EP0311796B1 - Procédé de traitement au mouillé de matières en bandes - Google Patents

Procédé de traitement au mouillé de matières en bandes Download PDF

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Publication number
EP0311796B1
EP0311796B1 EP88114905A EP88114905A EP0311796B1 EP 0311796 B1 EP0311796 B1 EP 0311796B1 EP 88114905 A EP88114905 A EP 88114905A EP 88114905 A EP88114905 A EP 88114905A EP 0311796 B1 EP0311796 B1 EP 0311796B1
Authority
EP
European Patent Office
Prior art keywords
liquor
web
moisture content
salt
treatment
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
EP88114905A
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German (de)
English (en)
Other versions
EP0311796A1 (fr
Inventor
Johannes Kutz
Günter von Harten
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.)
Eduard Kuesters Maschinenfabrik GmbH and Co KG
Original Assignee
Eduard Kuesters Maschinenfabrik GmbH and Co KG
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 Eduard Kuesters Maschinenfabrik GmbH and Co KG filed Critical Eduard Kuesters Maschinenfabrik GmbH and Co KG
Publication of EP0311796A1 publication Critical patent/EP0311796A1/fr
Application granted granted Critical
Publication of EP0311796B1 publication Critical patent/EP0311796B1/fr
Anticipated expiration legal-status Critical
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Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B21/00Successive treatments of textile materials by liquids, gases or vapours
    • 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
    • D06B3/10Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of fabrics
    • D06B3/18Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of fabrics combined with squeezing, e.g. in padding machines

