JP2006104626A - Textile cleaning method and textile treating apparatus used therefor - Google Patents

Textile cleaning method and textile treating apparatus used therefor Download PDF

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JP2006104626A
JP2006104626A JP2004295212A JP2004295212A JP2006104626A JP 2006104626 A JP2006104626 A JP 2006104626A JP 2004295212 A JP2004295212 A JP 2004295212A JP 2004295212 A JP2004295212 A JP 2004295212A JP 2006104626 A JP2006104626 A JP 2006104626A
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liquid
treatment
processing
tank
temperature
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JP4562484B2 (en
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Toru Shimizu
徹 清水
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Hisaka Works Ltd
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Hisaka Works Ltd
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Priority to JP2004295212A priority Critical patent/JP4562484B2/en
Priority to PCT/JP2005/018659 priority patent/WO2006038696A1/en
Priority to US11/664,897 priority patent/US20090013479A1/en
Priority to CNB200580033323XA priority patent/CN100567612C/en
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B23/00Component parts, details, or accessories of apparatus or machines, specially adapted for the treating of textile materials, not restricted to a particular kind of apparatus, provided for in groups D06B1/00 - D06B21/00
    • D06B23/20Arrangements of apparatus for treating processing-liquids, -gases or -vapours, e.g. purification, filtration or distillation
    • D06B23/22Arrangements of apparatus for treating processing-liquids, -gases or -vapours, e.g. purification, filtration or distillation for heating
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B3/00Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating
    • D06B3/28Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of fabrics propelled by, or with the aid of, jets of the treating material

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Treatment Of Fiber Materials (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a textile cleaning method by which a textile is effectively cleaned in a shorter time in a treatment method using a treatment apparatus of a type such as a liquid stream treatment apparatus, etc., for circulating a treatment liquid and treating a textile and a textile treating apparatus used therefor. <P>SOLUTION: The method comprises putting a fabric 1 in a treatment tank 4, bringing the fabric into contact with a high-temperature treatment liquid circulating the inside and outside of the treatment tank 4 so as to treat the fabric 1 and then cleaning the fabric with cleaning water. After treatment by the high-temperature treatment liquid, the high-temperature treatment liquid is gradually discharged from the treatment tank 4 and cleaning water is gradually fed to the treatment tank 4. In the operation, the high-temperature treatment liquid to be discharged is subjected to heat exchange with the cleaning water to be supplied, the discharged amount of the high-temperature treatment liquid is made equal to the supplied amount of the cleaning water and the liquid amount in the treatment tank 4 is constantly kept. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、布帛等の繊維品に対し染色その他の処理を行った後の洗浄方法およびそれに用いる繊維品の処理装置に関するものである。   The present invention relates to a cleaning method after dyeing and other treatments for textiles such as fabrics, and a textile processing apparatus used therefor.

繊維品に対する染色等の処理を行う装置として、例えば図4に示すような液流処理装置が汎用されている。この装置は、布帛1の滞留部2と、この滞留部2と布帛1の移送通路3とを接続した環状の処理槽4とを備えている。そして、上記滞留部2の底部に設けられた処理液吸い込み部5(この図では3個所)から処理液を吸い込み、循環ポンプ6、熱交換器7を介して、所定温度にコントロールされた処理液(通常、その最高温度は100℃以上の高温に設定される)を上記移送通路3の一端に付設された処理液噴射部8に還流させ、その液流で布帛1を移送しながら処理を行うようになっている。   For example, a liquid flow processing apparatus as shown in FIG. 4 is widely used as an apparatus for performing processing such as dyeing on textiles. This apparatus includes a staying portion 2 of the fabric 1 and an annular treatment tank 4 connecting the staying portion 2 and the transfer passage 3 of the fabric 1. Then, the processing liquid is sucked in from the processing liquid suction section 5 (three places in this figure) provided at the bottom of the retention section 2, and the processing liquid is controlled to a predetermined temperature via the circulation pump 6 and the heat exchanger 7. (Usually, the maximum temperature is set to a high temperature of 100 ° C. or higher) is returned to the treatment liquid ejecting section 8 attached to one end of the transfer passage 3, and the treatment is performed while the fabric 1 is transferred by the liquid flow. It is like that.

このような液流処理において、処理が完了した時点での処理液には、各種の染料その他の薬品、助剤等が残留している。また、布帛1から発生する、繊維重合時の生成物であるオリゴマーや毛羽、スケール等も含有されている。   In such a liquid flow treatment, various dyes, other chemicals, auxiliaries, etc. remain in the treatment liquid when the treatment is completed. Moreover, the oligomer, fluff, scale, etc. which are the products at the time of fiber polymerization generated from the fabric 1 are also contained.

