JPH0711565A - Ozone-containing liquid treating apparatus of fiber product - Google Patents

Ozone-containing liquid treating apparatus of fiber product

Info

Publication number
JPH0711565A
JPH0711565A JP5150486A JP15048693A JPH0711565A JP H0711565 A JPH0711565 A JP H0711565A JP 5150486 A JP5150486 A JP 5150486A JP 15048693 A JP15048693 A JP 15048693A JP H0711565 A JPH0711565 A JP H0711565A
Authority
JP
Japan
Prior art keywords
ozone
liquid
treatment
treated
fiber product
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.)
Withdrawn
Application number
JP5150486A
Other languages
Japanese (ja)
Inventor
Teruo Akashi
輝雄 明石
Akio Takeuchi
昭男 竹内
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP5150486A priority Critical patent/JPH0711565A/en
Publication of JPH0711565A publication Critical patent/JPH0711565A/en
Withdrawn legal-status Critical Current

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  • Treatment Of Fiber Materials (AREA)

Abstract

PURPOSE:To obtain an ozone treating apparatus of a fiber product having safety on environment and general-purpose properties and constructed so as to carry out uniform treatment in treating the fiber product in order to carry out scouring or bleaching or improve fiber performance such as pile resistance, shrink proofing property, dyeing properties and water absorption. CONSTITUTION:This ozone-containing liquid treating apparatus of a fiber product is provided with an injecting and mixing tool for injecting, mixing and dissolving an ozone-containing gas into a treating liquid, a holding tool 2 holding a fiber product 1 to be treated in laminated state and having fine holes through which a treating liquid can be passed and the fiber product to be treated can not be passed, a treating tank capable of packing a holding tool and the fiber product to be treated, a space part equipped with a circulating system for circulating a circulating system for circulating the ozone-containing liquid so as to pass the ozone-containing liquid through space among the fiber product to be treated, kept in laminated state and a pump 10 and collecting the waste ozone gas on the upper part of the treating tank, a gas-discharging pipe 15 for discharging the waste ozone gas from this space part out of the treating tank, a liquid-injecting pipe 8 for injecting the treating liquid into the treating tank and a discharge pipe 12 for discharging the treated waste liquid.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は繊維製品のオゾン含有液
による処理装置に関する。より詳しくは繊維製品のオゾ
ン含有液による精練、漂白又は抗ピル性、防縮性、染色
性、吸水性等の繊維性能の向上を目的として処理する装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating a textile product with an ozone-containing liquid. More specifically, it relates to an apparatus for treating textile products for the purpose of improving fiber performance such as scouring, bleaching or anti-pill property, shrinkproofing property, dyeing property and water absorption property with ozone-containing liquid.

【0002】[0002]

【従来の技術】従来、繊維製品のオゾンによる処理は種
々の目的のために研究されているが、種々の難点があ
り、実用化され難いのが実情である。種々の難点の内、
特記すべき事項は環境上安全で、汎用性に富み、均一な
処理加工性を有する処理装置が無い事である。
2. Description of the Related Art Conventionally, treatment of textiles with ozone has been studied for various purposes, but there are various difficulties and it is difficult to put them into practical use. Of the various difficulties,
What is worth mentioning is that there is no processing device that is environmentally safe, versatile, and has uniform processability.

【0003】特開昭49−41700号公報および特開
昭50−136477号公報には繊維製品の有機溶媒中
のオゾン処理についての開示があるが、有機溶媒からの
環境問題がある。特開昭50−136478号公報は、
被処理物を浸漬した水溶液中にオゾン含有気体を注入す
るのみで、均一な処理が行われ難いのは明白である。特
開平3−146094号公報および実開平3−8847
8号公報は、洗濯槽を使用し、水溶液中にオゾン含有気
体を注入し、繊維製品を攪拌処理するが、衣服等の限定
された形態の繊維製品のみの処理に関わり、且つ、大量
処理に適さない。
Japanese Patent Laid-Open No. 49-41700 and Japanese Patent Laid-Open No. 50-136477 disclose ozone treatment of a textile product in an organic solvent, but there are environmental problems caused by the organic solvent. Japanese Patent Laid-Open No. 50-136478 discloses
It is obvious that uniform treatment is difficult to perform only by injecting the ozone-containing gas into the aqueous solution in which the object to be treated is immersed. JP-A-3-146094 and Japanese Utility Model Laid-Open No. 3-8847.
No. 8 gazette uses a washing tub, injects an ozone-containing gas into an aqueous solution, and agitates a textile product, but is concerned with the treatment of only a limited form of textile products such as clothes, and for mass treatment. Not suitable.

【0004】特開平3−19961号公報は、ウールト
ップの処理で攪拌しているが、ピーカースケールの少量
処理故に処理出来るのであって、トップ形態の儘の攪拌
処理は出来ない。繊維製品の染色処理に先立ち、原綿ま
たは原毛からの不純物、紡績糸においては紡績油剤、編
織物においては編み立て油剤または糊剤が大量に付着し
ているから、精練または精練漂白を行う必要がある。
According to Japanese Patent Laid-Open No. 3-19961, the wool top is agitated, but it can be treated because of a small amount of peaker scale treatment, and cannot be agitated in the top form. Prior to dyeing of textile products, impurities from raw cotton or raw wool, spinning oil agent in spun yarn and knitting oil agent or sizing agent in knitted fabric are adhered in large quantities, so scouring or scouring bleaching is required. .

