EP0650518B1 - Verfahren zum einspülen eines percarbonathaltigen textilwaschmittels mit hoher schüttdichte - Google Patents

Verfahren zum einspülen eines percarbonathaltigen textilwaschmittels mit hoher schüttdichte Download PDF

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EP0650518B1
EP0650518B1 EP93916935A EP93916935A EP0650518B1 EP 0650518 B1 EP0650518 B1 EP 0650518B1 EP 93916935 A EP93916935 A EP 93916935A EP 93916935 A EP93916935 A EP 93916935A EP 0650518 B1 EP0650518 B1 EP 0650518B1
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Prior art keywords
weight
laundry detergent
alkali metal
detergent composition
percarbonate
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French (fr)
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EP0650518A1 (de
EP0650518A4 (de
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Gerald Marcel Baillely
Carolyn Jayne Brown
Graham Alexander 1 Breamish Ellington Sorrie
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Procter and Gamble Co
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Procter and Gamble Co
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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/12Water-insoluble compounds
    • C11D3/124Silicon containing, e.g. silica, silex, quartz or glass beads
    • C11D3/1246Silicates, e.g. diatomaceous earth
    • C11D3/1253Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite
    • C11D3/1273Crystalline layered silicates of type NaMeSixO2x+1YH2O
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/0039Coated compositions or coated components in the compositions, (micro)capsules
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/06Powder; Flakes; Free-flowing mixtures; Sheets
    • C11D17/065High-density particulate detergent compositions
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/39Organic or inorganic per-compounds
    • C11D3/3902Organic or inorganic per-compounds combined with specific additives
    • C11D3/3905Bleach activators or bleach catalysts
    • C11D3/3907Organic compounds
    • C11D2111/12

Definitions

  • This invention relates to a low temperature process for washing laundry in a domestic washing machine, and more especially to such a process wherein a high density detergent composition comprising a carbonate/sulphate coated alkali metal percarbonate salt and a bleach activator is delivered to the wash via a dispensing device.
  • the inorganic perhydrate bleach most widely used in laundry detergent compositions is sodium perborate in the form of either the monohydrate of tetrahydrate.
  • concerns about the impact of boron salts on the environment have led to an increasing interest in other perhydrate salts, of which sodium percarbonate is the most readily available.
  • Detergent compositions containing sodium percarbonate are known in the art.
  • Sodium percarbonate is an attractive perhydrate for use in detergent compositions because it dissolves readily in water, is weight efficient and, after giving up its available oxygen, provides a useful source of carbonate ions for detergency purposes.
  • percarbonate salts in laundry detergent compositions has been restricted hitherto by the relative instability of the bleach.
  • percarbonate salts decompose rapidly when stored in a moist and/or warm atmosphere. It is known that acceptable storage characteristics may however be obtained through the protection of the carbonate by coating the crystalline product, or by the inclusion of stabilizing agents during its manufacture, or both.
  • suitable coating agents include silicates and mixtures of inorganic sulphate and carbonate salts.
  • WO 92/06163 describes percarbonate coated with silicate.
  • coating of the percarbonate bleach improves its storage stability the presence of the coating may act so as to inhibit the performance of the bleach, particularly when used in low temperature washing processes. This is one reason which accounts for the fact that coated percarbonate bleaches have not found widespread use as replacements for perborate bleaches in detergent products.
  • a dispensing device containing an effective amount of a granular laundry detergent composition is introduced into th drum of the washing machine before the commencement of the wash, wherein said dispensing device permits progressive relase of said granular laundry detergent composition into the wash liquor during the wash, and wherein said granular laundry detergent composition has a bulk density greater than 650 g/litre and comprises:
  • said process is conducted at a temperature of no more than 45°C, and most preferably no more than 40°C.
  • the first essential component of the granular detergent compositions in accord with the invention is from 1% to 60%, by weight of the composition, preferably from 3% to 30% by weight, most preferably from 5% to 25% by weight of an alkali metal percarbonate bleach coated with a mixed salt comprising an alkai metal carbonate and an alkali metal sulphate salt.
  • the alkali metal percarbonate bleach is usually in the form of the sodium salt.
  • Sodium percarbonate is an addition compound having a formula corresponding to 2Na 2 CO 3 3H 2 O 2 .
  • the percarbonate bleach is coated with a mixed salt of an alkali metal sulphate and carbonate.
  • the weight ratio of the mixed salt coating material to percarbonate lies in the range from 1:200 to 1:4, more preferably from 1:99 to 1:9, and most preferably from 1:49 to 1:19.
  • the mixed salt is of sodium sulphate and sodium carbonate which has the general formula Na 2 SO 4 .n.Na 2 CO 3 wherein n is from 0.1 to 3, preferably n is from 0.3 to 1.0 and most preferably n is from 0.2 to 0.5.
  • carbonate/sulphate coated percarbonate bleach may include a low level of a heavy metal sequestrant such as EDTA, 1-hydroxyethylidene 1,1-diphosphonic acid (HEDP) or an aminophosphonate, that is incorporated during the manufacturing process.
  • a heavy metal sequestrant such as EDTA, 1-hydroxyethylidene 1,1-diphosphonic acid (HEDP) or an aminophosphonate
  • Preferred heavy metal sequestrants for incorporation as described herein above include the organic phosphonates and amino alkylene poly(alkylene phosphonates) such as the alkali metal ethane 1-hydroxy diphosphonates, the nitrilo trimethylene phosphonates, the ethylene diamine tetra methylene phosphonates and the diethylene triamine penta methylene phosphonates.
  • organic phosphonates and amino alkylene poly(alkylene phosphonates) such as the alkali metal ethane 1-hydroxy diphosphonates, the nitrilo trimethylene phosphonates, the ethylene diamine tetra methylene phosphonates and the diethylene triamine penta methylene phosphonates.
  • the second essential component of the granular detergent compositions in accord with the invention is from 1 % to 40% by weight of the composition, preferably from 2% to 15% by weight, most preferably from 3% to 10% by weight of a peroxyacid bleach activator.
  • Peroxyacid bleach activators as additional bleaching components in accord with the invention can be selected from a wide range of classes and are preferably those containing one or more N- or O-acyl groups.
  • Suitable classes include anhydrides, esters, amides and acylated derivatives of imidazoles and oximes, and examples of useful materials within these classes are disclosed in GB-A-1586789.
  • the most preferred classes are esters such as are disclosed in GB-A-836 988, 864 798, 1 147 871 and 2 143 231 and amides such as are disclosed in GB-A-855 735 and 1 246 338.
  • Particularly preferred bleach activator compounds as additional bleaching components in accord with the invention are the N,N,N'N' tetra acetylated compounds of formula where x can be O or an integer between 1 and 6.