このため、例えばポリエステル濃色染色等を実施する場合、上記処理の終了後、熱交換器7に冷却水を通して処理液の温度を下げながら処理液を循環させ、処理液が80℃前後に下がった時点で、その温度を保ちながら、ハイドロサルファイトやアルカリ剤(苛性ソーダやソーダ灰等)を処理槽4内に注入して上記残留物等を還元処理する、いわゆる「還元洗浄」を行っている。そして、上記還元洗浄後、再度処理液を60℃前後に冷却したのち処理液を排出し、洗浄水(通常、水)の給水、水洗、排水を複数回繰り返して繊維品の洗浄を行ったのち、繊維品を処理槽4内から取り出すようにしている。   For this reason, for example, when polyester deep color dyeing or the like is performed, the treatment liquid is circulated while lowering the temperature of the treatment liquid through the cooling water through the heat exchanger 7 after the treatment is completed, and the treatment liquid is lowered to about 80 ° C. At that time, while maintaining the temperature, so-called “reduction cleaning” is performed in which hydrosulfite or an alkaline agent (caustic soda, soda ash, or the like) is injected into the treatment tank 4 to reduce the residue or the like. After the reduction cleaning, the processing liquid is cooled again to around 60 ° C., and then the processing liquid is discharged. After the cleaning of the textiles by repeating the supply of cleaning water (usually water), rinsing and draining a plurality of times, The fiber product is taken out from the treatment tank 4.

しかしながら、上記洗浄方法では、洗浄に時間がかかるとともに、冷却時の温度勾配がスムーズにならず、繊維品にシワ等が生じて得られる繊維品の品質が低下する場合があり、問題となっている。また、高温で溶解していたオリゴマー等が、冷却によって再析出して処理槽4内に残留付着するため、いわゆる釜洗処理を頻繁に行わなければならず、煩雑であるという問題もある。したがって、これらの問題の解決が強く望まれている。   However, in the above cleaning method, cleaning takes time, the temperature gradient during cooling is not smooth, and the quality of the fiber product obtained by causing wrinkles or the like in the fiber product may be deteriorated, which is a problem. Yes. Moreover, since the oligomer etc. which were melt | dissolved at high temperature reprecipitate by cooling, and remain | survive and adhere in the processing tank 4, what is called a kettle washing process must be performed frequently and there also exists a problem that it is complicated. Therefore, it is strongly desired to solve these problems.

ところで、本出願人は、処理液と気流との気液混合流体を繊維品に噴射させて処理槽内を循環移動させながら処理を行う気流処理装置において、上記処理液を高温で排出し、かつその処理排水と熱交換しながら洗浄水を供給する全く新しい洗浄方法を提案し、すでに実用化している(特許文献1参照)。
特開平8−269863号公報
By the way, the present applicant, in the airflow treatment apparatus that performs the treatment while injecting the gas-liquid mixed fluid of the treatment liquid and the airflow to the textile and circulatingly moving the inside of the treatment tank, discharges the treatment liquid at a high temperature, and A completely new cleaning method for supplying cleaning water while exchanging heat with the treated waste water has been proposed and already put into practical use (see Patent Document 1).
JP-A-8-269863

そこで、上記気流処理装置における洗浄方法を、液流処理装置に適用することが考えられるが、気流処理装置は、用いる処理液量が少量で、装置構成も異なることから、上記洗浄方法をそのまま液流処理装置に適用することは、難しいことが判明した。   Therefore, it is conceivable to apply the cleaning method in the airflow processing apparatus to the liquid flow processing apparatus. However, since the airflow processing apparatus uses a small amount of processing liquid and the apparatus configuration is different, the cleaning method is used as it is. It has proven difficult to apply to flow treatment equipment.

本発明は、このような事情に鑑みなされたもので、液流処理装置等、処理液を循環させて繊維品を処理するタイプの処理装置を用いた処理方法において、より短時間で効果的な洗浄処理を行うことのできる繊維品の洗浄方法と、それに用いる繊維品の処理装置の提供をその目的とする。   The present invention has been made in view of such circumstances, and is effective in a shorter time in a processing method using a processing apparatus of a type that circulates a processing liquid and processes a fiber product, such as a liquid flow processing apparatus. It is an object of the present invention to provide a method for cleaning a fiber product that can be subjected to a cleaning process, and a fiber product processing apparatus used therefor.

上記の目的を達成するため、本発明は、繊維品を処理槽内に装填し、処理槽内外を循環する高温処理液と上記繊維品とを接触させることにより繊維品を処理し、ついで洗浄水による洗浄を行う方法であって、上記高温処理液による処理終了後、上記高温処理液を処理槽内から徐々に排出するとともに洗浄水を処理槽内に徐々に供給し、その際、排出される高温処理液と供給する洗浄水とを熱交換し、かつ上記高温処理液の排出量と洗浄水の供給量を等量にして処理槽内の液量が一定に保たれるようにした繊維品の洗浄方法を第1の要旨とする。   In order to achieve the above object, the present invention loads a fiber product into a treatment tank, treats the fiber product by bringing the high-temperature treatment liquid circulating inside and outside the treatment tank into contact with the fiber product, and then washing water. After the treatment with the high-temperature treatment liquid is completed, the high-temperature treatment liquid is gradually discharged from the treatment tank and the cleaning water is gradually supplied into the treatment tank, and is discharged at that time. Heat exchange between the high temperature treatment liquid and the supplied wash water, and the amount of discharge of the high temperature treatment liquid is equal to the supply amount of the wash water so that the amount of liquid in the treatment tank is kept constant. This cleaning method is the first gist.

また、本発明は、そのなかでも、特に、上記高温処理液の排出と洗浄水の供給により、処理槽内の液が所定温度域まで下がった時点で、洗浄水を高温処理液と熱交換することなく直接処理槽内に供給して洗浄を行う繊維品の洗浄方法を第2の要旨とする。   In addition, the present invention exchanges heat of the cleaning water with the high temperature processing liquid particularly when the liquid in the processing tank is lowered to a predetermined temperature range by discharging the high temperature processing liquid and supplying the cleaning water. The second gist is a method for washing a fiber product that is supplied directly into the treatment tank and washed.

