EP0945538B1 - Procédé et dispositif pour le traitement des étoffes textiles sous forme de boyau - Google Patents

Procédé et dispositif pour le traitement des étoffes textiles sous forme de boyau Download PDF

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Publication number
EP0945538B1
EP0945538B1 EP99105286A EP99105286A EP0945538B1 EP 0945538 B1 EP0945538 B1 EP 0945538B1 EP 99105286 A EP99105286 A EP 99105286A EP 99105286 A EP99105286 A EP 99105286A EP 0945538 B1 EP0945538 B1 EP 0945538B1
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EP
European Patent Office
Prior art keywords
container
steam
treatment
transport nozzle
textile material
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EP99105286A
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German (de)
English (en)
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EP0945538A1 (fr
Inventor
Harald Dörfer
Wilhelm Christ
Klaus Beck
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T H E N Maschinen- und Apparatebau GmbH
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T H E N Maschinen- und Apparatebau GmbH
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Publication of EP0945538A1 publication Critical patent/EP0945538A1/fr
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    • 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
    • D06B3/28Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of fabrics propelled by, or with the aid of, jets of the treating material
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06CFINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
    • D06C7/00Heating or cooling textile fabrics
    • D06C7/02Setting

Definitions

  • the invention relates to a method and a device for the treatment of strand-like textile goods.
  • Aerodynamic piece dyeing machines are described, for example, in Melliland Textile Reports 69 (1988, pages 748 to 754), in textile technology 38 (1988, Pages 31 to 35) and in International Textile Bulletin Refinement 31 (1985, 3, pages 27 to 41), where an aerodynamic System for refining piece goods in detail is explained.
  • the aerodynamic treatment system is essentially based on the fact that an endless line of goods in a closed container using a transport nozzle system often in the form of a jet nozzle, in circulation which is charged with a gas stream, which the goods train its feed movement in the predetermined Direction of circulation granted.
  • EP 0 078 022 B2 (preamble of claim 14) describes a method for treatment of textile goods in jet dyeing plants, which is also known works on the aerodynamic principle and at the dyes, chemicals and auxiliaries in the treatment fleet and the transport nozzle (jet nozzle) acted upon, circulated gas flow in the area of Nozzle section for the goods drive can be added.
  • the fleet is distributed finely and evenly on the Distributed surface of the textile goods forming the goods strand.
  • the penetration of the fibers and thus the Fleet exchanges in the textile goods are optimal. simultaneously allows this aerodynamic system with one extremely short liquor ratio even when the Container and thus the total water consumption, as well as the use of chemicals, auxiliaries, dyes, etc. to reduce.
  • the aerodynamic Very high drive of the circulating line of goods Goods speeds.
  • the textile treatment machines working in an aerodynamic system e.g. also in EP 0 665 319 A3 and 0 640 710 A2 described.
  • EP 0 640 710 A2 Process for treating a textile web is out the web has an endless web loop, which during its by one of a gaseous fluid flowed through nozzle within the treatment facility a mechanical and / or thermal transport Is subjected to treatment to reduce the volume, the handle, the surface appearance or the water content of the Change the web loop in a targeted manner.
  • a final and finishing treatment to the as Fluid can also be used with steam, if necessary a gaseous or mist-like treatment agent is added is evenly applied to the web becomes.
  • the object of the invention is a method and Device for treating strand-like textile goods create that allow even those who are difficult to treat Textile goods in piece dyeing machines have high requirements the surface quality and especially the Stability of a refined piece goods in terms of Dimensional stability, the avoidance of creases and wrinkles, Bolder, etc. to suffice.
  • the invention is based on proceeded the method of claim 1.
  • One to carry out device suitable for this method is according to further invention subject of claim 14.
  • the invention is based on the consideration that the Causes of color irregularities, wrinkles and the like often lie in the raw material.
  • Flat structures are tensions resulting from the manufacture included, which thereby frictionally blocked are that the yarns are in the fabric or knitted fabric cross over or devour each other.
  • the States of tension in the textile goods partially removed, with the result that after finishing in undesired local phenomena of the finished goods, e.g. Wrinkles or creases become visible.
  • This is moving hence that the voltage states during different Phases of the treatment process in uncontrolled Be resolved in a way and thereby a corresponding Uneven treatment effect on the textile goods results. Basically the same applies to signs of shrinkage, the during the course of treatment occur.
  • the new procedure will time before treatment with the treatment agent, e.g. B. the dye liquor, in at least one separate preparation or pre-treatment step through direct exposure to water vapor (Steaming) on the textile goods present in the textile goods Tensions are released and / or there is a shrinkage of the Textile goods causes.
