JPH0135944B2 - - Google Patents
Info
- Publication number
- JPH0135944B2 JPH0135944B2 JP57138277A JP13827782A JPH0135944B2 JP H0135944 B2 JPH0135944 B2 JP H0135944B2 JP 57138277 A JP57138277 A JP 57138277A JP 13827782 A JP13827782 A JP 13827782A JP H0135944 B2 JPH0135944 B2 JP H0135944B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- tank
- steamer
- cooling tank
- filter
- 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
Links
- 239000007788 liquid Substances 0.000 claims description 103
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 239000004744 fabric Substances 0.000 claims description 24
- 238000010583 slow cooling Methods 0.000 claims description 21
- 238000010438 heat treatment Methods 0.000 claims description 16
- 239000002699 waste material Substances 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 8
- 239000000706 filtrate Substances 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 5
- 238000007789 sealing Methods 0.000 description 13
- 238000004140 cleaning Methods 0.000 description 11
- 238000011282 treatment Methods 0.000 description 9
- 239000000110 cooling liquid Substances 0.000 description 8
- 238000004043 dyeing Methods 0.000 description 4
- 208000016261 weight loss Diseases 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- 239000003518 caustics Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009990 desizing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013585 weight reducing agent Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
- D06B23/00—Component 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
- D06B23/14—Containers, e.g. vats
- D06B23/16—Containers, e.g. vats with means for introducing or removing textile materials without modifying container pressure
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
- D06B23/00—Component 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
- D06B23/20—Arrangements of apparatus for treating processing-liquids, -gases or -vapours, e.g. purification, filtration or distillation
- D06B23/22—Arrangements of apparatus for treating processing-liquids, -gases or -vapours, e.g. purification, filtration or distillation for heating
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Treatment Of Fiber Materials (AREA)
Description
【発明の詳細な説明】
本発明は、布帛を連続的に湿熱処理する高圧ス
チーマにおいて、この高圧スチーマ缶体より排出
する排熱を再使用して熱エネルギーの無駄を省く
と共に熱エネルギーの有効利用を達成し、更には
高圧スチーマ缶体より排出される排液を再使用し
て水資源の節約を達成できるようにした布帛の連
続湿熱処理装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention is a high-pressure steamer that continuously performs wet heat treatment on fabrics, and the waste heat discharged from the high-pressure steamer can is reused to eliminate wasted thermal energy and to effectively utilize thermal energy. The present invention relates to a continuous wet heat treatment apparatus for fabrics which achieves this and further enables the conservation of water resources by reusing waste liquid discharged from a high-pressure steamer can.
工業的に生産する布帛を、糊抜き、精練、染
色、縮じゆう、減量等の処理加工（以下これらの
処理加工を単に湿熱処理と称す）を連続的に行な
う方法においては、例えば本発明者が開発した高
圧スチーマを使用することが公知とされている
が、この湿熱処理を行なう高圧スチーマの運転時
においては、高圧スチーマの外部に設備せしめた
液槽あるいは、高圧スチーマの入口側シール機構
内に形成されている液封層内に予め入れられてい
る処理液（前処理、減量処理時には苛性液、染色
処理時には染色液等）内に被処理布を通し、次い
でこの含液布を高圧スチーマ缶体内に導入してス
チーミングと、ボイリング（含水）を繰返し行な
つて目的とする処理加工を行なつている。 In a method in which industrially produced fabric is continuously subjected to treatments such as desizing, scouring, dyeing, shrinking, and weight loss (hereinafter, these treatments are simply referred to as moist heat treatment), the present inventor, for example, It is well known that the high-pressure steamer developed by The fabric to be treated is passed through a treatment liquid (caustic liquid for pre-treatment and weight reduction treatment, dyeing liquid for dyeing treatment, etc.) that has been placed in advance in the liquid sealing layer formed in the liquid sealing layer, and then this liquid-impregnated fabric is passed through a high-pressure steamer. The material is introduced into the can and subjected to repeated steaming and boiling (hydration) to perform the desired processing.
ところが、上記高圧スチーマの運転時、即ち処
理時においては、そのスチーマ缶体内から逐次排
出される高温加熱排液を廃棄しているために熱エ
ネルギーの無駄が生じている。またスチーマ缶体
の布帛導入口及び布帛導出口に設けられているシ
ール機構には、シールロールの洗浄液及び徐冷液
を逐次供給しなければならないことから、消費水
量が多量となつていた。 However, during operation of the high-pressure steamer, ie, during processing, thermal energy is wasted because the high-temperature heated waste liquid successively discharged from the steamer can is discarded. Furthermore, the sealing mechanism provided at the fabric inlet and fabric outlet of the steamer can has to be successively supplied with seal roll cleaning liquid and slow cooling liquid, resulting in a large amount of water consumption.
