JP2003129368A - Method for dyeing flame-retardant polyester fabric having rich design property - Google Patents
Method for dyeing flame-retardant polyester fabric having rich design propertyInfo
- Publication number
- JP2003129368A JP2003129368A JP2001320736A JP2001320736A JP2003129368A JP 2003129368 A JP2003129368 A JP 2003129368A JP 2001320736 A JP2001320736 A JP 2001320736A JP 2001320736 A JP2001320736 A JP 2001320736A JP 2003129368 A JP2003129368 A JP 2003129368A
- Authority
- JP
- Japan
- Prior art keywords
- flame
- temperature
- yarn
- dyeing
- shrinkage
- 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
Links
Landscapes
- Artificial Filaments (AREA)
- Treatment Of Fiber Materials (AREA)
- Fireproofing Substances (AREA)
- Coloring (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は燐原子を含有するポ
リエステルを用いた難燃性布帛の染色加工方法に関する
ものであり、更に詳しくには該難燃性布帛にソフトタッ
チ、膨らみ感とチンチラ効果のある生地表面感を持たせ
ることを目的とする、カーテン、テーブルクロス等、生
活資材用途に好適な難燃性ポリエステル布帛の染色加工
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 dyeing and processing a flame-retardant fabric using a phosphorus atom-containing polyester, and more particularly, to the flame-retardant fabric having a soft touch, a swelling feeling and a chinchilla effect. The present invention relates to a method for dyeing and processing a flame-retardant polyester cloth suitable for daily use such as curtains, table cloths, etc., for the purpose of giving a certain textured cloth surface feeling.
【0002】[0002]
【従来の技術】従来からカーテン、椅子張り、ベットカ
バー他インテリア用途に於いては難燃性を要求されてお
り、特に公共団体の施設備品用途として難燃商品が多数
上市、展開されている。これらの大多数のものは後加工
による吸尽法、パディング法によるものであり、例えば
トリス(1−アジリジニル)ホスフィンオキシド、トリ
ス(2,3−ジブロムプロピル)ホスフェート、ビス
(2,3−ジブロムプロピル)ホスフェート化合物等が
その代表的なものとして例示される。2. Description of the Related Art Conventionally, curtains, chair upholstery, bed covers, and other interior applications have been required to have flame retardancy, and in particular, many flame retardant products have been put on the market and deployed for use as equipment for public facilities. Most of these are by exhaustion method and padding method by post-processing, and include, for example, tris (1-aziridinyl) phosphine oxide, tris (2,3-dibromopropyl) phosphate, bis (2,3-diamine). A typical example thereof is a bromopropyl) phosphate compound.
【0003】これらは毒性が強い有害物質として規制さ
れつつある物質で、特にCl、Br等ハロゲン化物は将
来使用禁止になる可能性が極めて高く、安全性が高い新
規難燃物質を早急に選択せねばならないという問題を抱
えている。更に後加工法による難燃処理は比較的安価で
あるが、耐久性に優れるものではなく繰り返し洗濯等で
難燃性能が極端に低下してしまうという問題を抱えてい
る。更に加工工程中の廃液内に毒性の強い有害物質が混
入、漏洩してしまう可能性が極めて高く、環境問題に発
展する可能性が否めない。These are substances which are being regulated as highly toxic and harmful substances, and particularly halides such as Cl and Br are very likely to be prohibited from being used in the future, and new flame-retardant substances with high safety should be selected immediately. I have a problem of having to do it. Further, although the flame-retardant treatment by the post-processing method is relatively inexpensive, it is not excellent in durability and has a problem that the flame-retardant performance is extremely deteriorated by repeated washing and the like. Further, there is a very high possibility that a highly toxic harmful substance may be mixed and leaked into the waste liquid during the processing step, and the possibility of developing an environmental problem cannot be denied.
【0004】[0004]
【発明が解決しようとする課題】本発明は上記従来の方
法を改善し、素材となるポリエステルに難燃物質を共重
合せしめた重合体からなる糸条を布帛化することで難燃
耐久性を向上させると共に後加工と比較し難燃性能も極
端に改善させつつ、従来の難燃ポリエステルでは実現し
得なかったチンチラ調外観品位、ソフト感を実現させる
ことを課題とするものである。DISCLOSURE OF THE INVENTION The present invention improves the above-mentioned conventional method, and improves the flame-retardant durability by forming a yarn made of a polymer in which a flame-retardant substance is copolymerized with a raw material polyester into a fabric. It is an object to realize a chinchilla-like appearance quality and soft feeling which could not be realized by the conventional flame-retardant polyester, while improving the flame-retardant performance as compared with post-processing.
【0005】[0005]
【課題を解決するための手段】本発明は以下の構成より
なる。燐原子を500〜50000ppm含有し、下記
に示された燐化合物を添加して得られた共重合ポリエス
テルを溶融紡糸してなるポリエステルマルチフィラメン
ト糸条を少なくとも一部に使用してなる布帛構造物を染
色加工するに際して湿熱リラックス処理を、該マルチフ
ィラメント糸条の熱収縮応力曲線から得られる糸条収縮
開始温度より20℃低い温度から糸条収縮開始温度より
30℃高い温度まで+5℃/分以上+10℃/分以下で
急昇温させて処理することを特徴とする意匠性に富む難
燃性ポリエステル布帛の染色加工方法。The present invention has the following constitution. A fabric structure containing at least a part of a polyester multifilament yarn containing 500 to 50,000 ppm of phosphorus atom and melt-spun of a copolyester obtained by adding the phosphorus compound shown below. In the dyeing process, a wet heat relaxation treatment is performed from a temperature 20 ° C lower than the yarn shrinkage start temperature obtained from the heat shrinkage stress curve of the multifilament yarn to a temperature 30 ° C higher than the yarn shrinkage start temperature + 5 ° C / min or more +10. A method for dyeing and processing a flame-retardant polyester cloth having a high design property, which is characterized in that the temperature is rapidly raised at a rate of not more than ° C / min for processing.
【0006】[0006]
【化2】
(式中、R1は1価のエステル形成性官能基であり、R
2、R3は同じか或いは異なる基であり、それぞれハロゲ
ン原子、炭素数1〜10個の炭化水素基、R1より選ば
れ、Aは2価又は3価の有機残基を表す。また、n1は
1又は2であり、n2、n3はそれぞれ0〜4の整数を表
す。)[Chemical 2] (In the formula, R 1 is a monovalent ester-forming functional group,
2, R3 are the same or different groups, each selected from a halogen atom, a hydrocarbon group having 1 to 10 carbon atoms, and R1, and A represents a divalent or trivalent organic residue. Further, n1 is 1 or 2, and n2 and n3 each represent an integer of 0-4. )
【0007】更には仕上巾に対する織上巾の比及び/又
は仕上長さに対する織上長さの比が1.00:1.20〜
1.00:1.45を満足する条件で処理を施すことを特
徴とする上記難燃性ポリエステル布帛の染色加工方法。Further, the ratio of the woven width to the finished width and / or the ratio of the woven length to the finished length is from 1.00: 1.20.
The method for dyeing and processing a flame-retardant polyester fabric, which is characterized in that the treatment is carried out under a condition satisfying 1.00: 1.45.
【0008】並びにHLB値が8〜15であるノニオン
系界面活性剤を含む水溶液中で湿熱リラックス処理を施
すことを特徴とする上記難燃性ポリエステル布帛の染色
加工方法。A method for dyeing and processing a flame-retardant polyester cloth, which is characterized in that a wet heat relaxation treatment is carried out in an aqueous solution containing a nonionic surfactant having an HLB value of 8 to 15.
【0009】[0009]
【発明の実施の形態】本発明のポリエステル難燃性ポリ
エステル布帛は、燐原子を500〜50000ppm含
有した燐化合物を添加して得られた共重合ポリエステル
マルチフィラメントを少なくとも一部に使用してなる布
帛であることが難燃性を付与するためには必要である。
燐原子含有量が500ppm未満の範囲では難燃性能が
劣るだけでなく、溶融紡糸及び延伸に於いて分子鎖が配
向し易くなるため繊維の弾性率が向上し布帛構造物のソ
フト感が得難くなり好ましくない。また燐原子含有量が
50000ppmを超過する範囲となれば燐原子を含有
する燐化合物の共重合量を増加させることが必要であ
り、得られるポリマーの融点が極端に低下し曵糸性が悪
化するばかりか、繊維の強度も低下してしまい実用に供
するものにはならない。燐原子含有量として好ましく
は、1500〜30000ppmであり、更に好ましく
は3000〜10000ppmである。BEST MODE FOR CARRYING OUT THE INVENTION The polyester flame-retardant polyester cloth of the present invention is a cloth using at least a part of a copolymerized polyester multifilament obtained by adding a phosphorus compound containing 500 to 50,000 ppm of phosphorus atoms. It is necessary to impart flame retardancy.
When the phosphorus atom content is less than 500 ppm, not only the flame retardancy is inferior, but also the molecular chain is easily oriented during melt spinning and drawing, so that the elastic modulus of the fiber is improved and it is difficult to obtain a soft feeling of the fabric structure. It is not preferable. Further, if the phosphorus atom content exceeds the range of 50,000 ppm, it is necessary to increase the copolymerization amount of the phosphorus compound containing the phosphorus atom, and the melting point of the obtained polymer is extremely lowered, resulting in poor spinnability. Not only that, the strength of the fiber is also reduced, and it cannot be put to practical use. The phosphorus atom content is preferably 1500 to 30000 ppm, more preferably 3000 to 10000 ppm.
