JPH0638152Y2 - Liquid-flow textile processing equipment - Google Patents

Liquid-flow textile processing equipment

Info

Publication number
JPH0638152Y2
JPH0638152Y2 JP1991025912U JP2591291U JPH0638152Y2 JP H0638152 Y2 JPH0638152 Y2 JP H0638152Y2 JP 1991025912 U JP1991025912 U JP 1991025912U JP 2591291 U JP2591291 U JP 2591291U JP H0638152 Y2 JPH0638152 Y2 JP H0638152Y2
Authority
JP
Japan
Prior art keywords
heat exchanger
control valve
liquid
steam inlet
dyeing
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.)
Expired - Lifetime
Application number
JP1991025912U
Other languages
Japanese (ja)
Other versions
JPH04100281U (en
Inventor
和雄 山田
▼たか▲夫 西川
正雄 新田
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.)
Toray Industries Inc
Toyota Motor Corp
Original Assignee
Toray Industries Inc
Toyota Motor 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 Toray Industries Inc, Toyota Motor Corp filed Critical Toray Industries Inc
Priority to JP1991025912U priority Critical patent/JPH0638152Y2/en
Publication of JPH04100281U publication Critical patent/JPH04100281U/ja
Application granted granted Critical
Publication of JPH0638152Y2 publication Critical patent/JPH0638152Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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  • Treatment Of Fiber Materials (AREA)

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】本考案は、液流式繊維製品処理装
置に関する。詳しく述べるならば、処理液噴射条件に合
わせ温度ハンチングを最小限にして処理する液流染色機
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid flow type textile product processing apparatus. More specifically, the present invention relates to a jet dyeing machine that performs processing by minimizing temperature hunting in accordance with processing solution jetting conditions.

【0002】[0002]

【従来技術】処理液循環中にある1ケの熱交換器により
処理液の温度制御を行っていた。尚、1ケの処理機に複
数の熱交換器を使用したものはあるが、(特開昭49−
81663号)滞溜槽と液噴射部とをつなぐ処理液循環
路中に設けたものではない。
2. Description of the Related Art The temperature of a processing liquid is controlled by a single heat exchanger in the circulation of the processing liquid. Incidentally, there is one in which a plurality of heat exchangers are used in one processing machine (see Japanese Patent Laid-Open No. 49-
No. 81663) It is not provided in the processing liquid circulation path that connects the retention tank and the liquid injection unit.

【0003】[0003]

【本考案が解決しようとする課題】通常、液流染色機は
染色処理と缶体洗滌処理とに使い分けるが、缶体洗滌の
場合には染色に使用する処理液量の3〜5倍の処理液量
を必要とし、昇温時間を短縮するため、可能な限り大き
な熱交換機を設けているが、染色の場合、特に処理布帛
が低目付になるほど循環をスムーズに行うのに液噴射部
からの噴射流量は極端に少ないので、前記洗滌の場合の
熱交換器を使用すると温度ハンチングが大きくなり、温
度差により染めムラが発生するので昇温に時間をかけて
おり、温度ハンチングを最小にし染色時間を短縮し生産
性を向上させることが望まれていた。
[Problems to be Solved by the Invention] Normally, a jet dyeing machine is used separately for dyeing treatment and can body washing treatment. However, in the case of can body washing, the treatment amount is 3 to 5 times the amount of treatment liquid used for dyeing. A large amount of heat exchanger is provided as much as possible in order to reduce the temperature rise time because it requires a liquid amount. Since the injection flow rate is extremely low, temperature hunting increases when using a heat exchanger in the case of the above washing, and uneven dyeing occurs due to the temperature difference, so it takes time to raise the temperature and minimize temperature hunting and dyeing time. It has been desired to shorten the period and improve the productivity.

【0004】本考案は上記の如き欠点を解消し、温度ハ
ンチングを最小とした高精度の温度制御と染色に必要な
温度域以外の処理には急速昇温ができることを可能とし
た生産性の高い装置を提供するのが目的である。
The present invention solves the above-mentioned drawbacks and enables high-accuracy temperature control with minimum temperature hunting and rapid temperature rise for processes other than the temperature range necessary for dyeing, which is highly productive. The purpose is to provide a device.

