EP1032638A1 - Produit de detergent non particulaire revetu electrostatiquement - Google Patents
Produit de detergent non particulaire revetu electrostatiquementInfo
- Publication number
- EP1032638A1 EP1032638A1 EP99915234A EP99915234A EP1032638A1 EP 1032638 A1 EP1032638 A1 EP 1032638A1 EP 99915234 A EP99915234 A EP 99915234A EP 99915234 A EP99915234 A EP 99915234A EP 1032638 A1 EP1032638 A1 EP 1032638A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- carrier material
- perfume
- particulate detergent
- electrically conductive
- conductive surface
- 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- Withdrawn
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
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/0047—Detergents in the form of bars or tablets
- C11D17/0065—Solid detergents containing builders
-
- 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
- C11D17/0034—Fixed on a solid conventional detergent ingredient
-
- 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
- C11D17/0047—Detergents in the form of bars or tablets
- C11D17/0065—Solid detergents containing builders
- C11D17/0073—Tablets
- C11D17/0082—Coated tablets
-
- 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
- C11D3/50—Perfumes
-
- 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
- C11D3/50—Perfumes
- C11D3/502—Protected perfumes
- C11D3/505—Protected perfumes encapsulated or adsorbed on a carrier, e.g. zeolite or clay
Definitions
- the present invention relates to detergent compositions in non-particulate form. More particularly, the invention relates to a process for improving the aesthetics of detergent compositions in non-particulate form, e.g., tablet, block or bar, by improving the neat product odor of a non-particulate detergent and also enabling the delivery of different fragrances to a non-particulate detergent product as compared to the odor delivered to the laundry by a perfume incorporated within the detergent, by using electrostatic techniques.
- Non-particulate solids detergents are an alternative to granular or paniculate forms of detergents for simplifying the dosing of such detergents for automatic laundry or dishwashing washing machines.
- Such non-particulate detergents are usually supplied in the form of bars or tablets or briquettes.
- Such non-particulate detergents not only prevent spillage of the detergent composition but also eliminate the need for the consumer to estimate the correct dosage of the detergent composition per wash. Further, such non-particulate detergents also minimize the contact by the consumer with the detergent.
- non-particulate detergent An important factor for successful performance of a non-particulate detergent is its ability to dissolve in the washing machine in a controlled manner according to a desired dissolution profile during the program cycle of the machine. Another important performance factor is that the non-particulate detergent should be hard enough to facilitate easy handling of the detergent prior to use, so that it does not inadvertently lose its structure, crumble, or deteriorate, both during the packaging, transport and storage and during handling by the end consumer prior to actual use. Such performance aspects are an important feature of the non-particulate detergent, 2
- a very desirable feature of a non-particulate detergent is its appearance and odor. From an aesthetics standpoint, consumers prefer to use detergent tablets that have a fragrant odor. It is thus desirable to improve the neat product odor of detergent tablets.
- most detergent compositions include a perfume incorporated within the detergent.
- the tablets are occasionally encapsulated by a protective coating. This coating can substantially mask the odor of the perfume incorporated within the detergent. By dusting the tablet with a perfume carrier, one can improve the neat product odor and make the tablet detergent product more aesthetically pleasing.
- the deposition of a perfume carrier coating on a detergent tablet enables the delivery of different fragrances to the detergent tablet product as compared to the odor delivered to the laundry by a perfume incorporated within the detergent composition.
- a laundry detergent tablet with a core which is formed by compressing a paniculate material, the paniculate material having a surfactant and detergent builder, which is coated with a perfume in order to improve its odor. It is also desirable to provide a laundry tablet with a hard, thin, coating which has a perfume coating deposited on it, so that the laundry tablet has a pleasant odor, it can be stored, shipped and handled, but the coating is broken when the tablet is in the washing machine exposing the soft core which breaks up easily and rapidly, releasing the active ingredients into the wash solution. Thus, it is highly desirable to improve the neat product odor of a non- particulate detergent. It is also highly desirable to have a process for providing a non-particulate detergent tablet with a perfume carrier in a manner so that the perfume carrier would adhere to the tablet and remain so during packaging, transport, storage and handling prior to eventual use.
