JPH11350334A - Treatment of fiber product and device therefor - Google Patents

Treatment of fiber product and device therefor

Info

Publication number
JPH11350334A
JPH11350334A JP16679498A JP16679498A JPH11350334A JP H11350334 A JPH11350334 A JP H11350334A JP 16679498 A JP16679498 A JP 16679498A JP 16679498 A JP16679498 A JP 16679498A JP H11350334 A JPH11350334 A JP H11350334A
Authority
JP
Japan
Prior art keywords
processing
dyeing
filter
liquid
tank
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.)
Granted
Application number
JP16679498A
Other languages
Japanese (ja)
Other versions
JP3755707B2 (en
Inventor
Kazuo Yamada
和雄 山田
Toshimi Hioki
敏美 日置
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.)
Nissen Corp
Original Assignee
Nissen Corp
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 Nissen Corp filed Critical Nissen Corp
Priority to JP16679498A priority Critical patent/JP3755707B2/en
Publication of JPH11350334A publication Critical patent/JPH11350334A/en
Application granted granted Critical
Publication of JP3755707B2 publication Critical patent/JP3755707B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Fiber Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for treating a fiber product, capable of effectively separating a residual dye not dyed on the fiber product and contained in a dyeing liquid drainage, omitting a water-washing process and largely reducing the cost of water used therein. SOLUTION: Treating liquid circulation routes 10-16 are formed on the outside of a treating tank 1 through a pump 12. Routes 25 and 31 used for separating and circulating the dyeing liquid, branched from a part of the treating liquid circulation routes 10-16 and returned to the treating tank 1 are disposed. A cooling device 28 and a filtration device 30 are disposed on the upstream and downstream sides, respectively, in the routes 25 and 31 used for separating and circulating the dyeing liquid.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[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)の精錬・染色などの処理方法及びその装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for refining and dyeing textile products (hereinafter also referred to as "fabric").

【0002】[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。
2. Description of the Related Art Conventionally, in the dyeing treatment of textile products,
As shown in FIG. 3, for example, the treatment liquid is heated to about 20 ° C. (point A).
To about 130 ° C. (point B), hold this temperature for a certain period of time (up to point C), dye from point A to point C, and finish the dyeing (point C). After cooling and discharging at point D, as shown at point E, water supply and drainage were repeated and washed twice or three times to wash off undyed dyes and other used chemicals.

【0003】[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。
In the above-mentioned conventional processing method, drainage is repeatedly performed to obtain a specified color fastness.
Since the water supply needs to be repeated, there is a problem that a large amount of water is required in the washing step of the fabric, and the dye adheres to the inside of the processing tank, so that the kettle needs to be washed at the time of color change.

【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。
Accordingly, an object of the present invention is to provide a method and an apparatus for treating textile products, which can simplify the above-mentioned washing step and washing in a pot.

【0005】[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、
冷却器と濾過器を有する染料分離循環路を設け、繊維製
品の染着終了後に処理液を上記染料分離循環路へ分流し
て上記冷却器で冷却した後、濾過器で濾過して処理タン
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。
Means for Solving the Problems In order to solve the above-mentioned problems, a first invention according to claim 1 is a method for dyeing a textile at a predetermined temperature in a processing tank.
A dye separation circuit having a cooler and a filter is provided, and after the dyeing of the textile product is completed, the treatment liquid is divided into the dye separation circuit and cooled by the cooler. A method for treating a fiber product, wherein the fiber product is returned.

【0006】請求項2記載の第2の発明は、上記の方法
を達成するために、処理タンクの外部にポンプを介して
処理液循環路を形成し、該処理液循環路の一部より分岐
して処理タンクに戻る染料分離循環路を設け、該染料分
離循環路に、上流側に位置して冷却器を設け、下流側に
位置して濾過器を設けたことを特徴とする繊維製品の処
理装置である。
According to a second aspect of the present invention, in order to achieve the above-described method, a processing liquid circulation path is formed outside the processing tank via a pump, and a part of the processing liquid circulation path is branched. And a dye separation circuit for returning to the treatment tank, a cooling device provided on the upstream side of the dye separation circuit, and a filter provided on the downstream side of the dye separation circuit. Processing device.