【0005】特開昭49−41700号公報、特開昭5
4−11381号公報、実開平2−1312670号公
報および実開平4−40772号公報は乾燥状態のオゾ
ン含有気体の処理であり、特開昭55−142759号
公報はオゾン含有気体とスチームの混合処理であり、ま
た特開昭50−126997号公報は繊維製品を水溶液
に含浸・搾液後オゾン含有気体中で処理を行う方法であ
り、いずれもオゾン処理後、別途、繊維製品に付着して
いる物質や、オゾン分解物質を除去するための他の機種
を使用した工程が必要であり、繁雑である。
JP-A-49-41700 and JP-A-5-41
No. 4-11381, Japanese Utility Model Laid-Open No. 2-1312670 and Japanese Utility Model Laid-Open No. 4-40772 deal with dry ozone-containing gas, and JP-A-55-142759 discloses mixed treatment of ozone-containing gas and steam. Japanese Patent Laid-Open No. 50-126997 discloses a method of impregnating an aqueous solution with an aqueous solution, squeezing it, and then treating it in an ozone-containing gas, both of which are separately attached to the textile after the ozone treatment. The process using other models for removing substances and ozone decomposing substances is required, which is complicated.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、繊維
製品のオゾンによる精練、漂白又は抗ピル性、防縮性、
染色性、吸水性等の繊維性能の向上を目的として処理す
るに、前記の特許公報の発明または考案の如き問題点、
即ち、環境上の安全性、非汎用性、処理の不均一性等の
難点を解消し、且つ、オゾン処理と同時に、オゾン分解
物質、水溶性物質等を除去し、次いで、同処理装置で染
色工程、その他の処理加工を行える様にした繊維製品の
オゾン処理装置を提供するにある。
DISCLOSURE OF THE INVENTION An object of the present invention is to scouring, bleaching or anti-pilling of textiles with ozone, shrinkproofing,
Dyeability, in treating for the purpose of improving the fiber performance such as water absorption, problems such as the invention or device of the above patent publication,
That is, the problems such as environmental safety, non-universality, and non-uniformity of treatment are eliminated, and at the same time as ozone treatment, ozone decomposing substances, water-soluble substances, etc. are removed and then dyed with the same treatment equipment. It is an object of the present invention to provide an ozone treatment device for textile products, which is capable of performing processes and other treatments.

【0007】[0007]

【課題を解決するための手段】すなわち、本発明は、オ
ゾン含有気体を処理液中に注入し、混合し、溶解する注
入混合具と、被処理繊維製品を積層状態に保持し、且
つ、上記処理液が通過する事が出来、上記被処理繊維製
品が通過する事が出来ない細孔を有する保持具と、上記
保持具と上記被処理繊維製品とを装填しうる処理槽と、
積層状態に保持された上記被処理繊維製品の空隙中をオ
ゾン含有液が通過する様、上記オゾン含有液を循環させ
る循環系統およびポンプを備え、上記処理槽上部に廃オ
ゾンガスを捕集する空間部と、この空間部から廃オゾン
ガスを上記処理槽外部に排出する排気管と、上記処理槽
に上記処理液を注入する注水管および処理廃液を排出す
る排水管を備えた繊維製品のオゾン含有液処理装置、で
ある。
That is, according to the present invention, an injection mixing tool for injecting, mixing, and dissolving an ozone-containing gas into a treatment liquid and a textile product to be treated are held in a laminated state, and A holder having a pore through which the treatment liquid can pass and the fiber product to be treated cannot pass through, and a treatment tank into which the holder and the fiber product to be treated can be loaded,
A space part for collecting waste ozone gas in the upper part of the processing tank, which is provided with a circulation system and a pump for circulating the ozone-containing liquid so that the ozone-containing liquid passes through the voids of the textile product to be treated held in a laminated state. And an ozone-containing liquid treatment of a textile product including an exhaust pipe for discharging waste ozone gas from the space to the outside of the treatment tank, a water injection pipe for injecting the treatment liquid into the treatment tank, and a drain pipe for discharging the treatment waste liquid Device.