  • the preparation and / or Pretreatment step the transport nozzle means only applied with steam, the line of goods during a predetermined exposure time of the steam driven, circulated.
  • the textile material is at a predetermined pretreatment temperature brought and / or kept on this, this pretreatment temperature regardless of Start temperature at the subsequent treatment stage with a treatment agent, for example a dye liquor.
  • the new process is based on an aerodynamic Piece dyeing machine carried out on the goods strand can circulate without loading the fleet.
  • the textile good can at the beginning of the preparation and / or pre-treatment step be dry or damp or wet.
  • the textile goods during the preparation or Pretreatment step only the action of the Line of goods exposed to circulating water vapor is, it can occur when passing through the transport nozzle means and one of these downstream samplers is good to open. This leads to that the line of goods better relocated so that the danger of permanent Wrinkle embossing in the textile goods reduced or completely is prevented. Because of the better opening can the textile goods are also better distributed in the store, so that the deformation in the fold area is significantly less is. This gives the textile goods the opportunity to to continuously relax the goods run, i.e. to relax so that, as explained above, the following Treatment steps for finishing the textile goods of a perfectly even, relaxed product going out, and no permanent in the dyeing process Deformations can occur more. With steam treatment and raising the textile material to the pretreatment temperature condensation of water vapor occurs on the textile fibers. The resulting resulting limited moisture absorption already causes a accordingly limited swelling of the textile fiber material, which in turn stabilizes the goods structure is achieved.
  • the pretreatment temperature of the textile material is independent from the treatment temperature at a subsequent one Treatment step, it may be appropriate if the textile goods at the end of the preparation or pre-treatment step from the pretreatment temperature a predetermined temperature is cooled. This can e.g. happen in such a way that the transport nozzle means with a temperature-controlled gas flow be charged. An inert gas stream can also be used for this be used.
  • the temperature of the textile goods during the preparation or pretreatment step and / or at one another step during his treatment can also go through Contact of the transport nozzle means flowing through the container pressurizing gas, steam or steam / air flow with one maintained outside in the container the surface of the liquid present be managed.
  • treatment liquor passed through a heat exchanger into the tank and there be adjusted to a level below of the goods line, so that this with the fleet does not come into contact.
  • the temperature of this fleet is regulated via the heat exchanger so that a controlled Cooling of the gas stream passing over it occurs.
  • the cooling of the gas or steam flow takes place through the direct contact with the colder treatment fleet and through the proportion of condensate resulting from the proportion of water vapor precipitates and at the same time heat the gas withdraws.
  • the heat exchange surface with the gas or Steam flow can be increased by the cooling Liquid down on the inside wall of the container will flow into a swamp.
  • the described to regulate the temperature of the Textile good liquid collects in the lower part of the container, from the sump of which they is suctioned off. If necessary, it can be used as a rinsing liquid (Rinse water) can continue to be used.
  • the container can at least in the preparation or Pretreatment step after the start of steam application the transport nozzle means temporarily to the atmosphere be opened, one in the container containing air volume, at least partially from the Container is removed and replaced with steam.
  • the steam is used in the air space of the container reduce remaining oxygen. This percentage of oxygen could, for example, in a subsequent treatment step reduced vat dyes used, which are in leuco form. Be next to it by expelling or reducing the oxygen content, Chemicals and products that are otherwise used Binding of atmospheric oxygen is required, saved, which means that with the resulting lesser Reduction needs also include a reduction the pollution of the wastewater is reached.
  • the one set up to carry out the new procedure Device has a closable, pressure-resistant Container, transport nozzle means for one in the form of an endless Textile material present and a pressure side with the transport nozzle means and suction side connected to the container gas circulation device.
  • an addition device for liquid treatment agent can treat agents in the field of transport nozzle means on the textile material with a given Treatment temperature can be brought into effect.
  • the device is with one to the transport nozzle means leading connection device for a Steam source provided, which at least during the preparation or pre-treatment step with steam is.
  • the device has a container containing the separate circuit separate from the gas circulation for liquid treatment agent, the circulation pump agent contains.