さらに、本発明は、上記第1または第2の要旨である繊維品の洗浄方法に用いられる繊維品の処理装置であって、繊維品を装填して処理液と接触させる処理槽と、上記処理槽内の処理液を処理槽外に取り出し循環ポンプおよび熱交換器を経由して上記処理槽内に繰り返し供給する処理液循環路とを備え、上記処理液循環路の循環ポンプ吸い込み側に接続され上記処理槽内の処理液を一部取り出して排出する処理液排出配管と、同じく上記処理液循環路の循環ポンプ吸い込み側であって上記処理液排出配管接続部より下流側に接続され洗浄水を上記処理液循環路内に供給する洗浄水供給配管と、上記処理液排出配管を通過する処理液と洗浄水供給配管を通過する洗浄水とを熱交換する熱交換器とが設けられ、上記処理液排出配管から排出される処理液量と上洗浄水供給配管から供給される洗浄水量とが、互いに等量となるよう制御されるようになっている繊維品の処理装置を第3の要旨とする。   Furthermore, the present invention is a textile processing apparatus used in the textile cleaning method according to the first or second aspect, wherein the textile tank is loaded with the processing tank and brought into contact with the processing liquid, and the above processing. A treatment liquid circulation path that takes out the treatment liquid in the tank from the treatment tank and repeatedly supplies it into the treatment tank via a circulation pump and a heat exchanger, and is connected to the circulation pump suction side of the treatment liquid circulation path. A processing liquid discharge pipe for taking out and discharging a part of the processing liquid in the processing tank, and a cleaning pump connected to the circulating pump suction side of the processing liquid circulation path and downstream from the processing liquid discharge pipe connection portion. A cleaning water supply pipe for supplying the processing liquid circulation path, a heat exchanger for exchanging heat between the processing liquid passing through the processing liquid discharge pipe and the cleaning water passing through the cleaning water supply pipe are provided, Discharged from the liquid discharge pipe A cleaning water supplied from the physical fluid volume and the upper washing water supply pipe, and in that processor of the third aspect of textiles adapted to be controlled to be equal amounts from each other.

すなわち、本発明の繊維品の洗浄方法は、処理に用いた高温処理液を、高温のまま排出し、その際、洗浄のために処理槽内に供給される洗浄水と熱交換するようになっているため、洗浄時の温度が従来に比べて格段に高くなり、優れた洗浄効果を奏する。したがって、高温の洗浄水排出後に繰り返す水洗の回数を、従来に比べて減らすことができる。また、処理液を高温のまま排出するため、オリゴマーや染料残留物等が処理液中に溶解した状態で除去されることになり、従来のポリエステル濃色染色等において必要であった還元洗浄処理を省略することができる。したがって、上記還元洗浄処理において昇温に用いられる蒸気や薬剤が不要となり、コストの低減化を図ることができる。そして、上記オリゴマーや染料残留物等が処理槽の内壁等に付着して残留する量が少なくなるため、処理槽を定期的に洗浄する等のメンテナンスにおける負担が軽減されるという利点を有する。しかも、高温処理液の排出量と洗浄水の供給量を、互いに等量となるよう制御するため、染色等の処理から洗浄処理に移行しても、処理槽内を循環する液量が一定に保たれることとなり、繊維品に負担がかからず良好な仕上がりとなる。   That is, in the method for cleaning a textile product of the present invention, the high-temperature treatment liquid used for the treatment is discharged at a high temperature, and at that time, heat exchange is performed with the washing water supplied into the treatment tank for washing. Therefore, the temperature at the time of cleaning becomes much higher than before, and an excellent cleaning effect is achieved. Therefore, it is possible to reduce the number of times of water washing repeated after discharging hot washing water as compared with the conventional case. In addition, since the treatment liquid is discharged at a high temperature, oligomers and dye residues are removed in a state of being dissolved in the treatment liquid. Can be omitted. Therefore, the steam and chemicals used for raising the temperature in the reduction cleaning process are not necessary, and the cost can be reduced. And since the quantity which the said oligomer, dye residue, etc. adhere to the inner wall of a processing tank, etc. remain decreases, it has the advantage that the burden in maintenance, such as cleaning a processing tank regularly, is eased. In addition, since the discharge amount of the high-temperature treatment liquid and the supply amount of cleaning water are controlled to be equal to each other, the amount of liquid circulating in the treatment tank is kept constant even after shifting from the dyeing process to the cleaning process. As a result, the fiber product is not burdened and the finish is good.