【0005】[0005]

【課題を解決するための手段】本考案は前記の課題を解
決するために、繊維製品(以下、処理布帛という)を真
直状態で移送させる移送管と、蛇行状態で移送させる滞
溜槽とを連結して環状の処理布帛移送通路を形成し、該
通路内に無端状の処理布帛を架設すると共に処理液を上
記滞溜槽よりポンプを介して移送管の上流端に設けた液
噴射部に圧送する処理液循環路を形成したものにおい
て、前記処理液循環路中に染色工程時に使用する第1の
熱交換器(13)に内蔵するスチーム管に蒸気入口コン
トロール弁(24)を設け、且つ上記第1の熱交換器
(13)の外に上記処理液循環路中には、更に前記第1
の熱交換器(13)に比し数倍の昇温能力を有する第2
の熱交換器(17)を設け、この第2熱交換器に内蔵す
るスチーム管にも蒸気入口コントロール弁(23)を設
け、両熱交換器の蒸気入口コントロール弁を、染色工程
時には第2の熱交換器のコントロール弁(23)を閉に
し、第1の熱交換器のコントロール弁(24)を開にし
て作用状態となし、弁体洗浄工程時には第2熱交換器の
コントロール弁(23)を開にして作用状態とし、第1
熱交換器のコントロール弁(24)を閉ないしは適宜に
制御するように両熱交換器に制御手段を設けたことを特
徴とするものである。
In order to solve the above-mentioned problems, the present invention connects a transfer pipe for transferring a fiber product (hereinafter referred to as treated cloth) in a straight state and a retention tank for transferring in a meandering state. To form an annular treatment cloth transfer passage, an endless treatment cloth is installed in the passage, and the treatment liquid is pressure-fed from the retention tank through a pump to a liquid injection section provided at the upstream end of the transfer pipe. In the case where the treatment liquid circulation passage is formed, the first treatment liquid circulation passage is used in the dyeing step.
The steam pipe installed in the heat exchanger (13) is connected to the steam inlet
A first heat exchanger provided with a trawl valve (24)
In addition to (13), in the processing liquid circulation path, the first
Second, which has several times the heating capacity compared to the heat exchanger (13)
A heat exchanger (17) is installed in this second heat exchanger.
A steam inlet control valve (23) is also installed on the steam pipe.
, The steam inlet control valve of both heat exchangers, the dyeing process
Sometimes the control valve (23) of the second heat exchanger is closed
Then open the control valve (24) of the first heat exchanger.
And the second heat exchanger is not activated during the valve body cleaning process.
Open the control valve (23) to activate it and
The control valve (24) of the heat exchanger is closed or appropriately
It is characterized in that both heat exchangers are provided with control means for controlling .

【0006】[0006]

【作用】本考案によれば処理布帛を無端状に結反し、真
直状態で移送させる移送管と蛇行状態で移送させる滞溜
槽とを連結して環状の処理布帛移送通路を有し、移送管
上流端に液噴射部を配設し、一方、滞溜槽に設けられた
1ケ所以上の吸込管及びポンプ、直列又は並列配置とし
た2ケの熱交換器を介して、前記液噴射部に至る処理液
循環路を形成し、前記2ケの熱交換器のうちの片方を染
色に必要な温度特性をもった昇温能力を与え、他方を缶
体洗滌工程を目的として、前記染色用熱交換器の3〜5
倍の昇温能力を与えたことにより、任意に片方又は両方
の熱交換器を選択することができる。
Contrary forming the treated fabric according to the present invention endlessly, and connects the Todokotamari tank for transferring a serpentine state transfer pipe for transferring an annular treated fabric transport path in straight state, the transfer pipe upstream A process to reach the liquid injection unit through a liquid injection unit arranged at the end, while one or more suction pipes and pumps provided in the retention tank and two heat exchangers arranged in series or in parallel are provided. Forming a liquid circulation path, one of the two heat exchangers is provided with a temperature raising ability having a temperature characteristic required for dyeing, and the other heat exchanger for dyeing for the purpose of a can body washing step. 3-5
One or both heat exchangers can be arbitrarily selected by giving the double heating ability.

