EP1725708A2 - Method for optical brightening of synthetic fibres or of synthetic fibres mixed with natural fibres - Google Patents
Method for optical brightening of synthetic fibres or of synthetic fibres mixed with natural fibresInfo
- Publication number
- EP1725708A2 EP1725708A2 EP05715882A EP05715882A EP1725708A2 EP 1725708 A2 EP1725708 A2 EP 1725708A2 EP 05715882 A EP05715882 A EP 05715882A EP 05715882 A EP05715882 A EP 05715882A EP 1725708 A2 EP1725708 A2 EP 1725708A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- carbon atoms
- weight
- radical
- aliphatic
- synthetic fibers
- 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.)
- Granted
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
- D06P3/34—Material containing ester groups
- D06P3/52—Polyesters
- D06P3/54—Polyesters using dispersed dyestuffs
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06L—DRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
- D06L4/00—Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs
- D06L4/60—Optical bleaching or brightening
- D06L4/664—Preparations of optical brighteners; Optical brighteners in aerosol form; Physical treatment of optical brighteners
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06L—DRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
- D06L4/00—Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs
- D06L4/60—Optical bleaching or brightening
- D06L4/671—Optical brightening assistants, e.g. enhancers or boosters
Definitions
- the present invention relates to a process for the optical brightening of synthetic fibers or of synthetic fibers in a mixture with natural fibers, the synthetic fibers or mixtures of the synthetic fibers with natural fibers being treated in a treatment bath containing optical brighteners to which a microemulsion has been added ,
- optical brighteners are known for their ability to give textiles or plastics a white color.
- EP 0023 026 discloses compounds of the general formula I.
- radicals R 1 and R 2 can be, for example, H, F, Cl, phenyl, CF 3 , alkyl or numerous other radicals, and where V is selected from
- a disadvantage of using compounds of general formula I as optical brighteners is that their low temperature yield is limited, i.e. you need a lot of product to achieve the desired brightening effect.
- EP-A 0 023 027 and EP-B2 0 032 917 disclose the use of mixtures of two or more dicyanostyrylbenzene compounds for the optical brightening of polyesters.
- DE 102 19 993 AI relates to a process for lightening textile materials, in which compounds of the general formula I, a dicyanostyrylbenzene compound and one
- the optical brightening of textile materials is generally carried out by the pull-out or thermosol process.
- the textile material to be lightened is usually padded with an aqueous liquor which contains the optically lightening substances, optionally a blue or violet shading dye or mixtures thereof and optionally additives (see above).
- the liquor intake is generally 30 to 100%.
- the textile material is then dried and fixed at a temperature of 150 to 200 ° C for 5 to 60 seconds.
- thermosol process A disadvantage of the thermosol process is that the fixing temperature of 150 to 210 ° C, in particular of 170 to 190 ° C, requires a high level of energy. At these high fixing temperatures, additives or any contaminants adhering to the textile material from previous treatment steps smoke and lead to gaseous emissions. Despite the high temperatures, only a ring brightening is achieved in the thermosol process, which is inferior to that of a pull-out coloring in terms of whiteness. In the case of mixtures of the chemical fibers with natural fibers or with synthetic cellulose fibers, the natural fiber or synthetic cellulose fiber may brown.
- Another known process is the exhaust process, in which the aqueous liquor is usually used at temperatures of 90 to 135 ° C.
- the textile material to be lightened is usually brought into an aqueous liquor at a temperature of 10 to 50 ° C, which contains the optically brightening Bonds, optionally a blue or violet shading dye or a mixture thereof and optionally additives, for example dispersants, carboxylic acids or bases, and the pH value of which is usually 3 to 12, preferably 3 to 8.
- the liquor ratio (weight ratio of textile material: liquor) is 1: 1.5 to 1:40, preferably 1: 5 to 1:20.
- the bath is then heated to a temperature of 95 to 135 ° C. within 15 to 60 minutes and held at this temperature for 15 to 60 minutes.
- the lightened textile material is then rinsed and dried.