Definitions

  • the invention relates to a method according to the preamble of claim 1.
  • the starting point of the invention has been problems which have been pending for a long time in continuous dyeing with direct dyes (noun dyes) (see Fischer-Bobsien "International Lexicon textile finishing + border areas” 4th edition 1975, columns 419-422).
  • the dyeing liquor can be applied in a foulard, so that the web is passed through the larger amount of dyeing liquid in the pool of the foulard. This has resulted in unavoidable end processes, both at the beginning and at the end of the web.
  • parts of the fleet are towed out of the web, which cause a corresponding depletion of the fleet, which must be readjusted.
  • the invention is based on the object of designing a method in such a way that a uniform treatment failure occurs over the length of the web.
  • the method is primarily considered for the treatment of flat fabrics.
  • the first treatment liquor which is either the salt liquor or the color liquor, the other liquor following in the subsequent second step, is applied in some way and then squeezed to 60 to 120%.
  • the moisture values always relate to the amount of treatment liquor in relation to the dry weight of the web to which the treatment liquor has been applied.
  • a value of 120% is the upper limit of what can still be squeezed evenly in a squeezing device with interacting rollers; at higher moisture contents, the squeezing mechanism would have to be driven with line pressures so low that the uniformity of the squeezing would no longer be guaranteed and there would even be a risk of the rollers lifting off from one another in certain areas.
  • the second treatment liquor (color liquor or salt liquor, depending on what has been applied beforehand) is now applied to the web loaded with the specified amount of moisture, in a special way.
  • the material web should not be led through a larger fleet, in which there is a risk of concentration changes due to the amount of treatment agent carried out by the material web.
  • the second treatment fleet when the second treatment fleet is applied, the web should only be in contact with the smallest possible amount of liquor, which is very quickly absorbed and transported away by the web and which is accordingly constantly renewed or supplemented by introducing fresh treatment fleets.
  • Fresh liquor is therefore always applied to the web on both sides, through which no longer lengths of the web have yet passed. In this way, changes in concentration in the amount of treatment liquor in contact with the material web and corresponding differences in treatment failure can be minimized.
  • the second treatment liquor is not squeezed off after application. By squeezing, no total moisture content can be set evenly, which is significantly above 120%. If squeezed after the application of the second treatment fleet, it would at best be possible to add a few 10% of the second treatment fleet, which in many cases is too little for the interaction of the two treatment fleets and the failure of the treatment. For this reason, the web is stripped off after the second treatment liquor has been applied, so that the same amount of treatment liquid can be added in the order of magnitude as in the first application and total moisture contents can be achieved which are in the range of what the web can hold in terms of moisture at all without the moisture dripping from the web or runs down on it.
  • Such loads of liquor which have been pushed to the limits of the drip-free moisture content, are advantageous for many treatments, because this gives great water mobility on the web and the transport of the treatment agents between the two fleets and in particular the drawing up of the treatment agents from the entire fleet onto the fibers in the steaming step that generally follows the order.
  • a continuous process for dyeing a textile web in which it is provided with a first treatment liquor, partially dehumidified and then passed through an intermediate application unit with another treatment liquor, is known per se from DE-AS 10 78 527.
  • the known design is also out of the question for reasons of the required order quantities.
  • the gusset applicator comprises two rollers arranged at the same height, between which the web is passed from top to bottom, passing through the treatment liquor in the gusset between the rollers to a certain low height before it passes through the nip. Since the rollers have to seal the gusset downwards, they have to rest against each other with a certain line force, which inevitably means that the web is squeezed vigorously and higher order quantities are in principle not possible.
  • a preferred application example of the method according to the invention is the subject of claim 2.
  • Gusset application devices with which the application of the dyeing liquid from a small liquor stock and the subsequent stripping can be realized in a gap are known per se from FR-PS 13 81 081.
  • the invention does not lie in the gusset application device as such, but in the combination of an impregnation device with squeezing with an impregnation device with very little liquor content, in which subsequently stripped, ie a relatively large amount of liquor is left evenly on the web.
  • An application device with stripping is also apparent from DE-OS 20 36 520.
  • the web passes a container filled with treatment liquor, is deflected upward and passes through the gap between two horizontally opposite, rotatable, fixedly supported inflatable tubes, where the excess liquor is wiped off.
  • an embodiment of the invention is shown in the form of a device designated 100 as a whole for dyeing a flat fabric made of cotton with direct dyes.
  • the material web 1 is first passed through a padder 10 which forms the first application device and which comprises a plunge pool 2 which, with a width of the material web 1 of 1.80 m, comprises 30 to 60 l of a salt liquor 3, through which the material web in the manner shown is passed through a deflection roller 4, in order then to be directed vertically upwards and to be squeezed into the nip 5 between the nip rollers 6 and 7 to a moisture content of 70 to 90% by weight of the dry fabric web 1.
  • the material web loaded with this moisture is then deflected vertically downwards on a deflection roller 8 and thus passes into the gusset application device 20 which forms the second application device are essentially flat and slightly inclined to the web, ie approach it in the running direction.
  • the walls 11, 12 are connected to one another outside the edges of the material web 1, so that an upright, funnel-like trough 9 is formed, which can be filled with a treatment liquid 13 up to a selectable low fill level.
  • oblong recesses 15, 16 extending across the width of the material web are formed, in which inflatable pressure hoses 17, 18 are arranged.
  • the fabric web is slid through the gap 19 between the tubes 17, 18.
  • the treatment liquor 13, which in the exemplary embodiment is a dyeing liquor with direct dyes, received in the trough 9 is stripped down to a total moisture content determined by the pressure in the tubes 17, 18. This total moisture content is in the range of about 100 to 200%, i.e. the same amount of treatment liquor as that which has already been applied in the foulard 10 is added again in the gusset application device 20.
  • the level in the trough 9 is kept very low. With a web width of 1.80 m and the corresponding width of the trough 9 there are, for example, 4 to 8 l of the treatment liquor 13 in the trough 9. This amount would only suffice for a few meters of web 1 and would be used up very quickly. For this reason, the treatment liquor 13 is constantly supplied fresh by a feed device 14 and is kept in the trough 9 at a constant, albeit low, level. A significant change in the concentration of the treatment liquor 13 by treatment agents carried along by the material web 1 cannot therefore occur. Except for very small processes of the order of magnitude from 3 to 5 m, the entire length of the web 1 is colored evenly.
  • the material web 1 treated in this way now immediately moves into a damper 30 and then into a washing device 40 provided with several compartments.
  • a flat fabric made of cotton with a weight per unit area of 200 g / m 2 was provided in accordance with the prior art in a foulard without the addition of salt with the following dyeing liquor and then steamed in the steamer for 2 minutes: 3.0 ml / l Wetting agent 2.0 ml / l Blocking aids 1.0 g / l Oxidizing agent 0.5 ml / l ventilator 7.7 g / l Direct blue I 2.3 g / l Direct blue II
  • the fleet order was 85%, the working speed 30 m / min, the web width 1.8 m. The result was a blue-colored web with end drains of the order of 100 m, which had to be used for other purposes.

