EP0880581A1 - Verfahren zur herstellung einer teilchenförmigen bleichmittelaktivatorkomponente - Google Patents

Verfahren zur herstellung einer teilchenförmigen bleichmittelaktivatorkomponente

Info

Publication number
EP0880581A1
EP0880581A1 EP97902071A EP97902071A EP0880581A1 EP 0880581 A1 EP0880581 A1 EP 0880581A1 EP 97902071 A EP97902071 A EP 97902071A EP 97902071 A EP97902071 A EP 97902071A EP 0880581 A1 EP0880581 A1 EP 0880581A1
Authority
EP
European Patent Office
Prior art keywords
bleach activator
particulate
process according
particulate component
weight
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.)
Withdrawn
Application number
EP97902071A
Other languages
English (en)
French (fr)
Other versions
EP0880581A4 (de
Inventor
Sanjeev Sharma
David William York
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Procter and Gamble Co
Original Assignee
Procter and Gamble Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Procter and Gamble Co filed Critical Procter and Gamble Co
Priority to EP97902071A priority Critical patent/EP0880581A4/de
Publication of EP0880581A1 publication Critical patent/EP0880581A1/de
Publication of EP0880581A4 publication Critical patent/EP0880581A4/de
Withdrawn legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/39—Organic or inorganic per-compounds
    • C11D3/3902—Organic or inorganic per-compounds combined with specific additives
    • C11D3/3905—Bleach activators or bleach catalysts
    • C11D3/3935—Bleach activators or bleach catalysts granulated, coated or protected
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00—Special methods for preparing compositions containing mixtures of detergents
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00—Special methods for preparing compositions containing mixtures of detergents
    • C11D11/0082—Special methods for preparing compositions containing mixtures of detergents one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/0039—Coated compositions or coated components in the compositions, (micro)capsules
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/39—Organic or inorganic per-compounds
    • C11D3/3902—Organic or inorganic per-compounds combined with specific additives
    • C11D3/3905—Bleach activators or bleach catalysts
    • C11D3/3907—Organic compounds