【0010】本発明におけるポリエステルはテレフタル
酸又はナフタレンジカルボン酸を主たる酸成分とし少な
くとも1種のグリコール、好ましくはエチレングリコー
ル、トリメチレングリコール、テトラメチレングリコー
ルから選択された少なくとも1種のアルキレングリコー
ルを主たるグリコール成分としてなるポリエステルを指
すものであり、難燃性能を付与するために燐化合物を共
重合させて得られるものである。The polyester in the present invention contains terephthalic acid or naphthalenedicarboxylic acid as a main acid component and at least one glycol, preferably at least one alkylene glycol selected from ethylene glycol, trimethylene glycol and tetramethylene glycol. This refers to polyester as a component, and is obtained by copolymerizing a phosphorus compound in order to impart flame retardancy.
【0011】本発明の難燃性ポリエステル布帛で使用さ
れる燐化合物としてはポリエステルの構成成分であるジ
カルボン酸やジオールと反応してポリエステルに共重合
出来る化合物であることが必要である。特にポリエステ
ルの側鎖及び/又は末端に燐原子を導入出来る化合物で
あることが望ましく、単独の化合物のみでなく複数種の
化合物を同時に使用しても構わない。但し、ソフトな風
合いを得るためには分子鎖の配向を或程度抑制し、繊維
の弾性率をやや低下させることが好適であるため側鎖に
燐原子を導入した燐化合物を用いることが好ましい。ま
た、必要に応じて酸化防止剤や制電剤、顔料、艶消剤、
染色性改良剤等の添加物を必要に応じて含有させても構
わない。更に後加工工程、特に染色加工工程に於いて消
臭、抗菌、吸湿、芳香、制電、吸着その他の機能付与の
為に物理的及び/又は化学的処理を施しても構わない。
勿論、パディング法や吸尽法、サーモゾル法等による後
加工難燃処理の併用も必要に応じて実施することが出来
るが、環境汚染防止の為、特に加工廃液処理には注意を
要する。The phosphorus compound used in the flame-retardant polyester cloth of the present invention is required to be a compound capable of reacting with the dicarboxylic acid or diol which is a constituent component of the polyester and copolymerizing with the polyester. In particular, a compound capable of introducing a phosphorus atom into a side chain and / or a terminal of polyester is desirable, and not only a single compound but also plural kinds of compounds may be used at the same time. However, in order to obtain a soft texture, it is preferable to suppress the orientation of the molecular chains to some extent and to slightly reduce the elastic modulus of the fiber, and therefore it is preferable to use a phosphorus compound having a phosphorus atom introduced into the side chain. In addition, if necessary, antioxidants, antistatic agents, pigments, matting agents,
If necessary, additives such as dyeability improving agent may be contained. Further, physical and / or chemical treatment may be carried out in the post-processing step, particularly in the dyeing processing step, to impart functions such as deodorant, antibacterial, moisture absorption, fragrance, antistatic and adsorption.
Needless to say, post-processing flame retardant treatment such as padding method, exhaust method, thermosol method and the like can be carried out as required, but special attention is required for processing waste liquid treatment in order to prevent environmental pollution.
【0012】本発明に使用される燐化合物としては下記
[化3]で示される化合物であり、該燐化合物自体が共
重合ポリエステルの一部として組成されるものであるこ
とが、消費耐久性や環境汚染防止等の観点から好まし
い。The phosphorus compound used in the present invention is a compound represented by the following [Chemical Formula 3], and the phosphorus compound itself being a part of the copolyester, the consumption durability and the It is preferable from the viewpoint of preventing environmental pollution.
【0013】[0013]
【化3】
(式中、R1は1価のエステル形成性官能基であり、R
2、R3は同じか或いは異なる基であり、それぞれハロゲ
ン原子、炭素数1〜10個の炭化水素基、R1より選ば
れ、Aは2価又は3価の有機残基を表す。また、n1は
1又は2であり、n2、n3はそれぞれ0〜4の整数を表
す。)[Chemical 3] (In the formula, R 1 is a monovalent ester-forming functional group,
2, R3 are the same or different groups, each selected from a halogen atom, a hydrocarbon group having 1 to 10 carbon atoms, and R1, and A represents a divalent or trivalent organic residue. Further, n1 is 1 or 2, and n2 and n3 each represent an integer of 0-4. )
【0014】[化3]の具体例としては下記を例示する
ことが出来る。勿論、下記に限定されるものではなく、
一般式[化3]を満足する化合物は全て包括される。The following can be mentioned as specific examples of [Chemical Formula 3]. Of course, it is not limited to the following,
All compounds satisfying the general formula [Chemical Formula 3] are included.
【0015】[0015]
【化4】 [Chemical 4]
【0016】[0016]
【化5】 [Chemical 5]
【0017】[0017]
【化6】 [Chemical 6]
【0018】[0018]
【化7】 [Chemical 7]
【0019】[0019]
【化8】 [Chemical 8]
【0020】得られた共重合ポリエステルは特公昭55
−41610号公報等に記載の公知の方法で重合させる
ことが可能であり、該共重合ポリエステルを常法の溶融
紡糸法によって糸条とすることが出来る。特に限定を加
えるものではないが、紡糸引取速度は1500〜400
0m/分の範囲で未延伸糸として巻き取った後、或いは
巻き取らずに連続して延伸処理し、更には延伸条件、熱
処理条件を種々変更することによって同一ポリマーから
高収縮糸と低収縮糸を得る。これらを紡糸時或いは延伸
時に混繊することによって得られた糸条を布帛の経糸及
び/又は緯糸の一部に使用すると布帛に適度な膨らみ感
を与え、適度なチンチラ効果を付与することが可能とな
り、使用するに好ましい。また、単糸の断面形状につい
ても限定を加えるものではなく中実断面、中空断面の何
れであってもよく、丸断面の他、三角断面、多葉断面、
偏平断面等々の異型断面を目的・用途に応じて適宜採用
することが出来る。The copolyester obtained is Japanese Patent Publication Sho 55
It is possible to polymerize by a known method described in JP-A-41610, etc., and the copolyester can be formed into a yarn by a conventional melt spinning method. Although not particularly limited, the spinning take-up speed is 1500 to 400
After being wound as undrawn yarn in the range of 0 m / min, or continuously drawn without being wound, the high shrinkage yarn and the low shrinkage yarn can be made from the same polymer by variously changing the stretching conditions and heat treatment conditions. To get When a yarn obtained by mixing these during spinning or drawing is used as part of the warp and / or weft of the fabric, it gives the fabric an appropriate swelling feeling and can impart an appropriate chinchilla effect. Therefore, it is preferable to use. Further, the cross-sectional shape of the single yarn is not limited, and may be a solid cross section or a hollow cross section.
An irregular cross section such as a flat cross section can be appropriately adopted according to the purpose and application.
【0021】異収縮混繊糸条を得る為には上記のように
延伸条件、熱処理条件を種々変更して収縮率差を付与す
ることが好適であり、該熱処理はプレートヒーター、ホ
ットローラー等の接触加熱、チューブヒーター等の非接
触加熱の何れでもよい。また乾式、湿式の何れによって
も構わない。特に限定は加えるものではないが生産性、
品質の観点から接触式のローラー加熱が好ましく利用さ
れる。In order to obtain a different shrinkage mixed filament yarn, it is preferable to change the stretching condition and the heat treatment condition as described above to give a difference in shrinkage ratio. The heat treatment is performed by a plate heater, a hot roller or the like. Either contact heating or non-contact heating such as a tube heater may be used. Further, either a dry method or a wet method may be used. Productivity, although not particularly limited
From the viewpoint of quality, contact roller heating is preferably used.
【0022】布帛構造を得る際に使用する織機について
も特に限定されず、エアージェットルーム、レピアルー
ム、プロジェクタイルルーム、ウォータージェットルー
ムの何れも用いることが可能であるが、布帛構造物の外
観品位、特にチンチラ感を付与するためには染色加工工
程以前の熱付与を極力避ける必要がある。ウォータージ
ェットルーム使用の場合には生機乾燥温度を55℃未満
の乾燥温度で処理することが好ましい。The loom used for obtaining the fabric structure is not particularly limited, and any of an air jet loom, a rapier room, a projectile room and a water jet loom can be used. Especially, in order to impart a chinchilla feeling, it is necessary to avoid heat application before the dyeing process as much as possible. In the case of using a water jet room, it is preferable to perform the drying at a greige drying temperature of less than 55 ° C.
【0023】布帛構造物の組織についても特に限定を加
えるものではないが、特にチンチラ効果や布帛の膨らみ
感を向上させる目的で綾織、平二重織、二重朱子織、朱
子織、変則綾織、変則朱子織、ジャガード織等の経糸及
び/又は緯糸の浮き数が大きくなる織組織が好ましく適
用されるが、緯糸の浮き数を必要以上に多くすると耐ピ
リング性や耐スナッグ性が悪化してしまう為、緯糸浮き
数は6以下に抑えておくことが好ましいと言える。より
好ましい織組織としては朱子織を基本とする組織であり
5枚経朱子をベースとした二重朱子織、7枚経朱子織、
各種ジャガード織等が例示される。図1から図10に好
適な織組織の一完全組織の具体例を示したが、勿論これ
に限定されるものではない。The structure of the fabric structure is not particularly limited, but a twill weave, plain double weave, double satin weave, satin weave, irregular twill weave, especially for the purpose of improving the chinchilla effect and the swelling feeling of the fabric. Woven designs such as irregular satin weave and jacquard weave that increase the floating number of warp and / or weft are preferably applied, but if the floating number of weft is increased more than necessary, pilling resistance and snag resistance deteriorate. Therefore, it can be said that it is preferable to keep the weft floating number at 6 or less. A more preferable weave design is a satin weave-based design, which is a double satin weave based on 5 warp satin, a 7 warp satin weave,
Various jacquard weaves are exemplified. 1 to 10 show specific examples of one perfect weave design, but of course, the present invention is not limited to this.
