EP1112403B1 - Procede de traitement prealable de coloration reactive de matieres cellulosiques - Google Patents

Procede de traitement prealable de coloration reactive de matieres cellulosiques Download PDF

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Publication number
EP1112403B1
EP1112403B1 EP99955683A EP99955683A EP1112403B1 EP 1112403 B1 EP1112403 B1 EP 1112403B1 EP 99955683 A EP99955683 A EP 99955683A EP 99955683 A EP99955683 A EP 99955683A EP 1112403 B1 EP1112403 B1 EP 1112403B1
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EP
European Patent Office
Prior art keywords
pretreatment
treatment
per
compounds
cellulose material
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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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EP99955683A
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German (de)
English (en)
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EP1112403A1 (fr
Inventor
Kurt Van Wersch
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.)
A Monforts Textilmaschinen GmbH and Co KG
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A Monforts Textilmaschinen GmbH and Co KG
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Publication of EP1112403A1 publication Critical patent/EP1112403A1/fr
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L1/00Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods
    • D06L1/12Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods using aqueous solvents
    • D06L1/14De-sizing
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L4/00Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs
    • D06L4/10Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which develop oxygen
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P3/00Special processes of dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form, classified according to the material treated
    • D06P3/58Material containing hydroxyl groups
    • D06P3/60Natural or regenerated cellulose
    • D06P3/66Natural or regenerated cellulose using reactive dyes
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P5/00Other features in dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form
    • D06P5/002Locally enhancing dye affinity of a textile material by chemical means
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S8/00Bleaching and dyeing; fluid treatment and chemical modification of textiles and fibers
    • Y10S8/93Pretreatment before dyeing
    • Y10S8/931Washing or bleaching

