EP0200131B1 - Procédé de teinture uniforme de fibres cellulosiques avec des colorants réactifs - Google Patents
Procédé de teinture uniforme de fibres cellulosiques avec des colorants réactifs Download PDFInfo
- Publication number
- EP0200131B1 EP0200131B1 EP86105469A EP86105469A EP0200131B1 EP 0200131 B1 EP0200131 B1 EP 0200131B1 EP 86105469 A EP86105469 A EP 86105469A EP 86105469 A EP86105469 A EP 86105469A EP 0200131 B1 EP0200131 B1 EP 0200131B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- alkali
- addition
- dye
- fixation
- dyeing
- 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
Links
Classifications
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P3/00—Special processes of dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form, classified according to the material treated
- D06P3/58—Material containing hydroxyl groups
- D06P3/60—Natural or regenerated cellulose
- D06P3/66—Natural or regenerated cellulose using reactive dyes
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
- D06P1/0004—General aspects of dyeing
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S8/00—Bleaching and dyeing; fluid treatment and chemical modification of textiles and fibers
- Y10S8/916—Natural fiber dyeing
- Y10S8/918—Cellulose textile
Definitions
- the dyeing of textile material from cellulose fibers by pulling out alkaline fixing reactive dyes from an aqueous medium is by far the largest and most important area of application for this class of dyes and, according to the previous procedures, usually takes place in the "all-in process” or in a “preliminary process” or in a “stage process", which differ from one another in terms of the type of process management. This takes into account the fact that there is a very high risk of irregularity if, in the case of a reactive dyeing of the dye and electrolyte-containing liquor at dyeing temperature, all of the alkali required for fixing is available at once, which results in a rapid increase in the fixing of the dye.
- the entire amount of dye, salt, alkali and, if appropriate, a textile auxiliary at low temperature (room temperature) is put into the pull-out bath in the usual "all-in process" fed dyeing machine loaded with textile goods; thereupon the batch prepared in this way is heated to the intended dyeing temperature and the measures introduced for coloring the goods are now brought to a end for a certain time under the set temperature conditions, the fixing taking place.
- fast-fixing dyes are often used to achieve insufficient levelness of coloration in the presence of otherwise difficult material and / or machine conditions.
- an isothermal dyeing process is known from ZA-A-84/1967 and is used in practice, according to which, at dyeing temperature, an aqueous dye bath containing the dye, electrolyte, optionally a textile auxiliary and the cellulosic textile material is used continuously to fix the Reactive dye required alkali is metered.
- the alkali is dosed automatically; it starts with a small amount of alkali per unit of time, and this addition of alkali is increasingly increased in the course of the metering process in accordance with a specific program.
- the progression of metering can be controlled between 0% (linear) and 100% (exponential or logarithmic) in 10% steps.
- the dosing time can be 30, 60 or 90 minutes.
- the procedure described above is carried out automatically with the aid of a computer-controlled metering device (e.g. from the prototype shown in ZA-A-84/1967), which is capable due to its design features, the alkali metering into the fleet immediately under fixing conditions according to the prescribed Control addition scheme.
- a computer-controlled metering device e.g. from the prototype shown in ZA-A-84/1967
- the addition of the fixing alkali to the alkali-free dye bath can be carried out at a constant temperature be made in the range of 30-100 ° C; but there is also the possibility that the temperature is increased or decreased during the actual metering process.
- the isothermal procedure is preferred, with a relatively low temperature (range around 30-50 ° C.) or a relatively high temperature (range around 60-100 ° C.) being selected, depending on the type of dye or substrate.
- the precautions according to the invention for the continuous or approximately continuous control of the addition mode based on the dimensioning of a parabolic function can also be understood in such a way that within the scope of the dosing process, the addition of a first rate corresponding to 1/15 to 1/400, preferably 1/15 to 1 / 73, the total amount of alkali required for dye fixation begins that the addition rate decreases in quantity after 20 minutes at the latest and then continues to increase in volume from then on in accordance with the expiration of the time required for the alkali addition of the pull-out phase finally reached the maximum value.
- the one for the special The guidelines to be applied for programming the amount of alkali to be added per unit of time depend on the type of reactive dye or its reactive anchor, the type of textile material and the type of dyeing equipment used (for stationary or moving goods).
- the characteristic of the dosing curve symbolized by a diagram (depending on progression and time) can have a relatively flat or relatively steep curve.