【0024】本発明の難燃性ポリエステル布帛を得る場
合、高度の難燃性を保持するために布帛を構成する糸条
に付着しているオリゴマー成分、紡糸油剤成分、糊剤・
ワックス成分等の不純物を除去する必要がある。本発明
の染色加工方法に於ける湿熱リラックス処理は精練処理
を兼ねる工程であり、湿熱リラックス処理には界面活性
剤、アルカリ金属或いはアルカリ土類金属の水酸化物、
精練助剤、各種キレート剤、浴中柔軟剤等を含む水溶液
中にて処理を行う。アルカリ金属或いはアルカリ土類金
属の水酸化物としては水酸化ナトリウム、水酸化カリウ
ム、水酸化カルシウム等が例示され、精練助剤としては
ビルダーとして炭酸ナトリウム(ソーダ灰)、硫酸ナト
リウム(芒硝)、珪酸ナトリウム、アルミノ珪酸ナトリ
ウム等が例示される。キレート剤は硬水軟化の為に使用
するものでありトリポリリン酸ナトリウム、ヘキサメタ
リン酸ナトリウム、エチレンジアミンテトラ酢酸ナトリ
ウム塩(EDTA)が好適に使用される。これらは糸条
に付着している不純物の種類、量に応じて適宜、選定・
組合せて使用することができる。When obtaining the flame-retardant polyester cloth of the present invention, an oligomer component, a spinning oil agent component, a sizing agent, etc. attached to the yarns constituting the cloth in order to maintain a high degree of flame retardancy.
It is necessary to remove impurities such as wax components. The wet heat relaxing treatment in the dyeing processing method of the present invention is a step which also serves as a scouring treatment, and the wet heat relaxing treatment comprises a surfactant, a hydroxide of an alkali metal or an alkaline earth metal,
The treatment is carried out in an aqueous solution containing a scouring aid, various chelating agents, a bath softener and the like. Examples of hydroxides of alkali metals or alkaline earth metals include sodium hydroxide, potassium hydroxide, calcium hydroxide, and the like, and as scouring aids, sodium carbonate (soda ash), sodium sulfate (mirabilite), silicic acid as builders. Examples thereof include sodium and sodium aluminosilicate. The chelating agent is used for softening water, and sodium tripolyphosphate, sodium hexametaphosphate, and ethylenediaminetetraacetic acid sodium salt (EDTA) are preferably used. These are appropriately selected and selected according to the type and amount of impurities adhering to the yarn.
It can be used in combination.
【0025】界面活性剤についてはイオン性を示さない
ノニオン系のものを使用することが望ましく、洗浄力や
耐硬水性、生分解性、乳化分散性及び精練時の低起泡性
等の特徴を有する。アニオン系、カチオン系、両性イオ
ン系界面活性剤は何れもクラフト点を有し、その温度以
上にならないと界面活性を発揮しないため、精練・リラ
ックス完了後は高温状態で廃液処理せねば布帛への不純
物再付着等の問題を引き起こしてしまい好ましくない。
ノニオン系界面活性剤としてはポリオキシエチレンアル
キルエーテル、ポリオキシエチレンアルキルフェノール
エーテルが好ましく使用される。該ノニオン系界面活性
剤のHLB値としては8〜15のものを使用することが
望ましい。It is desirable to use a nonionic surfactant which does not show ionicity, and has characteristics such as detergency, hard water resistance, biodegradability, emulsion dispersibility, and low foaming property during scouring. Have. Anionic, cationic, and zwitterionic surfactants all have a crafting point and do not exhibit surface activity until the temperature is raised above that temperature. It is not preferable because it causes problems such as redeposition of impurities.
As the nonionic surfactant, polyoxyethylene alkyl ether and polyoxyethylene alkylphenol ether are preferably used. It is desirable to use one having an HLB value of 8 to 15 as the nonionic surfactant.
【0026】ここで、HLB値(Hydrophile-Lipophile
Barance)とはアメリカのAtlas Powder Co.社によっ
て最初に導出されたものであり、本発明では以下の[式
1]に基づき算出する。
[式1] HLB=7+11.7log(Mw/Mo)
(但し、Mw及びMoはそれぞれ活性剤中の親水部分と親
油部分の分子量である)更に複数種のノニオン系界面活
性剤を使用する際はHLBに加成性がある為、仮に第1
の活性剤のHLBをHAとし、第2の活性剤のHLBを
HBとした時、それぞれをa重量、b重量混合したとす
ると[式2]が成り立つ。
[式2] HLB=(a×HA+b×HB)/(a+b)
本発明は上記界面活性剤が単一種のみならず複数種のノ
ニオン系界面活性剤を併用することを当然含むものであ
る。Here, the HLB value (Hydrophile-Lipophile
Barance) is an American Atlas Powder Co. It was first derived by the company, and in the present invention,
Calculated based on 1]. [Formula 1] HLB = 7 + 11.7 log (Mw / Mo) (where Mw and Mo are the molecular weights of the hydrophilic part and lipophilic part in the activator) When using a plurality of nonionic surfactants Is the first one because HLB is additive.
[Formula 2] is established when HLB of the activator of (1) is HA and HLB of the second activator is HB, and a weight and a weight of each are mixed. [Formula 2] HLB = (a × HA + b × HB) / (a + b) The present invention naturally includes not only a single type of the above surfactants but also a combination of a plurality of nonionic surfactants.
【0027】本発明に使用するノニオン系界面活性剤の
HLB値としては8〜15、好ましくは10〜15、更
に好ましくは13〜15の範囲である。HLB値が8未
満となれば紡糸油剤やポリエステルオリゴマー、その他
不純物の除去が困難となる。また、HLB値が15を超
過する範囲となれば親油部分の分子量が極端に低いもの
になる結果、紡糸油剤、その他親油性不純物の捕捉能が
低下してしまい界面活性剤としての効力に乏しいものと
なってしまう。本発明の難燃性ポリエステル布帛は上記
の如き、紡糸油剤、ポリエステルオリゴマーその他不純
物の残存等による難燃効果の低下防止のため、HLB=
8〜15のノニオン系界面活性剤を使用して布帛からそ
れらを完全除去することが望ましい。The HLB value of the nonionic surfactant used in the present invention is in the range of 8 to 15, preferably 10 to 15, and more preferably 13 to 15. If the HLB value is less than 8, it will be difficult to remove the spinning oil, polyester oligomer and other impurities. Further, when the HLB value is in the range of more than 15, the molecular weight of the lipophilic part becomes extremely low, and as a result, the ability to trap spinning oil agents and other lipophilic impurities decreases, resulting in poor efficacy as a surfactant. It becomes a thing. The flame-retardant polyester cloth of the present invention has the HLB = HLB =
It is desirable to use 8-15 nonionic surfactants to completely remove them from the fabric.
【0028】該ポリエステルマルチフィラメント糸条を
使用し生機を得、染色加工工程にて精練・リラックス処
理を施した後、染色及び仕上げセットを施して生地を得
る。風合いに応じてアルカリ減量加工を染色前の工程に
て実施することも出来るが、この場合には精練・リラッ
クス後にヒートセッターを使用し、中間セットによる布
目矯正、生地巾調整を実施した後、液流減量等のバッチ
式減量、或いはパッドスチーム法等の連続減量を実施す
ることが好ましい上記精練・リラックス処理にては紡糸
油剤、糊剤、仮撚油剤等々の各種油剤を完全に除去せし
めることが難燃性能を保持させる上で望ましく、シリコ
ン系等の消泡剤の使用を控え、残存させぬよう廃液後は
十分な湯洗いを実施する。A raw fabric is obtained using the polyester multifilament yarn, and after scouring and relaxing in the dyeing process, dyeing and finishing set are applied to obtain a cloth. Depending on the texture, it is possible to carry out alkali weight reduction processing in the process before dyeing, but in this case, after scouring / relaxing, use a heat setter, straighten the texture with the intermediate set, adjust the fabric width, and then It is preferable to carry out batch type reduction such as flow reduction or continuous reduction such as pad steam method.In the above refining / relaxation treatment, various oil agents such as spinning oil agent, sizing agent, false twist oil agent, etc. can be completely removed. It is desirable to maintain the flame retardant performance, so refrain from using antifoaming agents such as silicone, and wash thoroughly with hot water after the waste liquid so that it does not remain.
【0029】また染色工程にても分散剤等の余分な染色
助剤は還元洗浄工程やソーピング工程で排除した上で乾
燥し仕上げセットを施すことが好ましいが、必要に応じ
て紫外線吸収剤、難燃加工剤等を吸尽法、サーモゾル
法、パディング法等によって付与することが出来る。仕
上げ樹脂についてもメラミン・ホルムアルデヒド系仕上
剤など製品の難燃性能を低下させる薬剤の使用は好まし
くないが難燃性能を阻害しない範囲でポリエステル系等
の柔軟剤、硬仕上剤、防汚加工剤等を用途に応じて併用
することが出来る。Also in the dyeing process, it is preferable to remove excess dyeing aids such as dispersants in the reduction washing process and the soaping process, and then dry and finish the set. It is possible to apply a flame-processing agent or the like by an exhaust method, a thermosol method, a padding method or the like. For finishing resins, it is not preferable to use chemicals such as melamine / formaldehyde finishing agents that reduce the flame retardant performance of the product, but softeners such as polyester, hard finishing agents, antifouling agents, etc. to the extent that flame retardant performance is not impaired. Can be used together depending on the application.