- the HT process high temperature process is usually used. If the color transition temperature of the polyester is exceeded sufficiently, the lightening process must be carried out by 130 ° C in order to achieve a lightening effect which is sufficient in practice. Since the lightening takes place in the aqueous medium, an autoclave, a high-pressure apparatus or a high-pressure machine must be used. Disadvantages include that such a unit is more expensive than an open unit, that the heating and cooling time and thus the machine occupancy is long and that the amount of energy required, especially for heating to 130 ° C, is very high.
- Carriers are often formulations based on emulsifiers, sometimes solvents and the active component.
- Active components are compounds based on liquid, halogenated benzene derivatives, alkyl aromatic compounds, aromatic hydroxy compounds, aromatic alcohols, ketones, carboxylic acids and their esters, alkyl phthalimides or substituted phenyl glycols and their esters.
- the most important active components are 1,2-dichlorobenzene, 1,2,4-trichlorobenzene, 2-phenylphenol, diphenyl, diphenyl ether, methyl, butyl or benzyl benzoates, methyl salicylates, dimethyl phthalates, phthalic acid N-butyl imides or chlorophenoxyethanol.
- the Carrier process brings excellent white effects in a short brightening time with a lower brightening temperature and thus lower energy consumption.
- carriers can cause stains.
- carriers are often carcinogenic.
- a low-temperature process has been developed as an alternative to the carrier process.
- mixtures of nonionic and ionic surfactants with aliphatic or aromatic dicarboxylic acid esters are used instead of the carcinogenic carriers. These mixtures are not fiber-active, but they increase the solubility of the brighteners in the dyeing liquor and thus enable them to be brightened at 98 to 110 ° C.
- the mixtures of non-ionic and ionic surfactants with aliphatic or aromatic dicarboxylic acid esters are also known as diffusion accelerators, ie they accelerate the diffusion of the brighteners from the dye liquor into the fiber.
- the process has several disadvantages: when diluted, the diffusion accelerators go through a swelling phase, which affects the homogeneous distribution in the lightening bath.
- the resulting whiteness is inferior to that of carrier lightening.
- the whitening effect quickly decreases at brightening temperatures below 100 ° C. If acceptable white effects are achieved at 98 ° C, the resulting whiteness at 95 ° C is no longer sufficient for many requirements.
- temperatures above 95 ° C cannot often be reached in open aggregates in an aqueous medium.
- the object of the present invention is to provide a lightening process which can be used in open aggregates, which achieves excellent degrees of whiteness, which is free of toxic or carcinogenic auxiliaries, which avoids liquor inhomogeneities (in particular due to swelling phases of surfactants) and which at temperatures around 95 ° C still produces excellent white effects.
- This object is achieved according to the invention by a process for the optical brightening of synthetic fibers or of mixtures of synthetic fibers with natural fibers, the synthetic fibers or mixtures of synthetic fibers with natural fibers in a treatment bath containing optical brighteners to which a microemulsion has been added was treated.
- microemulsions are already used as leveling aids in dyeing polyester in textile form. Dyeing of polyester in textile form often becomes u-negative, uneven, stained. Such irregularities can be prevented or significantly reduced by adding microemulsions to the staining solutions.
- the addition of the microemulsion stabilizes the disperse dye particles and controls the molecular transport process to the fiber and the dissolving process of the dye molecules in the polyester fiber.
- Another task of the microemulsion is to control the dilution process when preparing the dye liquor so that no highly viscous intermediate states are obtained. In the optical brightening of synthetic textile materials, there are usually no irregularities or they cannot be recognized by the sluggishness of the eye.
- microemulsions have no leveling effect when optically brightening synthetic fiber materials, they act as diffusion accelerators, ie the required fixing temperature, for example with polyester, can be reduced by approx. 35 ° C from approx. 130 ° C to approx. 95 ° C. without a noticeable reduction in whiteness.
- microemulsion which can be used according to the invention contains nonionic surfactants, ionic surfactants, organic solubilizers and water.
