EP1055763B1 - Procédé pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles - Google Patents
Procédé pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles Download PDFInfo
- Publication number
- EP1055763B1 EP1055763B1 EP00110496A EP00110496A EP1055763B1 EP 1055763 B1 EP1055763 B1 EP 1055763B1 EP 00110496 A EP00110496 A EP 00110496A EP 00110496 A EP00110496 A EP 00110496A EP 1055763 B1 EP1055763 B1 EP 1055763B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- steam
- web
- treatment
- fabric
- reactive dye
- 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
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Classifications
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- 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
- D06B23/04—Carriers or supports for textile materials to be treated
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- 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
- D06B19/00—Treatment of textile materials by liquids, gases or vapours, not provided for in groups D06B1/00 - D06B17/00
- D06B19/0005—Fixing of chemicals, e.g. dyestuffs, on textile materials
- D06B19/0029—Fixing of chemicals, e.g. dyestuffs, on textile materials by steam
- D06B19/0035—Fixing of chemicals, e.g. dyestuffs, on textile materials by steam the textile material passing through a chamber
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- 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
Definitions
- the invention relates to a process for the continuous treatment of a wet dyed textile web of natural fibers with steam applied to the reactive dyestuff.
- a reduction in the amount of urea is, as described in DE 43 03 129 C2, also made possible by spraying the printed and dried goods immediately before entering the Hänschleleifendämpfer with water. These fixation methods in the hanging loop damper require an average steaming time of 10 to 15 minutes.
- the goods content is generally 80 to 490 m, resulting in a goods speed of 5 to 50 m / min.
- the fixation of the reactive dye is usually carried out with saturated steam at about atmospheric pressure, that is, in a saturated steam atmosphere.
- a hanging loop damper with a product content of at least 80 m is not economically viable for smaller quantities to be dyed (smaller quantities).
- Another damper is known from DE 23 10 195 C2.
- This damper has a treatment chamber and a transport device with an at least partially horizontal goods guide by means of a conveyor belt.
- the treatment chamber is designed as a downwardly open hood.
- entrained air can precipitate out of the downwardly open vapor space, so that there is always a pure steam atmosphere available.
- a fixation of a dry web in this steam atmosphere, which is also a pure saturated steam atmosphere is not possible without urea.
- Disadvantage of this damper is that due to the above-mentioned steaming time in saturated steam atmosphere of 10 to 15 minutes in continuous operation only low speeds of goods can be driven. Higher speeds would only be possible with large lengths of the damper with correspondingly high investment and operating costs. Also, this damper is not economical for smaller quantities to be dyed.
- An apparatus and method for treating a web with steam is known from FR-A-1,090,013. It has a treatment chamber, a vapor-tight housing enclosing the treatment chamber and a transport device with rollers, through which the material web is guided horizontally.
- a recirculation device is provided with a circulating air fan and arranged above and below the web nozzle boxes.
- a dye-containing web is treated with saturated steam for a few seconds. With this use of saturated steam there is a high risk of condensation in the recirculation system and on the goods and thus of quality losses.
- a further disadvantage of the abovementioned methods is that after being exposed to a reactive dye dissolved in water, the web is first dried and only then is the reactive dye fixed to the fibers.
- the two stages of drying and fixing require two treatment devices.
- a printing machine is usually used for drying and for fixing one of the above-mentioned Dämpfvorrichtugen
- the web is moistened, wet printed and steamed in the wet state without intermediate drying.
- the damping is carried out in a saturated steam atmosphere for 1.0 to 20 minutes at 96 to 105 ° C.
- urea is used in the usual amount.
- GB-A-1,090,005 a process for dye fixation with superheated steam is described in which the material provided with dye and urea is first dried and then treated with superheated steam for 1.5 to 5 minutes.
- material which has been first charged with dye and then with a brightener and urea is treated with superheated steam.
- a method for heat treating a web, in particular for hot steam drying, by blowing hot steam is known from DE 195 46 344 A1.