Definitions

  • This invention relates to a process for the manufacture of a particulate bleach activator component.
  • EP-A-0 106 634 published on April 25th 1984, discloses an extrusion process using an axial or radial extruder. While not specifically mentioned it is known that these extruders typically operate at pressures well in excess of 25 bar.
  • the object of the invention is to provide a process for the manufacture of a particulate bleach activator component comprising the steps of:
  • particulate bleach activator component is substantially dust-free and still disperses and releases peracid rapidly upon contact with, or immersion in, wash solution containing peroxy acid bleach at typical domestic washing temperatures.
  • the breaking step may include a cutting or chopping step.
  • the breaking step is preferably carried out in a rotating disk type rounding unit, for example using a Marumeriser .
  • the particulate component comprises from 50% to 90% by weight of the bleach activator, the particulate component is dust-free. Even more preferably the particulate component further comprises: from 5% to 30% by weight of anionic surfactant; and from 0% to 10% by weight of a binding agent and from 0 to 20% of an acidic stabilising agent; and from 0 to 5% of a hydrotrope .
  • Particularly suitable bleach activators are caproyl oxybenzene sulfonate derivates; N,N,N 1 N 1 tetra acetylated compounds; benzoyloxybenzene sulphonate; benzoyl caprolactam; and mixtures thereof.
  • bleach activators are (6-octanamido-caproyl) oxybenzenesulfonate, (6-nonanamidocaproyl) oxy benzene sulfonate, (6-decanamido- caproyl) oxybenzenesulfonate, and mixtures thereof.
  • the particulate component may optionally be further treated by a coating and/or dusting step.
  • Bleach activators as defined herein include but are not limited to the following.
  • the solid peroxyacid bleach precursors of the present invention may comprise precursors containing one or more N- or O- acyl groups, which precursors can be selected from a wide range of classes.
  • Suitable classes include anhydrides, esters, imides 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-836988, 864,798, 1147871 and 2143231 and imides such as are disclosed in GB-A-855735 & 1246338.
  • a preferred precursor compounds is tetra acetyl ethylene diamine.
  • Particularly preferred precursor compounds are the amide substituted compounds of the following general formula:
  • 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.
  • R 2 can include alkyl, aryl, wherein said R 2 may also contain halogen, nitrogen, sulphur and other typical substituent groups or organic compounds.
  • R 5 is preferably H or methyl.
  • R 1 and R ⁇ should not contain more than 18 carbon atoms total. Amide substituted bleach activator compounds of this type are described in EP-A- 0170386.
  • L group The leaving group, hereinafter L group, must be sufficiently reactive for the perhydrolysis reaction to occur within the optimum time frame (e.g., a wash cycle) . However, if L is too reactive, this activator will be difficult to stabilize for use in a bleaching composition.
  • Preferred L groups are selected from the group consisting of:
  • R is an alkyl, aryl, or alkaryl group containing from 1 to 14 carbon atoms, R is
  • R is H or R 3
  • Y is H or a solubilizing group.
  • R may be substituted by essentially any functional group including, for example alkyl, hydroxy, alkoxy, halogen, amine, nitrosyl, amide and ammonium or alkyl ammmonium groups
  • the preferred solubilizing groups are -SO-, M , -CO ? M ,
  • M is an alkali metal, ammonium or substituted ammonium cation, with sodium and potassium being most preferred, and
  • X is a. alide, hydroxide, methylsulfate or acetate anion.
  • bleach activators of the above formulae include derivatives of caproyl oxybenzene sulfonate selected from (6-octanamido- caproyl)oxybenzenesulfonate, (6-nonanamidocaproyl) oxy benzene sulfonate, (6-decanamido- caproyl) oxybenzenesulfonate, and mixtures thereof as described in EP-A-0170386.
  • Such bleach activators have very poor water solubility (2.9g/l at 20C) and are therefore particularly suitable for processing via the present invention.
  • Still another preferred class of bleach activator is the class of alkyl percarboxylic acid bleach precursors.
  • Preferred alkyl percarboxylic acid precursors include nonanoyl oxy benzene sulphonate (NOBS described in US 4,412,934) and 3 , 5, 5-tri-methyl hexanoyl oxybenzene sulfonate (ISONOBS described in EP120,591) and salts thereof .
  • the peroxyacid bleach precursors are normally incorporated at a level of from 20% to 95% preferably 50% to 90% by weight of the particulate bleach activator component and most preferably at least 60% by weight thereof.
  • the peroxyacid bleach precursor is typically from 1% to 20% by weight, more preferably from 1% to 10% by weight, most preferably from 1% to 7% by weight of the detergent compositions.
  • the particles of particulate peroxyacid bleach activator component preferably have a particle size of from 250 micrometers to 2000 micrometers.