【0030】適度なチンチラ効果を得る為には精練・リ
ラックスの工程にて皺移動を従来条件よりもやや抑制し
つつ浴温を上記糸条の熱収縮開始温度−20℃から同収
縮開始温度+30℃まで+5〜+10℃/分の昇温条件
で昇温させることがチンチラ感を付与する上で効果的で
ある。昇温速度が+5℃/分未満であれば湿熱リラック
ス時の生地の押し込み皺等の防止が可能であるが外観が
プレーンなものとなってしまう。また+10℃/分を超
過する条件であれば織物の緯方向に生じる押し込み皺や
経方向に生じるロープ皺が強度に残存し、外観品位を損
ねてしまう他、緯糸の飛び出し欠点が多量に発生し、好
ましい条件ではない。In order to obtain an appropriate chinchilla effect, the bath temperature is slightly suppressed from the thermal contraction start temperature of the above-mentioned yarn from -20 ° C to the same contraction start temperature +30 while slightly suppressing wrinkle movement in the scouring / relaxing process as compared with the conventional condition. It is effective to raise the temperature to + 5 ° C./min under the temperature rising condition of +5 to + 10 ° C./min in order to impart a chinchilla feeling. If the rate of temperature rise is less than + 5 ° C / minute, it is possible to prevent the fabric from being pushed in when wrinkled by heat and moisture, but the appearance becomes plain. If the condition exceeds + 10 ° C / min, indentation creases in the weft direction of the woven fabric and rope creases in the warp direction remain strong, impairing the appearance quality, and a large number of weft protrusion defects occur. , Not a preferable condition.
【0031】湿熱リラックスを液流処理にて実施する場
合には浴比やノズル圧、衝撃板形状、衝撃板設置角度、
ノズル種類等を種々調整することが肝要である。ノズル
形状については通常の液流精練で使用されるベンチュリ
角度が大きなスパンノズルよりベンチュリ角度の小さい
フィラメントノズルを用いることが好ましい。該フィラ
メントノズルを使用するとロープ皺が発生し易くなり、
生地面としては楊柳調に仕上るが揉み効果は増大する
為、外観品位や膨らみ感を付与する上には有効である。When the wet heat relaxation is carried out by liquid flow treatment, the bath ratio, nozzle pressure, impact plate shape, impact plate installation angle,
It is important to adjust the nozzle type and other factors. Regarding the nozzle shape, it is preferable to use a filament nozzle having a smaller Venturi angle than a span nozzle having a large Venturi angle used in ordinary liquid flow refining. Rope wrinkles tend to occur when the filament nozzle is used,
Although the material has a Yangyanagi-like finish, the rubbing effect increases, so it is effective in imparting appearance quality and bulging.
【0032】湿熱リラックスに使用する機種としては上
記液流リラクサーの他に高圧ロータリーワッシャー等、
公知の機種を用いて実施することが出来る。また必要に
応じて各種湿熱前処理、乾熱前処理を併用しても構わな
い。高圧ロータリーワッシャー使用の場合には円筒状綿
袋に織物生機を細かく押し込んで精練・リラックス処理
して皺をつけるクラッシュ皺加工がチンチラ感及び外観
の意匠性を向上させる為に効果的である。該クラッシュ
皺加工を実施する場合には上記ワッシャーリラックス完
了後、脱水処理し円筒状綿袋から生機を取り出し拡布し
た状態でオープンソーパーによるソーピング或いは液流
精練等を再度実施し除去仕切れなかった紡糸油剤、糊
剤、オリゴマー成分等の不純物を完全除去することが望
ましい。As a model used for moist heat relaxation, in addition to the above liquid flow relaxer, a high pressure rotary washer, etc.
It can be implemented using a known model. If necessary, various wet heat pretreatments and dry heat pretreatments may be used in combination. In the case of using a high-pressure rotary washer, a crushed wrinkle process in which a textile machine is finely pressed into a cylindrical cotton bag and subjected to scouring / relaxation to make wrinkles is effective for improving the chinchilla feeling and the appearance design. When the crushed wrinkle processing is performed, after completion of the above washer relaxation, dehydration treatment is performed, and the raw fabric is taken out from the cylindrical cotton bag and expanded, and then soaping with an open soaper or liquid scouring is performed again, and the spinning oil agent that cannot be completely removed It is desirable to completely remove impurities such as a sizing agent and an oligomer component.
【0033】上記湿熱リラックスにおける急昇温温度領
域は糸条の熱収縮開始温度−20℃から同熱収縮開始温
度+30℃までであることが望ましい。同熱収縮開始温
度+30℃以降の高温範囲については特に規定しない
が、昇温速度を下げた状態で段階的に昇温させ最高到達
温度で30〜60分程度の揉み効果を与えることが精練
性や風合い出しの為には効果的である。糸条の熱収縮開
始温度付近の温度は、特に布帛の外観品位や風合いの観
点からも重要な位置を占める温度領域であり、上記温度
領域に於いて昇温速度をコントロールすることによって
適度な外観品位、膨らみ感を得ることが可能となる。It is desirable that the temperature rising temperature range in the wet heat relaxation is from the thermal contraction start temperature of the yarn of −20 ° C. to the thermal contraction start temperature of + 30 ° C. Although the high temperature range after the same heat shrinkage start temperature + 30 ° C is not specified, it is necessary to raise the temperature in stages while decreasing the temperature raising rate to give a rubbing effect of about 30 to 60 minutes at the maximum reached temperature. It is effective for making texture. The temperature near the thermal contraction start temperature of the yarn is a temperature region that occupies an important position particularly from the viewpoint of the appearance quality and texture of the fabric, and by controlling the heating rate in the above temperature region, a suitable appearance can be obtained. It is possible to obtain a feeling of quality and swelling.
【0034】布帛の仕上巾に対する織上巾の比及び/又
は布帛の仕上長さに対する織上長さの比は仕上:織上の
比として1.00:1.20〜1.00:1.45の範囲、
特に好ましくは1.00:1.30〜1.00:1.40の
範囲である。尚、ここでいう織上巾及び織上長さは織機
上での性量ではなく織機から生機を取り出しフリーの状
態にした性量を指す。また仕上巾及び仕上長さも最終の
仕上げセット工程におけるヒートセッター上の性量では
なく、セット後生機をフリー状態にした際の性量であ
る。The ratio of the woven width to the finished width of the cloth and / or the ratio of the woven length to the finished length of the cloth is 1.00: 1.20 to 1.00: 1 as a finish: woven ratio. 45 range,
Particularly preferably, it is in the range of 1.00: 1.30 to 1.00: 1.40. The weaving width and the weaving length referred to here are not the properties on the loom, but the properties in which the raw loom is taken out from the loom and put in a free state. Further, the finishing width and the finishing length are not the physical properties on the heat setter in the final finishing setting step, but the physical properties when the post-setting raw machine is in a free state.
【0035】仕上:織上の比が1.00:1.20未満で
あれば布帛の膨らみ感、外観のチンチラ効果等が非常に
乏しいものになってしまう他、メヨレやスリップの諸問
題の発生が懸念され好ましくない。又、仕上:織上の比
が1.00:1.45を超過する領域になると布帛はフカ
ツキ感を感じる風合いとなる他、表面感も乱れたチンチ
ラ感に仕上る他、経糸及び/又は緯糸の飛び出し等によ
るピリング、スナッグの発生を誘発し好ましい範囲では
ない。If the finishing: weaving ratio is less than 1.00: 1.20, the swelling feeling of the cloth, the chinchilla effect of the appearance and the like are very poor, and various problems such as misalignment and slippage occur. Is unfavorable because of concern. Further, in the area where the finish: weave ratio exceeds 1.00: 1.45, the fabric feels fluffy, and the surface feel is also disturbed, resulting in a chinchilla feel, and warp and / or weft This is not preferable because it induces pilling and snag due to jumping out.
【0036】本発明の難燃性ポリエステル布帛を染色す
る場合は分散染料による染色を実施するが液流染色機等
による浸染の他、ロータリースクリーンやフラットスク
リーン、インクジェット等による捺染の何れによっても
よい。浸染の場合は高圧120〜130℃の浴温が染色
堅牢度等の観点より好ましく、捺染の場合は湿熱リラッ
クス処理した後の布帛についてヒートセッターを使用し
て布目矯正、巾調整した後に捺染用分散染料、糊料等を
調整した捺染糊剤を該布帛表面に塗布し、表面温度10
0〜120℃のシリンダーロールを通して予備乾燥を実
施した後、発色機にて160〜180℃程度の雰囲気温
度で染料吸尽、固着させる発色工程を経て、不要な糊料
や染料をソーピング除去した後、ヒートセッターによる
仕上げセットを実施して仕上げる。When the flame-retardant polyester cloth of the present invention is dyed, it is dyed with a disperse dye. However, in addition to dip dyeing with a jet dyeing machine, printing with a rotary screen, a flat screen, an ink jet or the like may be used. In the case of dip dyeing, a bath temperature of 120 to 130 ° C is preferable from the viewpoint of dyeing fastness, and in the case of printing, the cloth after wet heat relaxation treatment is subjected to straightening and width adjustment using a heat setter before dispersion for printing. A printing paste containing a dye, paste, etc., is applied to the surface of the cloth to give a surface temperature of 10
After preliminarily drying through a cylinder roll of 0 to 120 ° C, after removing unnecessary glue and dye by soaping through a coloring step of exhausting and fixing the dye at an ambient temperature of about 160 to 180 ° C with a color developing machine. Finish by performing a finishing set with a heat setter.
【0037】何れの染色処方についても余分な染料、分
散助剤等を布帛から除去することが難燃性を向上させる
上で望ましく、特に濃色の場合には還元洗浄を十分に実
施しておくことが望ましい。また必要に応じて染色同浴
処理にて紫外線吸収剤を繊維に吸尽処理させてもよい。
更に染色後の布帛にはノニオン系のポリエステル系帯電
防止剤や柔軟剤をパッド法等により難燃性に支障のない
範囲で処理してもよい。In any of the dyeing formulations, it is desirable to remove excess dyes, dispersion aids, etc. from the fabric in order to improve the flame retardancy, and especially in the case of a dark color, reduction washing is sufficiently carried out. Is desirable. If necessary, the fibers may be exhausted with the ultraviolet absorber by the same dyeing bath treatment.