Definitions

  • the invention relates to a process for pretreatment, namely desizing and decoction, and optionally bleaching, of cellulose goods in which a Treatment liquor containing a per-compounds, such as hydrogen peroxide Pretreatment agent applied to the cellulose product and in the goods in the Pretreatment effect is brought to effect. It also relates to a method for applying the treating agents in reactive dyeing and dye fixing Cellulose product in which the product pretreated before dye fixing, namely desized, boiled and / or bleached.
  • cellulose product Under a web-shaped "cellulose product" are textile fabrics made of cellulose - Including cotton, viscose, regenerated cellulose and mixtures thereof with each other and / or with synthetic fibers - understood. The procedure is primarily to find application in textile fabrics, such as web or Knitted fabric, in principle, but also comes with the use of threads or sherds in question.
  • suitable per-compounds - short "Per" - which split off oxygen in solution, preferably by decomposition of hydrogen peroxide, are e.g. Perborates or percarbonates.
  • the respective treatment agent is preferably applied by dipping in a treatment vehicle fleet.
  • Desizing and decoction and optionally bleaching are among the preparatory operations, the so-called "pre-treatment", in textile finishing.
  • the purpose of desizing is to strip off all sizing the fiber of applied substances.
  • Starch-containing sizing agents can be desized with the help of enzymes.
  • an oxidative Desirability required.
  • a combined desizing, washing and bleaching process for raw textiles Cotton which is to be carried out continuously, is described in CH 560 789.
  • the cellulose product is moistened with an aqueous solution which is essential Ingredients an alkali metal hydroxide and per-compounds, such as hydrogen peroxide and peroxidiphosphate.
  • the goods are at a treatment temperature heated from about 80 to 135 ° C.
  • treatment temperatures of 100 ° C and atmospheric pressure contains the treatment room 100 vol.% Steam.
  • the im Known provided lower temperature limit of 80 ° C and atmospheric pressure Almost 100% by volume steam is also reached in the treatment room.
  • the goods are washed. Short treatment times of down to 1 minute are only at 135 ° C and 100 vol.% steam in the pressure vessel and accordingly discontinuous possible.
  • DE 31 24 961 A1 discloses a batch process for simultaneous dyeing and desizing. It is a cold dwell process, in the case of the paint and desizing agent (amylase) and soda, the treatment bath be added. After diving and squeezing and a liquor pick-up of about 70%, the textile is rolled up and - with a plastic wrap wrapped - stored for 24 hours at about 20 ° C and slow rotation. Subsequently Among other things, the goods are passed through a boiling soap bath. If If the product is to be bleached, the soap bath can be the bleaching hydrogen peroxide contain. The simultaneous dyeing and desizing process can namely with bleaching is not combined because the bleach would damage the paint.
  • the invention has for its object to provide a pretreatment process, which allows a continuous continuous driving, the pretreatment summarized essentially in a treatment unit or aggregate type, particular neutralizing agents for eliminating any residues of per-compounds not needed and - without overpressure - compared to the state of Technique requires shorter processing times of the treated textile product.
  • Another The task is to reduce the consumption of pre-treatment and dye-fixing total amount of chemical aids required in reactive dyeing, in particular to alkali substances, without the pretreatment success or affect the color yield.
  • the solution according to the invention is used for the initially mentioned method for pretreatment, in which per-compounds are used, described in claim 1. It is crucial in particular that the per-compounds by continuous Dry with circulating air are expelled from the cellulose product.
  • One Process for reactive dyeing and dye fixing in cellulose goods is in the claim 6 indicated.
  • the invention can be achieved that the water content in the textile when drying in approximately the same extent so at about the same speed is reduced, such as the proportion of per-compounds, in particular hydrogen peroxide, - At the respective treatment temperature - decays or consumed becomes.
  • concentration of per-compounds in each of the product still existing fleet remain approximately constant according to the invention should.
  • the rate of disintegration of the per-compounds e.g. according to their respective task and / or treatment temperature, -
  • the rate of disintegration of the per-compounds e.g. according to their respective task and / or treatment temperature, -
  • stabilizers or destabilizers - so to control that the disintegration and drying rates close to the approximately complete decomposition or consumption of the per-compounds approximately the same run.
  • the relative effect of the per-compounds changes - because of their almost constant concentration on the product - during the virtually the entire pretreatment process.
  • the actual pretreatment process, followed by a further drying of the goods can be considered completed when the per-connections have completed their task.
  • the amount of per-compounds used can be sized that the latter - at (initially) approximately constant concentration on the goods - consumed at the end of the pretreatment process to an absolutely imperceptible level are. Because of any remains of the per-compound is therefore a washing, e.g. before dyeing, not required. The acquaintance had to wash it or neutralized because of the concentration of per compounds in the treatment liquor within the goods constantly decreased and - when towards the end of Process should have any effect at all - the per-connections (initially) were to be supplied in excess.
  • the method according to the invention can be carried out when hot and humid - not wet-hot - drying air is used.
  • the invention used Drying air should contain only so much moisture that an approximate Synchronization of drying speed of the product and decay rate the Per connection used is achieved. A drying air that meets these conditions is met, is referred to in the invention as "wet-hot”.
  • the pretreatment according to the invention should preferably be in one with circulating air operated air dryer, whose "hot-humid" drying air a the Drying rate per se elongating steam content, in particular of the order of magnitude about 30% by volume of steam.
  • This measure can be significant, e.g. vary by ⁇ 10% by volume. So it becomes an atypical operated air dryer provided that not - as usual - with the lowest possible water vapor content, but operated with relatively high water vapor content in the circulating air becomes.
  • the water vapor content should be so low that in any case a constant drying takes place during the treatment process and a Residence time within the circulating air of 2 to 5 minutes suffices to dry, when the temperature of the circulating air in the order of 100 ° C and more lies.
  • the aforementioned lower limit of the duration of treatment about 2 minutes, becomes defined by the time in which the proportion of per-compounds, e.g. hydrogen peroxide, depending on the height of the treatment temperature to a no longer disturbing degree consumed or chemically disintegrated.
  • the upper limit of the treatment duration is determined by the quality, in particular the severity, of the treated product. For light goods, a total treatment time may be sufficient, which is about the same the consumption or disintegration time of the per-connections.
  • the actual pretreatment is completed after the aforementioned minimum time. So if another Drying of the goods is not required, this pre-treatment can be stopped.