- GB-A-0 989 683 published on 22nd April 1965, discloses a process for preparing a particulate detergent from surfactants and inorganic salts; spraying on water-soluble silicate; and pressing the detergent particles into a solid form-retaining tablet.
- a readily water-soluble organic film-forming polymer for example, polyvinyl alcohol
- EP-A-0 716 144 published on 12th June 1996, also discloses laundry detergent tablets with water-soluble coatings which may be organic polymers including acrylic/maleic co-polymer, polyethylene glycol, PVPVA, and sugar
- U.S. Patent No 5,648,328 discloses a process for producing a particulate laundry additive composition for perfume delivery primarily in laundry detergent and fabric softening products The process utilizes a porous carrier material loaded with a perfume and as a result of this process, the perfume is sealed into the carrier material sufficiently to not permit exposure until subjected to the laundering or softening process.
- the preferred perfume carrier materials are zeolite X, zeolite Y, and mixtures thereof.
- the focus of the '328 patent is on particulate laundry composition additives and not on non-particulate detergents having perfume deposited on the surface
- U.S. Patent No. 5,000,978 discloses a process for making coated detergent granules by producing detergent granules and then uniformly distributing finely divided powder onto the surfaces of the detergent granules by means of an electrostatic charging and delivery system. 4
- the invention meets the needs above by providing a process for producing a 95 non-particulate detergent having an improved neat product odor, and a process for producing a non-particulate detergent product having a perfume loaded carrier material coating.
- the process comprises the steps of (a) providing a powdered porous carrier material; (b) adsorbing a perfume onto the
- the process includes the step of providing a non-particulate detergent composition having an electrically conductive surface.
- the process further includes the step of grounding the electrically
- the process includes the step of providing an electrostatically chargeable carrier material having a perfume adsorbed therein.
- the process includes the step of coating the electrostatically chargeable carrier material onto the electrically conductive surface of the non-particulate detergent composition by means of applying an
- electrostatic charge with an electrostatic charging and delivery system, such that the electrostatically charged carrier material is adhered to the electrically conductive surface of the detergent composition, even after the electrostatic charge has dissipated.
- the phrase "electrically conductive” means that the surface is capable of allowing electric current to pass through it without offering a substantial resistance to the flow of current. 5
- electrostatic chargeable means a powder that is ionically chargeable by electrostatic induction means
- the process of the invention unexpectedly provides a means by which a non- particulate detergent composition, say, a tablet, can be coated with a finely sized uniformly dispersed, thin layer coating of a perfume loaded powder, thus improving its neat product odor and also enabling the delivery of different fragrances to the
- 135 amount of time according to the claimed process invention is more than ten times greater than the amount of perfume loaded powder depositable without following the steps of the claimed process invention. Further, this process unexpectedly produces an extremely uniform coating of a de-agglomerated perfume loaded powder, which enhances the aesthetics of the detergent tablet, such as appearance and smell.
- the porous carrier particles loaded with perfume can be electrostatically deposited on the surface of the detergent tablet without treating the detergent tablet surface
- the detergent tablet surface can be electrostatically charged or connected to a grounding source
- the detergent tablet having the electrically conductive coating is electrically connected to a grounding source
- a porous carrier material having perfume adsorbed therein, as described hereinafter, is also provided.
- the porous carrier material selected must be electrostatically chargeable The porous carrier material is electrostatically charged and delivered to the grounded detergent
- the detergent tablets to be coated with a perfume can be prepared simply by mixing the solid ingredients together and compressing the mixture in a conventional tablet press as used, for example, in the pharmaceutical industry. Any liquid ingredients, for example the surfactant or suds suppresser, can be incorporated in a
- the principal ingredients are used in a particulate form.
- the ingredients such as builder and surfactant can be spray-dried in a conventional manner and then compacted at a suitable pressure.