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Coloring (AREA)
  • Professional, Industrial, Or Sporting Protective Garments (AREA)

Claims (5)

  1. procédé en continu de teinture d'une nappe de produits textiles selon lequel on applique sur la nappe un bain de teinture et de sel et on humidifie la nappe en partie à une valeur déterminée, procédé caractérisé en ce que,
    - le sel est appliqué dans un bain de traitement distinct du bain de teinture,
    - la nappe de produits après application du premier bain de traitement (bain de teinture ou bain de sel) est exprimée jusqu'à une teneur en humidité de 60 à 120 %,
    - sur la nappe encore humide, on applique le second bain de traitement de façon que la nappe soit toujours en contact qu'avec une petite réserve de liquide, épuisée en continu et renouvelée au fur et à mesure de son épuisement,
    - et en ce qu'on humidifie partiellement la nappe de produits directement de manière qu'en glissant à travers la fente avec au moins une délimitation élastique adjacente on arrive à une teneur totale en humidité de 100 à 200 %.
  2. Procédé selon la revendication 1, caractérisé en ce que,
    - on applique un bain de sel et un bain de teinture à colorants directs,
    - on applique tout d'abord un premier bain et on exprime à une teneur en humidité de 70 - 90 %,
    - puis on applique le second bain,
    - puis on racle la nappe à une teneur totale en humidité de 130 à 160 %.
  3. Procédé selon la revendication 1, caractérisé en ce qu'on applique un bain de sel et un bain de teinture à colorants au souffre et,
    - on applique tout d'abord le premier de ces bains et on exprime jusqu'à une teneur en humidité de 70 -  90 %,
    - puis on applique le second bain,
    - puis on racle la nappe pour arriver à une teneur totale en humidité comprise entre 160 et 200 %.
  4. Procédé selon la revendication 1, caractérisé en ce que,
    - on applique un bain d'alcali le cas échéant avec du sel et un bain de teinture avec des colorants réactifs,
    - on applique tout d'abord un premier bain, puis on exprime jusqu'à une teneur en humidité de 70 -  100 %,
    - puis on applique le second bain,
    - et on racle la nappe de produits jusqu'à une teneur totale en humidité de 160 à 200 %.
  5. Procédé selon l'une des revendications 1 à 4, caractérisé en ce que les deux bains de traitement sont appliqués à la même température.
EP88114905A 1987-10-08 1988-09-13 Procédé de traitement au mouillé de matières en bandes Expired - Lifetime EP0311796B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3733997A DE3733997C3 (de) 1987-10-08 1987-10-08 Verfahren und Vorrichtung zum kontinuierlichen Färben einer textilen Warenbahn
DE3733997 1987-10-08

Related Child Applications (1)

Application Number Title Priority Date Filing Date
EP92101276.1 Division-Into 1988-09-13

Publications (2)

Publication Number Publication Date
EP0311796A1 EP0311796A1 (fr) 1989-04-19
EP0311796B1 true EP0311796B1 (fr) 1992-12-09

Family

ID=6337866

Family Applications (2)

Application Number Title Priority Date Filing Date
EP88114905A Expired - Lifetime EP0311796B1 (fr) 1987-10-08 1988-09-13 Procédé de traitement au mouillé de matières en bandes
EP19920101276 Withdrawn EP0483114A3 (en) 1987-10-08 1988-09-13 Method and apparatus for continuously bleaching a textile sheet-like material

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP19920101276 Withdrawn EP0483114A3 (en) 1987-10-08 1988-09-13 Method and apparatus for continuously bleaching a textile sheet-like material

Country Status (8)

Country Link
US (2) US4878365A (fr)
EP (2) EP0311796B1 (fr)
JP (1) JPH01124669A (fr)
BR (1) BR8805186A (fr)
DD (1) DD282934A5 (fr)
DE (1) DE3733997C3 (fr)
ES (1) ES2036642T3 (fr)
RU (1) RU2050427C1 (fr)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3733997C3 (de) * 1987-10-08 1996-12-19 Kuesters Eduard Maschf Verfahren und Vorrichtung zum kontinuierlichen Färben einer textilen Warenbahn
DE3923318A1 (de) * 1989-07-14 1991-01-17 Kuesters Eduard Maschf Verfahren und anlage zur vorbehandlung von bahnfoermigem, einen pol aufweisendem textilgut, insbesondere teppichware, vor dem faerben
AT398089B (de) * 1989-09-12 1994-09-26 Johannes Zimmer Verfahren zum färben mit reaktivfarbstoffen von textilen flächengebilden
DE4005980A1 (de) * 1990-02-26 1991-08-29 Kuesters Eduard Maschf Kontinue-verfahren zur behandlung von textilen warenbahnen und entsprechende einrichtung
FR2661927B1 (fr) * 1990-05-11 1994-02-18 Sandoz Sa Procede pour le mercerisage et la teinture au mouille de materiau cellulosique humide.
DE19531663C2 (de) * 1995-08-29 1997-08-14 Kuesters Zittauer Maschf Gmbh Vorrichtung zum Mercerisieren einer textilen Warenbahn
DE19940608C1 (de) * 1999-08-27 2001-05-10 Kuesters Eduard Maschf Verfahren zum Herstellen eines Musters eines Behandlungsausfalls an einer textilen Warenprobe
US7398660B2 (en) * 2005-09-14 2008-07-15 Zzakey Technologies Ltd Dyeing apparatus and method therefor
DE102009013979A1 (de) 2009-03-19 2010-09-23 Dürr Systems GmbH Elektrodenanordnung für einen elektrostatischen Zerstäuber
CN102321959B (zh) * 2011-09-01 2013-03-13 绍兴县永通丝绸印染有限公司 一种面料上浆机
CN113564845B (zh) * 2021-07-12 2023-05-23 晋江市宏兴服饰织造有限公司 一种保暖弹性的泳装面料生产设备及其制备工艺

