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JP4659939B2 - Textile product processing method and apparatus - Google Patents
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JP4659939B2 - Textile product processing method and apparatus - Google Patents

Textile product processing method and apparatus Download PDF

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Publication number
JP4659939B2
JP4659939B2 JP34986299A JP34986299A JP4659939B2 JP 4659939 B2 JP4659939 B2 JP 4659939B2 JP 34986299 A JP34986299 A JP 34986299A JP 34986299 A JP34986299 A JP 34986299A JP 4659939 B2 JP4659939 B2 JP 4659939B2
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Prior art keywords
tank
liquid
processing
filter
dyeing
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JP2001164481A (en
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和雄 山田
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日金加工株式会社
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Description

【0001】
【発明の属する技術分野】
本発明は、繊維製品(以下布帛ともいう)の精練・染色などの処理方法及びその装置に関する。
【0002】
【従来の技術】
従来、繊維製品の染色処理においては、図3に示すように、例えば、処理液を約20℃(A点)から約130℃(B点)に昇温してこの温度を一定時間(C点まで)保持し、このA点からC点間で染着し、この染着終了(C点)から処理液を冷却してD点で排出し、その後、E点に示すように、2〜3回、給水、排水を繰り返して水洗いし、未染着の染料や他の使用済み薬品を洗い落としていた。
【0003】
【発明が解決しようとする課題】
上記従来の処理方法においては、規定の染色堅牢度を得るのに、何度も排液、給水を繰り返す必要があるため、布帛の水洗い工程で大量の水を必要とし、かつ、処理タンク内に染料付着を生じて色替え時の釜洗浄を必要とするなどの問題がある。
【0004】
そこで本発明は、上記の水洗い工程や釜洗浄を簡略化できる繊維製品の処理方法及びその装置を提供することを目的とするものである。
【0005】
【課題を解決するための手段】
上記の課題を解決するために、請求項1記載の第1の発明は、処理タンク内において所定温度で繊維製品を染色処理するものにおいて、繊維製品の染着終了後に処理タンク内の処理液を全部または一部処理タンクの外部に設けた貯液槽に排出し、
前記処理タンクから排出された処理液を冷却手段で冷却した後に濾過器へ供給して、濾過器で濾過し、この濾過した液を熱交換器に供給した後に、処理タンクに戻すようにしたことを特徴とする繊維製品の処理方法である。
【0007】
請求項記載の第の発明は、処理タンク内の処理液を全部または一部移して貯溜する貯液槽と、前記貯液槽内の処理液を取り出して濾過する濾過器と、前記処理タンクから取り出した濾過前の処理液を冷却する冷却手段と、前記濾過器の下流に設けた熱交換器と、前記熱交換器を経た処理液を上記処理タンクへ戻す流路とからなることを特徴とする繊維製品の処理装置である。
【0009】
上記発明において、処理タンク内の処理液は加熱後一定の温度に維持され、この温度で布帛が処理され、所定時間経過により布帛の染着は、ほぼ限界に達する。この染着終了後、処理タンク内の処理液の全部または一部を貯液槽へ移し、その後、濾過器により濾過して処理タンク内へ戻す。また、必要により、処理液を冷却して濾過器へ供給する。
【0010】
これにより、未染着の染料は濾過器により捕捉され、その処理液は水洗い用として利用されるが、特に冷却により処理液中に溶融して存在するオリゴマー等の不純物を析出させ、濾過器にて分離させることができる。
【0011】
したがって、染色終了後の処理液は脱色され、従来のような水洗い工程を省略できる上に処理タンク内面の染料汚れを防止できる。
【0012】
更に、脱色された処理液は再利用できるので補給水を必要としない。
【0013】
【発明の実施の形態】
図1に示す実施例に基いて本発明の実施の形態について説明する。
【0014】
処理タンクを構成する滞溜槽1における滞溜部の下流側底面はテーパ状の立上り部2に形成され、該立上り部2の終端にリールボックス3が配置されている。