- the web is partially transported horizontally through several treatment chambers.
- the steam is inflated by arranged above and below the web nozzle boxes on the web.
- the object of the invention is to develop a process for the continuous treatment of a reactive dye acted upon, wet textile web of native fibers with vapor dye according to the preamble of claim 1, which is suitable for fixing reactive dye.
- a method is to be developed, which largely does not require urea and is economical for smaller Metragen, as well as rapid heating, gentle transport of the web allows and leads to good Fixierlingern.
- the steam treatment should be effective and thus fast to carry out. It should also be suitable for fixing printed webs.
- the steam is in the form of superheated steam, that is used as superheated steam at about atmospheric pressure.
- the superheated steam consists of at least 80% by volume, preferably 95 to 100% by volume (pure superheated steam) of water vapor.
- the superheated steam has a temperature of 130 to 230 ° C, in particular from 160 to 230 ° C, on.
- the wet web is dried during the steam treatment by the use of superheated steam. It has been found that drying the web during the fixing treatment leads to an acceleration of the reaction of the reactive dye with the native fibers. This results in a further reduction of the fixation time.
- a horizontal web guide allows gentle transport of the reactive dye acted upon, moist web.
- the use of a horizontal web guide which requires a large volume of construction in saturated steam atmosphere based on the goods content, can also be used for smaller quantities in connection with the effective steam treatment with superheated steam.
- the superheated steam in the treatment chambers is inflated onto the material web through nozzle boxes arranged above and below the material web.
- the superheated steam is conducted in the recirculation method.
- the web is sprayed with superheated steam.
- the spraying allows a higher rate of exchange of the treatment vapor on the surface of the web and thereby a greater energy input per time than a stationary Dampfatmosotrore.
- the use of superheated steam has the advantage of a lower risk of condensation in the recirculation system compared to saturated steam in the case of spraying via a recirculation system.
- the treatment method according to the invention can be dispensed with the use of urea for most reactive dyes.
- the residence time of the web in the treatment chambers may be according to claim 55 to 60 seconds, preferably 10 to 20 seconds. This time is sufficient for drying and complete fixation with good color yield and allows a device of small size.
- a device described below is suitable for carrying out the method according to claims 1 to 6.
- a steam-tight housing enclosing all treatment chambers allows the use of superheated steam.
- the recirculation devices with at least one circulating air fan and nozzle cheeses arranged above and below the material web, the steam treatment with superheated steam can also be made effective in the gentle, horizontal material web guidance.
- This device is therefore particularly suitable for fixing small coins.
- the transport of the web through a belt designed as a belt conveyor allows for a non-contact transport of the printed surface of the web steam delivery from the top and bottom of the web.
- the Device is therefore particularly suitable for color fixing printed webs.
- a large opening degree of the screen belt of 50 to 90% allows a large contact surface of the web to superheated steam. This leads to a high exchange rate and thus to a more effective steam treatment.
- a return of the conveyor belt below the housing requires only one inlet and one outlet slot for the conveyor belt and allows the arrangement of a clamping system and a drive for the conveyor belt outside of the vapor-tight housing. This simplifies the construction of the device.
- a running at an acute angle to the vertical through the entrance lock guide belt which may be formed by the conveyor belt itself or another band, allows deflections of the web by angles> 90 °.
- the acute angle is preferably 30 to 60 °.
- a feed belt projecting in the vicinity of the conveyor belt running through the treatment chambers simplifies the supply of the beginning of a new web to the conveyor belt.
- a feed belt extending through the entrance gate according to claim 11 is particularly suitable for devices having a conveyor belt returning through the treatment chamber.
- a device for carrying out the method has in each case a lock in front of and behind the housing.
- the locks extend from the floor to the transport plane of the web and are divided into a lower, downwardly open pre-chamber and a main chamber arranged above.
- Intake channels or suction boxes can be connected to the antechambers.