- the total metering process can generally be completed in a time between 10 and 120 minutes, preferably between 15 and 60 minutes, which makes up a substantial part of the total dyeing time.
- a step-by-step alkali metering is to be understood as a mode of operation in which the mode of addition for the alkali amounts over the entire metering period follows the course of a parabola, but in which the measures for metering take place in individual batches (e.g. analogous to the rhythm of a piston pump) or at that the rate of addition remains constant for a certain time (seconds or minutes) and then gradually changes to reduced or increased values.
- the alkali metering according to the invention can thus also proceed in such a way that certain constant units of quantity of the alkali are metered in at such a time cycle that the course of a parabola is observed over the entire metering period.
- the alkali to be used for dye fixation according to the process can be an alkali hydroxide, carbonate, bicarbonate, phosphate, metaphosphate, pyrophosphate, polyphosphate or another alkaline substance or also a mixture of various of these alkalis, in particular the corresponding sodium compounds.
- the needed amount and selection of such alkalis depends on the type of reactive dye used or its reactive anchor and corresponds to the recipes customary in dyeing practice.
- the process according to the invention leads to a surprisingly cheap, i.e. even course of dye fixation. This means that the dyeing process can be completed in a much shorter time than was possible according to the prior art and that one can still achieve excellent dye levelness.
- the organic dyes known under this generic term - regardless of the type of their fiber-reactive group - are considered as reactive dyes.
- This class of dyes is referred to in the Color Index, 3rd edition 1971 and additions in 1975 as "C.I. Reactive Dyes” and comprises chemical compounds with a dye character which are able to form a covalent bond with fibers containing OH groups. These are predominantly those dyes which contain at least one group which is reactive with polyhydroxyl fibers, a precursor therefor or a substituent which is reactive with the polyhydroxyl fiber.
- Particularly suitable as the base of the chromophoric system of these organic dyes are those from the series of the azo, anthraquinone and phthalocyanine compounds, it being possible for the azo and phthalocyanine dyes to be both metal-free and metal-containing.
- reactive groups and precursors which form such reactive groups include epoxy groups, the ethyleneimide group, the vinyl grouping in the vinylsulfone or acrylic acid residue, also the ⁇ -sulfatoethylsulfone group, the ⁇ -chloroethylsulfone group or the ⁇ -dialkylamino-ethylsulfone group.
- Derivatives of the tetrafluorocyclobutyl series, for example tetrafluorocyclobutyl acrylic acid, are also suitable for this process.
- the reactive substituents in reactive dyes are those that are easily removable and leave an electrophilic residue.
- halogen atoms on the following ring systems are of interest as substituents: quinoxaline, triazine, pyrimidine, phthalazine, pyridazine and pyridazone.
- Dyes with several identical or different types of reactive groups can also be used, as can combinations of dyes of the same or different types.
- Such reactive dyes of the type defined above often have more than one sulfonic acid group (apart from that in the reactive group of the dye) in the molecule, which can be distributed as desired over the chromophore, but are preferably bound to its aromatic radicals.
- Dyes of the vinyl sulfone type are preferably used for carrying out the claimed process, with which the fiber reacts via an addition mechanism via the vinyl sulfone form of the dye and which have either the vinyl sulfone residue itself or the ⁇ -sulfatoethyl sulfone group as reactive anchors.
- coloring substances are those dyes which, in addition to a reactive residue of the vinylsulfone type or precursor thereof, additionally have at least one group which reacts with the cellulose according to the substitution mechanism, e.g. a monochlorotriazinyl or monofluorotriazinyl group.
- cellulose fibers to be dyed according to the invention are cotton, mercerized or leached cotton, conventional regenerated cellulose fibers, (R) modal fibers and other vegetable fibers, such as flat to understand.
- the process according to the invention is suitable for mixtures of the abovementioned fibers with one another and with other fibers, such as, for example, polyester, polyamide, polyacrylonitrile fibers or silk.
- the dyeing itself can be in the various processing stages or presentation forms of the textile material, such as As a flake, as a sliver, as a yarn, as a fabric, as a knitted fabric or as a fleece. All machines or apparatuses customary for such dyeings in the exhaust process can be used to carry out the new process.
- a jet dyeing machine is loaded with 25 kg of cotton weave and with 250 l of water at 40 ° C. to carry out a dyeing process at a liquor ratio of 1:10.