  • TAMD tetra acetyl methylene diamine
  • TAED tetra acetyl ethylene diamine
  • TAHD tetraacetyl hexylene diamine
  • R 1 is an aryl or alkaryl group with from about 1 to about 14 carbon atoms
  • R 2 is an alkylene, arylene, and alkarylene group containing from about 1 to 14 carbon atoms
  • R 5 is H or an alkyl, aryl, or alkaryl group containing 1 to 10 carbon atoms and L can be essentially any leaving group.
  • R 1 preferably contains from about 6 to 12 carbon atoms.
  • R 2 preferably contains from about 4 to 8 carbon atoms.
  • R 1 may be straight chain or branched alkyl, substituted aryl or alkylaryl containing branching, substitution, or both and may be sourced from either synthetic sources or natural sources including for example, tallow fat. Analogous structural variations are permissible for R 2 . The substitution can include alkyl, aryl, halogen, nitrogen, sulphur and other typical substituent groups or organic compounds.
  • R 5 is preferably H or methyl. R 1 and R 5 should not contain more than 18 carbon atoms total. Amide substituted bleach activator compounds of this type are described in EP-A-0170386.
  • peroxyacid bleach activator compounds include sodium nonanoyloxy benzene sulfonate, sodium trimethyl hexanoyloxy benzene sulfonate, sodium acetoxy benzene sulfonate and sodium benzoyloxy benzene sulfonate as disclosed in, for example, EP-A-0341947.
  • compositions of the invention in addition comprise, in general terms, those ingredients conventionally found in laundry detergent products.
  • a wide range of surfactants can be used in the detergent compositions.
  • a typical listing of anionic, nonionic, amphyolytic and zwitterionic classes, and species of these surfactants, is given in U.S.P. 3,929,678 issued to Laughlin and Heuring on December 30, 1975.
  • a list of suitable cationic surfactants is given in U.S.P. 4,259,217 issued to Murphy on March 31, 1981.
  • Mixtures of anionic surfactants are suitable herein, particularly blends of sulphate, sulphonate and/or carboxylate surfactants.
  • Mixtures of sulphonate and sulphate surfactants are normally employed in a sulphonate to sulphate weight ratio of from 5:1 to 1:2, preferably from 3:1 to 2:3, more preferably from 3:1 to 1:1.
  • Preferred sulphonates include alkyl benzene sulphonates having from 9 to 15, especially 11 to 13 carbon atoms in the alkyl radical, and alpha-sulphonated methyl fatty acid esters in which the fatty acid is derived from a C 12 -C 18 fatty source, preferably from a C 16 -C 18 fatty source.
  • the cation is an alkali metal, preferably sodium.
  • Preferred sulphate surfactants in such sulphonate sulphate mixtures are alkyl sulphates having from 12 to 22, preferably 16 to 18 carbon atoms in the alkyl radical.
  • Another useful surfactant system comprises a mixture of two alkyl sulphate materials whose respective mean chain lengths differ from each other.
  • One such system comprises a mixture of C 14 -C 15 alkyl sulphate and C 16 -C 18 alkyl sulphate in a weight ratio of C 14 -C 15 : C 16 -C 18 of from 3:1 to 1:1.
  • the alkyl sulphates may also be combined with alkyl ethoxy sulphates having from10 to 20, preferably 10 to 16 carbon atoms in the alkyl radical and an average degree of ethoxylation of 1 to 6.
  • the cation in each instance is again an alkali metal, preferably sodium.
  • alkali metal sarcosinates of formula R-CON (R 1 )CH 2 COOM wherein R is a C 9 -C 17 linear or branches alkyl or alkenyl C group, R 1 is a C 1 -C 4 alkyl group and M is an alkali metal ion.
  • R is a C 9 -C 17 linear or branches alkyl or alkenyl C group
  • R 1 is a C 1 -C 4 alkyl group
  • M is an alkali metal ion.
  • Preferred examples are the lauroyl, Cocoyl (C 12 -C 14 ), myristyl and oleyl methyl sarcosinates in the form of their sodium salts.
  • One class of nonionic surfactants useful in the present invention comprises condensates of ethylene oxide with a hydrophobic moiety, providing surfactants having an average hydrophilic-lipophilic balance (HLB) in the range from 8 to 17, preferably from 9.5 to 13.5, more preferably from 10 to 12.5 in which the hydrophobic (lipophilic) moiety may be aliphatic or aromatic in nature.
  • HLB hydrophilic-lipophilic balance
  • Especially preferred nonionic surfactants of this type are the C 9 -C 15 primary alcohol ethoxylates containing 3-8 moles of ethylene oxide per mole of alcohol, particularly the C 14 -C 15 primary alcohols containing 6-8 moles of ethylene oxide per mole of alcohol and the C 12 -C 14 primary alcohols containing 3-5 moles of ethylene oxide per mole of alcohol.
  • a further preferred class of nonionic surfactants comprises polyhydroxy fatty acid amides of general formula: where R 1 is H, a C 1 -C 4 hydrocarbyl, 2 hydroxyethyl, 2-hydroxypropyl or mixtures thereof, R 2 is a C 5 -C 31 hydrocarbyl and Z is a polyhydroxyhydrocarbyl having a linear hydrocarbyl chain with at least three hydroxy groups directly connected to the chain, or an alkoxylated derivative thereof.
  • the polyhydroxy hydrocarbyl moiety is derived from glucose of maltose or mixtures thereof and the R 2 group is a C 11 -C 19 alkyl or alkenyl moiety as the R 1 group.
  • Compositions incorporating such highly preferred polyhydroxy fatty acid amides are disclosed in the copending British Application No. 9113139 filed June 18 1991.
  • Nonionic surfactants comprises alkyl polyglucoside compounds of general formula RO (C n H 2n O) t Z x wherein Z is a moiety derived from glucose; R is a saturated hydrophobic alkyl group that contains from 12 to 18 carbon atoms; t is from 0 to 10 and n is 2 or 3; x is from 1.3 to 4, the compounds including less than 10% unreacted fatty alcohol and less than 50% short chain alkyl polyglucosides.
  • Compounds of this type and their use in detergent compositions are disclosed in EP-B 0070074, 0070077, 0075996 and 0094118.
  • a further class of surfactants are the semi-polar surfactants such as amine oxides.
  • Suitable amine oxides are selected from mono C 8 -C 20 , preferably C 10 -C 14 -alkyl or alkenyl amine oxides and propylene-1,3-diamine dioxides wherein the remaining N positions are substituted by methyl, hydroxyethyl or hydroxypropyl groups.
  • Cationic surfactants can also be used in the detergent compositions herein and suitable quaternary ammonium surfactants are selected from mono C 8 -C 16 , preferably C 10 -C 14 N-alkyl or alkenyl ammonium surfactants wherein remaining N positions are substituted by methyl, hydroxyethyl ro hydroxypropyl groups.