  • FIG. 1 The high temperature shown in Figures 1 to 4 (HT) piece dyeing machine is a device for Implementation of the method according to the invention. She points one illustrated only schematically in FIG. 1 closed container 1, which as essentially cylindrical pressure vessel is formed. In the container 1 lead, as can be seen from Fig. 2, two operating opening 2, each one a memory 3 for an endless Goods strand 4 assigned and by an operator lock 5 can be closed in a pressure-tight manner.
  • the suction line 16 is coaxial to the container axis connected to the container 1 and leads into one coaxial guide cylinder 17 within the container 1.
  • the Guide cylinder 17 is on the opposite side of the suction line 16 Side open to the inside of the container. It contains a gas filter 18 which is part of the fan 15 and the lines 14, 16 formed gas circulation device.
  • a shut-off valve 19 is located in the pressure line 14 opens into the pressure line 14 through a valve 20 closable steam connection piece 21, which with a external steam source not shown in the figures is connected, which allows water vapor with an overpressure of approx. 1.7 bar (at approx. 130 ° C).
  • the steam connection piece can also be in the suction pipe 16 of the fan 15 open.
  • the blower 15 is frequency controlled Electric motor driven, which allows the speed and so that the performance of the blower 15 can be changed continuously.
  • the two stores 3 are in 2 at 22 indicated side walls, that do not reach the container wall, so that in the entire container 1 for all storage 3 a common Atmosphere is present.
  • a treatment medium circulation circuit which is a treatment medium circulation pump 25 contains.
  • the treatment agent circulation pump (25) is on the suction side via a liquid supply and drain connections 26, 27 containing suction line 28 with the treatment agent filter 24 connected, the suction line 28 a Shut-off valve 29 contains.
  • The is on your print page Treatment agent circulation pump 25 via a heat exchanger 30 and an injection line 31 with the nozzle housings 13 of the two memories 3 in connection. It therefore allows it via a control valve 32 assigned to each store 3 Treatment agent directly into each of the transport nozzles 12 to inject gas stream.
  • An additional container 33 is set up next to container 1, which via a pump 34 and a shut-off valve 35 containing line 36 with its lower part to the Suction line 28 is connected. From the additional container 33 goes through at the bottom on the suction side of the pump 34 a shut-off valve 37 shut-off drain line 38. In addition, a circulation line branches off from line 36 39, which contains a shut-off valve 40. Finally the additional container 33 is still a shut-off valve 41 containing line 42 with the pressure side of the treatment medium circulation pump 25 connected. At 43 are each 44 shut-off supply lines for Finishing products (additives) or water in the Additional container 33 indicated. The shut-off valve 35 in the Line 36 is provided with a control valve 45 containing bypass 46 connected to line 36 is bridged. In the embodiment shown in Figures 1 to 3 finally branches off from the injection line 31 Treatment agent circulation pump 25 in the flow direction behind the heat exchanger 30 is a treatment medium circulation line 47 starting in the treatment agent filter 24 opens and contains a shut-off valve 48.
  • the container 1 is in the area of its upper part provided with a vent valve 49 (FIG. 2), that comes from a vent line 50 into the closed gas connecting piece via a shut-off valve 51 52 leads, which allows e.g. inert gas (nitrogen) or introduce air into container 1.
  • the container 1 in each of the stores 3 each treated a strand-like textile material, the after introduction by the respective company the closure 5 closed loading opening 2 an endless strand 4 was put together.
  • the Line of goods 4 runs over the driven reel 8 in the Transport nozzle 12, which in operation via the pressure line 14 is acted upon by gas and the product line 4 one Feed in the specified direction of rotation (in Fig. 1 in Clockwise).
  • the scanner 10 is the the line of goods 4 that runs out of the conveyor line 9 are stacked initiated in the respective memory 3, in which he is stored in the form of a package of goods that at 53 in Fig. 1 is indicated.
  • the wet treatment of the respective strand 4 is done in one or more treatment steps, at which are typically the transport nozzle 12 via the blower 15 with gas drawn off from the container 1 in the form of a Steam / air mixture is applied through the container 1 and the fan 15 is not circulated.
  • the merchandise strand 4 circulates clockwise offset, wherein, as mentioned, the memory 3 passes.
  • About the injection line 31 is in the associated Nozzle housing 13 in the from the pressure line 14th injected gas stream treated treatment agent that through the gas flow to the one passing through the transport nozzle 12 Textile applied finely and on this for Action is brought.
  • the treatment agent is through the treatment medium circulation pump 25 in which the suction line 28 and the injection line 31, as well as the two Transport nozzles 12 and the circuit containing the container 1 circulated.
  • the shut-off valves 32 and 24 are open, while the shut-off valves 48, 41, 35 are closed are.
  • the treatment liquor In the lower part of the container 1 is from the both product lines 4 and the drains 3 dripping liquid treatment agents, the so-called treatment liquor.
  • the treatment fleet drained via the liquid drains 27.