  • peroxyacid bleach precursors can be partially replaced by preformed peracids such as N,N phthaloylaminoperoxy acid (PAP) , nonyl amide of peroxyadipic acid (NAPAA) , 1,2 diperoxydodecanedioic acid (DPDA) and trimethyl ammonium propenyl imidoperoxy mellitic acid (TAPIMA) .
  • PAP N,N phthaloylaminoperoxy acid
  • NAPAA nonyl amide of peroxyadipic acid
  • DPDA 1,2 diperoxydodecanedioic acid
  • TAPIMA trimethyl ammonium propenyl imidoperoxy mellitic acid
  • Surfactants are useful in the particulate components of the present invention in particular as solubilising agents.
  • Nonlimiting examples of surfactants useful herein include the conventional C11-C18 alkyl benzene sulphonates ("LAS") and primary, branched-chain and random C10-C20 alkyl sulphates (“AS”) , the C10-C18 secondary (2,3) alkyl sulphates of the formula CH 3 (CH 2 ) x (CHOSO3 " M + ) CH 3 and CH 3 (CH 2 ) y (CHOSO3 " M + ) CH CH 3 where x and (y+1) are integers of at least 7, preferably at least about 9, and M is a water-solubilising cation, especially sodium, unsaturated sulphates such as oleyl sulphate, the C10-C18 alkyl alkoxy sulphates (“AExS” ; especially EO 1-7 ethoxy sulphates) , C10-C18 alkyl alk
  • the solubilising effect of the surfactant can be further enhanced by addition of a hydrotrope .
  • Hydrotropes suitable for use herein are selected from the group lower alkyl aryl sulphonate salts, C 6 -C 12 alkanols, C]_-Cg carboxyiic sulphate or sulphonate salts, urea, C ⁇ -C ⁇ hydrocarboxylates, C ⁇ -C ⁇ carboxylates and C 2 -C4 diacids and mixtures thereof.
  • Suitable lower alkyl aryl sulphonates are preferably C7-C9 alkyl aryl sulphonates and include sodium, potassium, calcium and ammonium xylene sulphonates, sodium, potassium, calcium and ammonium toluene sulphonates, sodium, potassium, calcium and ammonium cumene sulphonate, and sodium, potassium, calcium and ammonium napthalene sulphonates and mixtures thereof.
  • Suitable CI ⁇ C Q carboxyiic sulphate or sulphonate salts are any water soluble salts or organic compounds comprising 1 to 8 carbon atoms (exclusive of substituent groups) , which are substituted with sulphate or sulphonate and have at least one carboxyiic group.
  • the substituted organic compound may be cyclic, acylic or aromatic, i.e. benzene derivatives.
  • Preferred alkyl compounds have from 1 to 4 carbon atoms substiuted with sulphate or sulphonate and have from 1 to 2 carboxyiic groups.
  • hydrotropes examples include sulphosuccinate salts, sulphophthalic salts, sulphoacetic salts, m-sulphobenzoic acid salts and diesters sulphosuccinates, preferably the sodium or potassium salts as disclosed in US 3 915 903.
  • Suitable C1-C hydrocarboxylates, C1-C4 carboxylates for use herein include acetates and propionates and citrates.
  • Suitable C 2 -C4 diacids for use herein include succinic, glutaric and adipic acids.
  • hydrotrope compounds which deliver hydrotropic effects suitable for use herein as a hydrotrope include Cg-C ⁇ alkanols and urea.
  • Preferred hydrotropes for use herein are sodium, potassium, calcium and ammonium cumene sulphonate, sodium, potassium, calcium and ammonium xylene sulphonate, sodium, potassium, calcium and ammonium toluene sulphonate and mixtures thereof. Most preferred is sodium toluene sulphonate. According to the present invention the compositions comprise more up to 5% of hydrotrope, preferably from 0.5% to 3% .
  • Acid are useful in the particulate components of the present invention in particular as stabilising agents.
  • Suitable acids include fatty acids, glycolic acid, glutaric acid, citric acid and polymeric carboxyiic acids.
  • Binding agents are useful in the particulate components of the present invention.
  • Suitable binding agents include starch, cellulose and cellulose derivatives (e.g. Na-CMC) , sugar and film-forming polymers such as polymeric carboxyiic acid, including copolymers, polyvinyl pyrrolidone, polyvinyl acetate, . Co-polymers of acrylic and maleic acid are particularly preferred.
  • Extrusion is an essential step of the present invention. Any extruder which can be operated with the required composition at a pressure of less than 25 bar is suitable for use in the present invention. Dome extruders are highly preferred including single- and twin-screw extruders such as the TDG 110 manufactured by Fuji Paudal . In such extruders material is conveyed by the screws to an end die plate which is in the form of one or two perforated hemispheres. The diameter of the perforations is selected to give the desired final particle size. Radial extruders may also be suitable if they can be operated within the required pressure range.
  • the extrudate must be broken into short lengths . This step is referred to herein as "breaking" . Depending upon the nature of the extrudate it may break up into short lengths without the need for any mechanical action, or it may be cut or chopped by a mechanical device or knife.
  • a preferred means of breaking is via a rotating device (e.g. a baffled drum) or an agitating device (e.g. a dynamic mixer) .