- the detergent tablets provided can be made in any size or shape and can, if desired, be surface treated before providing a perfume coating, according to the present invention.
- a surfactant in the core of the tablet is included a surfactant and a builder which normally provides a substantial part of the cleaning power of the tablet.
- builder is intended to mean all materials which tend to remove calcium ion
- the particulate material used for making the detergent tablet provided in this invention can be made by any particulation or granulation process.
- An example of such a process is spray drying (in a co-current or counter current spray drying tower) which typically gives low bulk densities 600g/l or lower.
- 180 higher density can be prepared by granulation and densification in a high shear batch mixer/granulator or by a continuous granulation and densification process (e.g. using Lodige® CB and/or Lodige® KM mixers).
- suitable processes include fluid bed processes, compaction processes (e.g. roll compaction), extrusion, as well as any particulate material made by any chemical process like flocculation, crystallization 7
- the individual particles can also be in any other form, such as for example, particle, granule, sphere or grain
- the particulate materials may be mixed together by any conventional means, for example, a concrete mixer, Nauta mixer, ribbon mixer or any other Alternatively the mixing process may be carried out continuously by metering each component by
- a liquid spray-on to the mix of particulate materials may be carried out
- Other liquid ingredients may also be sprayed on to the mix of particulate materials either separately or premixed
- perfume and slurries of optical brighteners may be sprayed
- a finely divided flow aid dustting agent such
- zeolites, carbonates, silicas can be added to the particulate materials after spraying the non-ionic, preferably towards the end of the process, to make the mix less sticky
- the detergent tablets provided may be manufactured by using any compacting process, such as tabletting, briquetting, or extrusion, preferably tabletting Suitable equipment includes a standard single stroke or a rotary press (such as Courtoy®,
- the tablets are coated with an electrically conductive coating in order to provide an electrically conductive surface for the detergent tablet
- the tablets are coated with a coating that is both electrically conductive and substantially insoluble in water so that the tablet does not absorb moisture, or absorbs moisture at only a very slow rate The coating is also strong so
- the coating is preferably brittle so that the tablet breaks up when subjected to stronger mechanical shock Furthermore it is advantageous if the coating material is dissolved under alkaline conditions, or is readily emulsified by surfactants.
- substantially insoluble means having a very low solubility in water This should be understood to mean having a solubility in water at 25°C of
- solubility is measured following the test protocol of ASTM El 148-87 entitled, "Standard Test Method for Measurements of Aqueous Solubility".
- Suitable coating materials are fatty acids, adipic acid and Cg-C ⁇ dicarboxylic acids, fatty alcohols, diols, esters and ethers.
- Preferred fatty acids are those having a
- Preferred dicarboxylic acids are adipic acid (C ⁇ ), suberic acid (Cg), azelaic acid (C 9 ), sebacic acid (C1 0 ), undecanedioic acid (C ⁇ ), dodecanedioic acid (C12) and tridecanedioic acid (C 13 ).
- Preferred fatty alcohols are those having a carbon chain length of from C ]2 to C22 and most preferably from C14 to C]g.
- Preferred diols are 1,2-octadecanediol and
- esters are tristearin, tripalmitin, ethylbehenate, ethylstearate.
- Preferred ethers are diethyleneglycol mono hexadecylether, diethyleneglycol mono octadecylether, diethyleneglycol mono tetradecylether, phenylether, ethyl naphtyl ether, 2 methoxynaphtalene, beta naphtyl methyl ether and glycerol monooctadecylether.
- Other preferred coating materials include dimethyl 2,2
- the electrically conductive coating is a hydrophobic material having a melting point preferably of from 40 °C to 180 °C.
- the electrically conductive coating can be applied in a number of ways. Two preferred coating methods are a) coating with a
- the coating material is applied at a temperature above its melting point, and solidifies on the tablet.
- the coating is applied as a solution, the solvent being dried to leave a coherent coating.