- microemulsion which can be used according to the invention contains the following components:
- R 1 , R 2 , R 3 independently of one another represent an aliphatic, aromatic or aromatic lipatic radical
- R 1 , R 2 , R 3 branched or unbranched, saturated, aliphatic radicals with 1-40 carbon atoms or branched or unbranched, unsaturated, aliphatic radicals with 2-40 carbon atoms, which are optionally selected from the group with at least one functional group Group consisting of hydroxy, ether, amino, thio, aldehyde, keto, carboxylic acid, ester, amido group and halogen may be substituted;
- R 4 independently of one another represents hydrogen or an aliphatic radical with 1-15 carbon atoms, an aromatic radical with 6-15 carbon atoms or an aromatic lipatic radical with 7-15 carbon atoms, R 4 is preferably hydrogen or a linear or branched, saturated, aliphatic radical with 1 to 10 carbon atoms or a linear or branched, unsaturated, aliphatic radical with 2 - 10 carbon atoms, R 4 is very particularly preferably hydrogen;
- R 5 is independently hydrogen or an aliphatic radical having 1-15 carbon atoms, an aromatic radical having 6-15 carbon atoms or an araliphatic radical having 7-15 carbon atoms;
- R 5 is preferably hydrogen or a linear or branched, saturated, aliphatic Radical with 1 to 10 carbon atoms or a linear or branched, unsaturated, aliphatic radical with 2 - 10 carbon atoms, very particularly preferably R 5 is independently hydrogen, methyl, ethyl or propyl;
- component B 1-25% by weight of a compound which is obtained by reacting a compound bl of the general formula V V wherein R 6 represents an aliphatic, aromatic or araliphatic radical;
- R 6 is preferably a branched or unbranched, saturated, aliphatic radical having 1 to 40 carbon atoms or a branched or unbranched, unsaturated, aliphatic radical having 2 to 40 carbon atoms, which optionally has at least one functional group selected from the group consisting of hydroxyl, Ether, amino, thio, aldehyde, keto, carboxylic acid, ester, amido group and halogen may be substituted; the radical R 6 is particularly preferably a partially unsaturated, aliphatic radical having 10-25 carbon atoms, which may optionally be substituted by at least one hydroxyl and or amino group;
- R 7 independently of one another is hydrogen or an aliphatic radical with 1-15 carbon atoms, an aromatic radical with 6-15 carbon atoms or an araliphatic radical with 7-15 carbon atoms, R 7 is preferably hydrogen or a linear or branched, saturated, aliphatic radical with 1 - 10 carbon atoms or a linear or branched, unsaturated, aliphatic radical with 2 - 10 carbon atoms, very particularly preferably R 7 is independently hydrogen, methyl, ethyl or propyl;
- R 8 is preferably a branched or unbranched, saturated, aliphatic radical having 1-40 carbon atoms or a branched or unbranched, unsaturated, aliphatic radical having 2-40 carbon atoms, which optionally has at least one functional group selected from the group consisting of hydroxy, Ether, amino, thio, aldehyde, keto, carboxylic acid, ester, amido group and halogen may be substituted;
- the radical R 8 is particularly preferably a partially unsaturated, aliphatic radical having 10-25 carbon atoms, which can optionally be substituted by at least one hydroxyl and / or amino group;
- R 9 is preferably a branched or unbranched, saturated, aliphatic radical having 1-12 carbon atoms or a branched or unbranched, unsaturated, aliphatic radical having 2-12 carbon atoms, which optionally has at least one functional group selected from the group consisting of hydroxy, Ether, amino, thio, aldehyde, keto, carboxylic acid, ester, amido group and halogen may be substituted;
- the radical R 9 is particularly preferably a saturated, aliphatic radical with 1-6 carbon atoms, which can optionally be substituted with at least one hydroxyl and / or amino group;
- the radical R 9 is very particularly preferably selected from the group consisting of ethyl, n-propyl, n-butyl and n-pentyl;
- the mean value for n in the formula VHI is a whole or fractional positive number from 1 to 10, preferably from 1 to 8, particularly preferably from 1 to 5; when mixtures of compounds of the general formula VHI are present, the mean value for n can assume fractional values.
