EP1266070B1 - Mediatorsysteme auf basis gemischter metallkomplexe zur reduktion von farbstoffen - Google Patents

Mediatorsysteme auf basis gemischter metallkomplexe zur reduktion von farbstoffen Download PDF

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Publication number
EP1266070B1
EP1266070B1 EP01911710A EP01911710A EP1266070B1 EP 1266070 B1 EP1266070 B1 EP 1266070B1 EP 01911710 A EP01911710 A EP 01911710A EP 01911710 A EP01911710 A EP 01911710A EP 1266070 B1 EP1266070 B1 EP 1266070B1
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EP
European Patent Office
Prior art keywords
mediator
complexing agent
dyes
iron
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
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EP01911710A
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German (de)
English (en)
French (fr)
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EP1266070A1 (de
Inventor
Thomas Bechtold
Stefan Mohr
Norbert Grund
Wolfgang Schrott
Wolfgang Hiebsch
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Dystar Textilfarben GmbH and Co Deutschland KG
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Dystar Textilfarben GmbH and Co Deutschland KG
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Classifications

    • 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
    • D06P1/00General 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
    • D06P1/44General 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 using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/673Inorganic compounds
    • D06P1/67333Salts or hydroxides
    • D06P1/6735Salts or hydroxides of alkaline or alkaline-earth metals with anions different from those provided for in D06P1/67341
    • 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
    • D06P1/00General 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
    • D06P1/22General 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 using vat dyestuffs including indigo
    • D06P1/221Reducing systems; Reducing catalysts
    • 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
    • D06P1/00General 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
    • D06P1/22General 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 using vat dyestuffs including indigo
    • D06P1/228Indigo
    • 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
    • D06P1/00General 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
    • D06P1/30General 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 using sulfur 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
    • D06P1/00General 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
    • D06P1/44General 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 using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/64General 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 using insoluble pigments or auxiliary substances, e.g. binders using compositions containing low-molecular-weight organic compounds without sulfate or sulfonate groups
    • D06P1/642Compounds containing nitrogen
    • D06P1/645Aliphatic, araliphatic or cycloaliphatic compounds containing amino groups
    • 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
    • D06P1/00General 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
    • D06P1/44General 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 using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/64General 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 using insoluble pigments or auxiliary substances, e.g. binders using compositions containing low-molecular-weight organic compounds without sulfate or sulfonate groups
    • D06P1/651Compounds without nitrogen
    • D06P1/65106Oxygen-containing compounds
    • D06P1/65118Compounds containing hydroxyl groups
    • 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
    • D06P1/00General 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
    • D06P1/44General 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 using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/673Inorganic compounds
    • D06P1/67333Salts or hydroxides
    • D06P1/67341Salts or hydroxides of elements different from the alkaline or alkaline-earth metals or with anions containing those elements
    • 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
    • D06P5/20Physical treatments affecting dyeing, e.g. ultrasonic or electric
    • D06P5/2016Application of electric energy
    • 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
    • Y10S8/916Natural fiber dyeing
    • Y10S8/918Cellulose textile