  • the detergent compositions comprise from 3% to 30% by weight of the composition of surfactant but more usually comprise from 5% to 20% by weight, more preferably from 5% to 15% by weight.
  • Combinations of surfactant types are preferred, more especially anionic-nonionic and also anionic-nonionic-cationic blends. Particularly preferred combinations are described in GB-A-2040987, GB 9113139 and EP-A-0087914.
  • the surfactants can be incorporated into the compositions as mixtures, it is preferable to control the point of addition of each surfactant in order to optimise the physical characteristics of the composition and avoid processing problems. Preferred modes and orders of surfactant addition are described hereinafter.
  • the granular detergent compositions in accord with the invention also preferably comprise a detergent builder system comprising one or more detergent builders, most preferably non-phosphate detergent builders. These can include, but are not restricted to alkali metal carbonates, bicarbonates, silicates, aluminosilicates, monomeric and oligomeric polycarboxylates, homo or copolymeric polycarboxylic acids or their salts in which the polycarboxylic acid comprises at least two carboxylic radicals separated from each other by not more than two carbon atoms, and mixtures of any of the foregoing.
  • the builder system is present in an amount of from 5% to 80% by weight of the composition, more preferably from 30% to 60% by weight.
  • Suitable silicates are those having an SiO 2 : Na 2 O ratio in the range from 1.6 to 3.4, the so-called amorphous silicates of SiO 2 : Na 2 O ratios from 2.0 to 2.8 being preferred.
  • These materials can be added at various points of the manufacturing process, such as in a slurry of components that are spray dried or in the form of an aqueous solution serving as agglomerating agent for other solid components, or, where the silicates are themselves in particulate form, as solids to the other particulate components of the composition.
  • the percentage of spray dried components is low ie 30%, it is preferred to include the amorphous silicate in the spray-dried components.
  • crystalline layered sodium silicates of general formula NaM(Si x O 2x+1 ) ⁇ yH 2 O wherein M is sodium or hydrogen, x is a number from 1.9 to 4 and y is a number from 0 to 20.
  • Crystalline layered sodium silicates of this type are disclosed in EP-A-0164514 and methods for their preparation are disclosed in DE-A-3417649 and DE-A-3742043.
  • x in the general formula above has a value of 2, 3 or 4 and is preferably 2. More preferably M is sodium and y is O and preferred examples of this formula comprise the ⁇ , ⁇ , ⁇ and ⁇ forms of Na 2 Si 2 O 5 .
  • Crystalline layered silicates are incorporated either as dry mixed solids, or as solid components of aggomerates with other components.
  • preferred sodium aluminosilicate zeolites have the unit cell formula Na z [(ALO 2 ) z (SiO 2 ) y ] xH 2 O wherein z and y are at least 6; the molar ratio of z to y is from 1.0 to 0.5 and x is at least 5, preferably from 7.5 to 276, more preferably from 10 to 264.
  • the aluminosilicate materials are in hydrated form and are preferably crystalline, containing from 10% to 28%, more preferably from 18% to 22% water in bound form.
  • the above aluminosilicate ion exchange materials are further characterised by a particle size diameter of from 0.1 to 10 micrometers, preferably from 0.2 to 4 micometers.
  • particle size diameter herein represents the average particle size diameter of a given ion exchange material as determined by conventional analytical techniques such as, for example, microscopic determination utilizing a scanning electron microscope or by means of a laser granulometer.
  • the aluminosilicate ion exchange materials are further characterised by their calcium ion exchange capacity, which is at least 200 mg equivalent of CaCO 3 water hardness/g of aluminosilicate, calculated on an anhydrous basis, and which generally is in the range of from 300 mg eq./g to 352 mg eq./g.
  • the aluminosilicate ion exchange materials herein are still further characterised by their calcium ion exchange rate which is at least 130 mg equivalent of CaCO 3 /litre/minute/(g/litre) [2 grains Ca ++ /gallon/minute/(gram/gallon)] of aluminosilicate (anhydrous basis), and which generally lies within the range of from 130 mg equivalent of CaCO 3 /litre/minute/(gram/litre) [2 grains/gallon/minute/(gram/gallon)] to 390 mg equivalent of CaCO 3 /litre/minute/(gram/litre) [6 grains/gallon/minute/(gram/gallon)], based on calcium ion hardness.
  • Optimum aluminosilicates for builder purposes exhibit a calcium ion exchange rate of at least 260 mg equivalent of CaCO 3 /litre/minute/(gram/litre) [4 grains/gallon/minute/(gram/gallon)].
  • Aluminosilicate ion exchange materials useful in the practice of this invention are commercially available and can be naturally occurring materials, but are preferably synthetically derived. A method for producing aluminosilicate ion exchange materials is discussed in US Patent No. 3,985,669.
  • Preferred synthetic crystalline aluminosilicate ion exchange materials useful herein are available under the designations Zeolite A, Zeolite B, Zeolite P, Zeolite MAP, Zeolite X, Zeolite HS and mixtures thereof.
  • the crystalline aluminosilicate ion exchange material is Zeolite A and has the formula Na 12 [(ALO 2 ) 12 (SiO 2 ) 12 ].
  • xH 2 O wherein x is from 20 to 30, especially 27.
  • Suitable water-soluble monomeric and oligomeric carboxylate builders can be selected from a wide range of compounds but such compounds preferably have a first carboxyl logarithmic acidity constant (pK 1 ) of less than 9, preferably of between 2 and 8.5, more preferably between 4 and 7.5.
  • pK 1 first carboxyl logarithmic acidity constant
  • the logarithmic acidity constant is defined by reference to the equilibrium where A - is the singly ionized anion of the carboxylate builder salt.
  • acidity constants are defined as 25°C and at zero ionic strength.
  • Literature values are taken where possible (see Stability Constants of Metal-Ion Complexes, Special Publication No. 25, the Chemical Society, London): where doubt arises they are determined by potentiometric titration using a glass electrode.
  • the carboxylate or polycarboxylate builders can be monomeric or oligomeric in type although monomeric carboxylates are generally preferred for reasons of cost and performance.
  • Monomeric and oligomeric builders can be selected from acyclic, alicyclic, heterocyclic and aromatic carboxylates having the general formulae
  • Suitable carboxylates containing one carboxy group include lactic acid, glycollic acid and ether derivatives thereof as disclosed in Belgian Patent Nos. 831,368, 821,369 and 821,370.