【0007】上記本発明において、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を染料
分離循環路へ分流し、冷却器により任意の温度まで急冷
却させ、その後、濾過器により濾過して処理タンク内へ
戻し、これを繰り返して循環させる。
In the present invention, the processing liquid in the processing tank is maintained at a constant temperature after heating, the cloth is processed at this temperature, and the dyeing of the cloth reaches almost the limit after a lapse of a predetermined time. After completion of the dyeing, the treatment liquid in the treatment tank is diverted to the dye separation circulation path, rapidly cooled to a desired temperature by a cooler, and then filtered by a filter and returned to the treatment tank. Circulate.

【0008】これにより、未染着の染料は濾過器により
捕捉されるが、特に冷却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、濾過器にて分離
させることができる。
As a result, undyed dyes are captured by the filter. In particular, impurities such as oligomers dissolved in the treatment liquid and precipitated by cooling can be separated by the filter.

【0009】したがって、染着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。また、上記の処理液の
冷却によって布帛も冷却される。
Therefore, the treatment liquid after the completion of the dyeing is decolorized, so that the conventional washing step can be omitted and the stain on the inner surface of the treatment tank can be prevented. In addition, the cloth is also cooled by cooling the processing liquid.

【0010】[0010]

【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。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によって処理
布帛の循環経路を構成している。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to the embodiment shown in FIG. A downstream surface of the accumulation section in the accumulation tank 1 constituting the processing tank is formed in a tapered rising section 2, and a reel box 3 is disposed at the end of the rising section 2. An injection nozzle 4 is provided at a lower portion of the reel box 3, and a transfer pipe 5 is connected by piping from a downstream side of the injection nozzle 4 to a bottom surface on an upstream (rear) side of the accumulation tank 1. The transfer pipe 5 constitutes a circulation path for the treated fabric.

【0011】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。
A reel 6 is provided in the reel box 3, and a processing cloth 7 is hung on the reel 6 and is disposed endlessly across the accumulation tank 1 and the transfer pipe 5. The cloth 7 is moved and circulated in the direction of the arrow by the ejection of the processing liquid.

【0012】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。
A casing 8 made of a perforated plate is provided at the bottom portion on the upstream side of the storage tank 1, and serves as a partition for separating the processing liquid 9 and the cloth 7 bonded endlessly at the time of normal dyeing.

【0013】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。
A liquid reservoir 10 communicating with the inside of the tank 1 is provided at the bottom of the downstream side (front portion) of the storage tank 1, and the liquid reservoir 10 is connected to a pump 12 via a suction pipe 11, The discharge nozzle 12 is connected to the injection nozzle 4 via a discharge pipe 13, a filter 14, a multi-tube heat exchanger 15, and an outlet pipe 16, and these constitute a treatment liquid circulation path.

【0014】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。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。
A shower pipe 17 is provided at the upper portion of the reservoir 1 on the upstream side.
Is connected to the heat exchanger 15 through a pipe 18 branched from the outlet pipe 16. 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 release valve provided in an air release pipe 24 for reducing the pressure in the storage tank 1.

【0015】上記処理液循環路を構成する出口管16に
は、処理液を分流する分岐管25が分岐されており、脱
色処理弁26、流量調節弁27を介して処理液の冷却手
段である冷却器28に連通されている。冷却器28の出
口管29には処理液の濾過手段である濾過器30が接続
され、その戻り管31が上記滞溜部1に接続されてい
る。
A branch pipe 25 for branching the processing liquid is branched from the outlet pipe 16 constituting the processing liquid circulation path, and serves as a cooling means for the processing liquid via a decolorization processing valve 26 and a flow rate control valve 27. It is connected to a cooler 28. The outlet pipe 29 of the cooler 28 is connected to a filter 30 which is a means for filtering the processing liquid, and the return pipe 31 is connected to the reservoir 1.

【0016】上記出口管16には処理液の温度を検知す
る温度計32が設けられ、出口管29には冷却器28に
より冷却された処理液の温度を検知する温度計33が設
けられている。
The outlet pipe 16 is provided with a thermometer 32 for detecting the temperature of the processing liquid, and the outlet pipe 29 is provided with a thermometer 33 for detecting the temperature of the processing liquid cooled by the cooler 28. .