【0008】本発明で言うオゾン含有気体とは、空気、
酸素富化空気または純酸素を原料とし、公知の方法、例
えば放電により原料中の酸素をオゾン化する事、により
得られたオゾンを含有する気体を言う。本発明で言う処
理液とは、処理の目的に応じた純水またはアルカリ、
酸、無機・有機薬品、繊維保護剤、反応促進剤等を溶
解、乳化、分解させた水を主体とした液状のもの(以下
水溶液と言う。)、または、これらの水溶液にオゾン含
有気体を注入、混合し、オゾンを溶解した水溶液(以
下、オゾン含有液と称する。)を言う。
The ozone-containing gas referred to in the present invention is air,
This is a gas containing ozone obtained by a known method using oxygen-enriched air or pure oxygen as a raw material, for example, by ozonizing oxygen in the raw material by electric discharge. The treatment liquid referred to in the present invention is pure water or alkali according to the purpose of treatment,
Liquid (mainly referred to as an aqueous solution) composed mainly of water obtained by dissolving, emulsifying, and decomposing an acid, an inorganic / organic chemical, a fiber protective agent, a reaction accelerator, or injecting an ozone-containing gas into these aqueous solutions. , And an aqueous solution in which ozone is dissolved (hereinafter referred to as an ozone-containing liquid).

【0009】オゾン含有気体は、斜流、軸流等のポンプ
類で循環する処理液に常圧または加圧状態で注入する。
オゾン含有気体の処理液への注入、混合および溶解は、
エジェクター、ディフューザ、散気盤、スタチックミキ
サー、ロータリーアトマイザー等の単独または組合せた
注入混合具を使用することが好ましい。本発明で言う繊
維製品とは、木綿、麻、羊毛、絹等の天然繊維、銅アン
モニアレーヨン、ビスコースレーヨン等のセルロース再
生繊維、ポリアクリル系、ポリアミド系、ポリエステル
系等の合成繊維からなる原綿、原毛、スライバー、ト
ウ、紡績糸、編織布、不織布及び上記繊維の混合された
混紡糸、交撚糸、交編織布等をいう。これらの繊維製品
は繊維製品の形態に従う保持具に積層状態に保持し、処
理槽に装填する。
The ozone-containing gas is injected into the processing liquid circulated by pumps such as oblique flow and axial flow under normal pressure or pressure.
Injection, mixing and dissolution of ozone-containing gas into the processing liquid
It is preferable to use an injection mixer such as an ejector, a diffuser, an air diffuser, a static mixer, or a rotary atomizer, either alone or in combination. The fiber product referred to in the present invention includes natural fibers such as cotton, hemp, wool and silk, cellulose regenerated fibers such as cuprammonium rayon and viscose rayon, and raw fibers made of synthetic fibers such as polyacrylics, polyamides and polyesters. , Fluff, sliver, tow, spun yarn, knitted fabric, non-woven fabric and mixed spun yarn in which the above fibers are mixed, mixed twisted yarn, mixed knitted woven fabric and the like. These fiber products are held in a laminated state on a holder according to the form of the fiber product and loaded into a processing tank.

【0010】繊維製品の形態に従う保持具および積層状
態とは、繊維製品が綿状または綛状であれば、処理液が
通過する事が出来、且つ、被処理繊維製品が通過する事
が出来ない細孔を、円筒状の同心円をなす内筒周面と外
筒周面に多数有し、内筒から外筒にわたる底面および上
面を有する保持具で、上面、底面、内筒および外筒に囲
まれた空間内に、繊維製品がランダムに、且つ、略均一
な充填密度で充填した状態を言う。
The holder and the laminated state according to the form of the fiber product means that the treatment liquid can pass and the fiber product to be treated cannot pass if the fiber product is cotton-like or crepe-like. A holder that has a large number of pores on the inner and outer peripheral surfaces of a cylindrical concentric circle and has a bottom surface and an upper surface that extend from the inner cylinder to the outer cylinder, and is surrounded by the upper surface, the bottom surface, the inner cylinder, and the outer cylinder. The state in which the fiber products are packed randomly and at a substantially uniform packing density in the filled space.

【0011】繊維製品がスライバーであれば、トップ状
の儘、上記保持具に充填する。繊維製品がトウであれ
ば、上記保持具内にトウを略均一な充填密度になる様に
振り落とし、上面を据える。繊維製品が編織布または不
織布であれは、処理液が通過する事が出来る細孔を周面
に多数有する円筒であって、円筒の周面の一端の細孔か
ら他端の細孔迄の距離が編織布または不織布の幅と略同
一となしえる保持具で、編織布又は不織布を円筒外周面
に、ロール状に巻く。
If the fiber product is a sliver, the top-shaped container is filled in the holder. If the fiber product is a tow, the tow is shaken off in the holder so as to have a substantially uniform packing density, and the upper surface is set. If the textile product is a woven or non-woven fabric, it is a cylinder having a large number of pores on the peripheral surface through which the treatment liquid can pass, and the distance from the pores at one end to the pores at the other end of the cylindrical peripheral surface. Is a holder that can be made substantially the same in width as the woven or non-woven fabric, and the woven or non-woven fabric is wound around the outer peripheral surface of the cylinder in a roll shape.