Family Cites Families (20)

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Publication number Priority date Publication date Assignee Title
DE1071035B (fr) * 1959-12-17
US521816A (en) * 1894-06-26 reffitt
DE107527C (fr) * 1898-01-17
US1979818A (en) * 1931-06-09 1934-11-06 Samcoe Holding Corp Method of dyeing
US2460206A (en) * 1945-12-07 1949-01-25 Du Pont Method of continuous dyeing
US2784583A (en) * 1953-07-24 1957-03-12 Dungler Julien Foulards or padders
DE1054048B (de) * 1956-11-02 1959-04-02 Benteler Werke Ag Dreiwalzenfoulard
DE1078527B (de) * 1957-03-11 1960-03-31 Haas Friedrich Maschf Vierwalzenfoulard
FR1212022A (fr) * 1957-07-15 1960-03-21 Muller Fichter & Cie X Foulard de teinture
NL295000A (fr) * 1962-07-05
FR1381081A (fr) * 1964-01-30 1964-12-04 Kleinewefers Soehne J Dispositif pour faire passer à travers une enceinte une matière quelconque, notamment une matière textile, en bande large ou en écheveau avec des traversées étanches à la pression
DE2036520A1 (en) * 1970-07-23 1972-02-03 Vepa Ag, Basel (Schweiz) Dye padding process - squeezing of excess liquor by passing between inflatable tubes
DE2116485A1 (en) * 1971-04-05 1972-10-12 Vepa Ag, Riehen (Schweiz) Washing endless material - in a continuous washing appliance suitable for strands and widths of textile material
US4193762A (en) * 1978-05-01 1980-03-18 United Merchants And Manufacturers, Inc. Textile treatment process
US4202774A (en) * 1978-05-24 1980-05-13 Dorr-Oliver Incorporated Flow distributor for fluid bed biological reactor
JPS5567059A (en) * 1978-11-13 1980-05-20 Santo Tekkosho Kk Continuous liquid impregnating apparatus for cloth
DE3037156A1 (de) * 1980-10-01 1982-05-06 Hoechst Ag, 6000 Frankfurt Verfahren zur kontinuierlichen, gleichmaessigen auftragen von faerbeflotten auf nasse, textile warenbahnen
CH668446A5 (de) * 1985-05-10 1988-12-30 Benninger Ag Maschf Vorrichtung zum behandeln einer laufenden textilbahn in einem fluessigkeitsbad.
EP0286767B1 (fr) * 1987-04-16 1991-07-31 Triatex International Procédé et installation pour l'application en continu des liquides sur une matière en bande absorbante compressible
DE3733997C3 (de) * 1987-10-08 1996-12-19 Kuesters Eduard Maschf Verfahren und Vorrichtung zum kontinuierlichen Färben einer textilen Warenbahn

Also Published As

Publication number Publication date
JPH01124669A (ja) 1989-05-17
DE3733997C2 (fr) 1990-10-04
DE3733997C3 (de) 1996-12-19
US4997453A (en) 1991-03-05
DD282934A5 (de) 1990-09-26
RU2050427C1 (ru) 1995-12-20
DE3733997A1 (de) 1989-04-27
ES2036642T3 (es) 1993-06-01
EP0311796A1 (fr) 1989-04-19
BR8805186A (pt) 1989-05-23
EP0483114A3 (en) 1992-07-22
US4878365A (en) 1989-11-07
EP0483114A2 (fr) 1992-04-29

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