- the fleet thus prepared is now 0.5 kg of a reactive dye of the formula dissolved in a little hot water, and 12.5 kg of Glauber's salt added and the product strand is then allowed to run for 5 minutes until these additives are evenly distributed, with the treatment liquid being circulated at the same time. Then, with further liquor circulation with the addition of a total of 527 cm3 conc.
- the temperature of the pull-out bath is kept constant at 40 ° C.
- the textile material is dyed to the end for a further 20 min at the set temperature and this dyeing is then completed as usual by rinsing, acidifying, soaping and rinsing again. You get a gray color with very good levelness.
- the textile material is then dyed for a further 15 minutes while the liquor cycle continues under the same temperature conditions and then finished as usual.
- a pink yarn dyeing is obtained which, after knitting, leads to completely level piece goods.
- a jet dyeing machine is fed with 300 kg of cotton jersey and a fleet of 2700 l of water for dyeing after the pull-out process. After heating to 30 ° C., this bath is initially 110 kg of a reactive dye of the formula which were previously dissolved in 100 l of hot water, added and distributed in the dyeing medium with rotation of the strand-guided textile material.
- the treated tricot fabric After 30 minutes of running the textile strand under the set conditions, the treated tricot fabric is finished as usual.
- the product image of the orange color obtained in this way is flawless and does not matter.
- a reel runner with liquor circulation is loaded with 100 kg of cotton lining material and filled with 2000 l of water.
- the liquor presented is now 3 kg of a reactive dye of the formula at room temperature and after 10 minutes of intermittent circulation, 140 kg of table salt were also added over the course of 30 minutes and in the form of 3 portions.
- the bath temperature is then raised to 80 ° C. within 30 minutes by heating. During this period, 52896 cm3 of an aqueous solution made from 10,000 g of soda and 10,000 cm3 of conc.
- the textile material is dyed for a further 30 minutes at the same temperature and then finished as usual.
- the yarn was wound from two dyed bobbins onto a fresh bobbin that the inner yarn layers of the first bobbin came to lie next to the outer yarn layers of the second bobbin. In this comparison, no nuance deviations could be determined, which proved a perfect level coloring.
- a jet dyeing machine 500 kg of a round-knit tubular fabric, consisting of a mixture of 35% polyester fiber and 65% cotton, are loaded and 3100 l of water are let into the dye container so charged. With the circulation pump running, 65 kg of table salt are then added to the liquor presented and this is then heated to 50 ° C., after which 1620 g of a reactive dye of the formula which have previously been dissolved in 50 l of hot water, are fed to the treatment bath via the preparation vessel. In this pulling-out liquor, an aqueous alkali batch of 119.4 l volume, consisting of 9750 g of soda, 165 cm 3 of conc., Is then left under constant circulation and at constant temperature conditions.
- the dyeing is completed as usual and then over-colored with commercially available disperse dyes.
- the nuance of the goods on the cotton component achieved in this way is immaterial.
- the coloring is complete after the dosing of the fixing alkali has been completed and is subjected to the aftertreatment as usual.
- the resulting blue-colored goods are perfectly level.
- a jet dyeing machine is loaded with 50 kg of cotton jersey. Then 430 l of water are poured into the dye container and 40 g of table salt are added; the temperature of the bath is 40 ° C. Then a mixture of 900 g of a reactive dye of the formula 600 g of the dye Reactive Orange 16 with the CI no. 17757 and 900 g of the dye Reactive Blue 19 with the CI no. 61200, which had previously been dissolved in 50 l of water, was added to the submitted liquor while the circulation was ongoing. To fix the dye, an alkaline fixing liquid is used outside the staining vessel. For this, 2 l conc.
- the dosing is done by means of an electropneumatically controlled air pressure pump.
- the connected processor controls the dosing process according to the selected curve.
- the pressure side of the metering pump is connected to the suction side of the liquor circulation pump.