【0012】また、他の例の保持具および積層状態とし
て、本発明は処理液の通過のために多数の細孔を有する
管を保持具として、この保持具の外周面に一定の綾角度
および巻密度をもって、糸がコーン状またはチーズ状に
巻かれ積層された状態があり、この例の場合は、さらに
管が多段に積み重ねる事が出来る様に、且つ、処理液が
通過する事が出来る様に、管内部に支持具を使用する事
が出来る。
As another example of a holder and a laminated state, the present invention uses a tube having a large number of pores for passage of a treatment liquid as a holder, and the outer peripheral surface of the holder has a constant traverse angle and Depending on the winding density, there is a state in which threads are wound in a cone shape or cheese shape and laminated, and in this example, the pipes can be stacked in multiple stages and the processing liquid can pass through. In addition, a support can be used inside the pipe.

【0013】細孔は被処理繊維製品の形態に拠るが、円
形、楕円形、または方形いずれでもよいが、好ましくは
0.1〜1cm2 の円形で、且つ、細孔と、処理液が通
過する事が出来ない部分との面積比は1対2〜1対20
が良い。オゾン含有液および処理液に溶解されなかった
オゾン含有気体の1部の未溶解気体は保持具の管または
内筒の細孔を通過し、次いで繊維積層体の繊維間空隙を
通過するか、または逆に繊維積層体の外層から内層へ通
過する。
The pores may be circular, elliptical or rectangular, depending on the form of the fiber product to be treated, but preferably have a circular shape of 0.1 to 1 cm 2 , and the pores and the treatment liquid pass through. The area ratio with the part that cannot be done is 1: 2 to 1:20
Is good. The ozone-containing liquid and a part of the undissolved gas of the ozone-containing gas that has not been dissolved in the treatment liquid pass through the pores of the tube or inner cylinder of the holder, and then pass through the interfiber voids of the fiber laminate, or Conversely, it passes from the outer layer of the fiber laminate to the inner layer.

【0014】廃オゾンガスとは、処理槽上部にオゾン含
有気体の1部の未溶解気体、被処理繊維製品からのオゾ
ンによる分解物の気体およびオゾンの自己分解からの酸
素等を捕集したものをいう。処理槽上部には、廃オゾン
ガスを排出する気液分離用の空間部と排気管を設ける。
必要に応じて、排気管は廃オゾンガス中のオゾンを除去
するためのオゾン吸収または分解装置を経て大気中に排
出する事が出来る。または排気管より、乾燥装置、その
他のオゾン以外の物質を除去・吸着する装置等を経てオ
ゾン発生機に戻す事も出来る。
The waste ozone gas is a gas obtained by collecting a part of undissolved gas containing ozone in the upper part of the treatment tank, a gas of a decomposed product of ozone from the fiber product to be treated, and oxygen from self-decomposition of ozone. Say. A space for gas-liquid separation for discharging waste ozone gas and an exhaust pipe are provided above the processing tank.
If necessary, the exhaust pipe can be discharged into the atmosphere through an ozone absorbing or decomposing device for removing ozone in the waste ozone gas. Alternatively, it can be returned to the ozone generator through an exhaust pipe, a drying device, a device for removing and adsorbing substances other than ozone, and the like.

【0015】気液分離後の処理液は再びポンプ類で循環
し、オゾン含有気体を注入・混合・溶解し、保持具・繊
維積層体を通過し、気液分離の循環系統に希望する時間
中、継続出来る。この循環系統内に処理液の冷却または
加熱のために、熱交換機を設けるか、または直接、冷却
媒体または加熱媒体を注入する管、温度計、温度制御装
置、時間制御装置、処理槽内圧・処理液吐出圧・オゾン
注入圧等用の圧力計、発生オゾン・廃オゾン濃度計、オ
ゾン液濃度計、各種薬剤の処理槽への注入・投入用付属
槽を設けることが出来る。
The treated liquid after gas-liquid separation is circulated again by pumps, the ozone-containing gas is injected / mixed / dissolved, passes through the holder / fiber laminate, and is passed through the gas-liquid separation circulation system for a desired time. , You can continue. In order to cool or heat the processing liquid in this circulation system, a heat exchanger is provided, or a pipe for directly injecting a cooling medium or a heating medium, a thermometer, a temperature control device, a time control device, a treatment tank internal pressure / treatment It is possible to provide a pressure gauge for liquid discharge pressure, ozone injection pressure, etc., a generated ozone / waste ozone concentration meter, an ozone liquid concentration meter, and an auxiliary tank for injecting / injecting various chemicals into the processing tank.

【0016】本発明の装置は、オゾンを取り扱うため、
テフロン、塩化ポリビニール、ポリプロピレン、ポリエ
チレン、アルミニューム、ステンレス・スチール等のオ
ゾンに対して反応しない機密性のある材料が良い。処理
目的に応じ、オゾン含有液のオゾン濃度を高濃度に保つ
必要のある場合、またはオゾン処理前後工程において、
高温・高圧の処理を行う場合のために、好ましくは耐圧
性であるステンレス・スチール製が良い。
Since the device of the present invention handles ozone,
Teflon, polyvinyl chloride, polypropylene, polyethylene, aluminum, stainless steel, and other sensitive materials that do not react with ozone are good. Depending on the purpose of the treatment, if it is necessary to keep the ozone concentration of the ozone-containing liquid at a high concentration, or before or after the ozone treatment,
For high temperature and high pressure processing, stainless steel, which is pressure resistant, is preferable.