  • a particularly preferred means of breaking is via a rotating disk type spheronising unit such as Model 700 manufactured by Cale.va and the Marumeriser" model QJ 1000 manufactured by Fuji Paudel. These units consist of a grooved horizontal plate rotating at high speed within a stationary vertical cylinder.
  • the broken extrudates are then preferably re-shaped by further action within the spheronising unit to form cylinders with rounded edges. Even more preferably the extrudates are further shaped into dumb-bells, ellipses and most preferably into spheres.
  • the ratio of the longest to shortest dimension of the final extrudate is preferably less than 10:1, more preferably less than 5:1, and most preferably less than 1.5:1.
  • Mean particle size is preferably in the range of from 0.25 mm to 2 mm.
  • the particulate component may be dried, preferably in a fluid-bed dryer and optionally coated or dusted to improve stability and/or handling properties.
  • Suitable coating agents include film forming materials such as synthetic polymers (such as copolymers of acrylic and maleic acid, polyvinyl alcohol, polyvinyl pyrrolidone polyethylene glycol) , natural polymers (such as Cellulose derivatives e.g. Na-CMC and Hydroxy propyl methyl cellulose) and surfactants such as Ethoxylated Alcohols .
  • Suitable dusting agents include zeolites, fumed and precipitated silicas.
  • the coating and dusting steps can be carried out in any suitable low shear mixing device, such as a drum mixer or a Loedige® ploughshare mixer.
  • the finished bleach activator particulate component is "dus -free".
  • dus -free what is meant herein is that the particle size of the particulate component less than 250 micrometers is less than 5%, preferably less than 1% and more preferably less than 0.5% by weight.
  • the particle size fraction is measured using a sieve with 250 micrometers (Tyler mesh 60) .
  • dust-free the particle must have sufficient resistance to prevent dust formation in handling and transportation,
  • the resistance of the bleach activator particulate to form dust upon handling is measured by a Heubach dus -meter (manufactured by Heubach Engineering GmbH, D-33 4 Langelsheim, Germany) and is such that less than lOO g of dust per gram of bleach activator particles is generated in the test. More preferably the amount of dust generated is less than 50mg/g and even more preferably less than 5mg/g.
  • the principle of the Heubach dustmeter is that four steel balls are placed together with the sample of bleach activator particles into a sample container. The balls stress_the sample by means of agitation.
  • Preferred bulk density of the particulate component is greater than 300 g/1, even more preferably from 600 to 1000 g/l.
  • the bleach activator entering the extrusion step has a medium particle size of less than 35 micrometers, preferably from 1 to 30 micrometers and more preferably from 5 to 20 micrometers. These small particle sizes can be achieved by any particle size reduction technique, such as grinding.
  • NACA-OBS is nonyl amido caproyl oxy benzene sulphonate
  • TAED is tetra acetyl ethylene diamine
  • LAS is sodium linear alkyl benzene sulphonate
  • C12/14 AE3S is ethoxylated alkyl sulphate having a carbon chain length of predominantly C12/C14 and a average of 3 ethoxy groups per molecule .
  • C12/14 AE3 is an ethoxylated alcohol having a carbon chain length of predominantly C12/C14 and an average of 3 ethoxy groups per molecule .
  • STS is sodium toluene sulphonate.
  • CMC is carboxymethyl cellulose
  • the bleach activator i.e. NACA- OBS or TAED
  • citric acid where present
  • AE3S or LAS where present
  • aqueous solution 40% active
  • CMC powder aqueous solution
  • a Loedige FM mixer optionally water is added to help plasticize the mix and, in the case of CMC to hydrate and activate the binder.
  • the premix was then fed into a dome extruder (Fuji Paudal Model DGL-1) having a die with 0.8 mm orifices and extruded at a pressure of about 20 bar.
  • the resulting extrudate was then fed into a rotating disc spheroniser (Fuji Paudal QJ-400) where they were broken down into short lengths and formed into substantially spherical particles.
  • the particles were then dried in a Niro vibrating fluid-bed dryer resulting in crisp, free-flowing dust free particles with a particle size range of from 0.25 mm to 2.00 mm and a Heubach dust measurement of less than lOOmg/g.
  • the particles produced in each of Examples 1 to 7 were taken and coated in a drum mixer with 0.4 parts of C12/14AE3 surfactant and then further dusted with 1 part of Zeolite in a second drum mixer.
  • the resultant particles remained crisp and free-flowing and showed improved resistance to dust-generation as demonstrated by a reduction in Heubach dust value from 35mg/g (un-coated) to 12 mg/g.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Detergent Compositions (AREA)
  • Paper (AREA)
EP97902071A 1996-01-29 1997-01-22 Verfahren zur herstellung einer teilchenförmigen bleichmittelaktivatorkomponente Withdrawn EP0880581A4 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP97902071A EP0880581A4 (de) 1996-01-29 1997-01-22 Verfahren zur herstellung einer teilchenförmigen bleichmittelaktivatorkomponente