Further, the dyed fabric may be treated with a nonionic polyester antistatic agent or a softening agent by a pad method or the like within a range that does not impair flame retardancy.
【0038】本発明にて得られた難燃性ポリエステル布
帛は用途に応じて裁断、縫製されカーテン、椅子張り
材、寝装寝具側地、壁紙材、テーブルクロスとして使用
される。製品自体の難燃性能を保持するために縫糸、ジ
ッパー、ボタン、シームテープ等々の縫製部材も難燃性
能を有するものの採用が好ましい。The flame-retardant polyester cloth obtained in the present invention is cut and sewn according to the use and used as a curtain, a upholstery material, a bedclothing bedding side material, a wallpaper material, and a table cloth. In order to maintain the flame-retardant performance of the product itself, it is preferable to use a sewing member such as sewing thread, zipper, button, seam tape, etc., which also has flame-retardant performance.
【0039】[実施例]以下実施例により本発明を更に
詳細に説明する。尚、本文中及び実施例中に記載の特性
値は以下の方法によるものである。また、本発明は以下
の実施例に何等限定されるものではない。[Examples] The present invention will be described in more detail with reference to the following examples. The characteristic values described in the text and examples are based on the following methods. Further, the present invention is not limited to the following examples.
【0040】[沸水収縮率(SHW)]試料(糸条)を
枠周1.125mの検尺機を使用し初荷重0.09g/
dtexをかけて120回/分の速度で巻返し、巻き回数2
0回の小かせを作成し、初荷重の40倍の荷重をかけて
かせ長L0(mm)を測定する。次いで荷重を外し、収縮が
妨げられない条件下で98℃±2℃の沸水中に30分間
浸漬した後、水平状態に保ち風乾する。風乾後に再度
0.09g/dtexの荷重をかけてかせ長L1(mm)を測定
し、下記式に基づき沸水収縮率SHWを算出する。実験
回数5回の平均値をもってその測定値とする。
[式3] SHW(%)=(L0−L1)/L0 ×100
尚、沸水収縮率差ΔSHWについては混繊前の低収縮
糸、高収縮糸を上記方法にて単独で測定評価し、両者の
収縮率差(%)で表す。[Boiling water shrinkage rate (SHW)] A sample (thread) was used with a measuring machine having a frame circumference of 1.125 m and an initial load of 0.09 g /
Rewind at a speed of 120 times / min by applying dtex, and the number of windings is 2
Create a small skein 0 times, apply a load 40 times the initial load, and measure the skein length L0 (mm). Then, the load is removed, and the sample is immersed in boiling water at 98 ° C. ± 2 ° C. for 30 minutes under conditions where shrinkage is not hindered, and then kept horizontal and air dried. After air-drying, a load of 0.09 g / dtex is applied again to measure the length L1 (mm), and the boiling water shrinkage SHW is calculated based on the following formula. The average value of 5 times of experiments is taken as the measured value. [Equation 3] SHW (%) = (L0-L1) / L0 × 100 The boiling water shrinkage difference ΔSHW was measured and evaluated by the above method independently for the low shrinkage yarn and the high shrinkage yarn before mixing, and both The difference in shrinkage (%) is expressed.
【0041】[乾熱160℃における寸法変化率]生地
に張力が掛らぬ状態で布目に沿うように20cm×20cm
の正方形の四隅に油性インクで印を付け、収縮が妨げら
れない条件で乾熱160℃に調整されたオーブン内で3
分間処理した後に試料(生地)を取り出し、室温になる
まで水平状態で空冷する。油性インクで印をつけた距離
(L2 cm)を実測し、下記に従い経方向及び緯方向の乾
熱160℃における寸法変化率を求める。1試料から経
方向、緯方向の寸法変化がそれぞれ2箇所測定出来る
為、測定試料(生地)2試料を用意し該寸法変化がそれ
ぞれn=4で測定するものとしそれらの平均値をもって
測定値とする。寸法変化測定では少数点第2位まで求め
る。
[式4]寸法変化率(%)=(L2−20)/20 ×100[Dimensional change rate at a dry heat of 160 ° C.] 20 cm × 20 cm so that the cloth is along the grain without tension.
Mark the four corners of the square with oil-based ink, and in an oven adjusted to a dry heat of 160 ° C under conditions where shrinkage is not hindered.
After the treatment for a minute, the sample (dough) is taken out and air-cooled in a horizontal state until it reaches room temperature. The distance (L2 cm) marked with the oil-based ink is measured, and the dimensional change rate at the dry heat of 160 ° C. in the warp direction and the weft direction is obtained according to the following. Since two dimensional changes in the warp direction and the weft direction can be measured from one sample, two measurement samples (fabric) are prepared and the dimensional changes are measured at n = 4. To do. In the measurement of dimensional change, obtain the second decimal place. [Formula 4] Dimensional change rate (%) = (L2−20) / 20 × 100
【0042】[難燃性能]1999年度版JIS L−
1091 A−1法(45°ミクロバーナ法)に従い1
分加熱後の燃焼面積(cm2)、残炎時間(秒)、残塵
時間(秒)を評価する。更に財団法人 日本防炎協会
防炎製品認定委員会発行の防炎製品の性能試験基準(平
成11年1月1日改正)第1 寝具類−2防炎性能試
験.1.(1).に記載のコイル法に従い評価した。
尚、試料の洗濯方法(水洗い洗濯、ドライクリーニン
グ)はそれぞれJIS L−1018の8.58.4b)
6.2のF−2法、JIS L−1018の8.58.4
b)5.2)のE−2法に準じて実施し、洗濯初期及び
水洗い洗濯5回、ドライクリーニング5回後の難燃性能
(残炎時間、残塵時間、燃焼面積)を評価する。[Flame retardant performance] 1999 version JIS L-
1091 A-1 method (45 ° micro burner method) 1
The burning area (cm 2 ) after the minute heating, the afterflame time (seconds), and the remaining dust time (seconds) are evaluated. Furthermore, the Japan Flame Retardant Association
Performance test standards for flameproof products issued by the Flameproof Product Certification Committee (revised January 1, 1999) 1st Bedding-2 Flameproof performance test. 1. (1). Evaluation was performed according to the coil method described in 1.
The sample washing method (washing washing, dry cleaning) is JIS L-1018 8.58.4b).
F-2 method of 6.2, 8.58.4 of JIS L-1018
b) Carry out according to the method E-2 of 5.2), and evaluate the flame retardancy (afterflame time, residual dust time, burning area) at the initial stage of washing, after 5 washes with water and after 5 times of dry cleaning.
【0043】[糸条の熱収縮開始温度]セイコーインス
ツルメント社製熱収縮応力測定装置SSC−5000型
を使用し、チャック間距離=20mm、昇温速度=20℃
/分、初荷重=0.045g/dtex、測定雰囲気ガス=
空気の各条件下で糸条の熱収縮応力を測定し、該熱収縮
応力曲線から糸条の熱収縮開始温度を直読した。尚、実
験回数5回の平均値をその測定値とした。また、図11
に熱収縮応力曲線からの熱収縮開始温度読出法を図示し
た。熱収縮開始温度の読出法については熱収縮応力曲線
にひいた2本の接線の交点温度をグラフ上から直読する
方法で求めた。[Temperature of contraction of heat shrinkage of yarn] Using a heat shrinkage stress measuring device SSC-5000 manufactured by Seiko Instruments Inc., distance between chucks = 20 mm, heating rate = 20 ° C.
/ Min, initial load = 0.045 g / dtex, measurement atmosphere gas =
The heat shrinkage stress of the yarn was measured under each condition of air, and the heat shrinkage initiation temperature of the yarn was directly read from the heat shrinkage stress curve. In addition, the average value of 5 times of experiment was made into the measured value. In addition, FIG.
The method for reading the thermal contraction onset temperature from the thermal contraction stress curve is illustrated in Fig. Regarding the method for reading the heat shrinkage initiation temperature, the temperature at the intersection of the two tangents drawn on the heat shrinkage stress curve was directly read from the graph.
【0044】[実施例1]テレフタル酸、エチレングリ
コールをそれぞれカルボン酸成分、グリコール成分とし
前記[化11]で示された燐化合物を燐原子含有量が6
000ppmとなるように共重合させた燐含有共重合ポ
リエステルを用い、紡糸温度265℃、未延伸糸引取速
度1500m/分で溶融紡糸してポリエステルマルチフ
ィラメント未延伸糸を得た。次いで該未延伸糸条を表面
温度80℃のホットローラー及び表面温度160℃のプ
レートヒーターに接触させつつ延伸倍率3.0倍で延伸
処理し42デシテックス24フィラメントの低収縮糸を
得た。沸水収縮率SHWは7.5%であった。[Example 1] The phosphorus compound represented by the above [Chemical Formula 11] was used as a carboxylic acid component and a glycol component of terephthalic acid and ethylene glycol, respectively, and had a phosphorus atom content of 6
Using a phosphorus-containing copolyester copolymerized to a concentration of 000 ppm, melt spinning was performed at a spinning temperature of 265 ° C. and an undrawn yarn take-up speed of 1500 m / min to obtain a polyester multifilament undrawn yarn. Then, the unstretched yarn was stretched at a draw ratio of 3.0 times while being brought into contact with a hot roller having a surface temperature of 80 ° C. and a plate heater having a surface temperature of 160 ° C., to obtain a low shrinkage yarn of 42 decitex 24 filaments. The boiling water shrinkage SHW was 7.5%.