該リールボックス3の下部には噴射ノズル4が設けられており、該噴射ノズル4の下流側から上記滞溜槽1の上流(後部)側底面に渡って移送管5が配管接続され、滞溜槽1と移送管5によって繊維製品である処理布帛7の循環経路を構成している。
【0015】
上記リールボックス3内にはリール6が備えられており、処理布帛7が、リール6に掛けられて上記滞溜槽1と移送管5に渡り無端状に配置され、噴射ノズル4からの処理液の噴出により、布帛7が矢印方向へ移動循環するようになっている。
【0016】
上記滞溜槽1の上流側底部には多孔板からなるケーシング8が設けられており、通常染色時、無端状に結合した布帛7と処理液9を分離する隔壁となっている。
【0017】
滞溜槽1の下流側(前部)底部には槽1内と連通した液溜部10が設けられ、該液溜部10は吸い込み配管11を介してポンプ12に接続され、更にポンプ12の吐出側より吐出管13、フィルタ14、多管式熱交換器15、出口管16を経て上記噴射ノズル4に接続されており、これらが処理液循環路を構成している。
【0018】
滞溜部1の上流側上部にはシャワー管17が配設され、出口管16より分岐した管18を通じて上記熱交換器15に接続されている。
【0019】
19は仕切弁、20は給水弁、21は排液弁、22は圧縮空気の供給路に設けた加圧弁、23は空気抜き弁で滞溜槽1内を減圧する空気抜き配管24に設けられている。上記出口管16には処理液の温度を検知する温度計25が設けられている。38は流量調節弁である。
【0020】
上記吸い込み配管11には、処理液を分流する分岐管30が分岐されており、該分岐管30には濾過用の排出弁31が設けられている。分岐管30における前記排出弁31の下流側は、処理タンクを構成する滞溜槽1の外部に設けた貯液槽32に連通されている。該貯液槽32の容量は前記滞溜槽1及び移送管5内に有する処理液を貯溜できる容量に形成されている。該貯液槽32の底部には排出管33が連通され、該排出管33にはポンプ34が設けられ、該ポンプ34の吐出側の排出管33は濾過器35に連通している。該濾過器35は例えば限外膜または逆浸透膜からなる膜濾過器を使用する。
【0021】
上記濾過器35の出口側には戻り管36が配管され、該戻り管36は給水弁37を介して上記吸い込み配管11に連通している。
【0022】
上記濾過器35で捕捉された染料が混入した濃縮液は、排出管39、排出弁40を通じて液溜部41に溜められ、ドレン弁42の開操作により所定部へ送られるようになっている。
【0023】
なお、上記分岐管30より排出された処理液が設定温度、例えば40℃以上の場合には、上記濾過器35へ入る前に処理液を冷却することが望ましい。そのため、このような冷却を行う冷却手段を設けるものであるが、この冷却手段としては上記の熱交換器15を利用するように配管してもよく、また、図1に示すように上記貯液槽32の外部に冷却水を通して処理液を冷却するような冷却器43を設けてもよい。このような冷却手段を作動させるには、貯液槽32に処理液の温度を検知する温度計44を設置して、設定温度以上のときに冷却器43を作動させるようにする。
【0024】
以上のようであるから、布帛7の染色に際しては、処理液を処理タンク内に入れ、滞溜槽1及び移送管5に、布帛7を図のように環状に配置して無端状に結合する。
【0025】
そして、排出弁31、給水弁37を閉じ、ポンプ12を起動して処理液を処理液循環路を循環させるとともに熱交換器15により処理液を所定温度に加熱する。熱交換器15で加熱された処理液は噴出ノズル4から噴出し、その噴出力により布帛7が矢印方向に循環移動して染色処理がなされる。この染着は、図2におけるA点〜C点、すなわち、上記図3のA点〜C点で行われる。
【0026】
次に染色工程が終った後、すなわち、図2のC点後、熱交換器15による加熱を停止し、任意の温度まで冷却して排出弁31を開き、滞溜槽1及び移送管5内の処理液を全部または一部貯液槽32に排出して貯溜する。このとき、貯液槽32に貯溜された処理液が設定温度、例えば40℃よりも高い場合は冷却手段43により処理液を設定温度まで冷却する。
【0027】
次に、処理タンク1内の処理液の全部が貯液槽32に移された場合は、排水弁31を閉じ、給水弁37を開いてポンプ34を起動する。これにより、貯溜槽32内の処理液は、ポンプ34、濾過器35、戻り管36、給水弁37、吸い込み管11を通って滞溜槽1に入る。また、処理タンク1内の処理液の一部が貯液槽32に移された場合は、ポンプ34及びポンプ12により管13,熱交換器15,管16を通じて滞溜槽に入れる。図2において、Gは処理液の貯液槽32への排出工程、Hは濾過工程、Iは滞溜槽1への戻し工程を示す。このように、処理液が濾過器35を通過することにより未染着の染料は濾過器35に捕捉される。このとき、処理液を冷却手段43により所定温度に冷却することにより、処理液中に溶解して存在するオリゴマー等の不純物を析出させ、濾過器35にて分離させることができる。
【0028】
次に、前記のように濾過した処理液を滞溜槽1内に戻した後、排出弁31と給水弁37を閉じてポンプ12により、処理液を滞溜槽1と吸い込み管11と管16を循環させて布帛7を循環移動し、布帛7に付着した不純物等をすすぎ洗いして取る。図2において、Jはすすぎ洗い工程を示す。
【0029】