- the substantially insoluble material can be applied to the tablet by, for example, spraying or dipping. Normally when the molten material is sprayed on to
- the materials melt in the range from 60 °C to 160 °C, more preferably from 70 °C to 120 °C. 9
- melting point is meant the temperature at which the material when heated slowly in, for example, a capillary tube becomes a clear liquid
- an electrically conductive coating of any desired thickness can be applied 250 according to the present invention
- the electrically conductive coating forms from 1% to 10%, preferably from 1.5% to 5%, of the tablet weight
- the detergent tablet may be imparted with an electrically conductive surface without providing a coating.
- One method of providing an electrically conductive surface is by providing an electrostatic charge on the surface 255 of the detergent tablet.
- Porous Carrier Particles means any material capable of supporting (e.g., by absorption onto the surface or adsorption into pores) a perfume agent for incorporation into the particulate compositions
- Such materials 260 include porous solids selected from the group consisting of amorphous silicates, crystalline nonlayer silicates, layer silicates, calcium carbonates, calcium/sodium carbonate double salts, sodium carbonates, clays, zeolites, sodalites, alkali metal phosphates, macroporous zeolites, chitin microbeads, carboxyalkylcelluloses, carboxyalkylstarches, cyclodextrins, porous starches and mixtures thereof 265
- Preferred perfume carrier materials are zeolite A, zeolite X, zeolite Y, zeolite
- zeolite refers to a crystalline aluminosilicate material
- the structural formula of a zeolite is based on the crystal unit cell, the smallest unit of structure represented by Mm/n[(Al ⁇ 2)m(SiO 2 )y]'xH 2 O 270 where n is the valence of the cation M, x is the number of water molecules per unit cell, m and y are the total number of tetrahedra per unit cell, and y/m is 1 to 100 Most preferably, y/m is 1 to 5
- the cation M can be Group IA and Group IIA elements, such as sodium, potassium, magnesium, and calcium 10
- the zeolites to be used herein preferably contain less than about 20% desorbable water, more preferably less than about 8% desorbable water, and most preferably less than about 5% desorbable water.
- Such materials may be obtained by first activating/dehydrating by heating to about 150° C to 350° C, optionally with reduced pressure (from about 0.001 to about 20 Torr). After activation, the
- perfume is slowly and thoroughly mixed with the activated zeolite and, optionally, heated to about 60°C for up to about 2 hours to accelerate absorption equilibrium within the zeolite particles.
- the perfume/zeolite mixture is then cooled to room temperature and is in the form of a free-flowing powder.
- the perfume is adsorbed on the surface of the perfume
- the zeolite powder can be electrostatically charged by any electrostatic charging system, such as an electrostatic spray gun, for example.
- Perfume As used herein the term “perfume” is used to indicate any odoriferous
- the perfume which is subsequently released into the aqueous bath and/or onto fabrics contacted therewith.
- the perfume will most often be liquid at ambient temperatures.
- a wide variety of chemicals are known for perfume uses, including materials such as aldehydes, ketones and esters. More commonly, naturally occurring plant and animal oils and exudates comprising complex mixtures of
- perfumes can be relatively simple in their compositions or can comprise highly sophisticated complex mixtures of natural and synthetic chemical components, all chosen to provide any desired odor.
- Typical perfumes can comprise, for example, woody/earthy bases containing exotic materials such as sandalwood, civet and 1 1
- the perfumes can be of a light floral fragrance, e.g., rose extract, violet extract, and lilac.
- the perfumes can also be formulated to provide desirable fruity odors, e.g., lime, lemon, and orange. Any chemically compatible material which exudes a pleasant or otherwise desirable odor can be used in the perfumed compositions herein.
- Perfumes also include pro-fragrances such as acetal pro-fragrances, ketal pro-fragrances, ester pro-fragrances (e.g., digeranyl succinate), hydrolyzable inorganic-organic pro-fragrances, and mixtures thereof. These pro-fragrances may release the perfume material as a result of simple hydrolysis, or may be pH-change- triggered pro-fragrances (e.g., pH drop) or may be enzymatically releasable pro- fragrances.