  • a treatment liquor containing a pretreatment agent loaded cellulose product (generally after immersion in the pre-treatment bath) continuously passed through the moist-hot drying air and there by the effect of damp heat on the pretreatment - in spite of the Moist continuous drying of the goods - at the same time desized, boiled and optionally bleached. All reactions sought during the pretreatment for the possibly various types of pretreatment can at the same time in the moist-hot drying air to be performed.
  • the cellulose product can be in the moist-hot drying air for a continuously following Dyeing to be fully prepared.
  • liquor can be applied to the cellulose product in several passes become. Preferably, this is done by soaking or dipping in one or several with each subsequent squeeze continuously connected in series Foulards. Between every two foulards, e.g. for better wetting, a dwell, e.g. an aisle, especially with a few tens of seconds Dwell time, be turned on. The squeezing effect can be adjusted be that the goods get into the air dryer with the usual residual moisture levels.
  • An advantageous device for carrying out the pretreatment method according to the invention comprises at least one treatment pad, an air dryer as well as washing and drying facilities.
  • an air dryer that is as a pretreatment unit, can a chamber with goods inlet and outlet and with controllable Exhaust air volume, controllable circulation fan and an adjustable steam injection be provided.
  • In the chamber should be on control means of exhaust air volume and steam injectors switched climate measuring device for adjusting a predetermined vapor content can be provided in the circulating air.
  • the treating agents in the reactive dyeing and dye fixing of cellulose products in which the Goods desized and boiled before dye fixing and optionally bleached - briefly pretreated - is, in that coming from the pretreatment Washed unwashed with reactive dye liquor and the dye then is fixed.
  • This part of the invention may be distinguished from the first part, the "pretreatment part” - be referred to as the "dyeing part”.
  • the dyeing part between the air dryer and the washer of the pretreatment part are set.
  • the goods can be washed after the pretreatment part and possibly dried and further processed in any (known) way become.
  • the coloring part of the invention may be any conventional Connect the pretreatment system and use the previously remaining alkali, if only no disturbing per-residue (in the goods to be dyed) remained.
  • the supplied for the pretreatment chemical Substances, in particular alkali, which leave the pretreatment plant are still present in the product, for the reaction mechanism used in reactive dye fixing.
  • the dyeing part so can in the Pre-treatment part of the invention of substances detached from the product and excess Treating agent remain on the goods and - so far when fixing the dye not consumed - only washed out after the end of the dye fixing process become.
  • the goods coming from the pretreatment as they is - if necessary, also undried - continuously and directly into the reactive dye liquor be directed.
  • the liquor must not contain any more harmful per-dyeing per-amounts.
  • the core of the dyeing part of the solution according to the invention is that the chemical substances already applied for or during the pretreatment - except for the per-compounds - not just for the physicochemical Process in the pretreatment, but a second time in dye fixing the reactive dye used.
  • the dyeing part of the invention contains the (pretreated and unwashed) goods already in contact with the reactive dye fleet that for the chemical Process of dye fixing in the device according to the aforementioned WO 97/14839 required alkali, etc.
  • This may indeed in the pre-treatment have been diluted in the goods, but for the Farbfixierprozeß ranges even a weak alkali.
  • subsequent to the reactive dye fixing Wash (usually with subsequent drying) will be at the same time the treatment agent surplus and reaction products, such as dirt - including remaining amounts of alkali - both the pretreatment and the dyeing separated.
  • the coloring part of the invention has an additional advantage: If not only the conventional adjoining the pretreatment Laundry, but also the drying can be omitted, will be the appropriate Saved investment and energy costs. Pre-treatment and dyeing then a common washing and drying plant is assigned. Surprisingly So comes to the advantage of saving amounts of alkali and reduced wastewater pollution, In addition, the advantage of reduced investment costs (it falls one complete washing and drying plant away) and the corresponding diminished Energy expenditure.
  • a plant according to the invention for pretreating cellulose goods can consist of Fig. 1 in principle of four units, namely from a padder 1 for the metered application of a pretreatment liquor onto the product, a Hotflue 2 for steam drying of the goods loaded in the padder 1, one of Hotflue 2 downstream washer 3 and a subsequent drying system 4, e.g. Hotflue, cylinder dryer or tenter.
  • a padder 1 for the metered application of a pretreatment liquor onto the product
  • a Hotflue 2 for steam drying of the goods loaded in the padder 1
  • Hotflue 2 downstream washer 3 e.g. Hotflue, cylinder dryer or tenter.
  • Each to be treated web-shaped cellulose product 5 is said units 1 to 4 continuously go through in the transport direction 6.
  • an aisle 13 e.g. With on the order of 20 to 40 seconds dwell time, turned on to to leave the pretreatment liquor of the first trough 1 a before the goods 5 in the second trough 1 b is running.
  • Fig. 1 in principle, it may be to carry out the invention Be favorable method, the chamber 12 of the air dryer 2 with a controllable Equip the exhaust duct 14 and with controllable steam injectors 15, and in the chamber on the control means of suction channel 14 (for the exhaust air volume) and steam injectors 15 connected climate measuring device 16 to arrange.
  • a predetermined minimum steam content of the wet-hot can be Recirculating air.
  • FIG. 3 shows the principle of a combination of pretreatment and dyeing system explained.
  • a moving in the transport direction 21 web-shaped Cellulose product 22 is characterized by a pretreatment agent application device symbolized as padder 23 passed with subsequent squeeze 24.
  • This device can like the pretreatment part according to the invention, e.g. as in Fig. 1 or 2, but also in be formed conventionally and then from one or more stages for applying the respective pretreatment 25 to the goods 22 exist.
  • Desizing, decoction and / or bleaching are preconditioning agents used, the alkali, in particular in the form of sodium hydroxide or the like Alkaline compound, included.
  • An alkali additive is for the physicochemical Activation system of pretreatment usually required.
  • the ones described in the Way in the padder 23 loaded goods 22 enters a somehow oroder multi-stage trained, but preferably in a pretreatment plant according to the invention 26th
  • the pretreated in Appendix 26 or the like asset 22 is in a Paint applicator out, in the drawing as a padder 27 with dyeing liquor 28th and downstream squeeze 29 is symbolized.
  • the dyeing liquor 28 should in the inventive Dyeing part of the process Reactive dye (and optionally Wetting agent). New alkali is not required. That for the reaction in the downstream Farbfixierstrom 30 required alkali (possibly including Other chemical aids) should the goods 22 already as (conventional to be washed out) from the pretreatment plant 26. However, remnants of per-compounds should no longer be present in the product be.
  • a washer 31 - e.g. the car wash 3 of Fig. 1 - connect.
  • all substances are washed out, which would interfere with the further equipment of the goods 22.
  • These include in particular the dissolved or converted sizing agents, released dirt, the excess dye and unused or converted adjuvants.
  • the cleaned in the car wash 31 goods 22 may finally by a Run dryer 32 and then fed to another processing or stored become.