Definitions

  • the present invention relates to mediator systems obtainable by mixing one or more salts of a metal which can form a plurality of valence states, with at least one amino group-containing complexing agent (K1) and at least one hydroxyl-containing, but not containing amino groups complexing agent (K2) in an alkaline aqueous medium
  • Complexing agents may be present as salts and the molar ratio of K1 to metal ion is 0.1: 1 to 10: 1 and the molar ratio of K2 to metal ion is 0.1: 1 to 5: 1.
  • the invention relates to a process for the reduction of dyes and a process for dyeing cellulosic textile material using these Mediatorsysteme.
  • Vat dyes and sulfur dyes are important classes of textile dyes.
  • Vat dyes are of great importance for the dyeing of cellulose fibers, in particular because of the high fastnesses of the dyeings.
  • the insoluble oxidized dye When using these dyes, the insoluble oxidized dye must be converted to its alkali-soluble leuco form by a reduction step. This reduced form shows high affinity for the cellulose fiber, absorbs it and is converted to its insoluble form by an oxidation step on the fiber.
  • the class of sulfur dyes is of particular importance for the production of lower cost dyes with average fastness requirements.
  • the implementation of a reduction and oxidation step is also required in order to fix the dye on the goods can.
  • a common feature of these reducing agents is the lack of a suitable way to regenerate their reducing action, so that these chemicals are released into the wastewater after use with the dyebath. In addition to the costs of the fresh chemicals to be used also creates additional effort in the treatment of wastewater.
  • Iron (II) complexes with triethanolamine (WO 90/15182 . WO 94/23114 ), with bicin (N, N-bis (2-hydroxyethyl) glycine) ( WO-A-95/07374 ), with triisopropanolamine ( WO-A-96/32445 ) and with aliphatic hydroxy compounds which may contain a plurality of hydroxyl groups and may additionally be functionalized by aldehyde, keto or carboxyl groups, such as di- and polyalcohols, di- and Polyhydroxyaldehyden, di- and polyhydroxyketones, di- and polysaccharides, di- and Polyhydroxymono and dicarboxylic acids and hydroxytricarboxylic acids, wherein the compounds derived from sugars, in particular the acids and their salts, for example gluconic and heptagluconic acid, and citric acid are emphasized as
  • iron (II) complexes have a reduction effect sufficient for dye reduction, which is described by the (negative) redox potential which can be measured at a specific molar ratio of iron (II): iron (III) in alkaline solution.
  • Many of these iron (II) complexes e.g. the complexes with triethanolamine, bicine, gluconic acid and heptagluconic acid, moreover, have the advantage of being capable of being electrochemically regenerated and thus of being used as mediators in the electrochemical reduction of dyes and in electrochemical dyeing processes.
  • iron complexes with gluconate or heptagluconate have very good complex stability in the pH range of 10 to 12, the cathodic current densities achievable with these complexes leave something to be desired, so that correspondingly larger electrolysis cells must be used and / or the concentration of iron complex is increased what is detrimental to the user in terms of energy requirements, chemical consumption, costs and wastewater pollution.
  • the invention therefore an object of the invention to remedy the disadvantages mentioned and to enable the reduction of dyes in an advantageous, economical manner.
  • mediators which are characterized in that the above-defined Mediator systems uses.
  • the mediator systems according to the invention that a combination of the metal ion with the complexing agents K1 and K2 is present, in which the molar ratio K1 to metal ion is 0.1: 1 to 10: 1, preferably 0.5: 1 to 6: 1, and Molar ratio K2 to metal ion is 0.1: 1 to 5: 1, preferably 0.5: 1 to 3: 1.
  • the mediator systems according to the invention are obtainable by mixing the individual components, which can be used in the form of their water-soluble salts, in an alkaline aqueous medium.
  • the metal ion is complexed, wherein, depending on the present pH, which is generally about 10 to 14, the most favorable complex preferably forms.
  • the metal ion M1 can be used in both lower and higher valued form.
  • iron (II) - and iron (III) salts can be used in the particularly preferred metal iron, which are first reduced electrochemically without problems to iron (II).
  • aliphatic amines having at least two coordinating groups which contain at least one hydroxyl group are soluble in water or aqueous / organic media or can be mixed with water or the aqueous / organic media are suitable as complexing agents K1 containing amino groups.
  • the complexing agents K1 may additionally contain carboxyl groups.
  • Preferred complexing agents K1 are e.g. Alcohol amines, in particular mono-, di- and Trialkohol- (especially alkanol) amines, such as triethanolamine and triisopropanolamine, and mono-, di- and Polyhydroxyaminocarbon Acid such as N, N-bis (2-hydroxyethyl) glycine.
  • Particularly preferred complexing agents K1 are triisopropanolamine and especially triethanolamine.
  • mixtures of complexing agents K1 can be used.