- R 10 is preferably a branched or unbranched, saturated, aliphatic radical having 1-12 carbon atoms or a branched or unbranched, unsaturated, aliphatic radical having 2-12 carbon atoms, which optionally has at least one functional group selected from the group consisting of hydroxy , Ether, amino, thio, aldehyde, keto, carboxylic acid, ester, amido group and halogen may be substituted; the radical R 10 is particularly preferably a saturated, aliphatic radical with 1-6 carbon atoms, which can optionally be substituted with at least one hydroxyl and / or amino group;
- the radical R 10 is very particularly preferably selected from the group consisting of ethyl, n-propyl, n-butyl and n-pentyl;
- the mean value for m in formula IX is a whole or fractional positive number from 0 to 10, preferably from 0 to 8, particularly preferably from 0 to 5; in the case of mixtures of compounds of the general formula IX, the mean value for m can assume fractional values.
- Components A, B, C, D and E are preferably present in the microemulsion in the following proportions: component A: 5-35% by weight, component B: 5-20% by weight, component C: 1-10 % By weight, component D: 5-35% by weight, component E: 5-40% by weight and 5-35% by weight of water as solvent, the sum of the% by weight being 100% by weight. -% results.
- Components A, B, C, D and E are particularly preferably present in the microemulsion in the following proportions: component A: 10-30% by weight, component B: 5-15% by weight, component C: 2- 8% by weight, component D: 10-30% by weight, component E: 10-35% by weight and 10-30% by weight of water as solvent, the sum of the% by weight being 100% by weight .-% results.
- microemulsions which can be used according to the invention can be prepared by mixing the corresponding components in any order.
- the advantage of the microemulsion used according to the invention is its low viscosity at any mixing ratio with water. The product can therefore be used in dosing systems without any problems.
- the microemulsion is absolutely transparent. The oil phase contained in addition to the aqueous phase is thus so finely distributed in the microemulsion that no visible scatter is noticeable.
- the average size of the droplets of the disperse phase of the microemulsion used according to the invention can be determined according to the principle of quasi-elastic dynamic light scattering (the so-called z-average droplet diameter d z of the unimodal analysis of the autocorrelation function).
- the droplet size of the microemulsions used according to the invention is ⁇ 500 nm for d z .
- the value for d z is preferably 50 nm to 300 nm, particularly preferably the value for d z is 50 nm to 200 nm.
- the process according to the invention makes it possible to optically lighten polyesters, polyamides or mixtures of polyesters or polyamides with one another, it also being possible for these to be mixed with other synthetic or natural fibers.
- Examples of other synthetic or natural fibers are cellulose fibers, polyacrylonitrile fibers, polyurethane fibers, acetate fibers or wool fibers.
- the process according to the invention is particularly suitable for the optical brightening of polyester fibers or of mixtures of polyester fibers.
- Polyesters are understood to mean homopolymers, copolymers, mixtures and grafts of synthetic long-chain polyesters which, as an essential constituent, repeatedly have ester groups in the polymer main chain.
- the polyesters used according to the invention are produced from aromatic or aliphatic hydroxycarboxylic acids.
- the aliphatic hydroxycarboxylic acids used in the polyesters according to the invention are C 1 -C 6 -carboxylic acids which are optionally substituted by C t -s-alkyl chains and which, in addition to the COOH group, also contain at least one OH group.
- the Ci 8 alkyl chains mentioned are optionally substituted with further functional groups.
- Hydroxycarboxylic acids are preferably selected from the group consisting of 2-hydroxyacetic acid, 2-hydroxypropionic acid, 3-hydroxypropionic acid, 4-hydroxybutter- acid, 5-hydroxypentanoic acid, 6-hydroxyhexanoic acid, malic acid, tartaric acid and citric acid.
- the aromatic or aliphatic hydroxycarboxylic acids which can be used according to the invention contain 7 to 20 carbon atoms and at least one hydroxy functionality; ortho-, meta- or para-hydroxy-benzoic acid are preferably used in the polyesters which can be used according to the invention.
- the polyesters which can be used include diacids and diols.
- the diacids contained in the polyesters according to the invention can be aliphatic or aromatic diacids having 4 to 18 carbon atoms.