【0045】一方、同一紡糸条件で得られたポリエステ
ルマルチフィラメント未延伸糸を表面温度80℃のホッ
トローラーのみに接触させて延伸倍率3.0倍で延伸処
理し42デシテックス24フィラメントの高収縮糸を得
た。沸水収縮率は48.5%であった。得られた高収縮
糸、低収縮糸を同率供給条件にて常温高圧空気流による
交絡処理を施し、84デシテックス48フィラメントの
異収縮混繊糸とした。該異収縮混繊糸を構成する高収縮
糸/低収縮糸の沸水収縮率差(ΔSHW)は41.0
%、熱収縮応力曲線から得られた熱収縮開始温度は50
℃であった。On the other hand, the polyester multifilament unstretched yarn obtained under the same spinning conditions was contacted only with a hot roller having a surface temperature of 80 ° C. and stretched at a draw ratio of 3.0 to obtain a highly shrinkable yarn of 42 decitex 24 filaments. Obtained. The boiling water shrinkage was 48.5%. The high shrinkage yarns and low shrinkage yarns thus obtained were subjected to an entanglement treatment with a normal temperature and high pressure air flow under the same rate supply condition to obtain 84 decitex 48 filament heterogeneous shrinkage mixed yarns. The difference in boiling water shrinkage ratio (ΔSHW) between the high shrinkage yarn / low shrinkage yarn constituting the heterogeneous shrinkage mixed yarn is 41.0.
%, The heat shrinkage onset temperature obtained from the heat shrinkage stress curve is 50
It was ℃.
【0046】該混繊糸に400回/mの甘撚を付与し経
糸とし、緯糸としては該混繊糸に使用した燐含有共重合
ポリエステルを溶融紡糸して得られた部分配向糸(PO
Y)を延伸仮撚してなる167デシテックス48フィラ
メントの仮撚加工糸を無撚のまま、エアージェットルー
ムを使用し5枚朱子ベースの二重朱子組織に製織した。
織上密度は経110本/cm、緯26本/cm、織上巾15
2.5cm、織上長63.5mである。A partially twisted yarn (PO) obtained by melt-spinning the phosphorus-containing copolyester used in the mixed yarn as a weft yarn by applying a sweet twist of 400 times / m to the mixed yarn
Y) was false-twisted, and a 167-decitex 48-filament false-twisted yarn was woven in an untwisted manner using an air jet loom into a double-satin design based on 5 sheets of satin.
Weaving density is 110 warp / cm, weft 26 / cm, weave width 15
The length is 2.5 cm and the weaving length is 63.5 m.
【0047】得られた製織生機を直径30cmφの円筒状
袋(綿製)に細かく押し込み、袋の開口部を紐で縛った
上で、高圧ロータリーワッシャーを使用し浴温30℃か
ら80℃迄、+7℃/分で昇温させ、最高到達温度11
0℃で処理した。ノニオン系界面活性剤として[化9]
で示したポリオキシエチレンドデシルグリコールエーテ
ル(HLB=14.05)を1g/l、水酸化ナトリウ
ム1g/lを溶解した水溶液を調整して湿熱リラックス
処理を施した。The obtained weaving looms were finely pushed into a cylindrical bag (made of cotton) having a diameter of 30 cmφ, the opening of the bag was tied with a string, and the bath temperature was raised from 30 ° C to 80 ° C using a high pressure rotary washer. Raise the temperature at + 7 ° C / min to reach the maximum temperature of 11
Treated at 0 ° C. As a nonionic surfactant [Chemical formula 9]
An aqueous solution in which 1 g / l of polyoxyethylene dodecyl glycol ether (HLB = 14.05) and 1 g / l of sodium hydroxide were prepared was subjected to wet heat relaxation treatment.
【0048】[0048]
【化9】
廃液後に脱水処理し、円筒状袋を開封し生地を取り出し
拡布した上でオープンソーパーを通し十分にソーピング
を実施した上で表面温度110℃のシリンダーローラ
ー、雰囲気温度160℃のネットコンベア式乾熱リラク
サーにて経方向及び緯方向に過度の張力が掛らぬ条件で
乾燥処理を施した。[Chemical 9] After the waste liquid is dehydrated, the cylindrical bag is opened, the dough is taken out and spread, and after thoroughly soaping through an open soaper, a cylinder roller with a surface temperature of 110 ° C and a net conveyor dry heat relaxer with an ambient temperature of 160 ° C. Was subjected to a drying treatment under a condition that excessive tension was not applied in the warp direction and the weft direction.
【0049】次いで液流染色機を使用して分散染料によ
る高圧染色を施し、廃液後十分に還元洗浄及びソーピン
グを施し、脱水後に再度表面温度110℃のシリンダー
ローラー、雰囲気温度140℃のネットコンベア式乾熱
リラクサーを通し、処理温度160℃の条件で仕上げセ
ットを施した。得られた布帛の仕上密度は経137本/
cm、緯32本/cm、仕上巾123cm、仕上長50.8m
であった。仕上巾:織上巾=1.00:1.24、仕上
長:織上長=1.00:1.25である。乾熱160℃に
おける寸法変化率は経−0.5%、緯−1.5%であ
り、乾熱処理によってもへたりや収縮は軽度なものに留
まり、消費性能的にも満足するものであった。その他、
防炎性能等の物性値についても表1に纏めた。該布帛を
使用しカーテンとして仕上げた。適度なソフトタッチ、
膨らみ感、チンチラ効果のある表面感が得られ、病院・
劇場等の公共用途、家庭用途に好適なカーテン地に仕上
った。Next, high-pressure dyeing with a disperse dye is performed using a jet dyeing machine, and after the waste liquid is sufficiently reduced and washed and soaped, a cylinder roller with a surface temperature of 110 ° C and a net conveyor type with an ambient temperature of 140 ° C are again used after dehydration. A finishing set was performed through a dry heat relaxer at a treatment temperature of 160 ° C. The resulting fabric has a finishing density of 137 warps /
cm, 32 wefts / cm, finished width 123 cm, finished length 50.8 m
Met. Finish width: woven width = 1.00: 1.24, finish length: woven length = 1.00: 1.25. The dimensional change rates at dry heat of 160 ° C are -0.5% and weft-1.5%, and even after the dry heat treatment, the settling and shrinkage are mild and the consumption performance is satisfactory. It was Other,
The physical property values such as flameproof performance are also summarized in Table 1. The cloth was used as a curtain. Moderate soft touch,
A swelling feeling, a surface feeling with a chinchilla effect can be obtained,
Finished curtain material suitable for public use such as theaters and home use.
【0050】[実施例2]実施例1で作成した生機を使
用し、液流リラクサーで浴比1:7.5、浴温20℃か
ら80℃まで昇温速度+7℃/分で昇温し、最高到達温
度120℃で精練・リラックス処理した。浴温80℃の
時点で廃液を実施し湯洗・水洗を繰り返した後、表面温
度110℃のシリンダーローラー、雰囲気温度160℃
のネットコンベア式乾熱リラクサーにて経方向及び緯方
向に過度の張力が掛らぬ条件で乾燥処理を施した。ノニ
オン系界面活性剤として[化10]で示したポリオキシ
エチレンノニルフェニルグリコールエーテル(HLB=
12.78)を1g/l、水酸化ナトリウム1g/lを
溶解した水溶液を調整して湿熱リラックス処理を施し
た。[Example 2] Using the greige machine prepared in Example 1, a liquid-flow relaxer was used to increase the bath ratio from 1: 7.5 and the bath temperature from 20 ° C to 80 ° C at a heating rate of + 7 ° C / min. Then, scouring / relaxation treatment was performed at the maximum reaching temperature of 120 ° C. At the time of bath temperature 80 ℃, waste liquid is implemented and after repeated hot and cold washing, cylinder roller with surface temperature 110 ℃, ambient temperature 160 ℃
Was dried under the condition that excessive tension was not applied in the longitudinal direction and the weft direction. As the nonionic surfactant, polyoxyethylene nonylphenyl glycol ether (HLB =
An aqueous solution in which 1 g / l of 12.78) and 1 g / l of sodium hydroxide were prepared was subjected to a wet heat relaxation treatment.
【0051】[0051]
【化10】 [Chemical 10]
【0052】次いで液流染色機を使用して分散染料によ
る高圧染色を施し、廃液後十分に還元洗浄及びソーピン
グを施し、脱水後に再度表面温度110℃のシリンダー
ローラー、雰囲気温度140℃のネットコンベア式乾熱
リラクサーを通し、処理温度160℃の条件で仕上げセ
ットを施した。得られた布帛の仕上密度は経136本/
cm、緯31本/cm、仕上巾129cm、仕上長48mで
あり仕上巾:織上巾=1.00:1.18、仕上長:織上
長=1.00:1.32、乾熱160℃における寸法変化
率は経−1.0%、緯−1.0%であり、乾熱処理によ
ってもへたりや収縮は軽度なものに留まり、消費性能的
にも満足するものであった。その他、防炎性能等の物性
値についても表1に纏めた。Next, high-pressure dyeing with a disperse dye is carried out using a jet dyeing machine, and after the waste liquid is sufficiently reduced and washed and soaped, a cylinder roller with a surface temperature of 110 ° C and a net conveyor type with an ambient temperature of 140 ° C are again used after dehydration. A finishing set was performed through a dry heat relaxer at a treatment temperature of 160 ° C. The resulting fabric has a finishing density of 136 yarns /
cm, weft 31 strands / cm, finishing width 129 cm, finishing length 48 m, finishing width: woven width = 1.00: 1.18, finishing length: woven length = 1.00: 1.32, dry heat 160 The dimensional change rate at ° C was -1.0% and weft-1.0%, and even after the dry heat treatment, the settling and shrinkage were mild, and the consumption performance was satisfactory. Other physical properties such as flameproof performance are also summarized in Table 1.