  • the circulation line 47 allows it when open Valve 48 and closed shut-off valves 32 in one from the container 1 separate circuit from the additional container 33 to circulate removed processing agent and via the heat exchanger 30 to one for the subsequent one Injection into the gas stream generated by the blower 15 suitable temperature so that it e.g. isothermal Conditions with the textile is merged.
  • the textile goods present in the form of the goods 4 in a separate preparation or pre-treatment step subjected to steam treatment to thereby an at least almost complete relaxation and To reach shrinkage of the textile good before it through the subsequent wet treatment is refined. In doing so the latent tensions arising from the manufacture balanced and canceled in the textile goods.
  • the steam treatment is carried out on the textile direct inflowing water vapor from an adjustable Steam source via the steam connection piece 21 and the Pressure line 14 introduced into the respective nozzle housing 13 becomes.
  • the described water vapor pretreatment for dissolving of internal tension and shrinking of the textile goods can be used for dry or damp textile goods, but also for For example, wet textile goods originating from a prewash be performed. Below is some Exemplary embodiments explained:
  • the goods are transported aerodynamically when they are drawn in by means of the fan 15 from the container 1 sucked in and compressed by the fan 15 air flow of the transport nozzles 12 of the two stores 3 applied.
  • the goods are transported mechanically Supported by the powered reel 8.
  • After the beginning of the goods is from the inlet of the tubular goods the loading opening 2 removed and with the end the tubular fabric is sewn together.
  • the now endless line of goods 4 is initially in with the help of the gas cycle a relatively slow orbital movement, so no disruption to the flow of goods due to the goods being stowed occurs in the inlet part of the goods store 3.
  • the Operating locks 5 of the two memories 3 are closed and it is now with the steam treatment began.
  • the vent valve 49 When the vent valve 49 is open, the first phase of the steam inflow the heating rate of the textile goods until the so-called Locking temperature kept low of approx. 80 ° C, thus increasing the water vapor saturation of the initially a sufficient existing steam-air mixture Air can flow out via the vent valve 49. As soon as the air volume present in the container 1 largely displaced and replaced by steam, it becomes Vent valve 49 closed.
  • the product strands 4 are during the heating phase and the subsequent holding phase at approx. 130 ° C continuously kept in circulation.
  • a treatment bath is now in the additional container 33 prepared with detergent additives. It the shut-off valves 32, 35 are opened, which means that Treatment bath from the additional container 33 via the injection line 31 and the transport nozzles 12 on the textile with the textile material at the same temperature for exposure brought.
  • the valve 35 is closed while the Shut-off valve 29 opened and thus the treatment bath injection system is switched to circulation.
  • the heat exchanger 30 becomes the circulating treatment agent the start temperature of the next wet treatment step, with dispersion coloring on e.g. 50 ° C. cooled.
  • the treatment bath serving as a wash bath drained via the liquid drains 27.
  • the closures 5 After the closures 5 have been closed, the circulating endless product strands 4 are subjected to a water vapor pretreatment as in the first example. Steam pretreatment is used here in particular to prevent the occurrence of the so-called washboard effect, which can be caused by a different shrinkage behavior of the fiber components in the textile material. The resulting tensions are compensated for by damping.
  • the pretreatment is also carried out with steam from 130 ° C in the same way as in Example 1. After completing the holding phase, opening the Liquid drains 27 a rapid pressure drop in the Container 1 generated. Then the temperature of the Textile goods lowered to 60 ° C with a rinsing bath. After that one takes place in the so-called two-bath process Reactive dyeing as constant dyeing at 60 ° C and below a dispersion coloring with the one at the same time Hot rinsing of the reactive dye is connected.
  • the webware was broad before the strand treatment Condition desized, washed and dehumidified Condition docked on a winding roller.
  • the heating is basically the same Way as in Example 1, i.e. it will start with Open vent valve 49, which is in the container 1 contained air volume mainly through water vapor replaced. After closing the vent valve 49 the vapor pressure and the temperature in the container rise up to the steam pretreatment temperature of 120 ° C.
  • the textile material is then during a predetermined Holding time kept at the holding temperature of 120 ° C and then, similar to example 1, but on cooled to a temperature of 80 ° C. Because when heating up to the pretreatment temperature most of the air was drained from the container 1, arises in the Container when cooling from a temperature range of approx. 100 ° C a negative pressure. This creates this negative pressure compensated that the compressed gas shut-off valve 51 (Fig. 2) opened and nitrogen from a nitrogen source Overpressure is introduced into the container 1 until in this the vacuum is balanced again.
  • the steam treatment of the textile goods at 120 ° C is used as a pretreatment step for subsequent vat coloring of the textile goods on the same piece dyeing machine.