本発明は、かかることから鑑みてなされたもの
で、高圧スチーマ缶体より排出される熱エネルギ
ーを再使用して熱エネルギーの有効利用を実現さ
せ、更には、使用水量を可及的抑制して、従来の
消費水量を半減させて、省エネルギーと省資源に
役立ち、しかも効果的な処理が達成できる布帛の
湿熱処理装置を提供することを目的とするもので
ある。 The present invention has been made in view of the above, and realizes effective utilization of thermal energy by reusing the thermal energy discharged from the high-pressure steamer can, and further reduces the amount of water used as much as possible. It is an object of the present invention to provide a wet heat treatment apparatus for fabrics that can reduce the amount of water consumed by half compared to conventional methods, contribute to energy and resource conservation, and achieve effective treatment.
以下に本発明を図面に示す実施例に基いて詳細
に説明する。 The present invention will be explained in detail below based on embodiments shown in the drawings.
１は布帛を湿熱反応処理するための高圧スチー
マ缶体であつて、この高圧スチーマ缶体１は高圧
湿熱、例えば100℃以上160℃の湿熱が保たれるよ
うに、そのスチーマ缶体１に設けた布帛導入口２
及び布帛導出口３には夫々の導入側シール機構４
及び導出側シール機構５が設けられている。この
導入側シール機構４には、液封層４1と、この液
封層４1の上側開口部を閉塞する一対のシールゴ
ムロール４2と、このシールゴムロール４2を常時
洗浄するための洗浄槽４3を有し、更に上記液封
層４1においては、処理液等の給液管４4を具備せ
しめているものである。また前記の導出側シール
機構５の内部には略Ｕ字状の徐冷槽５1が構成さ
れており、更にこの徐冷槽５1には冷却液供給管
５2と、冷却液排出管５3と上記徐冷槽５1の上側
開口部を閉塞する一のシールゴムロール５4とが
設けられていて、この徐冷槽５1内には常温又は
冷却された液が循環され、その徐冷槽５1の出口
付近では約50℃の冷却水となるように液温と供給
液量が調整されている。 Reference numeral 1 denotes a high-pressure steamer can for subjecting fabric to a wet heat reaction treatment. Fabric introduction port 2
And the fabric outlet 3 is provided with an inlet-side seal mechanism 4.
and an outlet side sealing mechanism 5 are provided. The introduction-side sealing mechanism 4 includes a liquid sealing layer 4 1 , a pair of seal rubber rolls 4 2 that close the upper opening of the liquid sealing layer 4 1 , and a cleaning tank for constantly cleaning the seal rubber roll 4 2 . 4 3 , and the liquid sealing layer 4 1 is further provided with a liquid supply pipe 4 4 for supplying processing liquid or the like. Furthermore, a substantially U-shaped slow cooling tank 5 1 is configured inside the outlet side sealing mechanism 5 , and the slow cooling tank 5 1 further includes a cooling liquid supply pipe 5 2 and a cooling liquid discharge pipe 5 . 3 and a seal rubber roll 54 that closes the upper opening of the slow cooling tank 51 , and a room temperature or cooled liquid is circulated in the slow cooling tank 51 , and the slow cooling The liquid temperature and the amount of liquid supplied are adjusted so that the cooling water is approximately 50°C near the outlet of tank 51 .
スチーマ缶体１の内部には処理すべき布帛６を
上下蛇行状に移行せしめるための多数本のガイド
ロール７が配設されている。 A large number of guide rolls 7 are disposed inside the steamer can 1 to move the fabric 6 to be treated in an up-and-down meandering manner.