【0053】得られた難燃性ポリエステル布帛を裁断、
縫製しソファーの座面に用いた。適度なソフトタッチと
強すぎないチンチラ感が上品な表面感を醸し出し、嫌味
のない外観品位を有するソファーに仕上った。The obtained flame-retardant polyester cloth is cut,
It was sewn and used on the seat surface of the sofa. A moderate soft touch and not too strong a chinchilla feel create a refined surface feeling, resulting in a sofa with an unpleasant appearance.
【0054】[実施例3]実施例1で用いた84デシテ
ックス48フィラメントの異収縮混繊糸、167デシテ
ックス48フィラメントの仮撚加工糸を用い、該異収縮
混繊糸にS撚方向に400回/mの甘撚をかけて経糸と
なし、緯糸には上記仮撚加工糸を無撚のままレピアルー
ムを用い、織上密度が経74本/cm、緯26本/cm、織
上巾193cm、織上長71mの7枚経朱子(右上りサ
テン6/1(2飛))組織に製織した。該生機を実施例
1同様の方法を用いて染色加工布帛とした。仕上密度は
経105本/cm、緯35本/cm、仕上巾139cm、仕
上長51mであり、仕上巾:織上巾=1.00:1.3
9、仕上長:織上長=1.00:1.39、乾熱160℃
における寸法変化率は経−1.2%、緯−1.1%であ
り、乾熱処理によってもへたりや収縮は軽度なものに留
まり、消費性能的にも満足するものであった。その他、
防炎性能等の物性値については表1に纏めた。[Example 3] The 84-decitex 48-filament different-shrink mixed yarn and the 167 decitex 48-filament false twisted yarn used in Example 1 were used, and the different-shrink mixed-filament yarn was 400 times in the S twist direction. / M of sweet twist to form warp yarn, using the above-described false twisted yarn as the weft yarn in the rapier room without twisting, the weaving density is warp 74 yarns / cm, weft 26 yarns / cm, weaving width 193 cm, Weaving was carried out into a 7-sheet warp satin (upper right satin 6/1 (2 fly)) design with a weaving length of 71 m. Using the same method as in Example 1, the greige was used as a dyed fabric. Finishing density is 105 threads / cm, weft 35 threads / cm, finishing width 139 cm, finishing length 51 m, finishing width: weaving width = 1.00: 1.3
9, Finishing length: Textile length = 1.00: 1.39, dry heat 160 ° C
The dimensional change rate was −1.2% and the weft was −1.1%, and even after the dry heat treatment, the settling and the shrinkage were mild, and the consumption performance was satisfactory. Other,
Physical properties such as flameproof performance are summarized in Table 1.
【0055】得られた難燃性ポリエステル布帛を裁断、
縫製し寝装寝具側地(ベッドカバー)を得た。適度なソ
フトタッチと膨らみ感、嫌味のないチンチラ効果を有す
る、ベッドカバーとして良好なものに仕上った。The obtained flame-retardant polyester cloth is cut,
The sewn bedclothes bedding side cloth (bed cover) was obtained. It was a good bed cover with moderate soft touch, swelling, and chinchilla effect without dislike.
【0056】[比較例1]エチレンテレフタレートを主
たる構成単位とするポリエステルを常法に従い、溶融紡
糸・延伸処理を行い42デシテックス36フィラメント
のポリエステルマルチフィラメント延伸糸(低収縮糸)
を得た。該延伸糸の沸水収縮率SHWは6.0%であっ
た。また、テレフタル酸以外のカルボン酸成分としてイ
ソフタル酸を10モル%共重合させてなるポリエステル
を溶融紡糸・延伸処理を行い42デシテックス24フィ
ラメントのイソフタル酸共重合ポリエステルマルチフィ
ラメント延伸糸(高収縮糸)を得た。該延伸糸の沸水収
縮率SHWは55.5%であった。Comparative Example 1 A polyester multifilament drawn yarn (low shrinkage yarn) of 42 decitex 36 filaments was obtained by melt spinning and drawing treatment of polyester containing ethylene terephthalate as a main constituent unit according to a conventional method.
Got The boiling water shrinkage rate SHW of the drawn yarn was 6.0%. Further, a polyester obtained by copolymerizing 10 mol% of isophthalic acid as a carboxylic acid component other than terephthalic acid is melt-spun and stretched to obtain a 42 decitex 24 filament isophthalic acid-copolyester multifilament stretched yarn (high shrinkage yarn). Obtained. The boiling water shrinkage SHW of the drawn yarn was 55.5%.
【0057】上記イソフタル酸共重合ポリエステルマル
チフィラメント延伸糸(高収縮糸)とポリエステルマル
チフィラメント延伸糸(低収縮糸)を同率供給下で常温
高圧空気流による交絡処理を施し、84デシテックス6
0フィラメントのポリエステル異収縮混繊糸を得た。該
異収縮延伸糸の高収縮糸/低収縮糸の沸水収縮率差(Δ
SHW)は49.5%、熱収縮応力曲線から得られた熱
収縮開始温度は70℃であった。The isophthalic acid-copolymerized polyester multifilament drawn yarn (high-shrinkage yarn) and the polyester multifilament drawn yarn (low-shrinkage yarn) were subjected to entanglement treatment with a normal-temperature high-pressure air stream at the same rate to obtain 84 decitex 6
A 0-filament polyester different shrinkage mixed yarn was obtained. The difference in the boiling water shrinkage ratio of the high shrinkage yarn / low shrinkage yarn of the different shrinkage drawn yarn (Δ
SHW) was 49.5%, and the heat shrinkage initiation temperature obtained from the heat shrinkage stress curve was 70 ° C.
【0058】該混繊糸に400回/mの甘撚を付与し経
糸とし、緯糸としてポリエステルマルチフィラメント通
常延伸糸167デシテックス96フィラメント(商品名
・東洋紡エステル)にS撚及びZ撚方向に1500回/
mの実撚を挿入し撚糸条とし、レピアルームを使用して
織上密度が経75本/cm、緯24本/cm、織上巾17
2.5cm、織上長74mの7枚経朱子(右上りサテン
6/1(2飛))組織に製織した。400 times / m of sweet twist is applied to the mixed yarn to make a warp, and polyester multifilament normally drawn yarn 167 decitex 96 filament (trade name, Toyobo Ester) is used as weft 1500 times in S twist and Z twist directions. /
m real twist is inserted to make a twisted yarn, and using rapier room, weaving density is 75 yarns / cm, weft 24 yarns / cm, weave width 17
7 pieces of warp satin (upper right satin 6/1 (2 jumps)) of 2.5 cm and weaving length of 74 m were woven.
【0059】得られた製織生機を直径30cmφの円筒状
袋(綿製)に細かく押し込み、袋の開口部を紐で縛った
上で、高圧ロータリーワッシャーを使用し浴温30℃か
ら80℃まで昇温速度+7℃/分で昇温させ、最高到達
温度110℃で処理した。湿熱リラックス処理における
ノニオン系界面活性剤及び水酸化ナトリウム添加量、処
方は実施例1と全て同様の方法で調整した。廃液後に脱
水処理し、円筒状袋を開封し生地を取り出し拡布した上
でオープンソーパーを通し十分にソーピングを実施した
上で表面温度110℃のシリンダーローラー、雰囲気温
度160℃のネットコンベア式乾熱リラクサーにて経方
向及び緯方向に過度の張力が掛らぬ条件で乾燥処理を施
した。The weaving machine thus obtained was finely pressed into a cylindrical bag (made of cotton) having a diameter of 30 cm, the opening of the bag was tied with a string, and the bath temperature was raised from 30 ° C to 80 ° C using a high pressure rotary washer. The temperature was raised at a temperature rate of + 7 ° C / min, and the treatment was performed at the highest temperature of 110 ° C. The amounts of the nonionic surfactant and sodium hydroxide added and the formulation in the wet heat relaxation treatment were adjusted in the same manner as in Example 1. After the waste liquid is dehydrated, the cylindrical bag is opened, the dough is taken out and spread, and after thoroughly soaping through an open soaper, a cylinder roller with a surface temperature of 110 ° C and a net conveyor dry heat relaxer with an ambient temperature of 160 ° C. Was subjected to a drying treatment under a condition that excessive tension was not applied in the warp direction and the weft direction.
【0060】次いで液流染色機を使用して分散染料によ
る高圧染色を施す際に、含ハロゲン燐酸エステル系難燃
加工剤を浴中吸尽法によって染色同時吸尽させた。廃液
後十分に還元洗浄及びソーピングを施し、脱水後に再度
表面温度110℃のシリンダーローラー、雰囲気温度1
40℃のネットコンベア式乾熱リラクサーを通し、処理
温度160℃の条件で仕上げセットを施した。得られた
布帛の仕上密度は経87本/cm、緯35本/cm、仕上巾
135cm、仕上長57mであり仕上巾:織上巾=1.
28、仕上長:織上長=1.00:1.30、乾熱160
℃における寸法変化率は経−0.9%、緯−1.0%で
あり、乾熱処理によってもへたりや収縮は軽度なものに
留まり、消費性能的にも満足するものであった。その
他、防炎性能等の物性値については表1に纏めた。Then, when performing high-pressure dyeing with a disperse dye using a jet dyeing machine, the halogen-containing phosphoric acid ester flame retardant finishing agent was simultaneously exhausted by the in-bath exhaustion method. After the waste liquid is sufficiently reduced and washed and soaped, and after dehydration, the surface temperature of the cylinder roller is 110 ° C again, and the ambient temperature is 1
A net conveyor type dry heat relaxer at 40 ° C. was passed through, and a finishing set was performed at a processing temperature of 160 ° C. The obtained fabric has a finishing density of 87 warps / cm, 35 wefts / cm, a finishing width of 135 cm, and a finishing length of 57 m. Finishing width: woven width = 1.