そして、上記洗浄方法のなかでも、特に、上記高温処理液の排出と洗浄水の供給により、処理槽内の液が所定温度域まで下がった時点で、洗浄水を高温処理液と熱交換することなく直接処理槽内に供給して洗浄を行うようにしたものは、高温処理液を低温域に冷却する場合(例えば80℃から60℃に降温する場合)、より短時間で所定の低温域に降温させることができる。しかも、処理槽内に直接洗浄水を供給するため、冷却と同時に洗浄を行うことができ、洗浄効率がさらに向上する。そして、従来の方法では、低温域まで降温する際、スムーズな温度勾配で冷却することが困難なため、繊維品にシワが発生しやすかったが、この方法によれば、温度勾配がスムーズになり、シワが発生しにくいという利点を有する。   And among the above cleaning methods, in particular, when the liquid in the processing tank is lowered to a predetermined temperature range due to the discharge of the high temperature processing liquid and the supply of the cleaning water, the cleaning water is heat exchanged with the high temperature processing liquid. If the high-temperature treatment liquid is cooled to a low temperature range (for example, when the temperature is lowered from 80 ° C. to 60 ° C.), the temperature is reduced to a predetermined low temperature range in a shorter time. The temperature can be lowered. Moreover, since the cleaning water is directly supplied into the treatment tank, the cleaning can be performed simultaneously with the cooling, and the cleaning efficiency is further improved. In the conventional method, when it is lowered to a low temperature range, it is difficult to cool the fiber product with a smooth temperature gradient. Therefore, the fiber product is easily wrinkled. However, according to this method, the temperature gradient becomes smooth. , Has the advantage that wrinkles are less likely to occur.

また、本発明の繊維品の処理装置は、従来の処理装置に、簡単な構成を追加するだけのものであり、上記特殊な洗浄方法を、低コストで効率よく実施することができる。   In addition, the textile processing apparatus of the present invention simply adds a simple configuration to the conventional processing apparatus, and can perform the above-described special cleaning method efficiently at low cost.

つぎに、本発明を実施するための最良の形態について説明する。   Next, the best mode for carrying out the present invention will be described.

まず、図1は、本発明の一実施の形態である液流処理装置を示している。この装置は、図4に示す装置と同様、布帛1の滞留部2と、この滞留部2と布帛1の移送通路3とを接続した環状の処理槽4とを備えている。そして、上記滞留部2の底部に設けられた処理液吸い込み部5(この図では3個所)から処理液を吸い込み、循環ポンプ6、熱交換器7を介して、所定温度に維持された処理液を上記移送通路3の一端に付設された処理液噴射部8に還流させ、その液流で布帛1を移送しながら処理を行うようになっている。   First, FIG. 1 shows a liquid flow processing apparatus according to an embodiment of the present invention. Similar to the apparatus shown in FIG. 4, this apparatus includes a staying portion 2 of the fabric 1 and an annular processing tank 4 in which the staying portion 2 and the transfer passage 3 of the fabric 1 are connected. Then, the processing liquid is sucked in from the processing liquid suction section 5 (three places in this figure) provided at the bottom of the staying section 2, and is maintained at a predetermined temperature via the circulation pump 6 and the heat exchanger 7. Is recirculated to the treatment liquid injection section 8 attached to one end of the transfer passage 3, and the treatment is performed while the fabric 1 is transferred by the liquid flow.

また、上記循環ポンプ6および熱交換器7を備えた処理液循環路10において、循環ポンプ6の吸い込み側に、循環する処理液を一部取り出して排出する処理液排出配管11が接続されており、その接続部の下流側に、上記処理液循環路10内に洗浄水を供給する洗浄水供給配管12が、逆止弁13を介して接続されている。   Further, in the treatment liquid circulation path 10 provided with the circulation pump 6 and the heat exchanger 7, a treatment liquid discharge pipe 11 is connected to the suction side of the circulation pump 6 for extracting and discharging a part of the circulating treatment liquid. A cleaning water supply pipe 12 for supplying cleaning water into the processing liquid circulation path 10 is connected to the downstream side of the connecting portion via a check valve 13.

そして、上記処理液排出配管11と洗浄水供給配管12は、ともに熱交換器14を経由しており、この熱交換器14によって、高温処理液の温度が下がり、常温の洗浄水の温度が上がるようになっている。ただし、上記処理液排出配管11と洗浄水供給配管12には、それぞれ開閉弁15、16と、流量計17、18が設けられており、処理液の排出量と洗浄水の供給量を、互いに等量となるよう制御できるようになっている。また、19は洗浄水供給用のポンプ、20は給水弁である。   And both the said process liquid discharge piping 11 and the washing water supply piping 12 are passing through the heat exchanger 14, The temperature of a high temperature processing liquid falls by this heat exchanger 14, and the temperature of the normal temperature washing water rises. It is like that. However, the treatment liquid discharge pipe 11 and the cleaning water supply pipe 12 are provided with on-off valves 15 and 16 and flow meters 17 and 18, respectively. It can be controlled to be equal. Further, 19 is a pump for supplying cleaning water, and 20 is a water supply valve.