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Coloring (AREA)
Claims (7)
- Procédé pour teindre, de façon unie ou uniforme, de la matière textile en des fils cellulosiques dans un milieu aqueux, à l'aide de colorants réactifs pouvant être fixés avec une matière alcaline, selon la technique de teinture par extraction et épuisement, procédé dans lequel la quantité de matière alcaline nécessaire pour la fixation du colorant est introduite progressivement de façon dosée, en un intervalle prédéterminé de temps pendant la phase d'extraction et d'épuisement du bain selon un mode d'addition de quantité prédéterminée par unité de temps que l'on ajoute au bain de teinture contenant la matière à teindre, au moins un tel colorant ainsi qu'éventuellement tous les autres additifs, mais ne contenant encore pas de substance alcaline de fixation, procédé caractérisé en ce que l'addition de la substance alcaline a lieu selon une fonction parabolique, et l'on commence l'addition en continu ou par étapes, d'au moins 1/400 ème de la quantité totale de la substance alcaline , puis l'on diminue progressivement le débit d'addition de ces quantités de la matière alcaline et l'on tend vers une valeur minimale voisine de 0 ou égale à 0 puis finalement, par l'introduction en continu ou par étapes de quantités supplémentaires qui augmentent par unité de temps dans le liquide du bain, on augmente à nouveau le débit d'addition jusqu'à avoir ajouté ,pendant la phase d'extraction et d'épuisement du bain, la quantité de matière alcaline nécessaire au total pour la fixation des colorants réactifs en cause.
- Procédé selon la revendication 1, caractérisé en ce que, dans le cadre de l'addition dosée de la substance alcaline, on commence à effectuer l'addition à un premier débit représentant 1/15ème à 1/400ème, avantageusement 1/15ème à 1/73ème, de la quantité totale de la matière alcaline nécessaire pour fixer le colorant, puis le débit d'addition diminue et après 20 minutes au maximum, on atteint la valeur minimale, et, à partir de là, on continue encore à ajouter des quantités croissantes et, en correspondance avec l'écoulement du temps prévu pour la phase d'extraction du bain, l'addition de la substance alcaline atteint finalement sa valeur maximale.
- Procédé selon l'une au moins des revendications 1 et 2, caractérisé en ce que le débit d'addition des quantités de la matière alcaline demeure constant pendant une certaine fraction de la durée de la phase d'extraction et d'épuisement prévue pour l'addition dosée de la matière alcaline, puis l'on passe par étapes à l'addition de quantité réduite ou de valeurs élevées par unité de temps.
- Procédé selon l'une au moins des revendications 1 à 3, caractérisé en ce que l'addition dosée de la matière alcaline a lieu automatiquement avec une commande selon un programme.
- Procédé selon l'une au moins des revendications 1 à 4, caractérise en ce que l'addition dosée de la matière alcaline a lieu à température constante.
- Procédé selon l'une au moins des revendications 1 à 5, caractérisé en ce qu'il s'agit pour les colorants réactifs que l'on utilise, de ceux comportant comme groupe réactif d'ancrage un groupe de type β-sulfatoéthylsulfone ou de type vinylsulfone.
- Procédé selon l'une au moins des revendications 1 à 6, caractérisé en ce que la matière textile comportant des fibres cellulosiques est présente sous forme d'un mélange de ces fibres cellulosiques avec des fibres de polyester, de polyacrylonitrile, de polyamide ou de la soie.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT86105469T ATE76453T1 (de) | 1985-04-29 | 1986-04-21 | Verfahren zum egalen faerben von cellulosefasern mit reaktivfarbstoffen. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19853515407 DE3515407A1 (de) | 1985-04-29 | 1985-04-29 | Verfahren zum egalen faerben von zellulosefasern mit reaktivfarbstoffen |
DE3515407 | 1985-04-29 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0200131A2 EP0200131A2 (fr) | 1986-11-05 |
EP0200131A3 EP0200131A3 (en) | 1989-01-04 |
EP0200131B1 true EP0200131B1 (fr) | 1992-05-20 |
Family
ID=6269389
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP86105469A Expired - Lifetime EP0200131B1 (fr) | 1985-04-29 | 1986-04-21 | Procédé de teinture uniforme de fibres cellulosiques avec des colorants réactifs |