28, Finishing length: Weaving length = 1.00: 1.30, dry heat 160
The dimensional change rate at ° C was -0.9% and weft-1.0%, and even after the dry heat treatment, the degree of settling and shrinkage was slight, and the consumption performance was satisfactory. Other physical properties such as flameproof performance are summarized in Table 1.
【0061】上記後加工難燃処理ポリエステル布帛を裁
断、縫製しカーテンとして仕上げた風合いについてはソ
フト感、膨らみ感の良好なものとなり、チンチラ効果の
ある外観品位のものに仕上ったが、防炎性能について初
期値は満足するもののドライクリーニング5回後の防炎
性能は極端に低下し、洗濯耐久性に乏しいものとなり、
難燃カーテンとして望まれる性能を有するものにはなら
なかった。The post-processed flame-retardant polyester fabric was cut, sewn and finished as a curtain to give a soft and swelling feeling, and a finish with a chinchilla effect was obtained. Although the initial value is satisfied, the flameproof performance after 5 times of dry cleaning is extremely deteriorated and the washing durability is poor,
It did not have the desired performance as a flame-retardant curtain.
【0062】[0062]
【表1】 [Table 1]
【0063】[0063]
【発明の効果】上述の如く、本発明によると難燃性とソ
フトな触感、膨らみ感とチンチラ効果のある生地表面感
を具備するポリエステル布帛を得ることが可能であり、
特にカーテン、テーブルクロス、壁張り材など生活資材
用途に好適な素材となる。また従来の後加工難燃素材で
は洗濯耐久性に問題があったが、本発明によると難燃性
能は半永久的であり、更には後加工で難燃薬剤を何等使
用しないため環境にも優しく、経済的且つ効率よく性能
を付与することが出来る等の効果が期待出来る。As described above, according to the present invention, it is possible to obtain a polyester cloth having a flame-retardant property, a soft touch feeling, a bulge feeling, and a surface feeling of a cloth having a chinchilla effect.
In particular, it is a suitable material for daily use such as curtains, table cloths and wall coverings. Further, the conventional post-processed flame-retardant material had a problem in washing durability, but according to the present invention, the flame-retardant performance is semi-permanent, and further, since no flame-retardant agent is used in the post-process, it is environmentally friendly, An effect such as being able to impart performance economically and efficiently can be expected.
【図1】 本発明の実施態様(組織図)の1例であ
る。FIG. 1 is an example of an embodiment (organization chart) of the present invention.
【図2】 本発明の実施態様(組織図)の1例であ
る。FIG. 2 is an example of an embodiment (organization chart) of the present invention.
【図3】 本発明の実施態様(組織図)の1例であ
る。FIG. 3 is an example of an embodiment (organization chart) of the present invention.
【図4】 本発明の実施態様(組織図)の1例であ
る。FIG. 4 is an example of an embodiment (organization chart) of the present invention.
【図5】 本発明の実施態様(組織図)の1例であ
る。FIG. 5 is an example of an embodiment (organizational chart) of the present invention.
【図6】 本発明の実施態様(組織図)の1例であ
る。FIG. 6 is an example of an embodiment (organizational chart) of the present invention.
【図7】 本発明の実施態様(組織図)の1例であ
る。FIG. 7 is an example of an embodiment (organization chart) of the present invention.
【図8】 本発明の実施態様(組織図)の1例であ
る。FIG. 8 is an example of an embodiment (organizational chart) of the present invention.
【図9】 本発明の実施態様(組織図)の1例であ
る。FIG. 9 is an example of an embodiment (organization chart) of the present invention.
【図10】 本発明の実施態様(組織図)の1例であ
る。FIG. 10 is an example of an embodiment (organizational chart) of the present invention.
【図11】 糸条の熱収縮応力曲線から糸条の熱収縮開
始温度の読出法を図示したものである。該曲線にひいた
2本の接線の交点温度が熱収縮開始温度となる。FIG. 11 illustrates a method for reading the thermal contraction start temperature of the yarn from the thermal contraction stress curve of the yarn. The temperature at the intersection of the two tangents drawn on the curve is the heat shrinkage start temperature.
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3B154 AA07 AA18 AB20 BA21 BB12 BB32 BD07 BE05 BF01 BF06 BF14 BF20 BF30 DA03 DA09 DA13 DA16 4H028 AA35 AA37 4H057 AA02 DA01 DA17 DA40 FA17 HA01 JA10 JB01 4L035 BB32 BB89 BB91 EE14 GG01 JJ25 ─────────────────────────────────────────────────── ─── Continued front page F term (reference) 3B154 AA07 AA18 AB20 BA21 BB12 BB32 BD07 BE05 BF01 BF06 BF14 BF20 BF30 DA03 DA09 DA13 DA16 4H028 AA35 AA37 4H057 AA02 DA01 DA17 DA40 FA17 HA01 JA10 JB01 4L035 BB32 BB89 BB91 EE14 GG01 JJ25
Claims (3)
し、下記燐化合物を添加して得られた共重合ポリエステ
ルを溶融紡糸してなるポリエステルマルチフィラメント
糸条を少なくとも一部に使用してなる布帛構造物を染色
加工するにあたり、湿熱リラックス処理を、該マルチフ
ィラメント糸条の熱収縮応力曲線から得られる糸条収縮
開始温度より20℃低い温度から糸条収縮開始温度より
30℃高い温度まで+5℃/分以上+10℃/分以下で
急昇温させて処理することを特徴とする意匠性に富む難
燃性ポリエステル布帛の染色加工方法。 【化1】 (式中、R1は1価のエステル形成性官能基であり、R
2、R3は同じか或いは異なる基であり、それぞれハロゲ
ン原子、炭素数1〜10個の炭化水素基、R1より選ば
れ、Aは2価又は3価の有機残基を表す。また、n1は
1又は2であり、n2、n3はそれぞれ0〜4の整数を表
す。)1. A fabric structure comprising at least a part of a polyester multifilament yarn containing 500 to 50,000 ppm of phosphorus atom and melt-spun of a copolyester obtained by adding the following phosphorus compound. In the dyeing process, a wet heat relaxation treatment is performed at a temperature of 20 ° C lower than the yarn shrinkage start temperature obtained from the heat shrinkage stress curve of the multifilament yarn to a temperature 30 ° C higher than the yarn shrinkage start temperature + 5 ° C / min. A method for dyeing and processing a flame-retardant polyester cloth having a rich design property, which is characterized in that the temperature is rapidly raised at + 10 ° C./min or less for processing. [Chemical 1] (In the formula, R 1 is a monovalent ester-forming functional group,
2, R3 are the same or different groups, each selected from a halogen atom, a hydrocarbon group having 1 to 10 carbon atoms, and R1, and A represents a divalent or trivalent organic residue. Further, n1 is 1 or 2, and n2 and n3 each represent an integer of 0-4. )
上長さに対する織上長さの比が仕上:織上=1.00:
1.20〜1.00:1.45を満足する条件で加工を
施すことを特徴とする請求項1記載の意匠性に富む難燃
性ポリエステル布帛の染色加工方法。2. The ratio of the weaving width to the finishing width and / or the ratio of the weaving length to the finishing length is finished: weave = 1.00:
The method for dyeing and processing a flame-retardant polyester cloth having excellent design properties according to claim 1, wherein the processing is performed under a condition satisfying 1.20 to 1.00: 1.45.
面活性剤を含む水溶液中で湿熱リラックス処理を施す請
求項1乃至2の何れかに記載の意匠性に富む難燃性ポリ
エステル布帛の染色加工方法。3. Dyeing of a flame-retardant polyester cloth having a high design property according to claim 1, wherein the wet heat relaxation treatment is performed in an aqueous solution containing a nonionic surfactant having an HLB value of 8 to 15. Processing method.
Priority Applications (1)
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JP2001320736A JP2003129368A (en) | 2001-10-18 | 2001-10-18 | Method for dyeing flame-retardant polyester fabric having rich design property |
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JP2001320736A JP2003129368A (en) | 2001-10-18 | 2001-10-18 | Method for dyeing flame-retardant polyester fabric having rich design property |
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Publication Number | Publication Date |
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Family
ID=19138080
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007138359A (en) * | 2005-11-22 | 2007-06-07 | Teijin Fibers Ltd | Flame-resistant polyester woven fabric, method for producing the same, and flame-resistant fiber product |
KR101164065B1 (en) | 2012-05-14 | 2012-07-12 | 한국니트산업연구원 | Human friendly fabric having frame retardance and processing method thereby |
WO2020238687A1 (en) * | 2019-05-27 | 2020-12-03 | 浙江海利得新材料股份有限公司 | Method for preparing high-strength flame-retardant dacron industrial yarn |
WO2020238688A1 (en) * | 2019-05-27 | 2020-12-03 | 浙江海利得新材料股份有限公司 | Preparation method for high-modulus, low-shrinkage and flame retardant polyester industrial filament |
-
2001
- 2001-10-18 JP JP2001320736A patent/JP2003129368A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007138359A (en) * | 2005-11-22 | 2007-06-07 | Teijin Fibers Ltd | Flame-resistant polyester woven fabric, method for producing the same, and flame-resistant fiber product |
KR101164065B1 (en) | 2012-05-14 | 2012-07-12 | 한국니트산업연구원 | Human friendly fabric having frame retardance and processing method thereby |
WO2020238687A1 (en) * | 2019-05-27 | 2020-12-03 | 浙江海利得新材料股份有限公司 | Method for preparing high-strength flame-retardant dacron industrial yarn |
WO2020238688A1 (en) * | 2019-05-27 | 2020-12-03 | 浙江海利得新材料股份有限公司 | Preparation method for high-modulus, low-shrinkage and flame retardant polyester industrial filament |
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