  • Particularly preferred complexing agents K2 are citric acid and especially the monocarboxylic acids derived from sugars, especially gluconic acid and heptagluconic acid, and their salts, esters and lactones.
  • mixtures of complexing agents K2 can be used.
  • a particularly suitable example of this is a mixture of gluconic acid and heptagluconic acid, preferably in a molar ratio of 0.1: 1 to 10: 1, which gives particularly stable iron complexes even at relatively high temperatures.
  • mediator systems according to the invention contain iron (II / III) ions as the metal ion, and triethanolamine as complexing agent K1 and as complexing agent K2 gluconic acid and / or heptagluconic acid.
  • the particular advantages of the mediator according to the invention are that an electrochemical dye reduction at low concentration of low-valent metal ion and thus low concentration of active complex can be carried out at high cathodic current density and at the same time there is a complex system, even at lower pH values, in the Rule ⁇ 10, is stable. Unexpectedly, the achievable current densities and complex stabilities clearly exceed those expected for a mixture of the two individual systems (metal ion / K1 and metal ion / K2).
  • the mediator systems according to the invention are outstandingly suitable for the electrochemical reduction of dyes.
  • vat dyes examples include indigo and its bromo derivatives, 5,5'-dibromoindigo and 5,5 ', 7,7'-tetrabromoindigo, and thioindigo, acylaminoanthraquinones, anthraquinonazoles, anthrimides, anthrimidecarbazoles, phthaloylacridones, benzanthrones and indanthrones, and pyrenchinones, anthanthrones, Pyranthrones, Acedianthrone and perylene derivatives.
  • particularly important sulfur dyes are CI Sulfur Black 1 and CI Leuco Sulfur Black 1 and sulfur vat dyes such as CI Vat Blue 43.
  • the maximum amount used is usually approximately the amount of mediator required stoichiometrically for the dye reduction.
  • 2 mol of a mediator system according to the invention are generally calculated, based on the redox-active, an electron-supplying metal ion.
  • this mediator amount can be lowered by the electrochemical regeneration of the mediator (when dyeing with vat dyes, based on a liter of dyebath, usually up to about 0.1 to 1 mol reduced mediator per mole of dye). The greater the deficit in the mediator system, the higher the demands on the electrolysis cell.
  • the reduction process according to the invention can advantageously be part of the likewise inventive process for dyeing cellulose-containing textile material with vat and sulfur dyes.
  • the dye is added to the dyebath in prereduced form, e.g. an alkaline solution catalytically reduced indigo, and reduces the reoxidized during dyeing by air contact portion of the dye electrochemically using the mediator according to the invention.
  • the dyeing itself can be carried out as described in the literature mentioned above. In this case, by all known continuous and discontinuous dyeing methods, e.g. after the exhaust process and the padder process.
  • the further process conditions such as type of textile auxiliaries, amounts used, dyeing conditions, type of electrolysis cell, completion of the dyeings, can be selected as usual and described in the literature mentioned above.
  • all cellulose-containing textile materials can be dyed advantageously.
  • examples include: fibers of cotton, regenerated cellulose such as viscose and modal, and bast fibers such as flax, hemp and jute.
  • Forms of presentation include eg flake, ribbon, yarn, twine, woven, knitted, knitted and made-up pieces.
  • Mechanical forms can be packing systems, yarn skein, spool, warp beam and cloth beam as well as piece goods in strand and wide.
  • the electrolysis cell was a multi-cathode cell (10 electrodes, 0.18 m 2 viewing area, total area 4.3 m 2 ).
  • the anolyte used was 2% strength by weight sodium hydroxide solution (corresponding to the amount of charge flowed, 50% strength by weight sodium hydroxide solution was added in order to keep the cell voltage constant).
  • the separation of catholyte (dyebath) and anolyte was carried out by a cation exchange membrane.
  • the cathode used was a stainless steel mesh and the anode used was a platinum mixed oxide coated titanium electrode.
  • Dyeing was done as follows: 180 l of a dyebath of the composition 0.015 mol / l Iron (III) chloride (40% strength by weight aqueous solution, 4.3 ml / l) 0.068 mol / l Triethanolamine (85% strength by weight aqueous solution, 12 g / l) 0.005 mol / l Sodium gluconate (99%, 1 g / l) 0.37 mol / l Sodium hydroxide solution (50% strength by weight aqueous solution, 14.8 g / l) 1 g / l a commercial wetting agent 1.2 g / l a commercial dispersant 0.7 g / l a commercial water correction agent circulated through the yarn packages (30 l / kg min) and the electrolysis cell (100 l / min) and were reduced prior to dyeing.
  • the oxygen was first removed from the dyebath. After reaching a potential of -650 mV, the cell current was lowered to about 2 A in order to keep the dyebath potential below the leuco potential of the dye.