【0017】上記濾過器30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。該濾過器30で捕捉
された染料が混入した濃縮液は、排出管34、排出弁3
5を通じて液溜部36に溜められ、ドレン弁37の開操
作により所定部へ送られる。
As the filter 30, a membrane filter made of, for example, an ultra-membrane or a reverse osmosis membrane is used. The concentrated liquid mixed with the dye captured by the filter 30 is supplied to the discharge pipe 34 and the discharge valve 3.
The liquid is stored in the liquid storage part 36 through 5 and sent to a predetermined part by opening the drain valve 37.

【0018】38は流量調節弁である。以上のようであ
るから、布帛7の染色に際しては、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
するとともに処理液(染色液)を入れる。
Reference numeral 38 denotes a flow control valve. As described above, at the time of dyeing the cloth 7, the cloth 7 is arranged in an annular shape as shown in FIG.

【0019】そして、脱色処理弁26,26a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。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着処
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。
Then, the decolorization valves 26 and 26a are closed,
The pump 12 is activated to circulate the processing liquid through the processing liquid circulation path, and the heat exchanger 15 heats the processing liquid to a predetermined temperature. The heated treatment liquid is ejected from the ejection nozzle 4, and the ejection power causes the cloth 7 to circulate in the direction of the arrow to perform the dyeing treatment. This dyeing is performed at points A to C in FIG.
That is, the process is performed at points A to C in FIG.

【0020】次に染着工程が終った後、すなわち、図2
のC点後、熱交換器15による加熱を停止するとともに
冷却器28を冷却作動し、脱色処理弁26,26aを開
き、ポンプ12を駆動する。これにより、ポンプ12で
圧送された処理液は、処理液循環路を循環して布帛15
を移送するとともにその処理液の一部が出口管16より
分岐管25に分流され、冷却器28、濾過器30、脱色
処理弁26a、戻り管31を通じて滞溜槽1に入って循
環する。
Next, after the dyeing process is completed, ie, as shown in FIG.
After point C, the heating by the heat exchanger 15 is stopped, and the cooler 28 is cooled, the decolorization valves 26 and 26a are opened, and the pump 12 is driven. Thereby, the processing liquid pumped by the pump 12 circulates through the processing liquid circulation path and
And a part of the processing liquid is diverted from the outlet pipe 16 to the branch pipe 25, and circulates into the storage tank 1 through the cooler 28, the filter 30, the decolorization processing valve 26 a, and the return pipe 31.

【0021】この循環により、処理液は冷却器28によ
り冷却されるため、この処理液の温度を温度計33で検
知して、処理液を設定温度まで冷却する。なお、熱交換
器15を併用して処理液を冷却することもできる。上記
の処理液の循環により、未染着の染料は濾過器28に捕
捉されるが、特に冷却によって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、濾過機にて分離
させることができる。上記の処理液の冷却と濾過は図2
のC点からD点の範囲Fで行われ、その後、排液され
る。したがって、上記従来の図3のEで示した水洗いは
0〜1回程度でよい。
Since the processing liquid is cooled by the cooler 28 by this circulation, the temperature of the processing liquid is detected by the thermometer 33, and the processing liquid is cooled to the set temperature. Note that the processing liquid can be cooled by using the heat exchanger 15 in combination. Due to the circulation of the treatment liquid, undyed dyes are captured by the filter 28. In particular, impurities such as oligomers dissolved and present in the treatment liquid are precipitated by cooling, and separated by the filter. Can be. The cooling and filtration of the above processing solution is shown in FIG.
Is performed in the range F from the point C to the point D, and then the liquid is drained. Therefore, the conventional water washing shown by E in FIG.

【0022】次に、濾過器30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。
Next, a reverse immersion filter is used as the filter 30.
Polyester fiber is used as the cloth 7, and the disperse dye is 2%.
owf (dye (%) based on fiber weight)
An example in which the dye is separated at the above cooling step after dyeing at ° C. will be described.

【0023】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28によって
処理液を40℃まで冷却して約20〜30分循環させた
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。
In the case of polyester fiber, the oligomer is dissolved when the temperature of the treatment liquid is 100 ° C. or higher at the same time as the filtration treatment of the undyed dye, but the oligomer is dissolved when cooled to a predetermined temperature. When the processing solution is cooled to 40 ° C. by the cooler 28 and circulated for about 20 to 30 minutes, the processing solution becomes almost colorless and the oligomer can be removed. At this time, the processing solution is removed by a spectrophotometer. As a result of the measurement, the absorbance was as close to 0 as possible.