Country Status (5)
Country | Link |
---|---|
US (1) | US5167668A (fr) |
EP (1) | EP0200131B1 (fr) |
JP (1) | JPS61252379A (fr) |
AT (1) | ATE76453T1 (fr) |
DE (2) | DE3515407A1 (fr) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3515406A1 (de) * | 1985-04-29 | 1986-10-30 | Adcon AB, Borås | Verfahren zum egalen faerben von zellulosefasermaterialien mit reaktivfarbstoffen |
JPH0745635B2 (ja) * | 1987-03-26 | 1995-05-17 | 住友化学工業株式会社 | 反応染料の液状水性組成物 |
JPH01118681A (ja) * | 1987-10-27 | 1989-05-11 | Hisaka Works Ltd | セルロース系繊維製品の染色方法 |
JPH01118680A (ja) * | 1987-10-27 | 1989-05-11 | Hisaka Works Ltd | セルロース系繊維製品の染色方法およびそれに用いる装置 |
EP0470932A1 (fr) * | 1990-08-08 | 1992-02-12 | Ciba-Geigy Ag | Procédé de teintures de matériaux fibreux contenant de la cellulose avec des colorants de cuve |
US5314504A (en) * | 1990-11-15 | 1994-05-24 | E. I. Du Pont De Nemours And Company | Process for the application of dye fixing agents to polyamide fiber utilizing controlled fixing agent addition |
CA2220909C (fr) * | 1995-06-06 | 2001-02-27 | Valleylab, Inc. | Generation numerique de formes d'ondes pour generateur electrochirurgical |
US5846265A (en) * | 1996-07-26 | 1998-12-08 | North Carolina State University | Closed-loop textile dyeing process utilizing real-time metered dosing of dyes and chemicals |
US5840084A (en) * | 1996-11-22 | 1998-11-24 | Sybron Chemicals, Inc. | Dye bath and method for reactive dyeing |
DE19719610A1 (de) * | 1997-05-09 | 1998-11-12 | Dystar Textilfarben Gmbh & Co | Alkalisystem zum Färben von cellulosischen Textilien nach Klotzmethoden |
US6193764B1 (en) * | 1999-04-20 | 2001-02-27 | Farid A. Atala | Water, energy, and time efficient reactive rapid dyeing system |
US20030105753A1 (en) * | 2001-11-27 | 2003-06-05 | Judson Lee | Expert system for dyeing cotton fabrics with reactive dyes |
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 |
EP2262945B1 (fr) * | 2008-03-28 | 2013-03-13 | Clariant Finance (BVI) Limited | Action sur la réflectance des matériaux textiles colorés dans l'infrarouge proche |
WO2013189816A1 (fr) | 2012-06-18 | 2013-12-27 | Dystar Colours Distribution Gmbh | Colorants réactifs et leurs complexes métalliques, leur procédé de production et leur utilisation |
CN103382663B (zh) * | 2013-06-20 | 2015-07-15 | 东台市苏萌针织时装有限公司 | 蚕丝股线筒纱高压浸染工艺 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3117957A (en) * | 1958-12-19 | 1964-01-14 | Du Pont | Reactive polymeric dyes containing triazine |
GB1349755A (en) * | 1970-12-02 | 1974-04-10 | Ici Ltd | Dyeing process |
CH533073A4 (fr) * | 1973-04-13 | 1975-10-31 | ||
DE2914111C2 (de) * | 1979-04-07 | 1987-03-12 | Bayer Ag, 5090 Leverkusen | Verfahren zum Färben von Cellulosematerialien mit Reaktivfarbstoffen nach dem Ausziehverfahren |
SE441683B (sv) * | 1983-03-18 | 1985-10-28 | Adcon Ab | Forfarande vid fergbehandling av textila material samt anvendning av en anordning for genomforande av forfarandet |
FR2552789B1 (fr) * | 1983-10-01 | 1986-12-19 | Sandoz Sa | Procede de teinture par epuisement de fibres textiles |
FR2565266B1 (fr) * | 1984-06-01 | 1987-01-02 | Sandoz Sa | Procede de teinture par epuisement de fibres cellulosiques avec des colorants reactifs |
DE3515406A1 (de) * | 1985-04-29 | 1986-10-30 | Adcon AB, Borås | Verfahren zum egalen faerben von zellulosefasermaterialien mit reaktivfarbstoffen |
-
1985
- 1985-04-29 DE DE19853515407 patent/DE3515407A1/de not_active Withdrawn
-
1986
- 1986-04-21 DE DE8686105469T patent/DE3685365D1/de not_active Expired - Fee Related
- 1986-04-21 EP EP86105469A patent/EP0200131B1/fr not_active Expired - Lifetime
- 1986-04-21 AT AT86105469T patent/ATE76453T1/de not_active IP Right Cessation
- 1986-04-28 JP JP61097062A patent/JPS61252379A/ja active Pending
-
1990
- 1990-11-26 US US07/617,944 patent/US5167668A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
DE3685365D1 (de) | 1992-06-25 |
DE3515407A1 (de) | 1986-10-30 |
ATE76453T1 (de) | 1992-06-15 |
JPS61252379A (ja) | 1986-11-10 |
US5167668A (en) | 1992-12-01 |
EP0200131A2 (fr) | 1986-11-05 |
EP0200131A3 (en) | 1989-01-04 |
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