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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)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Claims (9)

  1. Procédé de traitement préparatoire, c'est-à-dire destiné à désencoller et à rebouillir ainsi qu'éventuellement à blanchir, une matière cellulosique (5) en forme de bande, dans lequel un bain de traitement (7) comprenant un agent de traitement préparatoire contenant des combinaisons per comme du peroxyde d'hydrogène, est appliqué à la matière cellulosique (5) et est mis en oeuvre dans la matière pour exécuter le traitement préparatoire, caractérisé en ce que le séchage de la matière cellulosique (5) est exécuté approximativement en parallèle avec la vitesse de décomposition des combinaisons per utilisées, et que la concentration des combinaisons per dans le bain de traitement qui est encore présent respectivement sur la matière cellulosique reste de façon correspondante à peu près constante.
  2. Procédé selon la revendication 1, caractérisé en ce que la matière cellulosique (5) est soufflée au moyen d'air pulsé et poursuit ainsi son parcours en continu.
  3. Procédé selon la revendication 2, caractérisé en ce qu'une humidité encore suffisante d'air est réglée dans l'air puisé pour maintenir une humidité de matière adaptée à la réaction pour exécuter le processus de traitement préparatoire.
  4. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce qu'un stabilisateur ou un déstabilisateur est ajouté à l'agent de traitement pour améliorer le synchronisme entre les vitesses de séchage et de décomposition.
  5. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que la matière cellulosique (5) est séchée en continu dans un sécheur à air (2), en particulier une hotflue, pour maintenir une humidité résiduelle d'une teneur volumique en vapeur de l'ordre de 25%, adaptée à la réaction pour exécuter le traitement préparatoire, jusqu'à ce que les teneurs en combinaisons per contenues dans la matière soient consommées ou décomposées.
  6. Procédé d'application de l'agent de traitement dans la teinture par colorant réactif et le fixage tinctorial d'une matière cellulosique (22), dans lequel la matière est préparée selon l'une au moins des revendications précédentes avant le fixage tinctorial effectué en continu dans un sécheur (32) à air pulsé, caractérisé en ce que la matière (22) provenant du traitement préparatoire (26) est saturée de matière tinctoriale réactive (28), sans avoir été lavée, et en ce que le colorant est fixé ultérieurement.
  7. Procédé selon la revendication 6, caractérisé en ce que les substances utilisées pour le traitement préparatoire sont sélectionnées de manière à être employées de façon répétée dans le fixage du colorant.
  8. Procédé selon la revendication 6 ou 7, caractérisé en ce que des substances chimiques ajoutées pour le traitement préparatoire, en particulier des combinaisons alcalines, qui sont encore présentes de façon active, c'est-à-dire non neutralisée, dans la matière cellulosique à la fin du processus de traitement préparatoire sont utilisées pour le mécanisme de réaction lors du fixage du colorant.
  9. Procédé selon l'une quelconque des revendications 5 à 8, caractérisé en ce que les substances et agents de traitement en excès dissous lors du traitement préparatoire de la matière (22) restent sur la matière lors du fixage du colorant réactif, et ne sont enlevés par lavage qu'à la fin du processus de fixage du colorant, dans la mesure où elles ne sont pas consommées lors du fixage du colorant.
EP99955683A 1998-09-19 1999-09-09 Procede de traitement prealable de coloration reactive de matieres cellulosiques Expired - Lifetime EP1112403B1 (fr)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
DE19843046 1998-09-19
DE19843046 1998-09-19
DE19843047 1998-09-19
DE19843047 1998-09-19
PCT/DE1999/002903 WO2000017437A1 (fr) 1998-09-19 1999-09-09 Procede de traitement prealable de coloration reactive de matieres cellulosiques