  • the dye was added. After a pigmentation time of 10 minutes at a redox potential of about -700 to -750 mV, the cell current was increased to 9 A in order to uniformly convert the dye into its reduced form by indirect electrolysis. The redox potential rose within 30 min to -920 mV and was then stabilized by regulating the cell current to a value between -930 and -940 mV. Under these conditions an additional 30 min was dyed. Meanwhile, the iron (II) was complex continuously regenerated electrochemically.
  • the dyeing result corresponded in color, color depth and levelness to the result obtained under the same conditions with a conventional reducing agent.
  • Dyeing was done as follows: 180 l of a dyebath of the composition 0.040 mol / l Iron (III) chloride (40% strength by weight aqueous solution, 11.5 ml / l) 0.068 mol / l Triethanolamine (85% strength by weight aqueous solution, 12 g / l) 0.031 mol / l Sodium gluconate (99%, 6.8 g / l) 0.5 mol / l Sodium hydroxide solution (50% strength by weight aqueous solution, 20 g / l) 1 g / l a commercial Egalisierangesmittels 1 g / l a commercial wetting agent 1 g / l a commercial dispersant 0.5 g / l a commercial water correction agent circulated through the yarn packages (30 l / kg min) and the electrolysis cell (100 l / min) and were reduced prior to dyeing.
  • the oxygen was first removed from the dyebath. After reaching At a potential of -700 mV, the cell current was lowered to about 1 A to keep the dyeing bath potential below the leuco potential of the dye.
  • the dye was added. After a pigmentation time of 30 minutes at a redox potential of about -765 to -780 mV, the cell current was increased to 30 A in order to uniformly convert the dye into its reduced form by indirect electrolysis. The redox potential rose within 20 min to -920 mV and was then stabilized by controlling the cell current to a value between - 930 and -940 mV. Under these conditions an additional 40 minutes was dyed. Meanwhile, the iron (II) was complex continuously regenerated electrochemically.
  • the dyeing result corresponded in color, color depth and levelness to the result obtained under the same conditions with a conventional reducing agent.
  • Dyeing was done as follows: 180 l of a dyebath of the composition 0.024 mol / l Iron (III) chloride (40% strength by weight aqueous solution, 6.8 ml / l) 0.051 mol / l Triethanolamine (85% strength by weight aqueous solution, 9 g / l) 0.017 mol / l Sodium gluconate (99%, 3.7 g / l) 0.34 mol / l Sodium hydroxide solution (50% strength by weight aqueous solution, 13.7 g / l) 1 g / l a commercial Egalisierangesmittels 1 g / l a commercial wetting agent 1 g / l a commercial dispersant 0.5 g / l a commercial water correction agent circulated through the bobbins (30 l / kg min) and the electrolysis cell (100 l / min) and were reduced before dyeing.
  • the oxygen was first removed from the dyebath. After reaching a potential of -670 mV, the cell current was lowered to about 1 A in order to keep the dyebath potential below the leuco potential of the dyes.
  • the dye mixture was added. After a pigmentation time of 30 min at a redox potential of about -765 to -780 mV, the cell current was increased to 40 A in order to uniformly convert the dye into its reduced form by indirect electrolysis. The redox potential rose within 60 min to -920 mV and was increased while keeping the cell current within 40 min to -950. Meanwhile, the iron (II) was complex continuously regenerated electrochemically.
  • the dyeing result corresponded in color, color depth and levelness to the result obtained under the same conditions with a conventional reducing agent.
  • Dyeing was done as follows: 180 l of a dyebath of the composition 0.010 mol / l Iron (III) chloride (40% strength by weight aqueous solution, 2.8 ml / l) 0.068 mol / l Triethanolamine (85% strength by weight aqueous solution, 12 g / l) 0.005 mol / l Sodium gluconate (99%, 1 g / l) 0.37 mol / l Sodium hydroxide solution (50% strength by weight aqueous solution, 14.8 g / l) 0.25 g / l a commercial dispersant circulated through the bobbins (30 l / kg min) and the electrolysis cell (100 l / min) and were reduced before dyeing.
  • the oxygen was first removed from the dyebath. After reaching a dyeing bath temperature of 60 ° C and a potential of -910 mV, the dye was added within 10 min. The redox potential was kept between -910 and -920 mV. After complete dye addition, the redox potential was stabilized by controlling the cell current between -920 and -940 mV. Under these conditions an additional 35 minutes was stained. Meanwhile, the iron (II) was complex continuously regenerated electrochemically.
  • the dyeing result corresponded in color, color depth and levelness to the result obtained under the same conditions with a conventional reducing agent.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Coloring (AREA)
  • Detergent Compositions (AREA)
EP01911710A 2000-03-02 2001-03-01 Mediatorsysteme auf basis gemischter metallkomplexe zur reduktion von farbstoffen Expired - Lifetime EP1266070B1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10010059 2000-03-02
DE10010059A DE10010059A1 (de) 2000-03-02 2000-03-02 Mediatorsysteme auf Basis gemischter Metallkomplexe zur Reduktion von Farbstoffen
PCT/EP2001/002308 WO2001065000A1 (de) 2000-03-02 2001-03-01 Mediatorsysteme auf basis gemischter metallkomplexe zur reduktion von farbstoffen

