligomer is attached thickly, a sufficient effect cannot be obtained. In this method, since the quaternary ammonium salt used as a catalyst is a cationic substance and remains in the dyeing machine, it may adversely affect the subsequent dyeing using an anionic substance. It's hard to say that it's a good way to remove it.
「発明が解決しようとする問題点」 ポリエステル繊維の染色において不均一染色、染色物の
風合を損う等の原因となつたり、染色機器からの除去の
困難なオリゴマーの繊維あるいは染色機器への付着を防
止し又はポリエステル繊維、染色機器等に付着したオリ
ゴマーを容易に除去する方法の開発が望まれている。“Problems to be solved by the invention” In dyeing polyester fibers, it may cause uneven dyeing, impair the texture of the dyed product, etc. It has been desired to develop a method of preventing the adhesion or easily removing the oligomer attached to the polyester fiber, dyeing equipment and the like.
「問題点を解決するための手段」 本発明者らは前記したような目的を達成すべく鋭意研究
を重ねた結果本発明に至ったものである。即ち本発明は
リグニン分子中のメトキシ基の数1に対してスルホン酸
基の数が0.15〜0.4であるスルホン化リグニンのアルカ
リ金属塩及び/又はクレゾールスルホン酸のホルマリン
縮合物のアルカリ金属塩からなるポリエステル繊維かの
オリゴマー除去剤及び該金属塩を含有する浴中で、染色
の終了したポリエステル繊維を処理することを特徴とす
るポリエステル繊維からのオリゴマー除去方法を提供す
る。“Means for Solving Problems” The present inventors have achieved the present invention as a result of intensive studies to achieve the above-described object. That is, the present invention comprises an alkali metal salt of sulfonated lignin and / or a formalin condensate of cresol sulfonic acid having 0.15 to 0.4 of sulfonic acid groups per 1 of methoxy groups in the lignin molecule. Provided is a method for removing oligomers from polyester fibers, which comprises treating the dyed polyester fibers in a bath containing an oligomer removing agent for the polyester fibers and the metal salt.
本発明でいうポリエステル繊維とは例えばポリエチレン
テレフレート、ポリブチレンテレフタレート、ポリエチ
レンテレフタレートとポリエチレンイソフタレートとの
共重合物等からなる繊維であり、そのアルカリ減量加工
品、酸改質されたものあるいはこれらのポリエステル繊
維と他種繊維との混紡繊維であつてもよい。The polyester fiber referred to in the present invention is, for example, a fiber made of polyethylene terephthalate, polybutylene terephthalate, a copolymer of polyethylene terephthalate and polyethylene isophthalate, or the like, an alkali weight reduction processed product thereof, an acid modified product or a product thereof. It may be a mixed fiber of polyester fiber and other kind of fiber.
本発明で用いられるリグニン分子中のメトキシ基の数1
に対してスルホン酸基の数が0.15〜0.4であるスルホン
化リグニンは低スルホン化リグニンとよばれそのアルカ
リ金属塩は通常亜硫酸パルプ溶出液にアルカリ性、高温
加圧下の条件でスルホン化剤を反応させて製造される。
この際スルホン化の条件(反応温度、反応時間、スルホ
ン化剤の量)を調整することによつて前記したようなス
ルホン化度の低いスルホン化リグニンのアルカリ金属塩
を得る。Number of methoxy groups in the lignin molecule used in the present invention 1
On the other hand, sulfonated lignin having a number of sulfonic acid groups of 0.15 to 0.4 is called low sulfonated lignin, and its alkali metal salt is usually reacted with sulfonating agent under the conditions of alkaline and high temperature pressurization with sulfite pulp eluate. Manufactured.
At this time, the alkali metal salt of sulfonated lignin having a low degree of sulfonation as described above is obtained by adjusting the sulfonation conditions (reaction temperature, reaction time, amount of sulfonating agent).
一方クレゾールスルホン酸のホルマリン縮合物は通常ク
レゾールをスルホン化し芒硝の存在下ホルムアルデヒド
水溶液を反応させて製造される。On the other hand, a formalin condensate of cresol sulfonic acid is usually produced by sulfonating cresol and reacting it with an aqueous formaldehyde solution in the presence of Glauber's salt.