- the amount of perfume adsorbed on the carrier material is preferably in the range of 0.1% to 50% by weight, more preferably in the range of 0.5% to 25% by weight, and most preferably in the range of 1% to 15% by weight of zeolite powder.
- the perfume loaded carrier material is uniformly distributed on the surface of the detergent tablets preferably by means of an electrostatic charging and delivery system.
- the electrostatic charging system contains electrodes which ionize the air surrounding them.
- the perfume loaded carrier material is preferably in a finely divided powder form. The finely divided powder is passed by these electrodes and acquires the ionic charges. The powder is then distributed in the area of the detergent tablets. Because of the electrostatic charges, the powder is attracted to and uniformly distributed on the surfaces of the detergent tablets. It is not necessary to charge the detergent tablets.
- the detergent tablets must be grounded. As a practical matter, the detergent tablets are not individually grounded but the object which contains them, preferably a conveyor belt, should be grounded. After the charged powder application, there is 12
- the preferred electrostatic system for use herein is an electrostatic powder spray gun.
- An electrostatic powder spray gun is described in U S Pat No 4,380,320, Hollstein et al , issued Apr 19, 1983, incorporated herein This step
- 340 preferably comprises charging the finely divided powder in an electrostatic powder spray gun and then spraying the charged finely divided powder from the gun onto the detergent tablets
- the most preferred electrostatic powder spray gun for use herein has three parts a gravity feed hopper, a control console, and the gun itself The finely divided
- the control console has controls for regulating flow rate, fluidizing rate, atomizing rate and voltage level
- the type of powder used generally controls which rate settings give the best results
- the finely divided powder is channeled from the gravity feed hopper into the central passageway of the gun Pressurized gas forces the powder through the passageway,
- the powder acquires an electrostatic charge and, when a trigger on the gun is pressed by an operator, the charged powder is emitted from the gun in a conical spray pattern
- electrostatic powder spray guns be mounted above and below a conveyor belt having perforations or openings therein.
- 355 nozzle of the gun is preferably pointed directly at the tablets from both sides of the conveyor belt
- the detergent tablets are placed on the conveyor belt randomly, when the cloud of charged powder particles is emitted from the gun
- the charged powder particles are attracted to the detergent tablet surface and are uniformly distributed on the surfaces of the tablets
- any other method for maintaining the tablets in the area of the charged powder particles can be used, for example, by placing the detergent tablets within a fluidized bed chamber In a fluidized bed chamber, the finely divided particles are charged by ionized air which passes through a perforated plate at the base of the chamber and the charged particles are uniformly deposited on the detergent tablets
- the electrically conductive tablet coating had the following composition dodecanedioc acid 8.39 carboxymethyl cellulose 0 93
- the tablets were formed by compressing the tablet ingredients in a cylindrical die having a diameter of 55 mm using a laboratory press having a trade name Carver 395 Model 3912, to form a tablet having a height of 20 mm.
- the formed tablets were then coated with the electrically conductive coating by dipping the tablet into a 14
- the molten bath of the coating for about 3 seconds.
- the molten coating bath was maintained at a temperature of about 145 degrees centigrade.
- NOBS extrudate is an acronym for the chemical 400 sodium nonanoyloxybenzene sulfonate, commercially available from Eastman Chemicals, Inc.
- carboxymethyl cellulose used in the above example is commercially available from Metsa-Serla and sold under the trade name, Nymcel ZSB-16.
- the perfume loaded zeolite (PLZ) 405 powder was prepared by mixing zeolite A powder with detergent perfume in a
- the above PLZ powders were applied on the coated detergent tablets using a brush, to achieve different amounts of PLZ deposits on the detergent, as shown hereunder.
- the tablet odor was then assessed by a trained perfumer to determine a 415 Neat Product Odor (NPO) grade for each tablet.
- NPO Neat Product Odor
- the NPO was reported in a scale of 0 to 10, to reflect the relative impact of the base tablet odor. A higher grade represents a better odor result.