このすすぎ洗いが終了した後、必要により再度前記のように処理液を貯液槽32に排出し、その後前記のように濾過器35を通じて濾過して滞溜槽1内へ戻し、再度布帛を循環移動して、前記G〜Jと同様の工程を行う。この工程を必要回繰り返した後、布帛を取り出す。図2のKは布帛の取り出しを示す。
【0030】
次に、濾過器35に逆浸膜濾過器を用い、布帛7としてポリエステル繊維を用い、分散染料を2%owf(繊維重量に対する染料(%))使用し、130℃で染色した後、上記のような冷却工程で染料を分離した実施例を説明する。
【0031】
ポリエステル繊維の場合、未染着染料の濾過処理と同時に処理液温度が100℃以上のときはオリゴマーが溶解しているが、これを所定温度に冷却すると析出する特性を有するため、上記の冷却器43によって処理液をポリエステル繊維の第1転移点以下(40℃)まで冷却して濾過器35で濾過したところ、処理液はほぼ無色になり、更に、オリゴマーの除去もでき、このときの処理液を分光光度計によって計測した結果、その吸光度は限りなく0に近い値が得られた。
【0032】
上記のように、処理液を濾過し、この濾過した処理液ですすぎ洗いした結果、布帛の水洗いや釜洗いは、従来法では3回行っていたが不要になった。そのため、再給水が不要になった。
【0033】
また、染料以外の成分を残したまま処理を繰り返すことができるので、次バッチに助剤を追加するのみで水が100%再利用できる。
【0034】
また、濾過器35で捕捉された染料等は、濃縮液となって排出管39から液溜部41に溜められ、ドレン弁42の開操作で所定部に送られる。この濃縮液は再度、染色に使用することができる。
【0035】
更に、上記のように処理液の冷却温度を冷却器43により40℃以下にすることにより、濾過器35の逆浸透膜の耐久性を長期間保つことができた。
【0036】
なお、上記実施例は、布帛を循環させる染色機に本発明を適用した例であるが、本発明はその他の型式の染色機にも、他の種類の染料にも使用できるもので、図の実施例の染色機に限定するものではない。
【0037】
【発明の効果】
以上のように本願の発明によれば、染色排液に含有する繊維製品に未染着の残留染料をほとんど分離除去することができるので、この水を利用してすすぎ洗いができ、再給水による水洗い工程を省略でき、使用水量を大幅に低減できる。更に、染色タンク内の染料付着を低減できるため、色替えによる釜洗浄を簡略化できる。
【図面の簡単な説明】
【図1】本発明の実施例を示すもので、処理タンク部を断面とした配管図。
【図2】本発明の処理工程を示す図。
【図3】従来の処理工程を示す図。
【符号の説明】
1…処理タンクである滞溜槽
10,11,13,16…処理液循環路を構成する管
32…貯液槽
35…濾過器
43…冷却器
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a processing method and apparatus for scouring and dyeing textile products (hereinafter also referred to as fabrics).
[0002]
[Prior art]
Conventionally, in the textile dyeing process, as shown in FIG. 3, for example, the temperature of the processing liquid is raised from about 20 ° C. (point A) to about 130 ° C. (point B), and this temperature is maintained for a certain time (point C). Until the dyeing is completed, the processing liquid is cooled and discharged at the point D after completion of the dyeing (the point C). The water was washed repeatedly with water, water, and drainage, and undyed dyes and other used chemicals were washed away.
[0003]
[Problems to be solved by the invention]
In the above conventional treatment method, in order to obtain the specified dyeing fastness, it is necessary to repeatedly drain and supply water, so that a large amount of water is required in the washing process of the fabric, and the treatment tank is filled with water. There is a problem that the dye is attached and the pot needs to be washed when changing colors.