- a lock known from DE 198 58 839, in which steam is blown onto the web in front of the inlet slit of the housing, is less suitable for fixing dye because of the risk of color gradients.
- Figure 1 shows a system for printing a textile web with a device for fixing the color of the first example
- Figure 2 shows this device with reference to a schematic cross section.
- An apparatus for color fixing of the second example is also shown with reference to a schematic cross section in Figure 3.
- a plant for printing a textile web 1 of native fibers, for example of cotton or cellulose, with reactive dye has arranged in the transport direction one behind the other a goods storage 2, a feed device 3, a printing device 40, a device for ink fixation 6, another supply device 7 and a another goods storage 8.
- the front goods storage 2 as winder
- the front Feed device 3 as a gallows
- the rear feed device 7 as Abtafler
- the rear goods storage 8 formed as a container.
- the printing device 40 is designed as a rotary printing machine.
- another printing machine such as a flatbed printing machine or an inkjet printing machine, may be used.
- the device 6 for color fixing has an entrance lock 9, a vapor-tight, heat-insulated housing 10 and an exit lock 11.
- the housing 10 comprises one or more, preferably one to four, modularly juxtaposed treatment chambers 12; that is, the interior of the housing 10 is divided by the treatment chamber 12 in one or more consecutively arranged fields.
- the housing 10 is not subdivided and comprises all treatment chambers, in this example a treatment chamber 12.
- each treatment chamber 12 is a recirculation device, that is a device for guiding superheated steam in a cycle, also called recirculation method, arranged with at least one circulating fan 14, at least one heating device not shown in the drawing and with nozzle boxes 15 with targeting the web 1 nozzle openings ,
- the nozzle boxes 15 are arranged above and below the web 1 and extend transversely across the web 1.
- one or more upper and lower nozzle boxes 15 may be arranged one behind the other.
- the treatment chamber 12 is provided with four upper and four lower nozzle boxes 15 and two circulating fans 14.
- Each of the recirculation fans 14 is associated with two upper and two lower nozzle boxes 15.
- the upper and lower nozzle boxes 15 may be arranged opposite to each other or offset from each other.
- the nozzle openings of the nozzle boxes 15 are preferably formed as slots.
- the transport device has a trained as a sieve belt 41, circulating conveyor belt, by two upper guide rollers 42, 43 with its upper Run through the treatment chamber 12 and through two lower guide rollers 44, 45 with its lower run under the treatment chamber 12 and below the housing 10 is guided.
- the upper front guide roller 42 is located completely in the entrance lock 9 and the upper rear guide roller 43 completely in the exit lock 11. Their arrangement is such that the web 1 in the treatment chamber 12 is flat and horizontal, that is in a horizontal transport plane, out , One of the lower guide rollers 44, 45 is connected to a drive, not shown.
- the transport device further comprises a, not shown, conventional tensioning device, through which the screen belt 41 is stretched, and optionally not shown support devices in the treatment chamber 12.
- the support devices may be formed by longitudinal slide rails attached to the sides on the nozzle boxes 15 or by support rollers mounted between the nozzle boxes 15.
- the screen belt 41 has an open area of at least 50% to a maximum of 90%. It consists in this example of a metal link belt with an open area of 80% and has chain links on its sides. Accordingly, the guide rollers 43, 44, 45 and 46 on their sides on gears. Alternatively, the screen belt 41 may be formed as a perforated metal strip or as a glass cloth tape.
- the housing 10 has on a front wall 26 an inlet slot 27 and on a rear wall 28 an outlet slot 29, through which the web 1 is guided in the housing 10 and out of it.
- the entrance lock 9 has a parallel to the front wall 26 extending, in the vicinity of a lower edge 30 to above the inlet slot 27 extending front plate 31, a ceiling plate 32 and two side plates, not shown.
- the sheets 31, 32 of the entrance lock 9 are vapor-tight with each other and connected to the front wall 26.