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
EP96300585 1996-01-29
EP96300585 1996-01-29
EP96304782 1996-06-28
EP96304782 1996-06-28
EP97902071A EP0880581A4 (de) 1996-01-29 1997-01-22 Verfahren zur herstellung einer teilchenförmigen bleichmittelaktivatorkomponente
PCT/US1997/001024 WO1997027280A1 (en) 1996-01-29 1997-01-22 Process for making particulate bleach activator component

Publications (2)

Publication Number Publication Date
EP0880581A1 true EP0880581A1 (de) 1998-12-02
EP0880581A4 EP0880581A4 (de) 2001-10-10

Family

ID=26143544

Family Applications (1)

Application Number Title Priority Date Filing Date
EP97902071A Withdrawn EP0880581A4 (de) 1996-01-29 1997-01-22 Verfahren zur herstellung einer teilchenförmigen bleichmittelaktivatorkomponente

Country Status (12)

Country Link
EP (1) EP0880581A4 (de)
AR (1) AR005591A1 (de)
AU (1) AU1582597A (de)
BR (1) BR9707475A (de)
CA (1) CA2243485C (de)
CZ (1) CZ229598A3 (de)
EG (1) EG21216A (de)
HU (1) HUP9901904A3 (de)
MA (1) MA24074A1 (de)
MX (1) MX9806071A (de)
TR (1) TR199801458T2 (de)
WO (1) WO1997027280A1 (de)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999027061A1 (en) * 1997-11-20 1999-06-03 The Procter & Gamble Company Detergent composition containing optimally sized bleach activator particles
CA2324397A1 (en) * 1998-03-19 1999-09-23 Donald Ray Brown Detergent composition containing cylindrically-shaped bleach activator extrudates having enhanced flowability
GB2345701A (en) * 1999-01-12 2000-07-19 Procter & Gamble Particulate bleaching components
US6497644B2 (en) 2000-06-02 2002-12-24 Eastman Chemical Company Process for recycling amido-carboxylic acid esters into amino-carboxylic acids
AU2001266708A1 (en) 2000-06-02 2001-12-11 Eastman Chemical Company Improved purification of phenyl ester salts
US6498124B2 (en) 2000-06-02 2002-12-24 Eastman Chemical Company Isolation of phenyl ester salts from mixtures comprising sulfolane
US6660712B2 (en) 2000-06-02 2003-12-09 Dale Elbert Van Sickle Stabilization of amido acids with antioxidants
US6500973B2 (en) 2000-06-02 2002-12-31 Eastman Chemical Company Extractive solution crystallization of chemical compounds
DE10134364A1 (de) 2001-07-14 2003-01-23 Clariant Gmbh Verfahren zur Herstellung von Bleichaktivator-Granulaten
GB2473275A (en) * 2009-09-08 2011-03-09 Reckitt Benckiser Nv Bleach activator granule comprising DOBA and a process of production thereof involving extrusion

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2162353A1 (de) * 1970-12-22 1972-07-13 Colgate-Palmolive Co., New York, N.Y. (V.StA.) Verfahren zur Herstellung von Enzymgranulaten
EP0328880A1 (de) * 1988-01-19 1989-08-23 Colgate-Palmolive Company Extrudat aus einer verstärkten synthetischen Waschmittelzusammensetzung in Teilchen und Stückform und Verfahren zu deren Herstellung und Verwendung
WO1991002047A1 (de) * 1989-08-09 1991-02-21 Henkel Kommanditgesellschaft Auf Aktien Herstellung verdichteter granulate für waschmittel
WO1991013678A1 (de) * 1990-03-09 1991-09-19 Henkel Kommanditgesellschaft Auf Aktien Verfahren zum herstellen von granulaten eines wasch- oder reinigungsmittels
WO1997013834A1 (de) * 1995-10-12 1997-04-17 Henkel Kommanditgesellschaft Auf Aktien Bleichaktivatoren in granulatform (iii)

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2048286A (en) * 1933-08-17 1936-07-21 Lever Brothers Ltd Apparatus for treating plastic materials
US3832431A (en) * 1969-11-10 1974-08-27 Lever Brothers Ltd Process for making marbleized soap or detergent
US4399049A (en) * 1981-04-08 1983-08-16 The Procter & Gamble Company Detergent additive compositions
US4678594A (en) * 1985-07-19 1987-07-07 Colgate-Palmolive Company Method of encapsulating a bleach and activator therefor in a binder
US5002691A (en) * 1986-11-06 1991-03-26 The Clorox Company Oxidant detergent containing stable bleach activator granules
GB8711153D0 (en) * 1987-05-12 1987-06-17 Warwick International Ltd Bleach activator compositions
DE4024759A1 (de) * 1990-08-03 1992-02-06 Henkel Kgaa Bleichaktivatoren in granulatform
DE4143016A1 (de) * 1991-12-24 1993-07-01 Henkel Kgaa Bleichaktivatoren in granulatform (ii)
US5534196A (en) * 1993-12-23 1996-07-09 The Procter & Gamble Co. Process for making lactam bleach activator containing particles
US5460747A (en) * 1994-08-31 1995-10-24 The Procter & Gamble Co. Multiple-substituted bleach activators