【0007】すなわち無端状に結合したデリケートな低
目付織物の染色に際しては、布帛の走行安定を得るのに
液噴射部からの噴射流量は極端に少なくなるので2ケの
熱交換器のうち染色用を目的とした熱交換器だけを用
い、温度ハンチングによる温度差を最小にし、染めムラ
が発生するのを防ぐことができるうえに2ケの熱交換器
を用いることにより、染色時の3〜5倍の処理液量を必
要とする缶体洗滌工程や温度ハンチングが問題にならな
い工程には急速に昇温と冷却ができるようにして処理時
間を短縮し、大幅な生産性向上が得られるようにしたも
のである。
That is, when dyeing a delicate low-basis weight fabric endlessly bonded, the jet flow rate from the liquid jetting part is extremely small in order to obtain stable running of the fabric. By using only the heat exchanger for the purpose of minimizing the temperature difference due to temperature hunting and preventing uneven dyeing, by using two heat exchangers, 3 to 5 at the time of dyeing can be obtained. In the can body cleaning process that requires double the amount of processing liquid and the process where temperature hunting is not a problem, rapid heating and cooling can be performed to shorten the processing time and significantly improve productivity. It was done.

【0008】[0008]

【実施例】次に添付図面に基づいて本考案の実施例を説
明する。第1図において1は滞溜槽で両端に入口部2と
出口部3を有している。 4は処理布帛9を直線状で移
送する移送管で上流端に液噴射部5が設けてある。6は
処理液面、7は滞溜槽1の入口部2に設けられたケーシ
ングで多孔板で形成され、処理液の一部が落下する構造
となっている。 8は処理布帛9を移送管4へ送り込ん
で循環させる駆動リールで処理液面6から処理布帛9を
引き上げ液噴射部5へ送り込む。
Embodiments of the present invention will be described below with reference to the accompanying drawings. In FIG. 1, reference numeral 1 designates a retention tank having an inlet portion 2 and an outlet portion 3 at both ends. Reference numeral 4 denotes a transfer pipe for transferring the treated cloth 9 in a straight line, and a liquid injection part 5 is provided at the upstream end. 6 is a surface of the treatment liquid, and 7 is a casing provided at the inlet 2 of the stagnant tank 1, which is formed of a perforated plate and has a structure in which a part of the treatment liquid falls. A drive reel 8 sends the treated cloth 9 to the transfer pipe 4 and circulates the treated cloth 9, and the treated cloth 9 is pulled up from the treated liquid surface 6 and fed to the liquid ejecting unit 5.

【0009】10及び11は処理液吸込部、12は吸込
部集合配管でスチーム管13’を内蔵して第1熱交換器
13を構成している。 14は主ポンプである。 処理
液は吐出管15を介してフィルタ16及び第2熱交換器
17を通り、熱交換器出口配管18で分岐され、一方は
19の流量調節弁を介して液噴射部5に至り、他方は流
量調節弁21を介して逆噴射部22に連結されている。
20は液噴射部5の布帛入口に向けたシャワーの流量調
節弁である。
Reference numerals 10 and 11 denote treatment liquid suction portions, and 12 denotes suction portion collecting pipes, which constitute a first heat exchanger 13 by incorporating a steam pipe 13 'therein. 14 is a main pump. The treatment liquid passes through the discharge pipe 15, the filter 16 and the second heat exchanger 17, and is branched by the heat exchanger outlet pipe 18. One reaches the liquid injection unit 5 through the flow rate control valve 19 and the other one. It is connected to the reverse injection unit 22 via the flow rate control valve 21.
Reference numeral 20 is a flow rate control valve of the shower directed to the cloth inlet of the liquid ejecting unit 5.

【0010】第2熱交換器17の昇温能力は、第1熱交
換器13の3〜5倍の昇温能力を発生できるようになっ
ている。23,24は蒸気入口コントロール弁、25,
26はスチームトラップである。 第1熱交換器と第2
熱交換器はそれぞれ図示していない冷却水コントロール
弁を付属している。27は吸水弁、28は排液弁であ
る。
The heating capacity of the second heat exchanger 17 is 3 to 5 times that of the first heat exchanger 13. 23 and 24 are steam inlet control valves, 25 and
26 is a steam trap. First heat exchanger and second
Each heat exchanger is equipped with a cooling water control valve (not shown). Reference numeral 27 is a water intake valve, and 28 is a drainage valve.