上記液流処理装置を用い、例えばつぎのようにして、繊維品の処理および洗浄を行うことができる。すなわち、まず、通常の液流処理装置と同様にして、布帛1を処理槽4内に装填し、開閉弁15、16を閉じた状態で、通常と同様の処理を行う。そして、処理が終了した時点で、給水弁20を開くとともにポンプ19を作動させ、上記開閉弁15、16を開くことにより、処理液循環路10内を循環する処理液の一部を、処理液排出配管11に取り出すと同時に、洗浄水を処理液循環路10内に供給する。このとき、熱交換器14を経由させることにより、排出される高温処理液と常温の洗浄水との間で熱交換を行う。また、流量計17、18および開閉弁15、16を用いて流量制御を行うことにより、処理液の排出量と洗浄水の供給量が、常に等量となるよう制御する。これにより、処理槽4内を循環する液(処理液が徐々に洗浄水に置換されていく混合液)の液量を一定に保ちながら、洗浄を行うことができる。   Using the above liquid flow treatment apparatus, for example, the fiber product can be treated and washed as follows. That is, first, in the same manner as a normal liquid flow processing apparatus, the fabric 1 is loaded into the processing tank 4 and the same processing as normal is performed with the on-off valves 15 and 16 closed. When the processing is completed, the feed water valve 20 is opened and the pump 19 is operated to open the on-off valves 15 and 16, whereby a part of the processing liquid circulated in the processing liquid circulation path 10 is treated with the processing liquid. Simultaneously with the discharge pipe 11, cleaning water is supplied into the processing liquid circulation path 10. At this time, heat is exchanged between the discharged high-temperature treatment liquid and normal-temperature washing water by passing through the heat exchanger 14. Further, by controlling the flow rate using the flow meters 17 and 18 and the on-off valves 15 and 16, the discharge amount of the processing liquid and the supply amount of the cleaning water are controlled to be always equal. Thereby, it is possible to perform cleaning while keeping the liquid amount of the liquid circulating in the processing tank 4 (a mixed liquid in which the processing liquid is gradually replaced with the cleaning water) constant.

そして、循環する液の温度が所定の低温域(例えば60℃)になった時点で、高温処理液の排出と洗浄水の供給を停止し、必要であれば、処理液循環路10の途中に設けられる排液口(図示せず)から液を直接排出し、新たな洗浄水を一定流量で供給して水洗処理を行い、再度排水と給水、水洗を行ったのち、布帛1を取り出して、一連の処理を終了する。   Then, when the temperature of the circulating liquid reaches a predetermined low temperature range (for example, 60 ° C.), the discharge of the high temperature processing liquid and the supply of cleaning water are stopped, and if necessary, in the middle of the processing liquid circulation path 10. The liquid is directly discharged from a drainage port (not shown) provided, and a new washing water is supplied at a constant flow rate to perform washing treatment. After draining, supplying water, and washing again, the fabric 1 is taken out, A series of processing ends.

上記洗浄方法によれば、排出される高温処理液と供給される洗浄水の熱交換により、洗浄時の温度が従来に比べて格段に高くなるため、優れた洗浄効果を奏する。したがって、高温の洗浄水排出後に繰り返す水洗の回数を、従来に比べて減らすことができる。また、処理液を高温のまま排出するため、オリゴマーや染料残留物等が処理液中に溶解した状態で除去されることになり、従来のポリエステル濃色染色等において必要であった還元洗浄処理を省略することができる。したがって、上記還元洗浄処理において昇温に用いられる蒸気や薬剤が不要となり、コストの低減化を図ることができる。そして、上記オリゴマーや染料残留物等が処理槽4の内壁等に付着して残留する量が少なくなるため、処理槽4を定期的に洗浄する等のメンテナンスにおける負担が軽減されるという利点を有する。しかも、高温処理液の排出量と洗浄水の供給量を、互いに等量となるよう制御するため、染色等の処理から洗浄処理に移行しても、処理槽4内を循環する液量が一定に保たれて安定した加工を行うことができ、良好な仕上がりとなる。   According to the above-described cleaning method, the temperature at the time of cleaning is significantly higher than that in the past due to the heat exchange of the discharged high-temperature treatment liquid and the supplied cleaning water, so that an excellent cleaning effect is achieved. Therefore, it is possible to reduce the number of times of water washing repeated after discharging hot washing water as compared with the conventional case. In addition, since the treatment liquid is discharged at a high temperature, oligomers and dye residues are removed in a state of being dissolved in the treatment liquid. Can be omitted. Therefore, the steam and chemicals used for raising the temperature in the reduction cleaning process are not necessary, and the cost can be reduced. And since the quantity which the said oligomer, dye residue, etc. adhere to the inner wall etc. of the processing tank 4 and remain | survives decreases, it has the advantage that the burden in maintenance, such as wash | cleaning the processing tank 4 regularly, is reduced. . Moreover, since the discharge amount of the high-temperature treatment liquid and the supply amount of the washing water are controlled to be equal to each other, the amount of liquid circulating in the treatment tank 4 is constant even when the process shifts from the dyeing process to the washing process. Therefore, stable processing can be performed and a good finish can be obtained.

なお、本発明において、「高温処理液」とは、処理液循環路10に設けられた熱交換器7によって加熱され供給時の液温から高い温度に設定されたものをいい、その温度は、処理の種類、繊維品の種類等によって、適宜に設定される。   In the present invention, the “high temperature treatment liquid” refers to a liquid heated by the heat exchanger 7 provided in the treatment liquid circulation path 10 and set to a high temperature from the liquid temperature at the time of supply. It is set appropriately depending on the type of treatment, the type of textile, and the like.

また、本発明において、「洗浄水」とは、上記高温処理液と熱交換して高温処理液の液温を下げることができる程度に、高温処理液より低温のものが用いられるが、その温度は、特に限定されるものではなく、通常、常温の水が用いられる。また、洗浄効果の向上や特定の風合いや機能の付与を目的として、適宜の薬剤を添加したものを用いることもできる。   Further, in the present invention, “washing water” is used that is lower in temperature than the high-temperature treatment liquid to such an extent that the liquid temperature of the high-temperature treatment liquid can be lowered by heat exchange with the high-temperature treatment liquid. Is not particularly limited, and water at normal temperature is usually used. Moreover, what added the appropriate chemical | medical agent can also be used for the purpose of the improvement of a cleaning effect, provision of a specific texture and function.