  • the woven fabric is relaxed by the steam treatment, with an additional stabilization of the tissue structure is achieved.
  • the cooling of the water vapor nitrogen mixture 80 ° C in the container 1 can by direct contact with a coolant can be made as shown 4 is explained:
  • the circulation line 47 of the piece dyeing machine 1 is replaced by the circulation line 47a, which are not in the treatment agent filter 24, but directly in the container 1 at a point at 55 opens out above the lowest point of the lower part of the container lies.
  • Shut-off valve 48 is by the treatment medium circulation pump 25 a cooling liquid, preferably water, circulate in the circuit containing the container 1 leave, which contains the heat exchanger 30.
  • the temperature of coolant kept at 80 ° C or below flows from the orifice 55 of the circulation line 47a in a thin layer on the inner wall the container 1 down, where they are in one Swamp collects, whose liquid level indicated at 56 below the product lines 4 in the two stores 3 stands so that it does not contain the coolant come into contact.
  • the water vapor-nitrogen mixture in the container 1 is from the blower 15 above the container 1 circulates and strokes the surface of the coolant. By direct contact with the colder Coolant and by the condensate content, which is the water vapor-nitrogen mixture is precipitated out of the water vapor portion deprived of heat at the same time, so that the strands 4 are also cooled.
  • the coloring is then according to the instructions for use the inking units completed, i.e. after a Holding time at 80 ° C, the textile is cooled to 60 °, so depending on the vat dye used in this Temperature another bath pull-out takes place. After that flushed without air and the alkali-soluble leuco compound of the dyes with the subsequent oxidation treatment to the insoluble starting dyes within of the fibers of the textile goods. The vat coloring is then ended.
  • Polyester woven fabric with a fabric width of 150 cm and a basis weight of 145 g / m 2 and a batch weight of 130 kg per store, corresponding to a draw-in length of 600 m, is prewashed at a temperature of 80 ° C using air and a corresponding low steam inflow at 21, through the transport nozzles 12 and the reels 8 through the open charging openings 2 into the two stores 3 of the container 1.
  • the two endless strands 4 put into circulation are subjected to a prewash at 80 ° C. in which the textile goods are cleaned of preparation residues.
  • the textile goods are subjected to a dry run during approx. 5 runs of the product strand without a treatment liquor so that they can drip off sufficiently.
  • the circulating product lines 4 by exposure to water vapor, after prior venting of the container as in Example 1, in an almost saturated steam atmosphere at 130 ° C pretreatment temperature heated.
  • the product lines 4 are about 20 minutes kept at this temperature and then with a Gradients cooled from 2.5 ° C / min to 80 ° C.
  • the cooling can be done in a similar manner as in Example 3, however, the negative pressure that forms in the container 1 not with nitrogen, but with compressed air.
  • a 0.5 percent dispersion coloring was carried out.
  • the injection amount will preset at 80l / min for each store 3.
  • the color fleet and the polyester woven goods are made according to a predetermined Temperature-time program then heated to 110 ° C.
  • the Woven goods are then opened during 5 rounds of goods Kept at 110 ° C.
  • the injection line 31 supplied injection quantity per store 3 10l / min reduced. With a temperature gradient of 3 ° C / min the textile material to a wet fixing temperature heated from 130 ° C.
  • the coloring is finished with a hot release.
  • the hot drain valve (27) is then still open as a preparation step for reductive cleaning the compressed gas connection 52 and the valve 51 nitrogen compressed gas introduced into the container 1. Because of that achieved very low air content in the water vapor-nitrogen mixture in the container 1 are the necessary Quantities of sodium hydroxide solution and hydrosulfite reduced considerably, to about a third of the otherwise required Amounts.
  • the staining is done after a treatment period for the reductive cleaning of about 10 minutes after each predefined, generally known regulations completed.
  • the inventive method explained can be according to the program control of the performance of the fan 15 predetermined parameters, such as the round trip time of the product lines 4, compliance with a predetermined slip between the line speed and the circulation speed the reel 8, the opening of the textile goods, which, especially in the case of tubular goods, not up to one inadmissible balloon formation in the area of the memory leak may lead, etc.
  • predetermined parameters such as the round trip time of the product lines 4, compliance with a predetermined slip between the line speed and the circulation speed the reel 8, the opening of the textile goods, which, especially in the case of tubular goods, not up to one inadmissible balloon formation in the area of the memory leak may lead, etc.
  • the to heat up of the textile goods according to a predetermined temperature-time gradient fed during the preparatory step Energy from the steam flowing into the container 1 and by the one delivered to the impeller in the blower 15 Work is delivered, it is usually required to achieve a tension-free transport of goods regulate and limit the power of the fan 15.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Preliminary Treatment Of Fibers (AREA)