【0017】[0017]

【作用】処理液が積層状態の被処理繊維製品の繊維空隙
を通過するため乱流となり、そのために、注入混合具の
みでは未溶解であった発生オゾンの1部のオゾンが繊維
空隙を通過中、随時溶解し、オゾン含有液のオゾン濃度
を高め、また、被処理繊維製品により消費されたオゾン
に見合ったオゾンが随時溶解し、繊維積層体の内層・中
層・外層共に同一オゾン濃度で処理されるため、本発明
の1目的である処理の均一性が達成出来るものと推定す
る。
The treatment liquid becomes a turbulent flow because it passes through the fiber voids of the laminated fiber product to be treated, and as a result, a part of the generated ozone which was not dissolved by the injection mixer alone is passing through the fiber voids. , It is dissolved at any time to increase the ozone concentration of the ozone-containing liquid, and the ozone that is commensurate with the ozone consumed by the textile product to be treated is dissolved at any time, and the inner layer, middle layer and outer layer of the fiber laminate are treated with the same ozone concentration. Therefore, it is presumed that the uniformity of processing, which is one of the objects of the present invention, can be achieved.

【0018】[0018]

【実施例】以下、図1を用いて、実施例で、より詳細に
説明するが、本発明はこれに限定されない。なお、実施
例中%は被処理繊維に対する重量%である。ピリング性
はJISL1076A法、判定標準写真3を使用した。
EXAMPLES Hereinafter, the present invention will be described in more detail with reference to FIG. 1, but the present invention is not limited thereto. In the examples,% means weight% with respect to the fiber to be treated. For the pilling property, JISL1076A method and judgment standard photograph 3 were used.

【0019】[0019]

【実施例1】番手2/48の羊毛糸を12ゲージの編機
で、密度が24/インチ、コース、18/インチ・ウエ
ル、幅が15cm、長さが20mの編地を編成した。円
筒の一端及び他端から1.5cmの間に直径4mmの細
孔3を有し、この間の細孔の面積と、細孔でない部分の
面積の比が1対4である外直径7cm、長さ17cmの
円筒2を保持具とし、上記編地で、細孔を全て覆う様に
ロール状に巻き、積層状の被処理繊維製品1とした。層
の厚さは5.2cmである。
Example 1 A knitted fabric having a density of 24 / inch, a course, an 18 / inch well, a width of 15 cm, and a length of 20 m was knitted with a 12-gauge knitting machine using a yarn of 2/48 count. An outer diameter of 7 cm, which has pores 3 having a diameter of 4 mm between one end and the other end of the cylinder and having a diameter of 4 mm, and the ratio of the area of the pores to the area of the non-pores is 1: 4 A cylinder 2 having a length of 17 cm was used as a holder, and the knitted fabric was wound in a roll shape so as to cover all the pores to obtain a laminated fiber product 1 to be treated. The layer thickness is 5.2 cm.

【0020】保持具及び繊維積層体を処理槽4に保持具
の固定のための支持具5及び6を使用し装填し、蓋7で
密閉し、純水を注水管8で液比(被処理繊維重量対液重
量)が1対12となる様に、液面17迄、注入し、付属
槽9よりスコアロール400(花王(株)製、非イオン
界面活性剤)を0.5g/リットルになる様に注入し、
ポンプ10を液流が循環経路を示す矢印方向で、且つ、
流量が30リットル/分になる様に稼働させた。熱交換
機11で液温度を50℃とし、10分間処理後、排水管
12で排液した。
The holder and the fiber laminate were loaded into the treatment tank 4 by using the supports 5 and 6 for fixing the holder, and the lid was closed with a lid 7, and pure water was introduced into a water injection pipe 8 to obtain a liquid ratio (treatment target). (Fiber weight to liquid weight) becomes 1 to 12, and liquid is injected up to the liquid surface 17, and score roll 400 (manufactured by Kao Corporation, nonionic surfactant) is adjusted to 0.5 g / liter from the auxiliary tank 9. To inject
The pump 10 in the direction of the arrow in which the liquid flow indicates the circulation path, and
It was operated so that the flow rate was 30 liters / minute. The temperature of the liquid was adjusted to 50 ° C. by the heat exchanger 11, and after the treatment for 10 minutes, the liquid was discharged through the drain pipe 12.

【0021】次いで、純水を液比が1対12になる様に
注入し、上記同様ポンプを稼働しつつ、水溶液のPHが
4.0となる迄、濃硫酸を徐々に注入した。液温度は2
5℃である。次いで、純酸素を使用し、放電によるオゾ
ン発生機13からのオゾン濃度3万ppm、流量2リッ
トル/分のオゾン含有気体を、ゲージ圧1.0kgf/
cm2 で、ノズル14より水溶液に注入した。
Next, pure water was injected so that the liquid ratio became 1:12, and concentrated sulfuric acid was gradually injected until the pH of the aqueous solution reached 4.0 while operating the pump in the same manner as above. Liquid temperature is 2
It is 5 ° C. Next, pure oxygen is used, and an ozone-containing gas from the ozone generator 13 by discharge has an ozone concentration of 30,000 ppm and a flow rate of 2 liters / minute, and a gauge pressure of 1.0 kgf /
It was injected into the aqueous solution from the nozzle 14 at a cm 2 .