またスチーマ缶体１の内底部には、ガイドロー
ル７によつてガイド移送される布帛６に液を再度
含浸せしめるための複数個の液付与槽８が所定の
間隔でしかも高低差が順次低くなるように配設さ
れており、各液付与層相互間には、上段の液付与
槽よりオーバーフローされた液を下段の液付与槽
へ順次供給せしめるための給液管９が配管されて
いる。１０はテンシヨン調整ロール、１１は蒸気
供給パイプ、１２はスチーマ缶体１内の適所に配
設されたしのぎバーである。１３は給水管であつ
てこの給水管１３からの水は一旦水槽１４内に貯
えられた後適量づつ、前記の洗浄槽４3内へ供給
される。１５はその洗浄槽４3より導出された洗
浄水を連続的に濾過する濾過器であり、この濾過
器１５より導出された濾過水は、冷却液供給管５
２を経て前記の徐冷槽５1内へ供給されるようにな
つている。１６は徐冷槽５1より排出された液を
濾過するための濾過器であつて、この濾過器１６
からの濾過液は液槽１７内に貯積される。１８は
スチーマ缶体１の最下段液付与槽８より排出され
る高温加熱液を流通する熱交換器であつて、この
熱交換器１８により、前記の液槽１７よりポンプ
１９で圧送される液は加熱され、スチーマ缶体１
内の最上段液付与槽８内へ順次供給されるように
なつている。２０はスチーマ缶体１の外部に設け
た液槽（サチユレータ）であるが、この液槽２０
の周囲は、加熱液槽２１による２重構造となつて
いる。そして、その加熱液槽２１内へは熱交換器
１８より排出された熱液が配管２２を経て供給さ
れ、更にこの加熱液槽２１から排出される液は濾
過器２３を経て、例えば図示しない洗浄機等の洗
浄液として使用されるものである。尚上記の濾過
器１５，１６，２３は、排液中に含される糸屑等
の不純物を連続的に分離できるものであればよ
く、例えば本発明者が既に出願している濾過装置
（特願昭54−164573号、特願昭54−164574号、特
願昭57−88471号）を利用することができる。 Furthermore, at the inner bottom of the steamer can body 1, a plurality of liquid application tanks 8 are arranged at predetermined intervals and the difference in height gradually decreases for impregnating the fabric 6 guided and transferred by the guide rolls 7 with liquid again. A liquid supply pipe 9 is installed between each liquid application layer to sequentially supply the liquid overflowing from the upper liquid application tank to the lower liquid application tank. 10 is a tension adjustment roll, 11 is a steam supply pipe, and 12 is a bridging bar disposed at a proper position within the steamer can body 1. Reference numeral 13 denotes a water supply pipe, and water from this water supply pipe 13 is once stored in a water tank 14 and then supplied in appropriate amounts into the cleaning tank 43 . 15 is a filter that continuously filters the washing water drawn out from the washing tank 43 , and the filtered water drawn out from this filter 15 is passed through the cooling liquid supply pipe 5.
2 and is supplied into the slow cooling tank 51 . 16 is a filter for filtering the liquid discharged from the slow cooling tank 51 , and this filter 16
The filtrate from is stored in the liquid tank 17. Reference numeral 18 denotes a heat exchanger through which the high-temperature heated liquid discharged from the lowermost liquid application tank 8 of the steamer can body 1 flows. is heated, steamer can body 1
The liquid is sequentially supplied into the uppermost liquid application tank 8 within the tank. 20 is a liquid tank (saturator) provided outside the steamer can body 1;
The area around the heating liquid tank 21 has a double structure. The hot liquid discharged from the heat exchanger 18 is supplied into the heated liquid tank 21 through a pipe 22, and the liquid discharged from the heated liquid tank 21 is further passed through a filter 23, and then, for example, is washed, not shown. It is used as a cleaning liquid for machines, etc. Note that the above-mentioned filters 15, 16, and 23 may be of any type as long as they can continuously separate impurities such as lint contained in the waste liquid. (Japanese Patent Application No. 54-164573, Japanese Patent Application No. 54-164574, Japanese Patent Application No. 88471/1983) can be used.