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Publication Number Publication Date
EP1266070A1 EP1266070A1 (de) 2002-12-18
EP1266070B1 true EP1266070B1 (de) 2008-12-03

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EP01911710A Expired - Lifetime EP1266070B1 (de) 2000-03-02 2001-03-01 Mediatorsysteme auf basis gemischter metallkomplexe zur reduktion von farbstoffen

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US (1) US6814763B2 (ko)
EP (1) EP1266070B1 (ko)
JP (1) JP2003525363A (ko)
KR (1) KR100683310B1 (ko)
CN (1) CN1289748C (ko)
AT (1) ATE416270T1 (ko)
BR (1) BR0108831A (ko)
DE (2) DE10010059A1 (ko)
ES (1) ES2317891T3 (ko)
HK (1) HK1053157B (ko)
MX (1) MXPA02008539A (ko)
WO (1) WO2001065000A1 (ko)

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DE10161265A1 (de) * 2001-12-13 2003-06-26 Dystar Textilfarben Gmbh & Co Verfahren zur Farbveränderung von gefärbten textilen Substraten
DE10234825A1 (de) * 2002-07-31 2004-02-19 Dystar Textilfarben Gmbh & Co. Deutschland Kg Verfahren zum Färben mit Schwefel- und Schwefelküpenfarbstoffen
US20050209602A1 (en) * 2004-03-22 2005-09-22 Disc Dynamics, Inc. Multi-stage biomaterial injection system for spinal implants
US20060265076A1 (en) * 2005-05-03 2006-11-23 Disc Dynamics, Inc. Catheter holder for spinal implant
CN102808339B (zh) * 2012-07-20 2014-05-14 濮阳宏业汇龙化工有限公司 一种激发态高效还原剂

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Publication number Priority date Publication date Assignee Title
AT398316B (de) 1989-06-01 1994-11-25 Verein Zur Foerderung Der Fors Verfahren zur reduktion von farbstoffen
WO1992009740A1 (de) 1990-12-03 1992-06-11 Verein Zur Förderung Der Forschung Und Entwicklung In Der Textilwirtschaft Verfahren zur reduktion von textilfarbstoffen
DE4206929A1 (de) 1992-03-05 1993-09-09 Basf Ag Verfahren zum faerben oder bedrucken von cellulosehaltigem textilmaterial mit kuepenfarbstoffen
DE4230870A1 (de) * 1992-09-16 1994-03-17 Basf Ag Verfahren zum Färben und Bedrucken von textilen Materialien aus Cellulosefasern
TW251325B (ko) * 1993-03-30 1995-07-11 Basf Ag
DE4320867A1 (de) * 1993-06-24 1995-01-05 Basf Ag Verfahren zum Färben von cellulosehaltigen Textilmaterialien mit Küpenfarbstoffen oder Schwefelfarbstoffen
DE4320866A1 (de) 1993-06-24 1995-01-05 Basf Ag Verfahren zum Färben oder Bedrucken von cellulosehaltigen Textilmaterialien mit Küpenfarbstoffen oder Schwefelfarbstoffen
AT402946B (de) 1993-09-08 1997-09-25 Verein Zur Foerderung Der Fors Elektrolysezelle
DE19513839A1 (de) 1995-04-12 1996-10-17 Basf Ag Verfahren zur elektrochemischen Reduktion von Küpenfarbstoffen
DE19919746A1 (de) * 1999-04-29 2000-11-02 Basf Ag Verfahren zur Herstellung von wäßrig-alkalischen Lösungen reduzierter indigoider Farbstoffe

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ATE416270T1 (de) 2008-12-15
MXPA02008539A (es) 2002-12-13
CN1289748C (zh) 2006-12-13
CN1406299A (zh) 2003-03-26
US20030121112A1 (en) 2003-07-03
DE10010059A1 (de) 2001-09-06
ES2317891T3 (es) 2009-05-01
DE50114544D1 (de) 2009-01-15
HK1053157B (zh) 2007-06-29
WO2001065000A1 (de) 2001-09-07
JP2003525363A (ja) 2003-08-26
HK1053157A1 (en) 2003-10-10
EP1266070A1 (de) 2002-12-18
BR0108831A (pt) 2002-12-10
US6814763B2 (en) 2004-11-09
KR20020086596A (ko) 2002-11-18
KR100683310B1 (ko) 2007-02-15

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