- the entrance lock 9 is characterized by intermediate plates 33, 34 extending from the front panel 31 and the front wall 26 into the interior of the entrance lock 9 and between them leave a gap 35 for the web 1 and possibly a conveyor belt, divided into an upper main chamber 36 and a lower prechamber 37.
- the pre-chamber 37 is open at the bottom.
- a suction device in this example connected to a fan, not shown suction channel 38 is connected.
- suction boxes 39 to which the suction channel 38 is connected, in the antechamber 37.
- the guide roller 44 of the transport device is located directly below the prechamber 37 and the guide roller 42 in front of the inlet slot 27th
- the exit lock 11 is constructed analogously to the entrance lock 9.
- the guide rollers 43, 45 are arranged analogously to those of the entrance lock 9.
- the transport device also has a guide roller 46 arranged behind the guide roller 45 for deflecting the web 1 and for separating it from the wire 41 and a feed belt 47 for feeding the web 1 to the device 6.
- the feed belt 47 guided around two rollers 48, 49 extends horizontally in this example and extends below the prechamber 37 of the inlet lock 9.
- the web 1 is withdrawn from the goods storage 2 via the feed device 3 designed as a gallows and supplied to the device 6 for color fixing by the printing device 40 designed as a rotary printing press.
- the web 1 is transported over the feed belt 47 of the transport device to below the antechamber 37 of the entrance lock 9. There, the screen belt 41 takes over the transport from below through the prechamber 37, through the gap 35 in the main chamber 36 to the guide roller 42 around, through the inlet slot 37 and through the treatment chamber 12. For this, the web 1, possibly automatically, to the sieve band clamped.
- the web 1 leaves the Device 6 through the exit slot 29 and the exit lock 11. It is supplied via the designed as Abtafler supply device 7 designed as a container goods storage 8.
- the web speed is, for example, 40 m / min.
- the web 1 is applied with printing paste.
- the moist web 1 is, while it is being transported through the treatment chamber 12 of the device 6, applied via the above and below the web 1 arranged nozzle boxes 15 directed to the web 1 nozzle openings with superheated steam.
- the nozzle pressure is 200 to 1000 PA and the heat transfer capacity about 240 W / m 2 .
- the temperature of the superheated steam is 130, in particular 160, to 230 ° C and the residence time of the web 1 in the treatment chamber 12 5 to 60 seconds, preferably 10 to 20 seconds.
- the residual moisture of the web 1 when leaving the housing 10 during printing is less than the equilibrium moisture content under normal conditions, that is, it is less than 10%.
- the steam content preferably between 95 and 100% by volume, is maintained by varying the amount of superheated steam extracted via the suction channels 38 of the antechambers 37 of the inlet and outlet sheaths 9, 11. A regulation of a certain residual moisture of the web 1 is not necessary.
- the temperature of the pure hot steam is 180 ° C.
- the nozzle pressure at the nozzle openings of the nozzle boxes 15 is 700 PA.
- Even after a residence time of 5 seconds the vast majority of the dye has reacts with the fibers of the web 1 and is fixed. After another 5 seconds, the web 1 is completely dried and the remaining part of the dye is fixed.
- the input moisture of about 20% is reduced in the device 6 to a value less than or about 5%.
- the total residence time in the device 6 is 10 seconds.
- the color fixing apparatus 6 of Example 2 is the same as that of Example 1 except for the features described below.
- Your housing 10 includes three treatment chambers 12, each treatment chamber 12 is provided with a circulating air fan 14 and an upper and a lower nozzle box 15.
- Your transport device also has a designed as a sieve belt 51, circulating conveyor belt, which is guided in contrast to Example 1 by two guide rollers 52 and 53 with its upper and with its lower run through the treatment chambers 12; that is, the conveyor belt is returned through the treatment chambers 12. Also, the guide roller 52 is completely in the entrance lock 9 and the guide roller 53 completely in the exit lock 11. Their arrangement is also such that the web 1 is guided in a horizontal transport plane.