以上が本実施例の構成であるが、次にその作用
について述べると、上記高圧スチーマを運転する
に当つては、先ずそのスチーマ缶体１内に加圧蒸
気を送り込んでスチーマ缶体内を例えば160℃の
高圧湿熱状態に保持せしめると共に、液槽２０内
には処理すべき布帛６に含浸させる処理液を充填
せしめる。尚導入側シール機構４の液封槽４1内
へ供給すべき液は、上記液槽２０内に供給した液
と同種のもの、あるいは水等を選択的に充填す
る。更に給水管１３より水槽１４内に供給した水
を洗浄槽４3内に逐次注入し、スチーマ缶体１の
内外に設備された布帛ガイドロールを駆動して液
槽２０内で所定の処理液を含浸せしめた布帛６を
高圧湿熱が保持されるスチーマ缶体１内に供給
し、このスチーマ缶体内で高圧湿熱により反応さ
せて、所望の処理（前処理、減量、染着、縮じゆ
う等）を連続的に行なうものであるが、一方洗浄
槽４3内に入れられた水は、回転するシールゴム
ロールの洗浄と冷却とを連続的に行なうので、こ
の洗浄槽４3内の水内にはシールゴムロールより
洗い落された糸屑等が含有され、またシールゴム
ロール４2の冷却により約35℃の加熱水となり更
にこの加熱水内にはシールゴムロール４2による
布帛の搾液作用により若干の処理液が混入され
る。この加熱水は、濾過器１５により不純物が除
去された後、導出側シール機構５の徐冷槽５1内
へ供給され、徐冷液となる。この徐冷液は該徐冷
槽５1内で約90℃に加熱されるが、この徐冷槽５1
より排出された加熱液は濾過器１６により濾過さ
れた後液槽１７内に貯えられる。この液槽１７内
の加熱液はポンプ１９の作用で熱交換器１８内の
加熱作用によつて100℃に近い加熱液となつてス
チーマ缶体１内の最上段の液付与槽８内へ供給さ
れ、以外下段の液付与槽８内へと順次移行して最
下段の液付与槽８内へ移行される。この最下段の
液付与槽８内に供給された液温はスチーマ缶体１
内の温度160℃に追従して、160℃近くまで加熱さ
れる。従つてこの加熱液を熱交換器１８に供給す
ることによつて最上段の液付与槽８へ供給する液
温をスチーマ缶体内部温度近くまで高めることが
できる。この熱交換器１８より排出された加熱液
は、加熱液槽２１内に供給されるので、液槽２０
内の液温を高めることができる。 The above is the configuration of this embodiment.Next, its operation will be described.When operating the high-pressure steamer, first pressurized steam is sent into the steamer can 1, and the inside of the steamer can is The fabric 6 to be treated is kept in a high-pressure, moist heat state at a temperature of 0.degree. The liquid to be supplied into the liquid sealing tank 41 of the introduction side sealing mechanism 4 is selectively filled with the same kind of liquid as the liquid supplied into the liquid tank 20, or water. Furthermore, water supplied into the water tank 14 from the water supply pipe 13 is sequentially injected into the cleaning tank 4 3 , and fabric guide rolls installed inside and outside the steamer can body 1 are driven to supply a predetermined treatment liquid in the liquid tank 20 . The impregnated fabric 6 is fed into the steamer can 1 where high-pressure moist heat is maintained, and reacted in the steamer can by high-pressure moist heat to perform desired treatments (pretreatment, weight loss, dyeing, shrinkage, etc.) On the other hand, the water in the cleaning tank 43 continuously cleans and cools the rotating seal rubber roll, so there is no water in the cleaning tank 43 . It contains thread waste washed off from the seal rubber roll, and heated water becomes approximately 35°C due to cooling of the seal rubber roll 42. Furthermore, this heated water is slightly treated by the squeezing action of the fabric by the seal rubber roll 42 . liquid is mixed in. After impurities are removed from this heated water by the filter 15, it is supplied into the slow cooling tank 51 of the outlet-side sealing mechanism 5, and becomes a slow cooling liquid. This slow cooling liquid is heated to about 90°C in the slow cooling tank 5 1 .
The heated liquid discharged is filtered by a filter 16 and then stored in a liquid tank 17. The heated liquid in the liquid tank 17 is turned into a heated liquid close to 100°C by the heating action in the heat exchanger 18 by the action of the pump 19, and is supplied to the liquid application tank 8 at the uppermost stage in the steamer can body 1. The liquid is then sequentially transferred to the liquid application tank 8 at the lower stage, and then transferred to the liquid application tank 8 at the lowest stage. The temperature of the liquid supplied into this lowermost liquid application tank 8 is the same as that of the steamer can body 1.
It follows the internal temperature of 160℃ and heats up to nearly 160℃. Therefore, by supplying this heated liquid to the heat exchanger 18, the temperature of the liquid supplied to the uppermost liquid application tank 8 can be raised to near the internal temperature of the steamer can. The heating liquid discharged from the heat exchanger 18 is supplied into the heating liquid tank 21.
It is possible to increase the temperature of the liquid inside.