これらにおいてアルカリ金属塩としてはナトリウム塩、
カリウム塩又はリチウム塩等が挙げられ通常はナトリウ
ム塩が用いられる。In these, the alkali metal salt is sodium salt,
Examples thereof include potassium salt and lithium salt, and sodium salt is usually used.
次に前記の低スルホン化リグニンのアルカリ金属塩及び
/又はクレゾールスルホン酸のホルマリン縮合物のアル
カリ金属塩(以後これらをオリゴマー除去剤という)を
用いたオリゴマー除去法について説明する。ポリエステ
ル繊維又は染色機器に付着したオリゴマーを除去するた
めにはオリゴマー除去剤を0.1〜20g/、好ましくは0.5
〜5.0g/含有する処理浴を調製しこの中でそのポリエ
ステル繊維を6.0〜140℃、好ましくは90℃〜135℃で10
〜60分処理するか染色機器の場合は上記のようにして調
製された処理浴を加えて上記と同じ条件で処理すればよ
い。処理が終ったポリエステル繊維、染色機器は単に水
洗するのみでよく特別な操作を必要としない。Next, an oligomer removal method using the alkali metal salt of low sulfonated lignin and / or the alkali metal salt of formalin condensate of cresol sulfonic acid (hereinafter referred to as oligomer remover) will be described. To remove the oligomer attached to the polyester fiber or dyeing equipment, 0.1 to 20 g of an oligomer removing agent, preferably 0.5
~ 5.0 g / containing a treatment bath in which the polyester fiber at 6.0 ~ 140 ℃, preferably 90 ~ 135 ℃ 10
For 60 minutes or in the case of dyeing equipment, the treatment bath prepared as described above may be added and treated under the same conditions as above. The treated polyester fiber and dyeing equipment need only be washed with water and do not require any special operation.
処理浴にカルシウムイオン、マグネシウムイオンの存在
する場合には本発明の方法の効果が損われるおそれがあ
るのでエチレンジアミン四酢酸ソーダ、ニトリロ三酢酸
ソーダ、ポリアクリル酸ソーダ等の金属封鎖剤を併用す
るのが好ましい。When calcium ions and magnesium ions are present in the treatment bath, the effect of the method of the present invention may be impaired, so a sequestering agent such as sodium ethylenediaminetetraacetate, sodium nitrilotriacetate, or sodium polyacrylate should be used in combination. Is preferred.
実施例 実施例によつて本発明を更に具体的に説明する。なお実
施例中スルホン化リグニンにおいて「スルホン化度」と
あるはリグニン中のメトキシ基の数を1とした場合のス
ルホン酸基の平均個数である。EXAMPLES The present invention will be described more specifically by way of examples. In the examples, the "sulfonation degree" of sulfonated lignin means the average number of sulfonic acid groups when the number of methoxy groups in lignin is 1.
実施例1 オリゴマー付着染布の作製 ポリエステル加工糸織物をステンレス製ホルダーに巻き
込み浴比1:10、pH=5(酢酸及び酢酸ナトリウムで調
整)のKayalon Polyester Black BX−SF paste 150(日
本化薬株式会社製分散染料)15% o.w.f.を含む染浴で1
35℃で30分染色を行い次いで還元洗浄し0.41%(重量
比)オリゴマーが付着したポリエステル加工糸織物の染
色物を得た。Example 1 Production of oligomer-attached dyed fabric Kayalon Polyester Black BX-SF paste 150 (Nippon Kayaku Co., Ltd.) with polyester processed yarn woven fabric wound in a stainless steel holder and having a bath ratio of 1:10 and pH = 5 (adjusted with acetic acid and sodium acetate) Company disperse dye) 1 in a dye bath containing 15% owf
Dyeing was carried out at 35 ° C. for 30 minutes and reduction washing was carried out to obtain a dyed polyester woven fabric with 0.41% (weight ratio) oligomer attached.
オリゴマー除去試験(除去法例) 上記によつて得られた0.41%のオリゴマーが付着したポ
リエステル加工糸織物を下記オリゴマー除去剤及び薬剤
を各々1g/を含む処理浴中で100℃で20分間処理し(浴
比1:30)、オリゴマーの除去度を測定した。 Oligomer removal test (Example of removal method) The polyester processed yarn woven fabric having 0.41% of the oligomer attached as described above is treated at 100 ° C. for 20 minutes in a treatment bath containing the following oligomer removing agent and chemicals (1 g / each) ( The bath ratio was 1:30) and the degree of oligomer removal was measured.