- the deflection roller 53 in the exit lock 11 is connected to a drive, not shown. In the exit lock 11 is also a clamping device, not shown, for the conveyor belt.
- the transport device furthermore has support rollers 54 in the field impacts, that is to say in the regions in which the treatment chambers 12 abut one another.
- the entrance lock 9 of this device 6 for color fixing runs at an acute angle to the vertical.
- the front plate 31 is arranged at this acute angle to the vertical and the side plates, not shown, are shaped accordingly.
- the outgoing of the front wall 26 intermediate plate 34 is extended according to the deflection of the front plate 31 and has at its front end to such a fold 55 that it ends with respect to the outgoing from the front plate 31 intermediate plate 33. Also, the outgoing from the front wall 26 nozzle box 39 is extended and folded accordingly.
- the transport device has in this example a guide roller 56 at the exit of the exit lock 11 and a feed belt 57.
- the feed belt 57 which is guided around two rollers 58, 59, runs parallel to the front plate 31 and extends through the front chamber 37 and the main chamber 36 of the entrance lock 9; i.e. the supply belt 57 forms at an acute angle to the vertical, through the entrance lock 9 extending guide band.
- the gap 35 between the intermediate plates 33 and 34 and the distance between the suction boxes 39 is formed correspondingly wide.
- the upper roller 59 of the feed belt 58 is arranged slightly in front of and slightly above the deflection roller 52 and the roller 56 in front of the prechamber 37 of the entrance lock 9.
- moist web 1 is transported via the feed belt 57 through the entrance lock 9, placed on the wire 51 from above and transported on the wire 51 through the treatment chambers 12 to the exit lock 11. From the exit lock 11, the web 1 is withdrawn via the guide roller 57.
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Treatment Of Fiber Materials (AREA)
- Coloring (AREA)
Claims (6)
- Procédé de traitement en continu par de la vapeur d'une étoffe (1) textile en fibres naturelles, humide et alimentée en colorant réactif,
dans lequel on transporte l'étoffe (1) au moins en partie horizontalement dans au moins une chambre (12) de traitement, on insuffle la vapeur dans les chambres (12) de traitement sur l'étoffe (1) par des boîtes (15) à buses disposées au dessus et en dessous de l'étoffe (1) et la vapeur est engagée sous la forme de vapeur surchauffée, c'est-à-dire de vapeur d'eau surchauffée, à une température de 130 à 230° C et, par l'utilisation de vapeur surchauffée, on sèche et on fixe l'étoffe humide pendant le traitement à la vapeur. - Procédé selon la revendication 1, dans lequel on effectue l'alimentation de l'étoffe en colorant réactif par teinture, caractérisé en ce que l'on règle l'humidité de l'étoffe (1) teinte avant le traitement par de la vapeur entre 40 et 80%.
- Procédé selon la revendication 1, dans lequel on effectue l'alimentation de l'étoffe (1) en colorant réactif par impression, caractérisé en ce que l'on règle l'humidité de l'étoffe à imprimer avant le traitement par de la vapeur entre 10 et 40 %.
- Procédé selon la revendication 1 ou 3, dans lequel on effectue l'alimentation de l'étoffe en colorant réactif par impression, caractérisé en ce que l'on sèche l'étoffe (1) pendant le traitement par de la vapeur, jusqu'à une humidité résiduelle de 1 à 10 %, notamment de 3 à 7%.
- Procédé selon l'une des revendications 1 à 4, caractérisé en ce que la durée de traitement par de la vapeur, c'est-à-dire la durée de séjour dans les chambres (12) de traitement, est comprise entre 5 à 60 secondes, notamment entre 10 et 20 secondes.