- Dicarboxylic acids are preferably selected from the group consisting of phthalic acid, terephthalic acid, isophthalic acid, naphthalene-1,4-dicarboxylic acid, naphthalene-2,3-dicarboxylic acid, naphthalene-2,6-dicarboxylic acid, cyclohexanedicarboxylic acid, cyclohexanediacetic acid, diphenyl-4,4-dicarboxylic acid , Succinic acid, gluataric acid, adipic acid,fugic acid, and sebacic acid or mixtures thereof.
- the diacids contained in the polyester are particularly preferably selected from terephthalic acid or naphthaldic acid or a mixture thereof.
- the diols contained in the polyester which can be used according to the invention can be cycloaliphatic diols having 6 to 20 carbon atoms or aliphatic diols having 2 to 20 carbon atoms.
- the diol contained in the polyester is preferably selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, 1,4-cyclohexanedimethanol, propane-1,3-diol, butane-1,4-diol, pentane-1,5-diol, hexane - 1, 6-diol, 2-methylpentane-l, 4-diol, 2,2,4-trimethylpentane-l, 3-diol, hexane-1,3-diol, 2,2-bis- (4-hydroxycyclohexyl) propane and 2,4-dihydroxy-l, l, 3,3-tetramethylcyclobutane or mixtures thereof.
- the polyester which can be used according to the invention contains ethylene glycol as the diol component.
- polyesters In a particularly preferred embodiment of the present invention, homopolymers of polyethylene terephthalate (PET) or mixtures of polyethylene terephthalate with other polyesters are used as polyesters.
- PET polyethylene terephthalate
- the molecular weight of the polyesters which can be used according to the invention is preferably in the range from 2000 to 50,000 g / mol.
- the polyesters which can be used according to the invention can be present in any possible thread size and in any form, ie as a flake, fiber, yarn, twine, woven, knitted or nonwoven.
- polyesters used according to the invention are produced by processes known to the person skilled in the art, see Encycl. Polym. Be. Engng. 12, 1 to 313 and Houben-Weyl E20 / 2, 1405 to 1429, Ulimann (4.) 19, 61 to 88.
- the method according to the invention is very particularly suitable for the optical brightening of polyester fibers based on PET or mixtures of PET with other synthetic or natural fibers.
- Preferred optical brighteners in the process according to the invention are 1,4-bis-dicyanostyrylbenzenes of the general formula X
- All possible isomers of 1,4-bis-dicyanostyrylbenzenes of the formula X can be used in the process according to the invention, such as, for example, ortho-ortho, ortho-meta, ortho-para, meta-meta, meta-para, para-para or mixtures of two or more.
- the ortho-para isomer, the ortho-meta isomer or the meta-para isomer or mixtures of two or three or all of the isomers with one another or mixtures of one, two or all three isomers with the ortho-ortho isomers are particularly preferred or can be used in the process according to the invention with a compound of the general formula I.
- Optical brighteners and shading dyes are generally used as aqueous preparations in the process according to the invention.
- Such preparations generally contain water and, based on the weight of the preparation, 1 to 40% by weight, preferably 2 to 25% by weight, particularly preferably 3 to 10% by weight, of the mixture of brightener described in more detail above and shading dye and 1 to 60% by weight, preferably 3 to 56% by weight, particularly preferably 5 to 52% by weight of auxiliaries.
- Suitable tools are e.g. anionic or nonionic dispersants, from the class of ethylene oxide adducts with fatty alcohols, higher fatty acids or alkylphenols or ethylenediamine-ethylene oxide-propylene oxide adducts, or dispersants, as described in DE-A-2 745 449, copolymers of N-vinylpyrolidone with 3-vinyl propionic acid , Water retention agents such as ethylene glycol, glycerin or sorbitol or biocides.
- a brightener preparation containing, in addition to water, in each case based on the weight of the preparation, 1 to 40% by weight, preferably 2 to 25% by weight, particularly preferably 3 to 10% by weight, of the Mixture of brightener and shading dye, specified in more detail above, 1 to 30% by weight, preferably 2 to 20% by weight, particularly preferably 3 to 12% by weight of anionic or nonionic dispersant and 1 to 50% by weight, preferably 1 to 35% by weight, particularly preferably 1 to 25% by weight of further auxiliaries (for example water retention agents or biocides).