Claims (20)

  1. Procédé pour le traitement de produits textiles en bandes, à base de fibres synthétiques ou naturelles ou de mélanges de telles fibres, selon lequel
    on place le produit textile dans une cuve (1), on l'introduit dans des buses de transport (12) et on l'assemble au niveau de ses extrémités pour former une bande de produit (4) sans fin,
    la bande de produit (4) sans fin est mise en mouvement par les buses de transport (12) dans un sens de circulation prédéterminé à l'intérieur de la cuve fermée,
    on alimente les buses de transport (12) avec un flux de gaz moteur qui fait avancer la bande de produit sans fin dans le sens de circulation prédéterminé, de l'air ou un mélange vapeur/air sous une température inférieure à 80°C environ étant utilisé pour ce flux de gaz pour introduire le produit textile dans la cuve,
    on soumet le produit textile, au cours d'au moins une étape de traitement, à un traitement avec un agent de traitement qui est amené sur le produit textile, à des fins d'action, sous une température de traitement prédéterminée, dans la région des buses de transport,
    chronologiquement avant le traitement avec l'agent de traitement, au cours d'au moins une étape de préparation ou de prétraitement, on élimine les tensions internes et/ou on provoque une contraction du produit textile en faisant agir directement de la vapeur d'eau sur ledit produit textile,
    dans lequel lors de l'étape de préparation ou de prétraitement, les buses de transport sont alimentées exclusivement avec de la vapeur et la bande de produit, pendant une durée d'action prédéterminée de la vapeur, est entraínée par celle-ci, le produit textile étant ainsi amené et/ou maintenu à une température de prétraitement prédéterminée, qui est indépendante de la température de traitement avec un agent de traitement lors d'étapes de traitement consécutives et
    dans lequel pour la préparation d'une étape de traitement, un agent de traitement liquide est mis en circulation dans un circuit distinct des buses de transport, sans qu'il agisse sur la bande de produit présente dans la cuve, la température de l'agent de traitement mis en circulation étant réglée en fonction de paramètres de traitement.
  2. Procédé selon la revendication 1, caractérisé en ce que le produit textile, à la fin de l'étape de préparation ou de prétraitement, est refroidi de la température de prétraitement jusqu'à une température prédéterminée.
  3. Procédé selon une des revendications précédentes, caractérisé en ce que la température du produit textile, pendant l'étape de préparation ou de prétraitement et/ou lors d'une autre étape durant son traitement est régulée par contact du flux de gaz, de vapeur ou de mélange vapeur/air alimentant les buses de transport et circulant à l'intérieur de la cuve avec une surface de liquide entretenue à l'intérieur de la cuve (1), en dehors de la bande de produit.
  4. Procédé selon une des revendications précédentes, caractérisé en ce que la cuve (1), au moins lors de l'étape de préparation ou de prétraitement, après le début de l'alimentation des buses de transport avec de la vapeur, est mise temporairement à l'atmosphère et en ce qu'un volume d'air présent dans la cuve (1) est au moins partiellement éliminé et remplacé par de la vapeur.
  5. Procédé selon une des revendications précédentes, caractérisé en ce qu'à la fin de l'étape de préparation ou de prétraitement, la pression de vapeur dans la cuve (1) est abaissée rapidement par ouverture de la cuve.
  6. Procédé selon une des revendications précédentes, caractérisé en ce que lors de l'étape de préparation ou de prétraitement, les buses de transport (12), après l'alimentation avec de la vapeur, sont alimentées avec un gaz inerte pendant un laps de temps prédéterminé.
  7. Procédé selon une des revendications précédentes, caractérisé en ce que le produit textile après l'étape de préparation ou de prétraitement est rincé la cuve (1).
  8. Procédé selon une des revendications précédentes, caractérisé en ce que les buses de transport (12) sont alimentées au moins partiellement avec de la vapeur ou un mélange vapeur/air aspiré dans la cuve (1) et mis en circulation par des moyens de mise en pression (15).