  • Polycarboxylates containing two carboxy groups include the water-soluble salts of succinic acid, malonic acid, (ethylenedioxy) diacetic acid, maleic acid, diglycollic acid, tartaric acid, tartronic acid and fumaric acid, as well as the ether carboxylates described in German Offenlegenschrift 2,446,686, and 2,446,687 and US Patent No. 3,935,257 and the sulfinyl carboxylates described in Belgian Patent No. 840,623.
  • Polycarboxylates containing three carboxy groups include, in particular, water-soluble citrates, aconitrates and citraconates as well as succinate derivatives such as the carboxymethyloxysuccinates described in British Patent No. 1,379,241, lactoxysuccinates described in British Patent No. 1,389,732, and aminosuccinates described in Netherlands Application 7205873, and the oxypolycarboxylate materials such as 2-oxa-1,1,3-propane tricarboxylates described in British Patent No. 1,387,447.
  • Polycarboxylates containing four carboxy groups include oxydisuccinates disclosed in British Patent No. 1,261,829,1, and the 1,2,2-ethane tetracarboxylates, 1,1,3,3-propane tetracarboxylates and 1,1,2,3-propane tetracarboxylates.
  • Polycarboxylates containing sulfo substituents include the sulfosuccinate derivatives disclosed in British Patent Nos. 1,398,421 and 1,398,422 and in US Patent No. 3,936,448, and the sulfonated pyrolysed citrates described in British Patent No. 1,082,179, while polycarboxylates containing phosphone substituents are disclosed in British Patent No. 1,439,000.
  • Alicyclic and heterocyclic polycarboxylates include cyclopentane-cis, cis,cis-tetracarboxylates, cyclopentadienide pentacarboxylates, 2,3,4,5-tetrahydrofuran - cis, cis, cis-tetracarboxylates, 2,5-tetrahydrofuran -cis - dicarboxylates, 2,2,5,5-tetrahydrofuran - tetracarboxylates, 1,2,3,4,5,6-hexane -hexacarboxylates and carboxymethyl derivatives of polyhydric alcohols such as sorbitol, mannitol and xylitol.
  • Aromatic polycarboxylates include mellitic acid, pyromellitic acid and the phthalic acid derivatives disclosed in British Patent No. 1,425,343.
  • the preferred polycarboxylates are hydroxycarboxylates containing up to three carboxy groups per molecule, more particularly citrates.
  • the parent acids of the monomeric or oligomeric polycarboxylate chelating agents or mixtures thereof with their salts eg citric acid or citrate/citric acid mixtures are also contemplated as components of builder systems useful in the present inention.
  • Suitable water soluble organic salts are the homo- or co-polymeric polycarboxylic acids or their salts in which the polycarboxylic acid comprises at least two carboxyl radicals separated from each other by not more than two carbon atoms.
  • Polymers of the latter type are disclosed in GB-A-1,596,756.
  • Examples of such salts are polyacrylates of MWt 2000-5000 and their copolymers with maleic anhydride, such copolymers having a molecular weight of from 20,000 to 70,000, especially about 40,000. These materials are normally used at levels of from 0-.5% to 10% by weight, more preferably from 0.75% to 8%, most preferably from 1% to 6% by weight of the composition.
  • the non-phosphate builder ingredient will comprise from 5% to 80% by weight of the composition, more preferably from 30% to 60% by weight.
  • a sodium aluminosilicate such as Zeolite A will comprise from 20% to 60% by weight of the total amount of builder
  • a monomeric or oligomeric carboxylate will comprise from 10% to 30% by weight of the total amount of builder
  • a crystalline layered silicate will comprise from 10% to 65% by weight of the total amount of builder.
  • the builder ingredient preferably also incorporates a combination of auxiliary inorganic and organic builders such as sodium carbonate and maleic anhydride/acrylic acid copolymers in amounts of up to 35% by weight of the total builder.
  • compositions of the invention may also contain organic peroxyacids of which a paerticularly preferred class are the amide substituted peroxyacids of general formulae : wherein R 1 is an aryl or alkaryl group with from about 1 to about 14 carbon atoms, R 2 is an alkylene, arylene, and alkarylene group containing from about 1 to 14 carbon atoms, and R 5 is H or an alkyl, aryl, or alkaryl group containing 1 to 10 carbon atoms and L can be essentially any leaving group.
  • R 1 preferably contains from about 6 to 12 carbon atoms.
  • R 2 preferably contains from about 4 to 8 carbon atoms.
  • R 1 may be straight chain or branched alkyl, substituted aryl or alkylaryl containing branching, substitution, or both and may be sourced from either synthetic sources or natural sources including for example, tallow fat. Analogous structural variations are permissible for R 2 . The substitution can include alkyl, aryl, halogen, nitrogen, sulphur and other typical substituent groups or organic compounds.
  • R 5 is preferably H or methyl. R 1 and R 5 should not contain more than 18 carbon atoms total. Organic peroxyacid compounds of this type are described in EP-A-0170386.
  • organic peroxyacids include diperoxy dodecanedioc acid, diperoxy tetra decanedoic acid, diperoxyhexadecanedoic acid, mono- and diperazelaic acid, mono-and diperbrassylic acid, monoperoxy phthalic acid, perbenzoic acid, and their salts as disclosed in, for example, EP-A-0341 947.
  • Preferred heavy metal sequestrants for inclusion in the detergent compositions of the invention include the organic phosphonates, including amino alkylene poly (alkylene phosphonates), alkali metal ethane 1-hydroxy diphosphonates, nitrilo trimethylene phosphonates, ethylene diamine tetra methylene phosphonates and diethylene triamine penta methylene phsophonates.
  • organic phosphonates including amino alkylene poly (alkylene phosphonates), alkali metal ethane 1-hydroxy diphosphonates, nitrilo trimethylene phosphonates, ethylene diamine tetra methylene phosphonates and diethylene triamine penta methylene phsophonates.
  • Such phosphonate compounds may be present either in their acid form or as a complex of either an alkali or alkaline metal ion, the molar ratio of said metal ion to said phosphonate compound being at least 1 : 1.
  • Organic phosphonate compounds, and mixtures thereof, may be present in the detergent compositions of the invention at levels of from 0.05 % to 10% by weight of the composition, preferably 0.1% to 2% by weight, most preferably 0.2% to 0.6% by weight.
  • compositions in accordance with the invention can also contain other optional detergent ingredients.
  • Anti-redeposition and soil-suspension agents, optical brighteners, soil release agents, dyes and pigments are examples of such optional ingredients and can be added in varying amounts as desired.
  • Anti-redeposition and soil-suspension agents suitable herein include cellulose derivatives such as methylcellulose, carboxymethylcellulose and hydroxyethylcellulose, and homo- or co-polymeric polycarboxylic acids or their salts.