[0004]
Therefore, an object of the present invention is to provide a textile processing method and apparatus capable of simplifying the water washing process and the pot washing.
[0005]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, the first invention described in claim 1 is for dyeing a textile product at a predetermined temperature in the treatment tank. After finishing the dyeing of the textile product, the treatment liquid in the treatment tank is used. Drain all or part of it into a storage tank outside the treatment tank,
The processing liquid discharged from the processing tank is cooled by a cooling means and then supplied to a filter, filtered by the filter, and the filtered liquid is supplied to a heat exchanger and then returned to the processing tank. Is a method for treating a textile product.
[0007]
The second invention of claim 2, a storage tank for reserving transferred the processing solution in the processing tank whole or in part, a filter for filtering takes out the treatment liquid in the liquid storage tank, the processing A cooling means for cooling the processing liquid before filtration taken out from the tank, a heat exchanger provided downstream of the filter, and a flow path for returning the processing liquid passed through the heat exchanger to the processing tank. It is the processing apparatus of the textiles characterized.
[0009]
In the above invention, the treatment liquid in the treatment tank is maintained at a constant temperature after heating, and the fabric is treated at this temperature, and the dyeing of the fabric almost reaches its limit after a predetermined time. After completion of the dyeing, all or a part of the processing liquid in the processing tank is transferred to the liquid storage tank, and then filtered by a filter and returned to the processing tank. If necessary, the treatment liquid is cooled and supplied to the filter.
[0010]
As a result, the undyed dye is captured by the filter, and the treatment liquid is used for washing with water.In particular, impurities such as oligomers melted in the treatment liquid by cooling are deposited, Can be separated.
[0011]
Therefore, the processing solution after the dyeing is decolorized, so that the conventional water washing step can be omitted and the stain on the inner surface of the processing tank can be prevented.
[0012]
Furthermore, since the decolorized processing solution can be reused, no replenishing water is required.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
An embodiment of the present invention will be described based on the example shown in FIG.
[0014]
A bottom surface on the downstream side of the stagnation portion in the stagnation tank 1 constituting the processing tank is formed in a tapered rising portion 2, and a reel box 3 is disposed at the end of the rising portion 2.
An injection nozzle 4 is provided at the lower part of the reel box 3, and a transfer pipe 5 is connected from the downstream side of the injection nozzle 4 to the upstream (rear) side bottom surface of the stagnation tank 1. The transfer pipe 5 constitutes a circulation path for the treated fabric 7 that is a textile product.
[0015]
A reel 6 is provided in the reel box 3, and a treatment fabric 7 is placed on the reel 6 in an endless manner across the stagnation tank 1 and the transfer pipe 5. The fabric 7 moves and circulates in the direction of the arrow by the ejection.
[0016]
A casing 8 made of a perforated plate is provided at the bottom on the upstream side of the stagnation tank 1, and serves as a partition wall for separating the endlessly bonded fabric 7 and the treatment liquid 9 during normal dyeing.
[0017]
A liquid reservoir 10 communicating with the interior of the tank 1 is provided at the bottom (front) bottom of the stagnation tank 1, and the liquid reservoir 10 is connected to a pump 12 via a suction pipe 11, and further discharged from the pump 12. The discharge pipe 13, the filter 14, the multi-tube heat exchanger 15, and the outlet pipe 16 are connected to the injection nozzle 4 from the side, and these constitute a processing liquid circulation path.
[0018]
A shower pipe 17 is disposed on the upper upstream side of the stagnation section 1 and connected to the heat exchanger 15 through a pipe 18 branched from the outlet pipe 16.
[0019]
19 is a gate valve, 20 is a water supply valve, 21 is a drain valve, 22 is a pressurization valve provided in a compressed air supply path, and 23 is an air vent valve provided in an air vent pipe 24 for decompressing the stagnation tank 1. The outlet pipe 16 is provided with a thermometer 25 for detecting the temperature of the processing liquid. 38 is a flow control valve.
[0020]
A branch pipe 30 that divides the processing liquid is branched into the suction pipe 11, and a filtration discharge valve 31 is provided in the branch pipe 30. The downstream side of the discharge valve 31 in the branch pipe 30 communicates with a liquid storage tank 32 provided outside the stagnation tank 1 constituting the processing tank. The capacity of the liquid storage tank 32 is formed to a capacity capable of storing the processing liquid contained in the stagnation tank 1 and the transfer pipe 5. A discharge pipe 33 communicates with the bottom of the liquid storage tank 32, a pump 34 is provided in the discharge pipe 33, and a discharge pipe 33 on the discharge side of the pump 34 communicates with a filter 35. As the filter 35, for example, a membrane filter made of an ultra-membrane or a reverse osmosis membrane is used.