【0011】処理布帛9は液噴射部5によって移送管4
を通り滞溜槽1に導入された後、無端状に装着される。
処理中、処理布帛9は液噴射部5により滞溜槽1の出口
部より引き上げられ移送管4を急速液流とともに送られ
ケーシング7より、再度、滞溜槽1へ送られ循環移送を
繰り返す。染色に際し、染色重要温度域に達すると、手
動又はプログラム設定器の信号などにより自動的に第1
熱交換器13のみが作動するように蒸気入口コントロー
ル弁24のみの制御状態とし、予め用意された温度プロ
グラムに従って処理が進行される。
The treated cloth 9 is transferred to the transfer pipe 4 by the liquid jetting unit 5.
After being introduced into the retention tank 1 through the above, it is mounted endlessly.
During the treatment, the treated cloth 9 is pulled up from the outlet of the retention tank 1 by the liquid jetting section 5 and sent through the transfer pipe 4 together with the rapid liquid flow, and again sent from the casing 7 to the retention tank 1 to repeat the circulation transfer. When dyeing reaches an important temperature range during dyeing, the first
Only the steam inlet control valve 24 is controlled so that only the heat exchanger 13 operates, and the process proceeds according to a temperature program prepared in advance.

【0012】次に温度ハンチングが問題にならない染色
温度域や缶体洗滌などは2ケの蒸気入口コントロール弁
23と24を同時に制御させることができる。本案は上
記のような構成のため低目付け織物の染色処理などのよ
うに液噴射部5からの噴射流量が極端に少なく大きな温
度ハンチングが生じ易い場合に昇温能力を必要最小限と
した第1熱交換器13により温度差を最小にし、さらに
缶体洗滌工程のような多量な処理流量を必要とし昇温時
間の短縮が望まれる場合には第1熱交換器13と第2熱
交換器17の両方を用いることにより処理時間を大幅に
短縮できるように構成されている。
Next, the two steam inlet control valves 23 and 24 can be controlled at the same time in the dyeing temperature range where temperature hunting does not pose a problem, the washing of the can body, and the like. According to the first aspect of the present invention, the temperature raising capacity is minimized when the jet flow rate from the liquid jetting section 5 is extremely small and a large temperature hunting is likely to occur, such as a dyeing treatment of a low-basis weight fabric. The first heat exchanger 13 and the second heat exchanger 17 are used when the temperature difference is minimized by the heat exchanger 13 and a large processing flow rate such as a can body washing process is required and a shortening of the temperature raising time is desired. Both are used so that the processing time can be significantly shortened.

【0013】[0013]

【考案の効果】本案は上述のように染色工程においては
第1熱交換器(13)のみを使用して温度ハンチングを
最小にして染めムラ発生を防ぐことができるうえに、温
度ハンチングの問題にならない缶体洗滌工程では第2熱
交換器(17)のみ或いはこれと第1熱交換器(13)
を併用して急速に昇温及び冷却することにより処理時間
を短縮し大幅に生産性を向上させることができる。
As described above, the present invention can prevent the uneven dyeing by minimizing the temperature hunting by using only the first heat exchanger (13) in the dyeing process, and at the same time, the problem of the temperature hunting is solved. Only the second heat exchanger (17) or this and the first heat exchanger (13) in the can body washing process which does not become
By using these together to rapidly raise the temperature and cool, the processing time can be shortened and the productivity can be greatly improved.

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

【図1】本案の実施例を示す側断面図である。FIG. 1 is a side sectional view showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 滞溜槽 4 移送管 5 液噴射部 9 処理布帛 13 第1熱交換器 14 主ポンプ 17 第2熱交換器 23,24 蒸気入口コントロール弁 1 Retention Tank 4 Transfer Pipe 5 Liquid Injection Section 9 Treated Fabric 13 First Heat Exchanger 14 Main Pump 17 Second Heat Exchanger 23, 24 Steam Inlet Control Valve