- further auxiliaries for example water retention agents or biocides
- the treatment bath containing optical brighteners can contain shading dyes.
- Shading dyes suitable according to the invention generally originate from the class of disperse, acid or vat dyes. These are common names. Such dyes are listed in the color index, for example under the name Disperse Blue or Disperse Violet or Acid Blue or Acid Violet or Vat Blue or Vat Violet. Blue dyes from the class of anthraquinones, azo dyes, methine dyes, violanthrones or indanthrones are particularly suitable.
- an aqueous treatment bath containing optical brightener which has the following ingredients: 0.001 to 1.00% by weight, preferably 0.01 to 0.75% by weight, particularly preferably 0.01 to 0.50% by weight of the described brightener preparation and
- the process according to the invention is carried out at a temperature of 80 to 120 ° C., preferably 90 to 110 ° C., particularly preferably 95 to 100 ° C.
- the process according to the invention is carried out over a period of 10 to 300 min, preferably over a period of 20 to 200 min, particularly preferably over a period of 30 to 120 min.
- the present invention further relates to the use of the treatment bath according to the invention, containing optical brighteners, for optically brightening synthetic fibers or mixtures of synthetic fibers with natural fibers.
- the present invention also relates to a treatment bath to which a microemulsion according to the invention has been added, for synthetic fibers or for synthetic fibers in a mixture with natural fibers containing water, optical brighteners and optionally shading dyes.
- the present invention relates to the use of the microemulsion according to the invention in treatment baths containing optical brighteners for synthetic fibers or synthetic fibers in a mixture with natural fibers.
- Example 1 In an autoclave, 10 g of polyester fabric were introduced at 25 ° C. into 100 ml of a healing bath containing 0.04 g of a brightener dispersion.
- the brightener dispersion contains the following optical brighteners
- the individual brightener components were first dispersed separately (“finished”) and then mixed. The bath was then heated to 95 ° C. in the course of 30 minutes and held at this temperature for a further 30 minutes. During this time, the liquor was stirred Tissue was removed from the bath, rinsed and dried and the optical whiteness was determined according to the CIE.
- Diffusion accelerator 1 is a mixture of an oleic acid ethoxylate with 5 EO units (50% by weight) and succinic acid n-butyl ester (50% by weight).
- Diffusion accelerator 2 is a mixture of an oleic acid ethoxylate with 5 EO units (45% by weight), phthalic acid di-n-butyl ester (30%) and an oleic acid ethoxylate with 12 EO units.
- Both diffusion accelerators are low-viscosity liquids, which form highly viscous states when diluted with water. These products are therefore not suitable for modern dosing systems.
- composition of the microemulsion used according to the invention (in% by weight): Castor oil ethoxylated with 40 EO 20
- the microemulsion used according to the invention is produced by mixing the components in the appropriate amounts, the order in which the individual components are added has no influence on the effectiveness of the microemulsion.
- the resulting whiteness levels are as follows:
- the resulting whiteness levels are as follows:
- polyester staple fiber yarn were introduced at 25 ° C. into 100 ml of a whitening bath which contains 0.04 g of a whitening agent dispersion.
- the brightener dispersion contains the following optical brighteners
- the individual brightener components were first dispersed separately (“finished”) and then mixed.
- the bath was then heated to 95 ° C. in the course of 30 minutes and held at this temperature for a further 30 minutes.
- the liquor was then stirred the staple fiber yarn was removed from the bath, rinsed and dried, and the optical whiteness was determined according to the CIE for analysis.
- the resulting whiteness levels are as follows:
- polyester / viscose knitwear (mixing ratio 50% polyester and 50% viscose) were introduced at 25 ° C. into 100 ml of a brightening bath which contains 0.04 g of a brightener dispersion.
- the brightener dispersion contains the following optical brighteners.
- the resulting whiteness levels are as follows:
- polyester staple fiber yarn were introduced at 25 ° C. into 100 ml of a whitening bath which contains 0.25 g of a brightener dispersion.