  • Polymers of this type include copolymers of maleic anhydride with ethylene, methylvinyl ether or methacrylic acid, the maleic anhydride constituting at least 20 mole percent of the copolymer. These materials are normally used at levels of from 0.5% to 10% by weight, more prefeably from 0.75% to 8%, most preferably from 1% to 6% by weight of the composition.
  • polyethylene glycols particularly those of molecular weight 1000 - 10000, more particularly 2000 to 8000 and most preferably about 4000. These are used at levels of from 0.20% to 5%, more preferably from 0.25% to 2.5% by weight. These polymers and the previously mentioned homo-or co-polymeric polycarboxylate salts are valuable for improving whiteness maintenance, fabric ash deposition, and cleaning performance of clay, proteinaceous and oxidizable soils in the presence of transition metal impurities.
  • Preferred optical brighteners are anionic in characters, examples of which are disodium 4,4 1 -bis-(2-diethanolomino-4-anilino-s- triazin-6-ylamino)stilbene-2:2 1 disulphonate, disodium 4, 4 1 -bis-(2-morpholino-4-anilino-s-triazin-6-ylamino stilbene-2:2 1 - disulphonate, disodium 4, 4 1 - bis-(2,4-dianilino-s-triazin-6-ylamino)stilbene-2:2 1 - disulphonate, monosodium 4 1 , 4 11 -bis-(2,4-dianilino-s-triazin-6 ylamino) stilbene-2-sulphonate, disodium 4, 4 1 -bis-(2-anilino-4-(N-methyl-N-2-hydroxyethylamino)-s-triazin-6-ylamino)stilbene-2,2 1 - dis
  • Soil-release agents useful in composition of the present invention are conventionally copolymers or terpolymers of terephthalic acid with ethylene glycol and/or propylene glycol units in various arrangements. Examples of such polymers are disclosed in the commonly assigned US Patent Nos. 4116885 and 4711730 and European Published Patent Application No. 0272033.
  • a particular preferred polymer in accordance with EP-A-0272033 has the formula (CH 3 (PEG) 43 ) 0.75 (POH) 0.25 [T-PO) 2.8 (T-PEG) 0.4 ]T(PO-H) 0.25 ((PEG) 43 CH 3 ) 0.75 where PEG is -(OC 2 H 4 )0-,PO is (OC 3 H 6 O) and T is (pCOC 6 H 4 CO).
  • Certain polymeric materials such as polyvinyl pyrrolidones typically of MW 5000-20000, preferably 10000-15000, also form useful agents in preventing the transfer of labile dyestuffs between fabrics during the washing process.
  • a suds suppressor exemplified by silicones, and silica-silicone mixtures.
  • Silicones can be generally represented by alkylated polysiloxane materials while silica is normally used in finely divided forms, exemplified by silica aerogels and xerogels and hydrophobic silicas of various types. These materials can be incorporated as particulates in which the suds suppressor is advantageously releasably incorporated in a water-soluble or water-dispersible, substantially non-surface-active detergent-impermeable carrier.
  • the suds suppressor can be dissolved or dispersed in a liquid carrier and applied by spraying on to one or more of the other components.
  • useful silicone suds controlling agents can comprise a mixture of an alkylated siloxane, of the type referred to hereinbefore, and solid silica. Such mixtures are prepared by affixing the silicone to the surface of the solid silica.
  • a preferred silicone suds controlling agent is represented by a hydrophobic silanated (most preferably trimethyl-silanated) silica having a particle size in the range from 10 nanometers to 20 nanometers and a specific surface area above 50 m 2 /g, intimately admixed with dimethyl silicone fluid having a molecular weight in the range from about 500 to about 200,000 at a weight ratio of silicone to silanated silica of from about 1:1 to about 1:2.
  • a preferred silicone suds controlling agent is disclosed in Bartollota et al US Patent 3,933,672.
  • Other prticularly useful suds suppressors are the self-emulsifying silicone suds suppressors, described in German Patent Application DTOS 2,646,126 published April 28, 1977.
  • An example of such a compound is DC-544, commercially available from Dow Corning, which is a siloxane/glycol copolymer.
  • the suds suppressor described above are normally employed at levels of from 0.001 % to 0.5% by weight of the composition, preferably from 0.01% to 0.1% by weight.
  • the preferred methods of incorporation comprise either application of the suds suppressors in liquid form by spray-on to one or more of the major components of the composition or alternatively the formation of the suds suppressors into separate particulates that can then be mixed with the other solid components of the composition.
  • the incorporation of the suds modifiers as separate particulates also permits the inclusion therein of other suds controlling materials such as C 20 -C 24 fatty acids, microcrystalline waxes and high MW copolymers of ethylene oxide and propylene oxide which would otherwise adversely affect the dispersibility of the matrix. Techniques for forming such suds modifying particulates are disclosed in the previously mentioned Bartollotta et al US Patent No. 3,933,672.
  • An other optional ingredient useful in the present invention is one or more enzymes.
  • Preferred enzymatic materials include the commercially available amylases, neutral and alkaline proteases, lipases, esterases and cellulases conventionally incorporated into detergent compositions. Suitable enzymes are discussed in US Patents 3,519,570 and 3,533,139.
  • Preferred commercially available protease enzymes include those sold under the tradnames Alcalase and Savinase by Novo Industries A/S (Denmark) and Maxatase by International Bio-Synthetics, Inc. (The Netherlands).
  • Preferred amylases include, for example, -amylases obtained from a special strain of B licheniforms, described in more detail in GB-1,296,839 (Novo).
  • Preferred commercially available amylases include for example, Rapidase, sold by International Bio-Synthetics Inc. and Termamyl, sold by Novo Industries A/S.
  • An especially preferred lipase enzyme is manufactured and sold by Novo Industries A/S (Denmark) under the trade name Lipolase (Biotechnology Newswatch, 7 March 1988, page 6) and mentioned along with other suitable lipases in EP-A-0258068 (Novo).
  • Levels of smectite clay are normally in the range from 5% to 15%, more preferably from 8% to 12% by weight, with the material being added as a dry mixed component to the remainder of the formulation.
  • Organic fabric softening agents such as the water-insoluble tertiary amines or dilong chain amide materials are incorporated at levels of from 0.5% to 5% by weight, normally from 1% to 3% by weight, whilst the high molecular weight polyethylene oxide materials and the water soluble cationic materials are added at levels of from 0.1 % to 2%, normally from 0.15% to 1.5% by weight.
  • these materials can be added to the aqueous slurry fed to the spray drying tower, although in some instances it may be more convenient to add them as a dry mixed particulate, or spray them as a molten liquid on to other solid components of the composition.
  • a feature of the composition of the present invention is that they are of relatively high density in comparison with conventional laundry detergent compositions.
  • Such high density compositions have become known as concentrated products and are characterised by a bulk density of at least 650 g/litre, more usually at least 700 g/litre and more preferably in excess of 800 g/litre.