さらに、本発明において、高温処理液の排出量と洗浄水の供給量を等量にして処理槽4内の液量を一定に保つ方法としては、上記の例のように、流量計17、18および開閉弁15、16を用いて両者の流量制御を行う方法に限らず、適宜の方法を用いることができる。なお、処理槽4内に液面センサを設け、液面レベルが常に一定に保たれるよう開閉弁15、16を制御する方法も考えられるが、液流処理装置の場合、処理槽4内を処理液が波立って循環しており、液面レベルの特定が難しいことから、上記の例のように、流量計17、18と開閉弁15、16を組み合わせた制御が好適である。   Furthermore, in the present invention, as a method for keeping the amount of liquid in the treatment tank 4 constant by equalizing the discharge amount of the high temperature treatment liquid and the supply amount of cleaning water, as in the above example, the flow meters 17 and 18 are used. In addition, not only the method of controlling the flow rate of both using the on-off valves 15 and 16, but also an appropriate method can be used. In addition, a method of providing a liquid level sensor in the processing tank 4 and controlling the on-off valves 15 and 16 so that the liquid level is always kept constant is conceivable. Since the processing liquid circulates in a rippled manner and it is difficult to specify the liquid level, control combining the flow meters 17 and 18 and the on-off valves 15 and 16 is suitable as in the above example.

そして、上記の例では、高温処理液の排出と洗浄水の供給によって、液温が所定の低温域になった時点で、液の排出を行い、新たな洗浄水を一定流量で供給して水洗処理を行うようにしたが、他の例として、液温が排出可能な低温域よりも高温の中温域(例えば80℃)に下がった時点で、開閉弁15を閉じて処理液排出配管11から高温処理液を取り出すことを停止し、洗浄水を、高温排出液と熱交換することなく直接処理槽4内に一定流量で供給して、循環する液の冷却を図ることができる。また、上記洗浄水の供給は、必ずしも一定流量でなくてもよい。なお、洗浄水の供給による処理槽4内の液の増量分は、排液弁から漸次排出される。そして、循環する液の温度が所定の低温域(例えば60℃)になった時点で、洗浄水の供給を停止し、前記の例と同様、必要であれば、排液口から液を直接排出し、新たな洗浄水を供給して水洗処理を行い、再度排水と給水、水洗を行ったのち、布帛1を取り出して、一連の処理を終了する。   In the above example, when the liquid temperature reaches a predetermined low temperature range by discharging the high-temperature treatment liquid and supplying cleaning water, the liquid is discharged, and new cleaning water is supplied at a constant flow rate. As another example, when the liquid temperature falls to a middle temperature range (for example, 80 ° C.) higher than the low temperature range where the liquid temperature can be discharged, the on-off valve 15 is closed and the processing liquid discharge pipe 11 is closed. It is possible to stop taking out the high-temperature treatment liquid and supply the cleaning water at a constant flow rate directly into the treatment tank 4 without exchanging heat with the high-temperature discharged liquid, thereby cooling the circulating liquid. Moreover, the supply of the washing water is not necessarily a constant flow rate. The increased amount of the liquid in the treatment tank 4 due to the supply of the washing water is gradually discharged from the drain valve. Then, when the temperature of the circulating liquid reaches a predetermined low temperature range (for example, 60 ° C.), the supply of the washing water is stopped, and if necessary, the liquid is directly discharged from the drainage port as in the above example. Then, after washing water is supplied by supplying new washing water, draining, water supply, and washing are performed again, the fabric 1 is taken out, and the series of processing ends.

この方法によれば、より短時間で所定の低温域に降温させることができるだけでなく、処理槽4内に直接洗浄水を供給するため、冷却と同時に洗浄を行うことができ、洗浄効率がさらに向上する。そして、従来の方法では、低温域まで降温する際、スムーズな温度勾配で冷却することが困難なため、繊維品にシワが発生しやすかったが、この方法によれば、温度勾配がスムーズになり、シワが発生しにくいという利点を有する。   According to this method, not only can the temperature be lowered to a predetermined low temperature range in a shorter time, but also the cleaning water can be supplied directly into the treatment tank 4, so that the cleaning can be performed simultaneously with the cooling, and the cleaning efficiency is further improved. improves. In the conventional method, when it is lowered to a low temperature range, it is difficult to cool the fiber product with a smooth temperature gradient. Therefore, the fiber product is easily wrinkled. However, according to this method, the temperature gradient becomes smooth. , Has the advantage that wrinkles are less likely to occur.

なお、本発明において、処理対象となる繊維品の種類は、特に限定するものではないが、例えば、ポリエステル、ポリアミド、アクリル等、各種の合成繊維、その混紡品、交織品、交編品、あるいは、綿、レーヨン、麻等のセルローズ系繊維、その混紡品、交織品、交編品等があげられる。そして、上記繊維品の形状、形態も、織生地、編生地、不織布、製品(ガーメント)等、どのようなものであっても差し支えない。   In the present invention, the type of fiber product to be treated is not particularly limited. For example, various synthetic fibers such as polyester, polyamide, and acrylic, blended products, union products, union products, or Cellulose fibers such as cotton, rayon and hemp, blended products, union products, union products and the like. The shape and form of the fiber product may be any woven fabric, knitted fabric, non-woven fabric, product (garment), or the like.