- the brightener dispersion contains the following optical brighteners
- the resulting whiteness levels are as follows:
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Detergent Compositions (AREA)
- Coloring (AREA)
- Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102004011957A DE102004011957A1 (en) | 2004-03-11 | 2004-03-11 | Process for the optical whitening of synthetic fibers or of synthetic fibers mixed with natural fibers |
PCT/EP2005/002496 WO2005088004A2 (en) | 2004-03-11 | 2005-03-09 | Method for optical brightening of synthetic fibres or of synthetic fibres mixed with natural fibres |
Publications (2)
Publication Number | Publication Date |
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EP1725708A2 true EP1725708A2 (en) | 2006-11-29 |
EP1725708B1 EP1725708B1 (en) | 2007-07-18 |
Family
ID=34895241
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP05715882A Active EP1725708B1 (en) | 2004-03-11 | 2005-03-09 | Method for optical brightening of synthetic fibres or of synthetic fibres mixed with natural fibres |
Country Status (9)
Country | Link |
---|---|
US (1) | US20070204410A1 (en) |
EP (1) | EP1725708B1 (en) |
CN (1) | CN1930340A (en) |
AT (1) | ATE367471T1 (en) |
BR (1) | BRPI0508569A (en) |
DE (2) | DE102004011957A1 (en) |
EA (1) | EA200601658A1 (en) |
ES (1) | ES2287904T3 (en) |
WO (1) | WO2005088004A2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
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US20100230061A1 (en) * | 2006-01-26 | 2010-09-16 | Achim Kohler | Process for Producing Optically Brightened Paper |
CN102977628A (en) * | 2012-12-20 | 2013-03-20 | 山东沾化奥仕化学有限公司 | One-pot synthesis method of fluorescent brightener ER-II |
WO2015130273A1 (en) | 2014-02-26 | 2015-09-03 | Empire Technology Development Llc | Presence-based device mode modification |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0033715A1 (en) * | 1980-01-31 | 1981-08-12 | Ciba-Geigy Ag | Auxiliary and its use in the dyeing or optical brightening of polyester fibre materials |
US5540740A (en) * | 1995-09-06 | 1996-07-30 | China Textile Institute | Low temperature microemulsion dyeing process for polyester fibers |
EP0773284A1 (en) * | 1995-11-10 | 1997-05-14 | The Procter & Gamble Company | Microemulsion with high level of anionic surfactants, using branched fatty acids |
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2004
- 2004-03-11 DE DE102004011957A patent/DE102004011957A1/en not_active Withdrawn
-
2005
- 2005-03-09 BR BRPI0508569-1A patent/BRPI0508569A/en not_active IP Right Cessation
- 2005-03-09 EP EP05715882A patent/EP1725708B1/en active Active
- 2005-03-09 DE DE502005001069T patent/DE502005001069D1/en not_active Expired - Fee Related
- 2005-03-09 US US10/592,096 patent/US20070204410A1/en not_active Abandoned
- 2005-03-09 AT AT05715882T patent/ATE367471T1/en not_active IP Right Cessation
- 2005-03-09 CN CNA2005800076103A patent/CN1930340A/en active Pending
- 2005-03-09 WO PCT/EP2005/002496 patent/WO2005088004A2/en active IP Right Grant
- 2005-03-09 ES ES05715882T patent/ES2287904T3/en active Active
- 2005-03-09 EA EA200601658A patent/EA200601658A1/en unknown
Non-Patent Citations (1)
Title |
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See references of WO2005088004A2 * |
Also Published As
Publication number | Publication date |
---|---|
US20070204410A1 (en) | 2007-09-06 |
EA200601658A1 (en) | 2007-02-27 |
DE502005001069D1 (en) | 2007-08-30 |
ES2287904T3 (en) | 2007-12-16 |
DE102004011957A1 (en) | 2005-09-29 |
ATE367471T1 (en) | 2007-08-15 |
WO2005088004A2 (en) | 2005-09-22 |
EP1725708B1 (en) | 2007-07-18 |
CN1930340A (en) | 2007-03-14 |
WO2005088004A3 (en) | 2006-02-09 |
BRPI0508569A (en) | 2007-08-14 |
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