  • Bulk density is measured by means of a simple funnel and cup device consisting of a conical funnel moulded rigidly on a base and provided with a flap valve at its lower extremity to allow the contents of the funnel to be emptied into an axially aligned cylindrical cup disposed below the funnel.
  • the funnel is 130 mm high and has internal diameters of 130 mm and 40 mm at its respective upper and lower extremities. It is mounted so that the lower extremity is 140 mm above the upper surface of the base.
  • the cup has an overall height of 90 mm, an internal height of 87 mm and an internal diameter of 84 mm. Its nominal volume is 500 ml.
  • the funnel is filled with powder by hand pouring, the flap valve is opened and powder allowed to overfill the cup.
  • the filled cup is removed from the frame and excess powder removed from the cup by passing a straight edged implement eg; a knife, across its upper edge.
  • the filled cup is then weighed and the value obtained for the weight of powder doubled to provide a bulk density in g/litre. Replicate measurements are made as required.
  • compositions of the present invention incorporate at least one multi-ingredient component ie they do not comprise compositions formed merely by dry-mixing individual ingredients.
  • compositions in which each individual ingredient is dry-mixed are generally dusty, slow to dissolve and also tend to cake and develop poor particle flow characteristics in storage.
  • compositions of the invention can be made via a variety of methods including dry mixing, spray drying, agglomeration and granulation and preferred methods involve combinations of these techniques.
  • a preferred method of making the composition involves a combination of spray drying, agglomeration in a high speed mixer and dry mixing.
  • Preferred detergent compositions in accordance with the invention comprise at least two particulate multi-ingredient components.
  • the first component comprises at least 15%, conventionally from 25% to 50%, but more preferably no more than 35% by weight of the composition and the second component from 1 % to 50%, more preferably 10% to 40% by weight of the composition.
  • one multi-ingredient component comprises an agglomerate of non-spray-dried ingredients together with a second multi-ingredient component comprising a spray-dried powder.
  • the first component comprises a particulate incorporating an anionic surfactant in an amount of from 0.75% to 40% by weight of the powder and one or more inorganic and/or organic salts in an amount of from 99.25% to 60% by weight of the powder.
  • the particulate can have any suitable form such as granules, flakes, prills, marumes or noodles but is preferably granular.
  • the granules themselves may be agglomerates formed by pan or drum agglomeration or by in-line mixers but are customarily spray dried particles produced by atomising an aqueous slurry of the ingredients in a hot air spream which removes most of the water.
  • the spray dried granules are then subjected to densification steps, eg by high speed cutter mixers and./or compacting mills, to increase density before being reagglomerated.
  • densification steps eg by high speed cutter mixers and./or compacting mills
  • the first component is described hereinafter as a spray dried powder.
  • Suitable anionic surfactants for the purposes of the first component have been found to be slowly dissolving linear alkyl sulfate salts in which the alkyl group has an average of from 16 to 22 carbon atoms, and linear alkyl carboxylate salts in which the alkyl group has an average of from 16 to 24 carbon atoms.
  • the alkyl groups for both types of surfactant are preferably derived from natural fats such as tallow. Shorter chain alkyl sulfates or carboxylates, in which the alkyl group is derived from sources comprising a mixture of alkyl moieties more than 40% of which contain 14 or less carbon atoms, are less suitable as they cause the first component to form a gel like mass during dissolution.
  • the level of anionic surfactant in the spray dried powder forming the first component is from 0.75% to 40% by weight, more usually 2.5% to 25%, preferably from 3% to 20% and most preferably from 5% to 15% by weight.
  • Water-soluble surfactants such as linear alkyl benzene sulphonates or C 14 -C 15 alkyl sulphates can be included or alternatively may be applied subsequently to the spray dried powder by spray on.
  • the other major ingredient of the spray dried powder is one or more inorganic or organic salts that provide the crystalline structure for the granules.
  • the inorganic and/or organic salts may be water-soluble or water-insoluble, the latter type being comprised by the, or the major part of the, water-insoluble builders where these form part of the builder ingredient.
  • Suitable water soluble inorganic salts include the alkali metal carbonates and bicarbonates.
  • Alkali metal silicates other than crystalline layered silicates can also be present in the spray dried granule provided that aluminosilicate does not form part of the spray dried component.
  • an aluminosilicate zeolite forms the, or part of the, builder ingredient, it is preferred that it is not added directly by dry mixing to the other components, but is incorporated into the multi-ingredient component(s).
  • any silicate present should not form part of the spray-dried granule.
  • incorporation of the silicate can be achieved in several ways, eg by producing a separate silicate-containing spray-dried particulate, by incorporating the silicate into an agglomerate of other ingredients, or more preferably by adding the silicate as a dry mixed solid ingredient.
  • the first component can also include up to 15% by weight of miscellaneous ingredients such as brighteners, anti-re-deposition agents, photoactivated bleaches and heavy metal sequestering agents.
  • miscellaneous ingredients such as brighteners, anti-re-deposition agents, photoactivated bleaches and heavy metal sequestering agents.
  • the first component is a spray dried powder it will normally be dried to a moisture content of from 7% to 11% by weight, more preferably from 8% to 10% by weight of the spray dried powder.
  • Moisture contents of powders produced by other processes such as agglomeration may be lower and can be in the range 1-10% by weight.
  • the particle size of the first component is conventional and preferably not more than 5% by weight should be above 1.4 mm, while not more than 10% by weight should be less than 0.15 mm in maximum dimension. Preferably at least 60%, and most preferably at least 80%, by weight of the powder lies between 0.9 mm and 0.25 mm in size.
  • the bulk density of the particles from the spray drying tower is conventionally in the range from 540 to 600 g/litre and this is then enhanced by further processing steps such as size reduction in a high speed cutter/mixer followed by compaction. Alternatively, processes other than spray drying may be used to form a high density particulate directly.
  • a second component of a preferred composition in accordance with the invention is another multi-ingredient particulate containing a water soluble surfactant.
  • This water-soluble surfactant may be anionic, nonionic, cationic or semipolar in type or a mixture of any of these. Suitable surfactants are listed hereinbefore but preferred surfactants are C 14 -C 15 alkyl sulphates linear C 11 -C 15 alkyl benzene sulphonates and fatty C 14 -C 18 methyl ester sulphonates.
  • the second component may have any suitable physical form ie; it may take the form of flakes, prills, marumes, noodles, ribbons or granules which may be spray-dried or non spray-dried agglomerates.
  • the second component could in theory comprise the water soluble surfactant on its own, in practice at least one organic or inorganic salt is included to facilitate processing. This provides a degree of crystallinity, and hence acceptable flow characteristics, to the particulate and may be any one or more of the organic or inorganic salts present in the first component.