[0021]
A return pipe 36 is provided on the outlet side of the filter 35, and the return pipe 36 communicates with the suction pipe 11 through a water supply valve 37.
[0022]
The concentrated liquid mixed with the dye captured by the filter 35 is stored in the liquid storage section 41 through the discharge pipe 39 and the discharge valve 40, and is sent to a predetermined section by opening the drain valve 42.
[0023]
In addition, when the processing liquid discharged | emitted from the said branch pipe 30 is preset temperature, for example, 40 degreeC or more, it is desirable to cool a processing liquid before entering the said filter 35. FIG. Therefore, a cooling means for performing such cooling is provided. As the cooling means, piping may be used so as to use the heat exchanger 15, and the liquid storage as shown in FIG. You may provide the cooler 43 which cools a process liquid through the cooling water outside the tank 32. FIG. In order to operate such a cooling means, a thermometer 44 for detecting the temperature of the processing liquid is installed in the liquid storage tank 32, and the cooler 43 is operated when the temperature is equal to or higher than a set temperature.
[0024]
As described above, when the fabric 7 is dyed, the processing liquid is put in the processing tank, and the fabric 7 is annularly arranged in the stagnation tank 1 and the transfer pipe 5 and joined endlessly as shown in the figure.
[0025]
Then, the discharge valve 31 and the water supply valve 37 are closed, the pump 12 is activated to circulate the treatment liquid in the treatment liquid circulation path, and the treatment liquid is heated to a predetermined temperature by the heat exchanger 15. The treatment liquid heated by the heat exchanger 15 is ejected from the ejection nozzle 4, and the fabric 7 is circulated and moved in the direction of the arrow by the ejection force to perform the dyeing process. This dyeing is performed at points A to C in FIG. 2, that is, points A to C in FIG.
[0026]
Next, after the dyeing process is completed, that is, after point C in FIG. 2, the heating by the heat exchanger 15 is stopped, the temperature is cooled to an arbitrary temperature, the discharge valve 31 is opened, and the inside of the stagnation tank 1 and the transfer pipe 5 is opened. All or part of the processing liquid is discharged into the liquid storage tank 32 and stored. At this time, when the processing liquid stored in the liquid storage tank 32 is higher than a set temperature, for example, 40 ° C., the cooling means 43 cools the processing liquid to the set temperature.
[0027]
Next, when all of the processing liquid in the processing tank 1 has been transferred to the liquid storage tank 32, the drain valve 31 is closed, the water supply valve 37 is opened, and the pump 34 is activated. Thus, the processing liquid in the storage tank 32 enters the stagnation tank 1 through the pump 34, the filter 35, the return pipe 36, the water supply valve 37, and the suction pipe 11. Further, when a part of the processing liquid in the processing tank 1 is transferred to the liquid storage tank 32, it is put into the stagnation tank through the pipe 13, the heat exchanger 15, and the pipe 16 by the pump 34 and the pump 12. In FIG. 2, G indicates a process for discharging the processing liquid to the liquid storage tank 32, H indicates a filtration process, and I indicates a return process to the retention tank 1. In this way, the undyed dye is captured by the filter 35 as the treatment liquid passes through the filter 35. At this time, by cooling the treatment liquid to a predetermined temperature by the cooling means 43, impurities such as oligomers dissolved and present in the treatment liquid can be precipitated and separated by the filter 35.
[0028]
Next, after the processing liquid filtered as described above is returned into the stagnation tank 1, the discharge valve 31 and the water supply valve 37 are closed, and the processing liquid is circulated through the stagnation tank 1, the suction pipe 11 and the pipe 16 by the pump 12. Then, the cloth 7 is circulated and moved, and the impurities adhering to the cloth 7 are rinsed and removed. In FIG. 2, J indicates a rinsing step.
[0029]
After the rinsing is completed, the treatment liquid is again discharged into the storage tank 32 as described above, if necessary, and then filtered through the filter 35 as described above to return to the stagnation tank 1 and the fabric is circulated again. And the process similar to said GJ is performed. After repeating this process as many times as necessary, the fabric is taken out. K in FIG. 2 indicates removal of the fabric.