- the results were as shown in Table A.3 hereunder.
- samples 2, 3 and 4 exhibited unexpected improvement in NPO and also possessed excellent appearance and other physical properties.
- the above perfume loaded zeolite powder was then electrostatically deposited on the detergent surface.
- the electrostatic charging and delivery system was a manual powder system, MPS-D, from American Industrial Co.
- the spraying gun s fixed at measured distance from the tablet, and the powder was sprayed in
- samples 7-8 which represent detergent tablets that were sprayed with non-electrostatically charged powder, exhibited a much lesser amount of perfume loaded zeolite powder deposited thereon, as shown in Table B.2 below: 16
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- 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)
- Dispersion Chemistry (AREA)
- Detergent Compositions (AREA)
Abstract
L'invention concerne un procédé de production d'un détergent à lessive non particulaire, qui comporte les étapes consistant à prévoir une matière porteuse poreuse en poudre, adsorber un parfum sur la matière porteuse poreuse en poudre, et déposer la matière porteuse poreuse en poudre comportant un parfum adsorbé sur le produit de détergent non particulaire. Un autre aspect de l'invention concerne un procédé de production d'un produit de détergent non particulaire qui présente un revêtement de matière porteuse chargée de parfum, le procédé comportant les étapes qui consistent à prévoir une composition de détergent non particulaire présentant une surface conductrice d'électricité; mettre à la terre la surface conductrice d'électricité de la composition de détergent non particulaire; prévoir en outre une matière porteuse pouvant être chargée électrostatiquement et qui comporte un parfum adsorbé; et finalement couvrir à l'aide de la matière porteuse pouvant être chargée électrostatiquement la surface conductrice d'électricité de la composition de détergent non particulaire au moyen d'un système d'apport et de charge électrostatiques, ce qui permet de faire adhérer la matière porteuse pouvant être chargée électrostatiquement à la surface conductrice d'électricité de la composition de détergent.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
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US8083598P | 1998-04-06 | 1998-04-06 | |
US8078298P | 1998-04-06 | 1998-04-06 | |
US80835P | 1998-04-06 | ||
US80782P | 1998-04-06 | ||
PCT/US1999/007313 WO1999051715A1 (fr) | 1998-04-06 | 1999-04-01 | Produit de detergent non particulaire revetu electrostatiquement |
Publications (1)
Publication Number | Publication Date |
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EP1032638A1 true EP1032638A1 (fr) | 2000-09-06 |
Family
ID=26763924
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP99915234A Withdrawn EP1032638A1 (fr) | 1998-04-06 | 1999-04-01 | Produit de detergent non particulaire revetu electrostatiquement |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP1032638A1 (fr) |
CA (1) | CA2321619A1 (fr) |
WO (1) | WO1999051715A1 (fr) |
Families Citing this family (23)
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DE19953503A1 (de) * | 1999-11-06 | 2001-05-10 | Henkel Kgaa | Verfahren zur Herstellung von Duftperlen |
GB2370243B (en) * | 2000-12-21 | 2004-06-16 | Phoqus Ltd | Electrostatic application of powder material to solid dosage forms in an elect ric field |
DE10064985A1 (de) * | 2000-12-23 | 2002-07-11 | Henkel Kgaa | Wasch- und Reinigungsmittelformkörper mit Beschichtung |
DE10209157A1 (de) * | 2002-03-01 | 2003-09-18 | Henkel Kgaa | Parfümierte Reinigungsmittelformkörper |