実施例2 実施例1でえられたオリゴマーの付着したポリエステル
加工糸織物をドイツ硬度20゜dHの水、スルホン化度0.18
のスルホン化リグニンのナトリウム塩1g/及びカヤキ
レータC−10001g/からなる処理浴で100℃で20分間処
理した。(処理浴1:30) オリゴマーの完全に除去されたポリエステル加工糸織物
がえられた。 Example 2 The polyester textured yarn woven fabric to which the oligomer obtained in Example 1 is attached is water having a German hardness of 20 ° dH and a sulfonation degree of 0.18.
Was treated with a treatment bath consisting of 1 g of the sodium salt of sulfonated lignin and 1100 g of Kayachelator C-10001 at 100 ° C for 20 minutes. (Treatment bath 1:30) A polyester textured yarn fabric was obtained in which oligomers were completely removed.
「発明の効果」 ポリエステル繊維の染色において不均一染色をおこした
りあるいは染色物の風合を損つたり染色機器の清掃を困
難なわしめるオリゴマーの付着を防止し又ポリエステル
繊維、染色機器等に付着したオリゴマーを容易に除去す
ることが可能になつた。"Effects of the Invention" Prevents adhesion of oligomers that cause uneven dyeing in dyeing of polyester fibers, impair the texture of dyed products, or make it difficult to clean dyeing equipment, and also adhere to polyester fibers, dyeing equipment, etc. It became possible to easily remove the oligomer.
Claims (2)
てスルホン酸基の数が0.15〜0.4であるスルホン化リグ
ニンのアルカリ金属塩及び/又はクレゾールスルホン酸
のホルマリン縮合物のアルカリ金属塩からなるポリエス
テル繊維からのオリゴマー除去剤。1. From an alkali metal salt of a sulfonated lignin and / or a formalin condensate of cresol sulfonic acid in which the number of sulfonic acid groups is 0.15 to 0.4 with respect to the number of methoxy groups in the lignin molecule is 1. Oligomer removal agent from polyester fiber.
てスルホン酸基の数が0.15〜0.4であるスルホン化リグ
ニンのアルカリ金属塩及び/又はクレゾールスルホン酸
のホルマリン縮合物のアルカリ金属塩を含有する浴中
で、染色の終了したポリエステル繊維を処理することを
特徴とするポリエステル繊維からのオリゴマー除去法。2. An alkali metal salt of sulfonated lignin and / or an alkali metal salt of a formalin condensate of cresol sulfonic acid, in which the number of sulfonic acid groups is 0.15 to 0.4 per the number of methoxy groups in the lignin molecule. A method for removing oligomers from polyester fibers, which comprises treating the dyed polyester fibers in a bath containing the same.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60188515A JPH07109062B2 (en) | 1985-08-29 | 1985-08-29 | Oligomer removing agent and oligomer removing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60188515A JPH07109062B2 (en) | 1985-08-29 | 1985-08-29 | Oligomer removing agent and oligomer removing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6253478A JPS6253478A (en) | 1987-03-09 |
JPH07109062B2 true JPH07109062B2 (en) | 1995-11-22 |
Family
ID=16225067
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60188515A Expired - Fee Related JPH07109062B2 (en) | 1985-08-29 | 1985-08-29 | Oligomer removing agent and oligomer removing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07109062B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104562776A (en) * | 2015-01-12 | 2015-04-29 | 张家港市德宝化工有限公司 | Method for dyeing polyester fiber type material by using oligomer removing agent |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5270181A (en) * | 1975-12-08 | 1977-06-10 | Sanyo Kokusaku Pulp Co | Method of manufacturing dispersing medium with improved contamination characteristics |
DE2934980A1 (en) * | 1979-08-30 | 1981-03-19 | Bayer Ag, 5090 Leverkusen | PHENOL FORMALDEHYDE CONDENSATES, THEIR PRODUCTION AND USE AS DISPERSING AGENTS, LIQUIDS AND TANNING AGENTS |
JPS5668173A (en) * | 1979-11-05 | 1981-06-08 | Sumitomo Chemical Co | High concentrated disperse dyestuff composition |
-
1985
- 1985-08-29 JP JP60188515A patent/JPH07109062B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS6253478A (en) | 1987-03-09 |
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