【0022】注入5分後の処理液のオゾン濃度は15.
1mg/リットルで、この濃度を維持すべくオゾン含有
気体を10分間注入し、計15分間処理し排液した。オ
ゾン処理中、廃オゾンガスは処理槽上部の空間部18に
捕集され、排気管15を経て、活性炭を使用した廃オゾ
ンガス処理装置16で処理後大気中に排出した。オゾン
処理を行った羊毛糸を水洗し、次いで商品名ラニールレ
ッドGG、2.0%及び商品名スミポンWB、2.0%
(ともに、住友化学工業(株)製、染料及び助剤)、硫
安、2.0%、酢酸でPH4.0とした水溶液で、流量
30リットル/分で昇温し、100℃、40分間染色
し、後、冷却、水洗し、処理槽より保持具及び編地を取
り出し脱水、乾燥した。均一に染色され、いずれの箇所
の編地もピリング性は4級であった。
The ozone concentration of the treatment liquid 5 minutes after the injection was 15.
At 1 mg / liter, ozone-containing gas was injected for 10 minutes to maintain this concentration, treated for a total of 15 minutes, and drained. During the ozone treatment, the waste ozone gas was collected in the space 18 above the treatment tank, passed through the exhaust pipe 15, and was discharged into the atmosphere after being treated by the waste ozone gas treatment device 16 using activated carbon. Ozone-treated wool yarn is washed with water, and then trade name Ranille Red GG, 2.0% and trade name Sumipon WB, 2.0%
(Both manufactured by Sumitomo Chemical Co., Ltd., dyes and auxiliaries), ammonium sulfate, 2.0%, an aqueous solution of pH 4.0 with acetic acid, heated at a flow rate of 30 liters / minute, and dyed at 100 ° C. for 40 minutes. Then, after cooling and washing with water, the holder and the knitted fabric were taken out from the treatment tank, dehydrated and dried. The knitted fabric was dyed uniformly, and the pilling property of the knitted fabric at any position was grade 4.

【0023】[0023]

【比較例1】オゾン含有気体を注入しない以外は、実施
例1と同様の処理を行った編地のピリング性は1級であ
った。
Comparative Example 1 The pilling property of the knitted fabric which was treated in the same manner as in Example 1 except that the ozone-containing gas was not injected was of the first grade.

【0024】[0024]

【実施例2】実施例1と同一の羊毛糸1.0kgを、上
外径が4.0cm、下外径が7.0cmのコーン状であ
る事以外は、実施例1と同様の保持具に、巻密度が0.
3g/cm3 になる様に巻き、実施例1と同様の非イオ
ン界面活性剤処理、濃硫酸注入PH調整処理及びオゾン
処理を行い、脱水し、乾燥した。次いで、実施例1と同
様の編地をコーン状の内層、中層、外層毎に編成し、ピ
リング性を測定した結果、いずれも4級であった。
Example 2 A holder similar to that of Example 1 except that 1.0 kg of the same wool yarn as in Example 1 is used in a cone shape having an upper outer diameter of 4.0 cm and a lower outer diameter of 7.0 cm. And the winding density is 0.
It was wound so as to have a weight of 3 g / cm 3 , and the same nonionic surfactant treatment, concentrated sulfuric acid injection pH adjustment treatment and ozone treatment as in Example 1 were performed, dehydrated and dried. Then, a knitted fabric similar to that of Example 1 was knitted for each of the cone-shaped inner layer, middle layer, and outer layer, and the pilling property was measured.

【0025】[0025]

【比較例2】実施例2と同一の保持具及び被処理繊維積
層体を、実施例2と同一の非イオン界面活性剤処理及び
濃硫酸注入PH調整処理後、保持具及び被処理繊維積層
体を処理層より取り出し、脱水した。脱水液を処理槽に
戻し、水溶液を循環しつつ、オゾン含有気体を注入し、
処理液のオゾン濃度が15.1mg/リットルに達した
時点で、保持具及び被処理繊維積層体を処理槽に装填し
た。
[Comparative Example 2] The same holder and treated fiber laminate as in Example 2 were subjected to the same nonionic surfactant treatment and concentrated sulfuric acid injection pH adjustment treatment as in Example 2, and then the holder and treated fiber laminate. Was taken out from the treated layer and dehydrated. Return the dehydrated liquid to the processing tank, inject the ozone-containing gas while circulating the aqueous solution,
When the ozone concentration of the treatment liquid reached 15.1 mg / liter, the holder and the fiber laminate to be treated were loaded into the treatment tank.