  9. Procédé selon la revendication 8, caractérisé en ce que de la vapeur fraíche est introduite dans la cuve (1) côté refoulement des moyens de mise en pression (15).
  10. Procédé selon la revendication 8, caractérisé en ce que de la vapeur fraíche est introduite dans la cuve (1) côté aspiration des moyens de mise en pression (15).
  11. Procédé selon une des revendications 9 à 10, caractérisé en ce que la puissance des moyens de mise en pression (15) est régulée.
  12. Procédé selon une des revendications précédentes, caractérisé en ce que les buses de transport (12), pendant au moins une étape de traitement, sont alimentées avec un flux de gaz auquel est ajouté un agent de traitement liquide qui est amené à agir sur le produit textile dans la région des buses de transport.
  13. Procédé selon la revendication 9, caractérisé en ce que la température de la bande de produit en circulation dans la cuve (1) est maintenue à une valeur déterminée ou amenée à cette valeur par action de vapeur et en ce que l'agent de traitement est introduit avec le produit textile sous des conditions prédéterminées, de préférence au moins sensiblement isothermes.
  14. Dispositif pour la mise en oeuvre du procédé selon une des revendications précédentes
    avec une cuve (1) résistante à la pression, qui peut être fermée,
    avec des buses de transport (12) pour un produit textile se présentant sous la forme d'une bande de produit (4) sans fin,
    avec un dispositif de circulation de gaz (11, 14, 15, 16) qui est connecté aux buses de transport côté refoulement et à la cuve côté aspiration,
    avec un dispositif de chargement (33, 34, 35) pour un agent de traitement liquide, à l'aide duquel l'agent de traitement peut être amené sur le produit textile, à des fins d'action, sous une température de traitement prédéterminée, dans la région des buses de transport,
    avec un moyen de stockage (3) aménagé à l'intérieur de la cuve (1) pour recevoir la bande de produit (4) déchargée côté sortie des buses de transport,
    avec un dispositif de raccordement (21) menant aux buses de transport pour une source de vapeur, qui est alimenté en vapeur, au moins pendant la phase préparation ou de prétraitement,
    caractérisé par un circuit propre, distinct du dispositif de circulation de gaz, qui comprend la cuve (1) ainsi que des pompes de circulation (25).
  15. Dispositif selon la revendication 14, caractérisé en ce que le dispositif de raccordement comprend un raccord de vapeur (21) qui débouche côté refoulement des moyens de mise en pression (15) du dispositif de circulation de gaz.
  16. Dispositif selon la revendication 14, caractérisé en ce que le dispositif de raccordement comprend un raccord de vapeur (21a) qui débouche côté aspiration de moyens de mise en pression (15) du dispositif de circulation de gaz.
  17. Dispositif selon la revendication 14, caractérisé en ce qu'un dispositif échangeur de chaleur (30) est disposé dans le circuit séparé pour l'agent de traitement liquide.
  18. Dispositif selon la revendication 14, caractérisé en ce que le circuit d'agent de traitement liquide est connecté au circuit de gaz comportant les buses de transport par l'intermédiaire de vannes (32) commandées.
  19. Dispositif selon une des revendications 14 à 18, caractérisé en ce que le circuit d'agent de traitement liquide débouche dans la cuve (1), dans la région d'une surface menant à la partie inférieure de la cuve (en 55), par laquelle le liquide de traitement est amené sans contact avec la bande de produit (4) dans la partie inférieure de la cuve (5) comportant un bac.
  20. Dispositif selon une des revendications 14 à 19, caractérisé en ce que le circuit d'agent de traitement liquide comporte un dispositif (57, 58) pour l'introduction d'adjuvants dans l'agent de traitement.
EP99105286A 1998-03-27 1999-03-15 Procédé et dispositif pour le traitement des étoffes textiles sous forme de boyau Expired - Lifetime EP0945538B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19813593 1998-03-27
DE19813593A DE19813593C2 (de) 1998-03-27 1998-03-27 Verfahren und Vorrichtung zur Behandlung von strangförmigem Textilgut