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2162353A1 (de) * 1970-12-22 1972-07-13 Colgate-Palmolive Co., New York, N.Y. (V.StA.) Verfahren zur Herstellung von Enzymgranulaten
EP0328880A1 (de) * 1988-01-19 1989-08-23 Colgate-Palmolive Company Extrudat aus einer verstärkten synthetischen Waschmittelzusammensetzung in Teilchen und Stückform und Verfahren zu deren Herstellung und Verwendung
WO1991002047A1 (de) * 1989-08-09 1991-02-21 Henkel Kommanditgesellschaft Auf Aktien Herstellung verdichteter granulate für waschmittel
WO1991013678A1 (de) * 1990-03-09 1991-09-19 Henkel Kommanditgesellschaft Auf Aktien Verfahren zum herstellen von granulaten eines wasch- oder reinigungsmittels
WO1997013834A1 (de) * 1995-10-12 1997-04-17 Henkel Kommanditgesellschaft Auf Aktien Bleichaktivatoren in granulatform (iii)

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO9727280A1 *

Also Published As

Publication number Publication date
BR9707475A (pt) 1999-07-27
CA2243485C (en) 2002-03-19
HUP9901904A2 (hu) 1999-10-28
HUP9901904A3 (en) 1999-11-29
AR005591A1 (es) 1999-06-23
EG21216A (en) 2001-02-28
WO1997027280A1 (en) 1997-07-31
TR199801458T2 (xx) 1998-10-21
MA24074A1 (fr) 1997-10-01
EP0880581A4 (de) 2001-10-10
AU1582597A (en) 1997-08-20
CA2243485A1 (en) 1997-07-31
MX9806071A (es) 1998-11-29
CZ229598A3 (cs) 1999-01-13

Similar Documents

Publication Publication Date Title
US5167852A (en) Process for preparing particulate detergent additive bodies and use thereof in detergent compositions
AU678363B2 (en) Process for making compact detergent compositions
CA2243485C (en) Process for making particulate bleach activator component
EP0376360B1 (de) Verfahren zur Herstellung von Bleichmittelgranulaten
JPS6222899A (ja) 漂白活性洗剤添加剤、その製造方法及び同添加剤を含有する洗剤組成物
US3833506A (en) Bleaching assistants and the preparation thereof
JPH05509119A (ja) 顆粒状の漂白活性化剤
JP3267626B2 (ja) 漂白剤前駆体を含有する非水性洗剤組成物
US5663136A (en) Process for making compact detergent compositions
EP0299599A1 (de) Zusammensetzung von Bleich-Aktivatoren
JPH0681840B2 (ja) 洗剤組成物及びその製造方法
JPH02284999A (ja) 粒状洗剤添加物製品、その製造方法及び洗剤組成物中での使用
US3177147A (en) Detergent compositions and preparation thereof
CA2248994C (en) Free-flowing agglomerated nonionic surfactant detergent composition and process for making same
JPH07502551A (ja) 顆粒状の漂白活性剤（■）
JPH11514027A (ja) コートされた粒子を含有している非水性液体クリーニング組成物
US5296156A (en) Bleaching granules
JP4219632B2 (ja) 顆粒状漂白活性化剤の製造方法
SE413411B (sv) Sett att skydda alkaliska jordartsmetallhypokloriter for inforlivning i en detergentkomposition
JP4514435B2 (ja) 粒状洗剤の製造方法
EP1124628A1 (de) Polymer-granulate durch wirbelschichtgranulation
JP2002507233A (ja) 漂白剤前駆物質組成物を含有する非水性粒状物含有洗剤組成物
JPH06136390A (ja) 漂白活性化剤造粒物の製造方法及び漂白活性化剤造粒物
JP3510386B2 (ja) 漂白活性化剤造粒物の製造方法、該漂白活性化剤造粒物を含有する漂白剤又は洗剤の製造方法
JPH0665598A (ja) 漂白活性化剤造粒物の製造方法及び漂白活性化剤造粒物

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 19980805

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LI LU NL PT SE

A4 Supplementary search report drawn up and despatched

Effective date: 20010824

AK Designated contracting states

Kind code of ref document: A4

Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LI LU NL PT SE

RIC1 Information provided on ipc code assigned before grant

Free format text: 7C 11D 11/00 A, 7C 11D 3/20 B, 7C 11D 3/26 B, 7C 11D 3/28 B, 7C 11D 3/395 B, 7C 11D 3/39 B

17Q First examination report despatched

Effective date: 20020220

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN

18W Application withdrawn

Effective date: 20040206