そして、本発明において、上記繊維品を処理し、洗浄を行う装置としては、処理槽内外を循環する処理液によって処理を行うタイプのものであれば、どのようなものであっても差し支えない。例えば、上記の例で示した液流処理装置の外、糸状の繊維品を、かせ状、チーズ状、コーン状等にパッケージ化して処理するパッケージ処理装置やビーム処理装置、糸や織編物等の繊維品を、懸垂式で処理したり平たく伸ばしたものを積層した状態で処理する処理装置等、各種のものをあげることができる。さらに、気流処理装置にも適用することができる。   And in this invention, as an apparatus which processes the said textiles and wash | cleans, what kind of thing may be used as long as it is a type which processes by the processing liquid which circulates inside and outside a processing tank. For example, in addition to the liquid flow processing apparatus shown in the above example, a package processing apparatus, a beam processing apparatus, a thread, a woven or knitted fabric, and the like, which are packaged and processed into a skein, cheese, corn, etc. Various types of processing devices such as a processing apparatus for processing fiber products in a suspended state or processing them in a state of being flattened can be listed. Furthermore, the present invention can be applied to an airflow processing device.

また、本発明において、繊維品に対する処理は、染色処理の外、上記液流処理装置の外、例えばリラックス加工、樹脂加工、精錬等、各種の処理広く適用することができる。   In the present invention, the treatment for the textile can be widely applied to various treatments such as relaxation processing, resin processing, refining, and the like, outside the dyeing treatment and the liquid flow treatment apparatus.

つぎに、本発明の実施例を比較例と併せて説明する。   Next, examples of the present invention will be described together with comparative examples.

〔実施例〕
図1に示す本発明の液流処理装置を用い、下記の条件に従い、繊維品の染色処理および洗浄を行った。
繊維品:ポリエステル布帛(ポリエステル糸56dtex/48fの平織)100kg
工程表:図2に従う。
染色工程で使用する薬剤: 染料 5kg
分散剤(ニッカサンソルトRM−340、日華化学社製) 600g
酢酸 600g
浴 比:1/12
〔Example〕
Using the liquid flow treatment apparatus of the present invention shown in FIG. 1, the fiber product was dyed and washed according to the following conditions.
Textile: 100 kg of polyester fabric (polyester yarn 56 dtex / 48 f plain weave)
Process chart: Follow FIG.
Agents used in the dyeing process: Dye 5kg
Dispersant (Nikka Sun Salt RM-340, manufactured by Nikka Chemical Co., Ltd.) 600 g
600g acetic acid
Bath ratio: 1/12

〔比較例〕
図4に示す従来の液流処理装置を用い、下記の条件に従い、繊維品の染色処理および洗浄を行った。
繊維品:実施例と同じ。
工程表:図3に従う。
染色工程で使用する薬剤:実施例と同じ。
還元洗浄工程で使用する薬剤:
NaOH 1200g
ハイドロサルファイト 1200g
浴 比:実施例と同じ
[Comparative Example]
Using the conventional liquid flow treatment apparatus shown in FIG. 4, the textiles were dyed and washed according to the following conditions.
Textile product: the same as in Example.
Process chart: Follow FIG.
Agents used in the staining process: the same as in the examples.
Agents used in the reduction cleaning process:
1,200 g of NaOH
Hydrosulfite 1200g
Bath ratio: Same as the example

上記実施例、比較例における蒸気、冷却水等の使用量等を調べて、下記の表1に対比してまとめた。   The amounts used of steam, cooling water, etc. in the above Examples and Comparative Examples were examined and summarized in comparison with Table 1 below.

上記の結果から、実施例の方法によれば、比較例の方法に比べ、蒸気、水、電力、薬剤のいずれについても使用量を低減することができ、また、図2および図3の工程表を対比すればわかるように、洗浄処理に要する時間も大幅に短縮されるため、大幅なコストダウンを実現することがわかる。しかも、実施例の方法によって得られる処理品は、温度勾配によるシワ等が発生しておらず、高品質のものとなる。   From the above results, according to the method of the example, compared to the method of the comparative example, it is possible to reduce the use amount of any of steam, water, electric power, and medicine, and the process charts of FIG. 2 and FIG. As can be seen from the comparison, the time required for the cleaning process is greatly shortened, and it can be seen that a significant cost reduction is realized. In addition, the processed product obtained by the method of the embodiment is free from wrinkles due to temperature gradients and has a high quality.

さらに、上記実施例の方法によって得られる処理品と、比較例の方法によって得られる処理品の摩擦堅牢度(JIS L 0849に従う)と水堅牢度(JIS L 0846に従う)を評価し、それらの結果を下記の表2にまとめた。なお、実施例品については、処理工程の途中までで処理を終了したものについても同様にして評価した。   Further, the friction fastness (according to JIS L 0849) and the water fastness (according to JIS L 0846) of the treated product obtained by the method of the above example and the treated product obtained by the method of the comparative example were evaluated, and the results thereof. Are summarized in Table 2 below. In addition, about the Example goods, what finished the process in the middle of the process step was also evaluated in the same manner.

上記の結果から、実施例品(水洗2回)は、比較例品(従来方法による処理品:水洗3回)に対し、水洗回数が1回少ないにもかかわらず、比較例品と同等の堅牢度を備えていることがわかる。   From the above results, the example product (2 times of water washing) is the same robustness as the comparative example product, although the number of times of water washing is less than that of the comparative example product (treated product by conventional method: 3 times of water washing). You can see that it has a degree.