Publications (2)

Publication Number Publication Date
EP0945538A1 EP0945538A1 (fr) 1999-09-29
EP0945538B1 true EP0945538B1 (fr) 2003-08-06

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EP99105286A Expired - Lifetime EP0945538B1 (fr) 1998-03-27 1999-03-15 Procédé et dispositif pour le traitement des étoffes textiles sous forme de boyau

Country Status (5)

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EP (1) EP0945538B1 (fr)
AT (1) ATE246740T1 (fr)
DE (2) DE19813593C2 (fr)
ES (1) ES2202945T3 (fr)
WO (1) WO1999050493A1 (fr)

Cited By (1)

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Publication number Priority date Publication date Assignee Title
DE102007036408B3 (de) * 2007-08-02 2008-12-18 Then Maschinen Gmbh Vorrichtung zum Behandeln von strangförmiger Textilware

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IT1314601B1 (it) * 2000-03-31 2002-12-20 Laip S N C Di Becheri Cecchi & Procedimento discontinuo di lavaggio di pezze di tessuto unite incorda ed una macchina per attuare il procedimento
US6676710B2 (en) 2000-10-18 2004-01-13 North Carolina State University Process for treating textile substrates
EP1241290A1 (fr) * 2001-03-14 2002-09-18 Chin-Lin Teng Dispositif pneumatique-hydraulique d'atomisation de liquide de teinture
EP1241289A1 (fr) * 2001-03-14 2002-09-18 Chin-Lin Teng Machine à teindre pneumatique-hydraulique
DE10124542B4 (de) * 2001-05-19 2004-03-11 Then Maschinen- Und Apparatebau Gmbh Vorrichtung zur Behandlung von strangförmigem Textilgut
CN1193127C (zh) * 2002-10-29 2005-03-16 邓金麟 气液式染液喷涂装置的改进
DE10349375B4 (de) * 2003-10-21 2008-04-10 Then Maschinen (B.V.I.) Ltd., Road Town Verfahren und Vorrichtung zum Spülen von strangförmigen Textilgut
DE10349374B4 (de) * 2003-10-21 2009-04-09 Then Maschinen (B.V.I.) Ltd., Road Town Nassbehandlungsmaschine für strangförmiges Textilgut
DE10349377B4 (de) * 2003-10-21 2008-04-10 Then Maschinen (B.V.I.) Ltd., Road Town Verfahren und Vorrichtung zum gleichmäßigen Aufbringen von Behandlungsmitteln auf einen Warenstrang
DE10349384B4 (de) 2003-10-21 2007-10-31 Then Maschinen (B.V.I.) Ltd., Road Town Vorrichtung zur Behandlung von strangförmiger Textilware
DE102004061186B4 (de) * 2004-12-20 2007-06-21 Then Maschinen (B.V.I.) Ltd., Road Town Verfahren und Vorrichtung zum Behandeln von strangförmiger Textilware
JP2006207041A (ja) * 2005-01-25 2006-08-10 Then Maschinen (Bvi) Ltd 紐状の繊維製品の湿式処理機械
JP2006207044A (ja) * 2005-01-25 2006-08-10 Then Maschinen (Bvi) Ltd 紐状の繊維製品を処理する装置
DE102005027070B3 (de) * 2005-06-11 2007-01-04 Then Maschinen Gmbh Verfahren und Vorrichtung zum gleichmäßigen Aufbringen von Behandlungsmitteln auf einen Warenstrang
CN101613919B (zh) * 2009-07-14 2013-10-30 无锡东宝机械制造有限公司 一种气流染色机的喷嘴
CN101613921B (zh) * 2009-07-14 2013-08-28 无锡东宝机械制造有限公司 一种气流染色机的摆布机构
DE202012013234U1 (de) * 2011-05-11 2015-08-13 Zhejiang Yinhe Printing & Dyeing Co., Ltd. Luftstromzerstäubungsfärbemaschinensystem
EP2570543A4 (fr) * 2011-06-10 2014-01-22 Zhejiang Yinhe Printing & Dyeing Co Ltd Système de teinture à débordement pour machine de teinture à atomisation par écoulement air et procédé d'utilisation d'eau associé
CN105401362A (zh) * 2015-12-14 2016-03-16 立信染整机械(深圳)有限公司 一种对织物于缸内进行预处理的设备及方法
CN110411522B (zh) * 2019-08-02 2020-12-04 中国核动力研究设计院 运动条件自然循环工况下脉动低流量测量实验装置及方法

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EP0014919B1 (fr) * 1979-02-17 1984-02-22 Hoechst Aktiengesellschaft Procédé de traitement de matières textiles dans des machines de teinture par jets
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Publication number Priority date Publication date Assignee Title
DE102007036408B3 (de) * 2007-08-02 2008-12-18 Then Maschinen Gmbh Vorrichtung zum Behandeln von strangförmiger Textilware
WO2009016179A1 (fr) 2007-08-02 2009-02-05 Then Maschinen Gmbh Dispositif et procédé de traitement de textile en forme de boyau

Also Published As

Publication number Publication date
EP0945538A1 (fr) 1999-09-29
DE59906472D1 (de) 2003-09-11
WO1999050493A1 (fr) 1999-10-07
DE19813593C2 (de) 2002-03-28
DE19813593A1 (de) 1999-10-07
ES2202945T3 (es) 2004-04-01
ATE246740T1 (de) 2003-08-15

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