次に本実施例による作用効果を順に説明する
と、先ず第１番目に液層２０内に供給される液温
を加熱液槽２１内に供給した排液によつて加熱す
ることができるので、この加熱作用によつて布帛
への含液吸収性を高めることができ、更にスチー
マ缶体から排出される排液の加熱量を利用して液
槽２０内の液を加熱していることから熱エネルギ
ーの経済性が高められる。第２番目の効果として
はスチーマ缶体１内に配した各液付与槽８内に供
給される液は、シールゴムロール４2の洗浄と徐
冷槽５1内の冷却を終えた液の再利用であるから、
水資源の節約が有効になされるものである。第３
番目の効果は各液付与槽８内へ供給される液温は
スチーマ缶体内温度近くまで加熱されていること
から、スチーマ缶体内蒸気のドレン化を抑制し、
スチーマ缶体内を良質の蒸気室に維持することが
でき、更に有効なボイリングが達成できる。第４
番目の効果はシールゴムロールの洗浄槽４3内に
おける溶剤含有液はスチーマ缶体内の各液付与槽
へ段階的に供給されることから、これらの各液付
与槽内を布帛を通過せしめることで薬剤の完全消
化が期待でき、薬剤の無駄も解消できる効果があ
る。 Next, the effects of this embodiment will be explained in order. First, the temperature of the liquid supplied into the liquid layer 20 can be heated by the drained liquid supplied into the heating liquid tank 21. The heating effect can increase the liquid absorbency of the fabric, and furthermore, since the liquid in the liquid tank 20 is heated using the heating amount of the waste liquid discharged from the steamer can, thermal energy is generated. The economic efficiency of The second effect is that the liquid supplied to each liquid application tank 8 arranged inside the steamer can body 1 is reused after cleaning the seal rubber roll 4 2 and cooling the slow cooling tank 5 1 . Because it is,
Water resources can be conserved effectively. Third
The second effect is that the temperature of the liquid supplied into each liquid application tank 8 is heated close to the temperature inside the steamer can, which suppresses the drainage of steam inside the steamer can.
A high-quality steam chamber can be maintained inside the steamer can, and more effective boiling can be achieved. Fourth
The second effect is that the solvent-containing liquid in the cleaning tank 43 for the seal rubber roll is supplied in stages to each liquid application tank in the steamer can, so by passing the fabric through each of these liquid application tanks, the chemical Complete digestion can be expected, and it has the effect of eliminating wasted medicine.
以上のように本発明は、導入側シールロールの
冷却槽を具備せしめた導入側シール機構と、徐冷
槽を具備せしめた導出側シール機構と、スチーマ
缶体内に複数の液付与槽を多段に設けている高圧
スチーマにおいて、上記冷却槽に給水するための
給水手段と、この冷却槽から排出される液を濾過
する濾過器と、この濾過器からの濾過液を前記の
徐冷槽内へ供給するための給液手段と、徐冷槽か
ら排液を濾過する濾過器と、この濾過器からの濾
過液をスチーマ缶体からの排液で加熱するための
熱交換器と、この熱交換器で加熱された液を、前
記の各液付与槽へ段階的に供給するための給液手
段を備えたことを特徴とする布帛の連続湿熱処理
装置であるから、給水手段から供給された水がシ
ールゴムロールの冷却液と、徐冷槽の冷却液と液
付与槽内へ供給される液としての仕事をなすこと
ができるので水資源の節約が有効になされ、更に
その液付与槽内へ供給される液は、スチーマ缶体
内の排熱を利用して予熱することができるので熱
エネルギーの無駄が解消できる省熱エネルギーに
役立つ等の効果がある。 As described above, the present invention has an inlet side seal mechanism equipped with a cooling tank for the inlet seal roll, an outlet side seal mechanism equipped with a slow cooling tank, and a plurality of liquid application tanks in a steamer can in multiple stages. The provided high-pressure steamer includes a water supply means for supplying water to the cooling tank, a filter for filtering the liquid discharged from the cooling tank, and a filtrate from the filter for supplying the filtrate into the slow cooling tank. a filter for filtering the waste liquid from the slow cooling tank; a heat exchanger for heating the filtrate from the filter with the waste liquid from the steamer can; and the heat exchanger. This is a continuous moist heat treatment apparatus for fabric, characterized in that it is equipped with a liquid supply means for supplying the heated liquid in stages to each of the liquid application tanks, so that the water supplied from the water supply means is Since it can serve as the cooling liquid for the seal rubber roll, the cooling liquid in the slow cooling tank, and the liquid supplied to the liquid application tank, water resources can be effectively saved, and furthermore, water resources can be effectively saved. The liquid can be preheated using the waste heat inside the steamer can, which has the effect of eliminating wasted thermal energy and helping to save energy.