本発明の一実施例の処理装置を示す説明図である。It is explanatory drawing which shows the processing apparatus of one Example of this invention. 上記実施例による工程表である。It is a process chart by the said Example. 従来例による工程表である。It is a process chart by a prior art example. 従来例の処理装置を示す説明図である。It is explanatory drawing which shows the processing apparatus of a prior art example.

符号の説明Explanation of symbols

1 布帛
4 処理槽
6 循環ポンプ
7、14 熱交換器
11 処理液排出配管 12 洗浄水供給配管
DESCRIPTION OF SYMBOLS 1 Fabric 4 Processing tank 6 Circulation pump 7, 14 Heat exchanger 11 Processing liquid discharge piping 12 Washing water supply piping

Claims (3)

繊維品を処理槽内に装填し、処理槽内外を循環する高温処理液と上記繊維品とを接触させることにより繊維品を処理し、ついで洗浄水による洗浄を行う方法であって、上記高温処理液による処理終了後、上記高温処理液を処理槽内から徐々に排出するとともに洗浄水を処理槽内に徐々に供給し、その際、排出される高温処理液と供給する洗浄水とを熱交換し、かつ上記高温処理液の排出量と洗浄水の供給量を等量にして処理槽内の液量が一定に保たれるようにしたことを特徴とする繊維品の洗浄方法。   A method of treating a fiber product by loading the fiber product into a treatment tank and bringing the fiber product into contact with a high-temperature treatment liquid circulating inside and outside the treatment tank, followed by washing with washing water. After the treatment with the liquid is completed, the high temperature treatment liquid is gradually discharged from the treatment tank and the cleaning water is gradually supplied into the treatment tank. At that time, the discharged high temperature treatment liquid and the supplied washing water are heat-exchanged. And the amount of the high-temperature treatment liquid discharged is equal to the amount of cleaning water supplied so that the amount of liquid in the treatment tank is kept constant. 上記高温処理液の排出と洗浄水の供給により、処理槽内の液が所定温度域まで下がった時点で、洗浄水を高温処理液と熱交換することなく直接処理槽内に供給して洗浄を行う請求項1記載の繊維品の洗浄方法。   When the liquid in the processing tank has dropped to the specified temperature range due to the discharge of the high-temperature processing liquid and the supply of cleaning water, the cleaning water is supplied directly into the processing tank without heat exchange with the high-temperature processing liquid for cleaning. The method for cleaning a textile product according to claim 1 to be performed. 請求項1または2記載の繊維品の洗浄方法に用いられる繊維品の処理装置であって、繊維品を装填して処理液と接触させる処理槽と、上記処理槽内の処理液を処理槽外に取り出し循環ポンプおよび熱交換器を経由して上記処理槽内に繰り返し供給する処理液循環路とを備え、上記処理液循環路の循環ポンプ吸い込み側に接続され上記処理槽内の処理液を一部取り出して排出する処理液排出配管と、同じく上記処理液循環路の循環ポンプ吸い込み側であって上記処理液排出配管接続部より下流側に接続され洗浄水を上記処理液循環路内に供給する洗浄水供給配管と、上記処理液排出配管を通過する処理液と洗浄水供給配管を通過する洗浄水とを熱交換する熱交換器とが設けられ、上記処理液排出配管から排出される処理液量と上洗浄水供給配管から供給される洗浄水量とが、互いに等量となるよう制御されるようになっていることを特徴とする繊維品の処理装置。   It is a textile processing device used for the textiles washing method according to claim 1 or 2, Comprising: The processing tank which loads textiles and contacts processing liquid, The processing liquid in the above-mentioned processing tank is outside a processing tank And a treatment liquid circulation path that is repeatedly supplied into the treatment tank via a circulation pump and a heat exchanger, and connected to the suction side of the circulation pump of the treatment liquid circulation path for collecting the treatment liquid in the treatment tank. The processing liquid discharge pipe for taking out and discharging the part, and also connected to the circulating pump suction side of the processing liquid circulation path and the downstream side of the processing liquid discharge pipe connection portion, and supply the cleaning water into the processing liquid circulation path A treatment liquid discharged from the treatment liquid discharge pipe is provided with a heat exchanger for exchanging heat between the wash water supply pipe, the treatment liquid passing through the treatment liquid discharge pipe, and the wash water passing through the wash water supply pipe Quantity and top wash water supply piping A cleaning water to be al supplied, textiles processing apparatus characterized by being adapted to be controlled to be equal amounts from each other.
JP2004295212A 2004-10-07 2004-10-07 Textile cleaning method and textile processing apparatus used therefor Expired - Fee Related JP4562484B2 (en)

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JP2004295212A JP4562484B2 (en) 2004-10-07 2004-10-07 Textile cleaning method and textile processing apparatus used therefor
PCT/JP2005/018659 WO2006038696A1 (en) 2004-10-07 2005-10-07 Method for washing textile product and textile product treatment apparatus used therefor
US11/664,897 US20090013479A1 (en) 2004-10-07 2005-10-07 Method of washing a textile product and textile product treatment apparatus used therefore
CNB200580033323XA CN100567612C (en) 2004-10-07 2005-10-07 The washing methods of fibre and be used for the treating apparatus of the fibre of this method

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US20090013479A1 (en) 2009-01-15

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