  • the particle size range of the second component is not critical but should be such as to obviate segregation from the particles of the first component when blended therewith. Thus not more than 5% by weight should be above 1.4 mm while not more than 10% should be less than 0.15 mm in maximum dimension.
  • the bulk density of the second component will be a function of its mode of preparation.
  • the preferred form of the second component is a mechanically mixed agglomerate which may be made by adding the ingredients dry or with an agglomerating agent to a pan agglomerator, Z blade mixer or more preferably an in-line mixer such as those manufactured by Schugi (Holland) BV 29 Chroomstraat 8211 AS, Lelystad, Netherlands and Gebruder Lodige Maschinenban GmbH, D-4790 Paderborn 1, Elsenerstrasse 7-9, Postfach 2050 FRG.
  • the second component can be given a bulk density in the range from 650 g/litre to 1190 g/litre more preferably from 750 g/litre to 850 g/litre.
  • compositions include a level of alkali metal carbonate in the second component corresponding to an amount of from 3% to 15% by weight of the composition, more preferably from 5% to 12% by weight. This will preferably provide a level of carbonate in the second component of from 20% to 40% by weight.
  • a highly preferred ingredient of the second component is also a hydrated water insoluble aluminosilicate ion exchange material of the synthetic zeolite type, described hereinbefore, present at from 10% to 35% by weight of the second component.
  • the amount of water insoluble aluminosilicate material incorporated in this way is from 1% to 10% by weight of the composition, more preferably from 2% to 8% by weight.
  • the surfactant salt is formed in situ in an inline mixer.
  • the liquid acid form of the surfactant is added to a mixture of particulate anhydrous sodium carbonate and hydrated sodium aluminosilicate in a continuous high speed blender such as a lodige C6 mixer and neutralised to form the surfactant salt whilst maintaining the particulate nature of the mixture.
  • the resultant agglomerated mixture forms the second component which is then added to other components of the product.
  • the surfactant salt is pre-neutralised and added as a viscous paste to the mixture of the other ingredients.
  • the mixer serves merely to agglomerate the ingredients to form the second component.
  • part of the spray dried product comprising the first granular component is diverted and subjected to a low level of nonionic surfactant spray-on before being reblended with the remainder.
  • the second granular component is made using the preferred process described above.
  • the first and second components together with other dry mix ingredients such as any carboxylate chelating agent, the sodium percarbonate bleach, bleach activator, soil-release polymer, silicate of conventional or crystalline layered type and enzyme are then fed to a conveyor belt, from which they are transferred to a horizontally rotating drum in which perfume and silicone suds suppressor are sprayed on to the product.
  • a further drum mixing step is employed in which a low (approx.
  • a dispensing device containing an effective amount of granular detergent product is introduced into the drum of a washing machine before the commencement of the wash cycle.
  • What constitutes an effective amount of granular detergent product for use in the process described here in above will depend on the volume and weight of the laundry load to be washed. Use of between 70-150 g of product would be typical for a normal wash load of between 2-6 kg of averagely soiled laundry.
  • the dispensing device is a container for the detergent product which is used to deliver the product directly into the drum of the washing machine. Its volume capacity should be such as to be able to contain sufficient detergent product as would normally be used in a washing process as hereinbefore described.
  • the dispensing device containing the detergent product is placed inside the drum.
  • water is introduced into the drum and the drum periodically rotates.
  • the design of the dispensing device should be such that it permits containment of the dry detergent product but then allows release of this product during the wash cycle in response to its agitation as the drum rotates and also as a result of its immersion in the wash water.
  • the device may possess a number of openings through which the product may pass.
  • the device may be made of a material which is permeable to liquid but impermeable to the solid product, which will allow release of dissolved product.
  • the detergent product will be rapidly released at the start of the wash cycle thereby providing transient localised high concentrations of product in the drum of the automatic washing machine at this stage of the wash cycle.
  • Preferred dispensing devices are reusable and are designed in such a way that container integrity is maintained in both the dry state and during the wash cycle.
  • Especially preferred dispensing devices for use in accord with the invention have been described in the following patents; GB-B-2, 157, 717, GB-B-2, 157, 718, EP-A-0201376, EP-A-0288345 and EP-A-0288346.
  • An article by J.Bland published in Manufacturing Chemist, November 1989, pages 41-46 also describes especially preferred dispensing devices for use with granular laundry products which are of a type commonly know as the "granulette”.
  • Another preferred means of carrying out the process of the invention is to introduce the composition into the liquid surrounding the fabrics that are in the drum via a reusable dispensing device having walls that are permeable to liquid but impermeable to the solid composition.
  • European Patent Application Publication Nos. 0343069 & 0343070 disclose a device comprising a flexible sheath in the form of a bag extending from a support ring defining an orifice, the orifice being adapted to admit to the bag sufficient product for one washing cycle in a washing process. A portion of the washing medium flows through the orifice into the bag, dissolves the product, and the solution then passes outwardly through the orifice into the washing medium.
  • the support ring is provided with a masking arrangemnt to prevent egress of wetted, undissolved, product, this arrangement typically comprising radially extending walls extending from a central boss in a spoked wheel configuration, or a similar structure in which the walls have a helical form.
  • the dispensing device may be a flexible container, such as a bag or pouch.
  • the bag may be of fibrous construction coated with a water impermeable protective material so as to retain the contents, such as is disclosed in European published Patent Application No. 0018678.
  • it may be formed of a water-insoluble synthetic polymeric material provided with an edge seal or closure designed to rupture in aqueous media as disclosed in European published Patent Application Nos. 0011500, 0011501, 0011502, and 0011968.
  • a convenient form of water frangible closure comprises a water soluble adhesive disposed along and sealing one edge of a pouch formed of a water impermeable polymeric film such as polyethylene or polypropylene.
  • the abbreviated component identifications have the following meanings :
  • composition A in accord with the invention is noted to give consistently better removal of bleachable stains as compared to composition B which is a comparative product containing 2.8 ratio silicate coated percarbonate.
  • Composition A is noted to perform, on average, equally well as composition C which contains perborate as the only peroxygen bleach.
  • the following particulate detergent composition with a bulk density of approximately 670g/litre was prepared in accordance with the invention : D LAS 9.5 TAS 0.5 25E3 3.2 Zeolite A 18.0 Citrate 1.5 MA/AA 4.0 Carbonate 9.0 TAED 5.0 Percarbonate (CO 3 /SO 4 coated) 17.0 DETPMP 0.4 MgSO4 0.4 Enzyme 1.4 CMC 0.5 NaSKS6 7.0 Citric 2.0 Bicarbonate 7.0 Water and minors up to 100
  • composition D gives good washing performance when used in a low temperature ( ⁇ 50°C) laundry process.