───────────────────────────────────────────────────── フロントページの続き (72)考案者 新田 正雄 滋賀県大津市園山1丁目1番1号 東レ株 式会社 滋賀事業場内 (56)参考文献 特開 昭49−81663(JP,A) 特開 昭50−53682(JP,A) 特公 昭51−46192(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Masao Nitta Inventor, Masao Nitta 1-1-1, Sonoyama, Otsu City, Shiga Toray Co., Ltd. Shiga Plant (56) References JP-A-49-81663 (JP, A) Special Features Kai 50-53682 (JP, A) JP-B 51-46192 (JP, B2)

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 繊維製品(以下、処理布帛という)を真
直状態で移送させる移送管と、蛇行状態で移送させる滞
溜槽とを連結して環状の処理布帛移送通路を形成し、該
通路内に無端状の処理布帛を架設すると共に処理液を上
記滞溜槽よりポンプを介して移送管の上流端に設けた液
噴射部に圧送する処理液循環路を形成したものにおい
て、前記処理液循環路中に染色工程時に使用する第1の
熱交換器(13)に内蔵するスチーム管に蒸気入口コン
トロール弁(24)を設け、且つ上記第1の熱交換器
(13)の外に上記処理液循環路中には、更に前記第1
の熱交換器(13)に比し数倍の昇温能力を有する第2
の熱交換器(17)を設け、この第2熱交換器に内蔵す
るスチーム管にも蒸気入口コントロール弁(23)を設
け、両熱交換器の蒸気入口コントロール弁を、染色工程
時には第2の熱交換器のコントロール弁(23)を閉に
し、第1の熱交換器のコントロール弁(24)を開にし
て作用状態となし、弁体洗浄工程時には第2熱交換器の
コントロール弁(23)を開にして作用状態とし、第1
熱交換器のコントロール弁(24)を閉ないしは適宜に
制御するように両熱交換器に制御手段を設けたことを特
徴とする液流式繊維製品処理装置。
1. An annular processing cloth transfer passage is formed by connecting a transfer pipe for transferring a fiber product (hereinafter referred to as a treated cloth) in a straight state and a retention tank for transferring in a meandering state, and forming an annular treated cloth transfer passage in the passage. in those processing liquid while bridging the endless treated fabric to form a treatment liquid circulation path for pumping the liquid ejection portion provided on the upstream end of the transfer pipe through the pump from the Todokotamariso, the treatment liquid circulation path First to use during the dyeing process
The steam pipe installed in the heat exchanger (13) is connected to the steam inlet
A first heat exchanger provided with a trawl valve (24)
In addition to (13), in the processing liquid circulation path, the first
Second, which has several times the heating capacity compared to the heat exchanger (13)
A heat exchanger (17) is installed in this second heat exchanger.
A steam inlet control valve (23) is also installed on the steam pipe.
, The steam inlet control valve of both heat exchangers, the dyeing process
Sometimes the control valve (23) of the second heat exchanger is closed
Then open the control valve (24) of the first heat exchanger.
And the second heat exchanger is not activated during the valve body cleaning process.
Open the control valve (23) to activate it and
The control valve (24) of the heat exchanger is closed or appropriately
A liquid flow type textile processing apparatus, characterized in that both heat exchangers are provided with control means for controlling .
JP1991025912U 1991-04-17 1991-04-17 Liquid-flow textile processing equipment Expired - Lifetime JPH0638152Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991025912U JPH0638152Y2 (en) 1991-04-17 1991-04-17 Liquid-flow textile processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991025912U JPH0638152Y2 (en) 1991-04-17 1991-04-17 Liquid-flow textile processing equipment

Publications (2)

Publication Number Publication Date
JPH04100281U JPH04100281U (en) 1992-08-31
JPH0638152Y2 true JPH0638152Y2 (en) 1994-10-05

Family

ID=31760973

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991025912U Expired - Lifetime JPH0638152Y2 (en) 1991-04-17 1991-04-17 Liquid-flow textile processing equipment

Country Status (1)

Country Link
JP (1) JPH0638152Y2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IL40966A (en) * 1972-11-29 1976-07-30 Klier S Process for continuous treatment of textile materials
JPS5053682A (en) * 1973-09-18 1975-05-12
JPS5146192A (en) * 1974-10-18 1976-04-20 Hitachi Ltd

Also Published As

Publication number Publication date
JPH04100281U (en) 1992-08-31

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