- Procédé selon une des revendications 1 à 5 caractérisé en ce que l'on transporte l'étoffe (1) dans les chambres (12) de traitement au moyen d'une bande convoyeuse (41) perforée.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP06020559A EP1746191A3 (fr) | 1999-05-28 | 2000-05-17 | Procédé et dispositif pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19924433 | 1999-05-28 | ||
DE19924433 | 1999-05-28 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06020559A Division EP1746191A3 (fr) | 1999-05-28 | 2000-05-17 | Procédé et dispositif pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1055763A2 EP1055763A2 (fr) | 2000-11-29 |
EP1055763A3 EP1055763A3 (fr) | 2002-01-30 |
EP1055763B1 true EP1055763B1 (fr) | 2006-10-18 |
Family
ID=7909435
Family Applications (4)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP00110496A Expired - Lifetime EP1055763B1 (fr) | 1999-05-28 | 2000-05-17 | Procédé pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles |
EP06020559A Withdrawn EP1746191A3 (fr) | 1999-05-28 | 2000-05-17 | Procédé et dispositif pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles |
EP00110489A Expired - Lifetime EP1063337B1 (fr) | 1999-05-28 | 2000-05-17 | Procédé pour le traitement thermique continu d'une étoffe textile, notamment pour le fixage des matières colorantes |
EP05011446A Expired - Lifetime EP1589141B1 (fr) | 1999-05-28 | 2000-05-17 | Dispositif pour le traitement thermique continu d'une étoffe textile, notamment pour le fixage des matières colorantes |
Family Applications After (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06020559A Withdrawn EP1746191A3 (fr) | 1999-05-28 | 2000-05-17 | Procédé et dispositif pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles |
EP00110489A Expired - Lifetime EP1063337B1 (fr) | 1999-05-28 | 2000-05-17 | Procédé pour le traitement thermique continu d'une étoffe textile, notamment pour le fixage des matières colorantes |
EP05011446A Expired - Lifetime EP1589141B1 (fr) | 1999-05-28 | 2000-05-17 | Dispositif pour le traitement thermique continu d'une étoffe textile, notamment pour le fixage des matières colorantes |
Country Status (6)
Country | Link |
---|---|
US (4) | US6471729B1 (fr) |
EP (4) | EP1055763B1 (fr) |
AT (3) | ATE302868T1 (fr) |
DE (5) | DE50011009D1 (fr) |
DK (2) | DK1063337T3 (fr) |
ES (1) | ES2247977T3 (fr) |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
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EP1055763B1 (fr) * | 1999-05-28 | 2006-10-18 | Moenus Textilmaschinen GmbH | Procédé pour le traitement continu à la vapeur d'une étoffe textile pour le fixage des colorants réactifs sur des fibres naturelles |
AU2003257391A1 (en) * | 2002-07-31 | 2004-03-03 | A. Monforts Textilmaschinen Gmbh And Co | Method for finishing denim |
US7931699B2 (en) * | 2002-12-27 | 2011-04-26 | Hbi Branded Apparel Enterprises, Llc | Compositions for spray dyeing cellulosic fabrics |
US7931700B2 (en) * | 2002-12-27 | 2011-04-26 | Hbi Branded Apparel Enterprises, Llc | Composition for dyeing of cellulosic fabric |
US7033403B2 (en) * | 2002-12-27 | 2006-04-25 | Sara Lee Corporation | Spray dyeing of garments |
US20060265816A1 (en) * | 2003-06-23 | 2006-11-30 | Michael Abbott | Formers for spray dyeing garments |