Claims (7)

  1. Verfahren zum Waschen von Wäsche in einer Haushaltswaschmaschine, wobei eine Dispensiervorrichtung, welche eine wirksame Menge einer granulären Wäschewaschmittelzusammensetzung enthält, in die Trommel der Waschmaschine vor Beginn der Wäsche eingebracht wird, wobei die Dispensiervorrichtung die progressive Freisetzung der granulären Wäschewaschmittelzusammensetzung in die Waschlauge während der Wäsche ermöglicht, und wobei die granuläre Wäschewaschmittelzusammensetzung eine Schüttdichte von größer als 650 g/Liter besitzt und umfasst:
    (a) 1 bis 60 Gew.-% eines Alkalimetallpercarbonat-Bleichmittels, beschichtet mit einem gemischten Salz, umfassend ein Alkalimetallcarbonat und ein Alkalimetallsulfatsalz: und
    (b) 1 bis 40 Gew.-% eines Peroxysäure-Bleichaktivators, und wobei:
    (i) das Gewichtsverhältnis des beschichteten Percarbonat-Bleichmittels zu dem Peroxysäure-Bleichaktivator im Bereich von 1:1 bis 10:1 liegt: und
    (ii) das Verfahren bei einer Temperatur von nicht mehr als 50°C durchgeführt wird.
  2. Verfahren nach Anspruch 1, wobei die Wäschewaschmittelzusammensetzung umfasst:
    (a) 3 bis 30 Gew.-% Tensid, gewählt aus anionischen, kationischen, nichtionischen, ampholytischen und zwitterionischen Tensiden und Mischungen hiervon: und
    (b) 5 bis 80 Gew.-% Nichtphosphat-Buildersalz, und Mischungen hiervon.
  3. Verfahren nach Anspruch 1 und/oder 2, wobei die Wäschewaschmittelzusammensetzung 0,05 bis 10 Gew.-% einer organischen Phosphonatverbindung oder eines Alkalimetall- oder Erdalkalimetallssalzes hiervon, oder Mischungen hiervon umfasst.
  4. Verfahren nach mindestens einem der Ansprüche 1-3, wobei die granuläre Wäschewaschmittelzusammensetzung eine Schüttdichte von größer als 800 g/Liter besitzt.
  5. Verfahren nach mindestens einem der Ansprüche 1-4, wobei das Verfahren bei einer Temperatur von nicht mehr als 40°C durchgeführt wird.
  6. Verfahren nach mindestens einem der Ansprüche 2-5, wobei das Nichtphosphat-Buildersalz ein kristallines Schichtsilikatmaterial der Formel NaM(SixO2x+1)·yH2O ist, worin M Natrium oder Wasserstoff ist, x eine Zahl von 1,9 bis 4 ist und y eine Zahl von 0 bis 20 ist.
  7. Verfahren nach Anspruch 6, wobei das kristalline Schichtsilikatmaterial δ-Na2Si2O5 ist.
EP93916935A 1992-07-14 1993-07-02 Verfahren zum einspülen eines percarbonathaltigen textilwaschmittels mit hoher schüttdichte Expired - Lifetime EP0650518B1 (de)

Applications Claiming Priority (3)

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GB9214890 1992-07-14
GB929214890A GB9214890D0 (en) 1992-07-14 1992-07-14 Washing process
PCT/US1993/006302 WO1994001521A1 (en) 1992-07-14 1993-07-02 Process of dispensing a high bulk density percarbonate-containing laundry detergent

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US5705466A (en) * 1993-08-17 1998-01-06 The Procter & Gamble Company High bulk density granular detergents containing a percarbonate bleach and a powdered silicate
DE69422100D1 (de) * 1993-08-17 2000-01-20 Procter & Gamble Percarbonat-Bleichmittel enthaltende Waschmittelzusammensetzungen
EP0736085B2 (de) 1993-12-21 2009-12-16 The Procter & Gamble Company Percarbonat , amylase und protease enthaltende waschmittelzusammensetzungen
GB9407533D0 (en) * 1994-04-13 1994-06-08 Procter & Gamble Detergent compositions
GB9407276D0 (en) * 1994-04-13 1994-06-08 Procter & Gamble Detergent compositions
GB2297978A (en) * 1995-02-15 1996-08-21 Procter & Gamble Detergent compositions containing amylase
DE19629381A1 (de) * 1996-07-20 1998-01-22 Eilenburger Elektrolyse & Umwelttechnik Gmbh Granulierter Aktivsauerstoffträger
CN1131300C (zh) 1997-05-30 2003-12-17 尤尼利弗公司 易流动的颗粒洗涤剂组合物
GB9711356D0 (en) 1997-05-30 1997-07-30 Unilever Plc Particulate detergent composition
GB9711359D0 (en) 1997-05-30 1997-07-30 Unilever Plc Detergent powder composition
GB9711350D0 (en) * 1997-05-30 1997-07-30 Unilever Plc Granular detergent compositions and their production
US6294512B1 (en) * 1998-01-13 2001-09-25 The Procter & Gamble Company Granular compositions having improved dissolution
US10280386B2 (en) 2015-04-03 2019-05-07 Ecolab Usa Inc. Enhanced peroxygen stability in multi-dispense TAED-containing peroxygen solid
US9783766B2 (en) 2015-04-03 2017-10-10 Ecolab Usa Inc. Enhanced peroxygen stability using anionic surfactant in TAED-containing peroxygen solid
EP3810743B1 (de) 2018-06-15 2024-03-13 Ecolab USA Inc. Verbesserte persauerstoffstabilität unter verwendung von fettsäure in einem persauerstofffeststoff enthaltenden bleichaktivator

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US4105827A (en) * 1973-04-20 1978-08-08 Interox Particulate peroxygen compounds coated with sodium sesquicarbonate or Na2 SO4 mNa2 CO3
DE3434854A1 (de) * 1984-09-22 1986-04-03 Henkel KGaA, 4000 Düsseldorf Verfahren zur herstellung einer koernigen, freifliessenden waschmittelkomponente
GB8811447D0 (en) * 1988-05-13 1988-06-15 Procter & Gamble Granular laundry compositions
GB9021761D0 (en) * 1990-10-06 1990-11-21 Procter & Gamble Detergent compositions

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GB9214890D0 (en) 1992-08-26
DE69331905D1 (de) 2002-06-13
ATE217341T1 (de) 2002-05-15
EP0650518A4 (de) 1999-04-28
EG20548A (en) 1999-07-31
ES2176205T3 (es) 2002-12-01
DE69331905T2 (de) 2002-12-12
JPH07509281A (ja) 1995-10-12
WO1994001521A1 (en) 1994-01-20

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