DE10335455A1 (de) * | 2003-08-02 | 2005-03-03 | Henkel Kgaa | Geschirrspülmittel mit verbesserter Duftwahrnehmung |
EP1574561A1 (fr) * | 2004-03-11 | 2005-09-14 | The Procter & Gamble Company | Comprimé détergent parfumé |
DE102004039722A1 (de) * | 2004-08-17 | 2006-03-02 | Henkel Kgaa | Parfum aufweisende sodahaltige Partikel zur Anwendung in Wasch- oder Reinigungsmitteln |
EP1828365A1 (fr) * | 2004-12-21 | 2007-09-05 | Degussa GmbH | Systeme de liberation de parfum |
US20060165740A1 (en) * | 2005-01-24 | 2006-07-27 | Goldschmidt Chemical Corporation | Perfume delivery system |
DK2045319T3 (en) * | 2007-09-19 | 2016-03-07 | Dalli Werke Gmbh & Co Kg | Coated detergent and process for its preparation |
DE102008015961A1 (de) | 2008-03-20 | 2009-09-24 | Gelita Ag | Verwendung von Gelatinepartikeln in Pulverbeschichtungsverfahren |
MX2011006129A (es) * | 2008-12-08 | 2011-07-20 | Procter & Gamble | Un sustrato solido, soluble y poroso; y complejos de perfume particulados inorganicos alojados en la superficie. |
MX345026B (es) | 2010-07-02 | 2017-01-12 | Procter & Gamble | Material de trama y método para su elaboración. |
WO2012003319A2 (fr) | 2010-07-02 | 2012-01-05 | The Procter & Gamble Company | Filaments comprenant des bandes non tissées avec agent actif et procédés de fabrication associés |
RU2555042C2 (ru) | 2010-07-02 | 2015-07-10 | Дзе Проктер Энд Гэмбл Компани | Способ доставки активнодействующего вещества |
MX2019008761A (es) | 2017-01-27 | 2019-09-18 | Procter & Gamble | Composiciones en la forma de estructuras solidas solubles que comprenden particulas aglomeradas efervescentes. |
EP3573593B1 (fr) | 2017-01-27 | 2023-08-30 | The Procter & Gamble Company | Compositions sous la forme de structures solides et solubles |
US11666514B2 (en) | 2018-09-21 | 2023-06-06 | The Procter & Gamble Company | Fibrous structures containing polymer matrix particles with perfume ingredients |
MX2021013141A (es) | 2019-06-28 | 2021-12-10 | Procter & Gamble | Articulos fibrosos solidos disolubles que contienen surfactantes anionicos. |
CN114555483B (zh) | 2019-10-14 | 2024-04-26 | 宝洁公司 | 含有固体制品的可生物降解的和/或家庭可堆肥的小袋 |
MX2022003979A (es) | 2019-11-20 | 2022-04-26 | Procter & Gamble | Estructura solida soluble porosa. |
JP7506249B2 (ja) | 2020-07-31 | 2024-06-25 | ザ プロクター アンド ギャンブル カンパニー | ヘアケア用プリル含有水溶性繊維パウチ |
EP4210492A1 (fr) | 2020-09-10 | 2023-07-19 | The Procter & Gamble Company | Article solide soluble contenant des agents actifs antibactériens |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5000978A (en) * | 1989-06-29 | 1991-03-19 | The Procter & Gamble Company | Electrostatic coating of detergent granules |
GB9422895D0 (en) * | 1994-11-14 | 1995-01-04 | Unilever Plc | Detergent compositions |
US5648328A (en) * | 1996-02-06 | 1997-07-15 | The Procter & Gamble Company | Process for producing a particulate laundry additive composition for perfume delivery |
ID17072A (id) * | 1996-06-24 | 1997-06-23 | Givaudan Roure Int | Sistem pengantaran parfum |
-
1999
- 1999-04-01 EP EP99915234A patent/EP1032638A1/fr not_active Withdrawn
- 1999-04-01 CA CA002321619A patent/CA2321619A1/fr not_active Abandoned
- 1999-04-01 WO PCT/US1999/007313 patent/WO1999051715A1/fr not_active Application Discontinuation
Non-Patent Citations (1)
Title |
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See references of WO9951715A1 * |
Also Published As
Publication number | Publication date |
---|---|
CA2321619A1 (fr) | 1999-10-14 |
WO1999051715A1 (fr) | 1999-10-14 |
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