図面は本発明よりなる装置の実施例を示した全
体説明図である。
１……スチーマ缶体、２……布帛導入口、３…
…布帛導出口、４……導入側シール機構、４1…
…液封層、４2……シールゴムロール、４3……洗
浄槽、４4……給液管、５……導出側シール機構、
５1……徐冷槽、５2……冷却液供給管、５3……
冷却液排出管、６……布帛、７……ガイドロー
ル、８……液付与槽、９……給液管、１０……テ
ンシヨン調整ロール、１１……蒸気供給パイプ、
１２……固定摩擦部材、１３……給水管、１４…
…水槽、１５，１６，２３……濾過器、１７……
液槽、１８……熱交換器、１９……ポンプ、２０
……液槽、２１……加熱液槽、２２……配管。
The drawing is an overall explanatory diagram showing an embodiment of the apparatus according to the present invention. 1... Steamer can body, 2... Fabric inlet, 3...
...Fabric outlet, 4...Introduction side seal mechanism, 4 1 ...
...liquid sealing layer, 4 2 ... seal rubber roll, 4 3 ... cleaning tank, 4 4 ... liquid supply pipe, 5 ... outlet side seal mechanism,
5 1 ... slow cooling tank, 5 2 ... coolant supply pipe, 5 3 ...
Coolant discharge pipe, 6... fabric, 7... guide roll, 8... liquid application tank, 9... liquid supply pipe, 10... tension adjustment roll, 11... steam supply pipe,
12... fixed friction member, 13... water supply pipe, 14...
...Aquarium, 15, 16, 23...Filter, 17...
Liquid tank, 18... Heat exchanger, 19... Pump, 20
...Liquid tank, 21...Heating liquid tank, 22...Piping.
Claims (1)
導入側シール機構と、徐冷槽を具備せしめた導出
側シール機構と、スチーマ缶体内に複数の液付与
槽を多段に設けている高圧スチーマにおいて、上
記冷却槽に給水するための給水手段と、この冷却
槽から排出される液を濾過する濾過器と、この濾
過器からの濾過液を前記の徐冷槽内へ供給するた
めの給液手段と、徐冷槽から排液を濾過する濾過
器と、この濾過器からの濾過液をスチーマ缶体か
らの排液で加熱するための熱交換器と、この熱交
換器で加熱された液を、前記の各液付与槽へ段階
的に供給するための給液手段を備えたことを特徴
とする布帛の連続湿熱処理装置。1. In a high-pressure steamer that has an inlet seal mechanism equipped with a cooling tank for the inlet seal roll, an outlet seal mechanism equipped with a slow cooling tank, and a plurality of liquid application tanks arranged in multiple stages within the steamer can, A water supply means for supplying water to the cooling tank, a filter for filtering the liquid discharged from the cooling tank, and a liquid supply means for supplying the filtrate from the filter into the slow cooling tank. , a filter for filtering the waste liquid from the slow cooling tank, a heat exchanger for heating the filtrate from this filter with the waste liquid from the steamer can, and a liquid heated by the heat exchanger, A continuous wet heat treatment apparatus for fabric, characterized in that it is equipped with a liquid supply means for supplying liquid in stages to each of the liquid application tanks.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57138277A JPS5930952A (en) | 1982-08-09 | 1982-08-09 | Continuous steam treating apparatus of fabric |
| DE19833328446 DE3328446A1 (en) | 1982-08-09 | 1983-08-06 | HIGH PRESSURE DAMPER |
| US06/522,250 US4517818A (en) | 1982-08-09 | 1983-08-09 | High pressure steamer for continuous wet-heat treatment of a cloth |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57138277A JPS5930952A (en) | 1982-08-09 | 1982-08-09 | Continuous steam treating apparatus of fabric |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5930952A JPS5930952A (en) | 1984-02-18 |
| JPH0135944B2 true JPH0135944B2 (en) | 1989-07-27 |
Family
ID=15218149
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57138277A Granted JPS5930952A (en) | 1982-08-09 | 1982-08-09 | Continuous steam treating apparatus of fabric |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5930952A (en) |
-
1982
- 1982-08-09 JP JP57138277A patent/JPS5930952A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5930952A (en) | 1984-02-18 |
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