【0024】その後、排液に続き、水洗いを従来法では
3回行っていたのを1回に省略して処理を完了したとこ
ろ、従来と同等の処理結果が得られた。また、濾過器3
0で捕捉された染料等は、濃縮液となって排出管34か
ら液溜部36に溜められ、ドレン弁37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。
Then, following the drainage, the washing was performed three times in the conventional method, but was omitted once, and the processing was completed. As a result, a processing result equivalent to the conventional one was obtained. Filter 3
The dye or the like captured at 0 is stored in the liquid storage section 36 from the discharge pipe 34 as a concentrated liquid, and is sent to a predetermined section by opening the drain valve 37. This concentrate can be used again for staining.

【0025】更に、上記のように処理液の冷却温度を4
0℃に設定することにより、濾過器30の逆浸透膜の耐
久性を長期間保つことができた。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。
Further, as described above, the cooling temperature of the
By setting the temperature to 0 ° C., the durability of the reverse osmosis membrane of the filter 30 could be maintained for a long time. In the above embodiment,
This is an example in which the present invention is applied to a dyeing machine that circulates a fabric. However, the present invention can be used for other types of dyeing machines and other types of dyes, and is limited to the dyeing machine in the illustrated embodiment. It does not do.

【0026】[0026]

【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、水洗い工程を省略で
き、処理時間の短縮と、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。
As described above, according to the invention of the present application, it is possible to separate and remove almost all of the undyed residual dye from the textile contained in the dyeing effluent, so that the washing step can be omitted and the processing time can be reduced. Shortening and the amount of water used can be greatly reduced.
Further, since the adhesion of the dye in the dyeing tank can be reduced, the washing of the kettle by changing the color can be simplified.

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

【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。
FIG. 1 shows an embodiment of the present invention, and is a piping diagram in which a processing tank section is sectioned.

【図2】本発明の処理工程を示す図。FIG. 2 is a view showing a processing step of the present invention.

【図3】従来の処理工程を示す図。FIG. 3 is a diagram showing a conventional processing step.

【符号の説明】[Explanation of symbols]

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 25,31…染料分離循環路を構成する管 28…冷却器 30…濾過器 DESCRIPTION OF SYMBOLS 1 ... Retention tank which is a processing tank 10, 11, 13, 16 ... Pipe which comprises a processing liquid circulation path 25, 31 ... Pipe which comprises a dye separation circulation path 28 ... Cooler 30 ... Filter

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 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、冷却器と濾過器を有す
る染料分離循環路を設け、繊維製品の染着終了後に処理
液を上記染料分離循環路へ分流して上記冷却器で冷却し
た後、濾過器で濾過して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。
1. A dyeing process for dyeing textiles at a predetermined temperature in a processing tank, wherein a dye separation circuit having a cooler and a filter is provided. And cooling the mixture with the cooler, followed by filtering with a filter and returning to a treatment tank.
【請求項2】 処理タンクの外部にポンプを介して処理
液循環路を形成し、該処理液循環路の一部より分岐して
処理タンクに戻る染料分離循環路を設け、該染料分離循
環路に、上流側に位置して冷却器を設け、下流側に位置
して濾過器を設けたことを特徴とする繊維製品の処理装
置。
2. A processing liquid circulation path is formed outside the processing tank via a pump, and a dye separation circulation path branched from a part of the processing liquid circulation path and returning to the processing tank is provided. And a cooling device provided on the upstream side and a filter provided on the downstream side.
JP16679498A 1998-06-15 1998-06-15 Textile product processing method and apparatus Expired - Lifetime JP3755707B2 (en)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16679498A JP3755707B2 (en) 1998-06-15 1998-06-15 Textile product processing method and apparatus

Publications (2)

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JPH11350334A true JPH11350334A (en) 1999-12-21
JP3755707B2 JP3755707B2 (en) 2006-03-15

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114277533A (en) * 2021-12-27 2022-04-05 江苏爱利多印机科技有限公司 Knitting soaping machine convenient to use and operate

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4659939B2 (en) * 1999-12-09 2011-03-30 日金加工株式会社 Textile product processing method and apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114277533A (en) * 2021-12-27 2022-04-05 江苏爱利多印机科技有限公司 Knitting soaping machine convenient to use and operate
CN114277533B (en) * 2021-12-27 2023-07-07 江苏爱利多印机科技有限公司 Knitting soaping machine convenient to use operation

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