[0030]
Next, a reverse osmosis filter is used as the filter 35, polyester fibers are used as the fabric 7, a disperse dye is used at 2% owf (dye (%) with respect to the fiber weight), and after dyeing at 130 ° C., An example in which the dye is separated in such a cooling step will be described.
[0031]
In the case of polyester fiber, the oligomer is dissolved when the treatment liquid temperature is 100 ° C. or more simultaneously with the filtration treatment of the undyed dye, but it has the property of being precipitated when cooled to a predetermined temperature. When the treatment liquid was cooled to below the first transition point (40 ° C.) of the polyester fiber by 43 and filtered with a filter 35, the treatment liquid became almost colorless and the oligomer could be removed. As a result of measuring with a spectrophotometer, the absorbance was infinitely close to 0.
[0032]
As described above, the treatment liquid was filtered and rinsed with the filtered treatment liquid. As a result, washing of the fabric with water and washing with a kettle was performed three times in the conventional method, but it became unnecessary. Therefore, re-watering became unnecessary.
[0033]
Further, since the treatment can be repeated while leaving components other than the dye, water can be reused 100% simply by adding an auxiliary agent to the next batch.
[0034]
Further, the dye or the like captured by the filter 35 is concentrated to be accumulated in the liquid reservoir 41 from the discharge pipe 39 and is sent to a predetermined portion by opening the drain valve 42. This concentrated solution can be used again for staining.
[0035]
Furthermore, the durability of the reverse osmosis membrane of the filter 35 could be maintained for a long time by setting the cooling temperature of the treatment liquid to 40 ° C. or lower by the cooler 43 as described above.
[0036]
In addition, although the said Example is an example which applied this invention to the dyeing machine which circulates a cloth, this invention can be used also for other types of dyeing machines, and other types of dyes. It is not limited to the dyeing machine of the examples.
[0037]
【The invention's effect】
As described above, according to the invention of the present application, residual dye that has not been dyed can be almost separated and removed from the fiber product contained in the dyeing waste liquid, so that this water can be used for rinsing and re-feeding. The washing step can be omitted, and the amount of water used can be greatly reduced. Furthermore, since the dye adhesion in the dyeing tank can be reduced, cleaning of the pot by color change can be simplified.
[Brief description of the drawings]
FIG. 1 shows an embodiment of the present invention and is a piping diagram with a section of a processing tank section.
FIG. 2 is a diagram showing processing steps of the present invention.
FIG. 3 is a view showing a conventional processing step.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Reservoir tank 10,11,13,16 which is a process tank ... Pipe 32 which comprises a process liquid circulation path ... Liquid storage tank 35 ... Filter 43 ... Cooler

Claims (2)

処理タンク内において所定温度で繊維製品を染色処理するものにおいて、繊維製品の染着終了後に処理タンク内の処理液を全部または一部処理タンクの外部に設けた貯液槽に排出し、
前記処理タンクから排出された処理液を冷却手段で冷却した後に濾過器へ供給して、濾過器で濾過し、この濾過した液を熱交換器に供給した後に、処理タンクに戻すようにしたことを特徴とする繊維製品の処理方法。
In the processing tank for dyeing textile products at a predetermined temperature, after finishing the dyeing of textile products, all or part of the processing liquid in the processing tank is discharged to a storage tank provided outside the processing tank,
The processing liquid discharged from the processing tank is cooled by a cooling means and then supplied to a filter, filtered by the filter, and the filtered liquid is supplied to a heat exchanger and then returned to the processing tank. A method for treating textile products.
処理タンク内の処理液を全部または一部移して貯溜する貯液槽と、前記貯液槽内の処理液を取り出して濾過する濾過器と、前記処理タンクから取り出した濾過前の処理液を冷却する冷却手段と、前記濾過器の下流に設けた熱交換器と、前記熱交換器を経た処理液を上記処理タンクへ戻す流路とからなることを特徴とする繊維製品の処理装置。A liquid storage tank for transferring all or part of the processing liquid in the processing tank and storing it, a filter for taking out and filtering the processing liquid in the liquid storage tank, and cooling the processing liquid before filtration taken out from the processing tank And a flow path for returning the treatment liquid that has passed through the heat exchanger to the treatment tank.
JP34986299A 1999-12-09 1999-12-09 Textile product processing method and apparatus Expired - Lifetime JP4659939B2 (en)

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