【0026】但し、ポンプを稼働させても、処理液及び
処理液に未溶解のオゾン含有気体の1部が繊維積層体の
繊維間空隙を通過し難い様に、支持具の一部をなす保持
具の上部の蓋6を解放し、この部分より処理液及び処理
液に未溶解のオゾン含有気体の1部が通過し循環する様
に装填した。次いで、処理液のオゾン濃度が15.1m
g/リットルを保持する様に、オゾン含有気体を注入し
つつ、15分間のオゾン処理を行い、脱水、乾燥した。
実施例2と同様の編地をコーン状の各層毎に編成し、ピ
リング性を測定した結果、最外層は4級であったが、他
の層は2級で効果は低かった。
However, even if the pump is operated, the treatment liquid and a part of the ozone-containing gas that is not dissolved in the treatment liquid do not easily pass through the inter-fiber voids of the fiber laminate, so that the holding liquid forms part of the support. The lid 6 on the upper part of the tool was opened, and the treatment liquid and a part of the ozone-containing gas undissolved in the treatment liquid passed from this portion and were charged so as to circulate. Then, the ozone concentration of the treatment liquid is 15.1 m
While injecting an ozone-containing gas so as to maintain g / l, ozone treatment was performed for 15 minutes, followed by dehydration and drying.
The same knitted fabric as in Example 2 was knitted into each of the cone-shaped layers and the pilling property was measured. As a result, the outermost layer was grade 4, but the other layers were grade 2, and the effect was low.

【0027】[0027]

【発明の効果】本発明の装置によれば、従来のものに比
べて、有機溶媒を使用せず、水溶液を媒体としたオゾン
処理が可能で、環境上の安全が確保出来る。実施例1で
示した様に、同一処理機でオゾン処理前後工程が行え、
汎用性がある。また、従来の技術例の如き、被処理繊維
製品またはオゾン含有液の攪拌によるオゾン処理でない
ため、保持具及び保持具の支持具の交換により、繊維形
態にとらわれずに、綿状、トウ状、トップ形態の繊維製
品も、同一処理機でのオゾン処理が可能で汎用性があ
る。
According to the apparatus of the present invention, compared with the conventional apparatus, it is possible to perform ozone treatment using an aqueous solution as a medium without using an organic solvent, and to ensure environmental safety. As shown in Example 1, before and after the ozone treatment can be performed in the same treatment machine,
It is versatile. Further, as in the conventional technology example, since it is not an ozone treatment by stirring the textile product to be treated or the ozone-containing liquid, by exchanging the holder and the support of the holder, without being restricted to the fiber form, cotton-like, tow-like, Even top-shaped textile products can be treated with ozone using the same processing machine and are versatile.

【0028】実施例では約1kgの小型試験機での結果
であるが、繊維積層体の繊維間空隙を強制的にオゾン含
有液を通過させている事から、大型化しても同様の効果
が得られる。実施例2と比較例2で判る様に、1kgの
繊維製品のオゾン処理で、単なるオゾン含有液の攪拌の
みでは均一な処理は困難であるが、本発明の装置で均一
なオゾン処理が可能となる。
In the examples, the results are obtained with a small tester of about 1 kg, but since the ozone-containing liquid is forced to pass through the interfiber spaces of the fiber laminate, the same effect can be obtained even if the size is increased. To be As can be seen in Example 2 and Comparative Example 2, it is difficult to uniformly treat the 1 kg of textile product with ozone simply by stirring the ozone-containing liquid, but the apparatus of the present invention enables uniform ozone treatment. Become.

【0029】また、他の技術例の、繊維製品を処理液に
含浸し、絞液し、処理液を保持した状態でのオゾン含有
気体による処理方法は、処理液が繊維表面を移動しない
ため反応速度は気・液・固体界面の境膜抵抗に大きく関
わるが、本発明の装置によれば、繊維表面のオゾン含有
液を乱流とする事が可能で、従って、反応速度を早める
事が可能で、且つ、同時に繊維表面からオゾン分解物質
及び水溶性物質等を除去出来る。
Further, in another method of treating a fiber product with an ozone-containing gas in which the textile product is impregnated in the treatment liquid, squeezed, and the treatment liquid is held, the treatment liquid does not move on the surface of the fiber. Although the velocity is largely related to the boundary film resistance at the gas / liquid / solid interface, the device of the present invention can make the ozone-containing liquid on the fiber surface into a turbulent flow, and thus can accelerate the reaction rate. At the same time, ozone decomposing substances and water-soluble substances can be removed from the fiber surface at the same time.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例の概念を模式的に示す断面図FIG. 1 is a sectional view schematically showing the concept of an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 被処理繊維製品 2 円筒形保持具 3 保持具の有する細孔 4 処理槽 5 保持具の固定用支持具 6 保持具の固定用支持具 7 蓋 8 注水管 9 付属槽 10 ポンプ 11 熱交換機 12 排水管 13 オゾンの発生機 14 オゾン注入用ノズル 15 排気管 16 廃オゾンガス処理装置 17 液面 18 空間部 DESCRIPTION OF SYMBOLS 1 Textile product to be treated 2 Cylindrical holder 3 Pore possessed by holder 4 Treatment tank 5 Support for fixing holder 6 Support for fixing holder 7 Lid 8 Water injection pipe 9 Attached tank 10 Pump 11 Heat exchanger 12 Drain pipe 13 Ozone generator 14 Ozone injection nozzle 15 Exhaust pipe 16 Waste ozone gas treatment device 17 Liquid level 18 Space