Publications (2)

Publication Number Publication Date
EP1112403A1 EP1112403A1 (fr) 2001-07-04
EP1112403B1 true EP1112403B1 (fr) 2005-12-28

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EP99955683A Expired - Lifetime EP1112403B1 (fr) 1998-09-19 1999-09-09 Procede de traitement prealable de coloration reactive de matieres cellulosiques

Country Status (5)

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US (1) US6582478B1 (fr)
EP (1) EP1112403B1 (fr)
AT (1) ATE314516T1 (fr)
DE (2) DE19942963A1 (fr)
WO (1) WO2000017437A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106521923A (zh) * 2016-11-22 2017-03-22 江苏联发纺织股份有限公司 一种tblc活化过氧化氢体系棉织物轧蒸漂白方法
WO2020254202A1 (fr) 2019-06-19 2020-12-24 A. Monforts Textilmaschinen Gmbh & Co. Kg Dispositif et procédé pour le traitement continu d'un produit plat

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10303328B4 (de) * 2003-01-28 2007-04-26 A. Monforts Textilmaschinen Gmbh & Co.Kg Verfahren zum kontinuierlichen enzymatischen Entschlichten
WO2011095944A1 (fr) * 2010-02-03 2011-08-11 Delta Galil Industries Ltd. Chaussette résistante à la lessive, et système et procédé de production d'une telle chaussette
CN106381679B (zh) * 2016-11-22 2019-02-01 江南大学 一种基于tblc活化过氧化氢体系的织物轧蒸漂白方法
CN109402921B (zh) * 2018-12-26 2021-08-03 诸暨信顺机电科技有限公司 一种布匹纺织用印染设备
CN110965240A (zh) * 2019-12-11 2020-04-07 福建福能南纺新材料有限公司 一种薄型干法革基布浅色品种一步法染色生产线及工艺

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2627517B1 (fr) * 1988-02-24 1990-10-12 Sandoz Sa Procede de blanchiment des matieres textiles avec destruction enzymatique de l'exces de peroxyde
DE3906769A1 (de) 1989-03-03 1990-09-06 Basf Ag Verfahren zum faerben von textilen materialien aus cellulosefasern im anschluss an eine peroxidbleiche
JP3165475B2 (ja) 1991-09-04 2001-05-14 化薬アクゾ株式会社 繊維の漂白染色法
FR2694310B1 (fr) 1992-07-29 1994-09-30 Protex Manuf Prod Chimiq Perfectionnement au procédé de teinture par des colorants réactifs avec blanchiment préalable.
DE59603066D1 (de) * 1995-10-16 1999-10-21 Monforts Textilmaschinen Gmbh Vorrichtung zum farbfixieren beim reaktivfärben

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106521923A (zh) * 2016-11-22 2017-03-22 江苏联发纺织股份有限公司 一种tblc活化过氧化氢体系棉织物轧蒸漂白方法
WO2020254202A1 (fr) 2019-06-19 2020-12-24 A. Monforts Textilmaschinen Gmbh & Co. Kg Dispositif et procédé pour le traitement continu d'un produit plat

Also Published As

Publication number Publication date
DE19942963A1 (de) 2000-03-23
EP1112403A1 (fr) 2001-07-04
DE59912990D1 (de) 2006-02-02
US6582478B1 (en) 2003-06-24
ATE314516T1 (de) 2006-01-15
WO2000017437A1 (fr) 2000-03-30

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