US7799097B2 (en) * | 2003-06-23 | 2010-09-21 | Hbi Branded Apparel Enterprises, Llc | Processes for spray dyeing fabrics |
US8814953B1 (en) | 2003-06-23 | 2014-08-26 | Hbi Branded Apparel Enterprises, Llc | System and method for spray dyeing fabrics |
KR20050017655A (ko) * | 2003-08-08 | 2005-02-22 | 삼성전자주식회사 | 드럼 세탁기 및 그 제어방법 |
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DE102006043600A1 (de) * | 2006-09-16 | 2008-03-27 | Mageba-Textilmaschinen Gmbh & Co. Ohg | Dampfschrank sowie Verfahren zum Dämpfen von textiler Bandware |
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-
2000
- 2000-05-17 EP EP00110496A patent/EP1055763B1/fr not_active Expired - Lifetime
- 2000-05-17 DE DE50011009T patent/DE50011009D1/de not_active Expired - Fee Related
- 2000-05-17 AT AT00110489T patent/ATE302868T1/de not_active IP Right Cessation
- 2000-05-17 ES ES00110489T patent/ES2247977T3/es not_active Expired - Lifetime
- 2000-05-17 DK DK00110489T patent/DK1063337T3/da active
- 2000-05-17 DE DE50013624T patent/DE50013624D1/de not_active Expired - Fee Related
- 2000-05-17 EP EP06020559A patent/EP1746191A3/fr not_active Withdrawn
- 2000-05-17 AT AT00110496T patent/ATE343010T1/de not_active IP Right Cessation
- 2000-05-17 DK DK00110496T patent/DK1055763T3/da active
- 2000-05-17 EP EP00110489A patent/EP1063337B1/fr not_active Expired - Lifetime
- 2000-05-17 DE DE10023722A patent/DE10023722A1/de not_active Withdrawn
- 2000-05-17 DE DE50014901T patent/DE50014901D1/de not_active Expired - Fee Related
- 2000-05-17 EP EP05011446A patent/EP1589141B1/fr not_active Expired - Lifetime
- 2000-05-17 DE DE10023721A patent/DE10023721A1/de not_active Withdrawn
- 2000-05-17 AT AT05011446T patent/ATE382729T1/de not_active IP Right Cessation
- 2000-05-26 US US09/580,261 patent/US6471729B1/en not_active Expired - Fee Related
- 2000-05-26 US US09/580,263 patent/US6485526B1/en not_active Expired - Fee Related
-
2002
- 2002-05-07 US US10/140,671 patent/US7089767B2/en not_active Expired - Fee Related
- 2002-05-13 US US10/144,367 patent/US6591639B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1090003A (en) * | 1964-10-29 | 1967-11-08 | Ici Ltd | Process for steaming fabrics |
EP0021055A1 (fr) * | 1979-06-01 | 1981-01-07 | Hoechst Aktiengesellschaft | Procédé de "rongeage blanc" ou "rongeage coloré" de teintures réalisées sur des matières textiles |
Also Published As
Publication number | Publication date |
---|---|
EP1055763A3 (fr) | 2002-01-30 |
EP1063337B1 (fr) | 2005-08-24 |
DE50013624D1 (de) | 2006-11-30 |
US6485526B1 (en) | 2002-11-26 |
EP1589141A1 (fr) | 2005-10-26 |
DE10023722A1 (de) | 2000-11-30 |
EP1063337A3 (fr) | 2002-01-30 |
EP1746191A2 (fr) | 2007-01-24 |
EP1746191A3 (fr) | 2007-02-21 |
US20020170118A1 (en) | 2002-11-21 |
DE50014901D1 (de) | 2008-02-14 |
US20020124327A1 (en) | 2002-09-12 |
US7089767B2 (en) | 2006-08-15 |
EP1589141B1 (fr) | 2008-01-02 |
EP1055763A2 (fr) | 2000-11-29 |
ES2247977T3 (es) | 2006-03-16 |
EP1063337A2 (fr) | 2000-12-27 |
DE50011009D1 (de) | 2005-09-29 |
ATE343010T1 (de) | 2006-11-15 |
ATE382729T1 (de) | 2008-01-15 |
DE10023721A1 (de) | 2001-02-08 |
US6471729B1 (en) | 2002-10-29 |
US6591639B2 (en) | 2003-07-15 |
DK1063337T3 (da) | 2006-01-09 |
ATE302868T1 (de) | 2005-09-15 |
DK1055763T3 (da) | 2007-02-19 |
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