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 オゾン含有気体を処理液中に注入し、混
合し、溶解する注入混合具と、被処理繊維製品を積層状
態に保持し、且つ、処理液が通過する事が出来、被処理
繊維製品が通過する事が出来ない細孔を有する保持具
と、保持具と被処理繊維製品とを装填しうる処理槽と、
積層状態に保持された被処理繊維製品の空隙中をオゾン
含有液が通過する様、オゾン含有液を循環させる循環系
統およびポンプを備え、処理槽上部に廃オゾンガスを捕
集する空間部と、この空間部から廃オゾンガスを処理槽
外部に排出する排気管と、処理槽に処理液を注入する注
水管および処理廃液を排出する排水管を備えた繊維製品
のオゾン含有液処理装置。
1. An injecting and mixing tool for injecting, mixing, and dissolving an ozone-containing gas in a treatment liquid and a textile product to be treated are kept in a laminated state, and the treatment liquid can pass therethrough. A holder having pores through which the fiber product cannot pass, a treatment tank in which the holder and the fiber product to be treated can be loaded,
A space system for collecting waste ozone gas in the upper part of the processing tank, which is equipped with a circulation system and a pump for circulating the ozone-containing liquid so that the ozone-containing liquid passes through the voids of the processed textile products held in a laminated state, An ozone-containing liquid treatment device for a textile product, comprising an exhaust pipe for discharging waste ozone gas from the space to the outside of the treatment tank, a water injection pipe for injecting the treatment liquid into the treatment tank, and a drain pipe for discharging the treatment waste liquid.
JP5150486A 1993-06-22 1993-06-22 Ozone-containing liquid treating apparatus of fiber product Withdrawn JPH0711565A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5150486A JPH0711565A (en) 1993-06-22 1993-06-22 Ozone-containing liquid treating apparatus of fiber product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5150486A JPH0711565A (en) 1993-06-22 1993-06-22 Ozone-containing liquid treating apparatus of fiber product

Publications (1)

Publication Number Publication Date
JPH0711565A true JPH0711565A (en) 1995-01-13

Family

ID=15497932

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5150486A Withdrawn JPH0711565A (en) 1993-06-22 1993-06-22 Ozone-containing liquid treating apparatus of fiber product

Country Status (1)

Country Link
JP (1) JPH0711565A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1072762A (en) * 1996-08-23 1998-03-17 Oshima Kikai Kk Modification of fiber with ozone
JP2002105844A (en) * 2000-09-21 2002-04-10 Inamoto Seisakusho:Kk Processing equipment for stabilizing morphology of textile product and method of processing
WO2003097916A1 (en) * 2002-05-17 2003-11-27 Howa Kabushiki Kaisha Textile product decoloring device and decoloring method
WO2008105108A1 (en) * 2007-02-27 2008-09-04 Shigenori Aono Process for production of bleached textile materials, equipment to be used in the process, and bleached textile materials obtained by the process
WO2008105132A1 (en) * 2007-02-27 2008-09-04 Shigenori Aono Process for producing bleached fiber product, apparatus for use therein, and thus obtained bleached fiber product
CN110926252A (en) * 2019-11-16 2020-03-27 山东明福染业有限公司 Heat energy recovery device and heat energy recovery process for dyeing waste liquid

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1072762A (en) * 1996-08-23 1998-03-17 Oshima Kikai Kk Modification of fiber with ozone
JP2002105844A (en) * 2000-09-21 2002-04-10 Inamoto Seisakusho:Kk Processing equipment for stabilizing morphology of textile product and method of processing
JP4490567B2 (en) * 2000-09-21 2010-06-30 株式会社稲本製作所 Textile product shape stabilization processing apparatus and processing method
WO2003097916A1 (en) * 2002-05-17 2003-11-27 Howa Kabushiki Kaisha Textile product decoloring device and decoloring method
US7252688B2 (en) 2002-05-17 2007-08-07 Howa Kabushiki Kaisha Decolorization apparatus and decolorization method for textile product
WO2008105108A1 (en) * 2007-02-27 2008-09-04 Shigenori Aono Process for production of bleached textile materials, equipment to be used in the process, and bleached textile materials obtained by the process
WO2008105132A1 (en) * 2007-02-27 2008-09-04 Shigenori Aono Process for producing bleached fiber product, apparatus for use therein, and thus obtained bleached fiber product
JP2008240224A (en) * 2007-02-27 2008-10-09 Shigenori Aono Method for producing bleached textile product and equipment to be used in the method
US8486225B2 (en) 2007-02-27 2013-07-16 Shigenori Aono Bleached fiber product production method, apparatus to be used therefor, and bleached fiber product produced thereby
CN110926252A (en) * 2019-11-16 2020-03-27 山东明福染业有限公司 Heat energy recovery device and heat energy recovery process for dyeing waste liquid

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