EP0451894B2 - Granulare Detergenszusammensetzungen mit hohem Schüttgewicht und Verfahren zu ihrer Herstellung - Google Patents

Granulare Detergenszusammensetzungen mit hohem Schüttgewicht und Verfahren zu ihrer Herstellung Download PDF

Info

Publication number
EP0451894B2
EP0451894B2 EP91200662A EP91200662A EP0451894B2 EP 0451894 B2 EP0451894 B2 EP 0451894B2 EP 91200662 A EP91200662 A EP 91200662A EP 91200662 A EP91200662 A EP 91200662A EP 0451894 B2 EP0451894 B2 EP 0451894B2
Authority
EP
European Patent Office
Prior art keywords
weight
granular detergent
detergent composition
builder
component according
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP91200662A
Other languages
English (en)
French (fr)
Other versions
EP0451894B1 (de
EP0451894A1 (de
Inventor
Michael C/O Unilever Research Curtis
Fransiscus Hermannus Unilever Res. Gortemaker
Bruno Rezzani
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.)
Unilever PLC
Unilever NV
Original Assignee
Unilever PLC
Unilever NV
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=10674150&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0451894(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Unilever PLC, Unilever NV filed Critical Unilever PLC
Publication of EP0451894A1 publication Critical patent/EP0451894A1/de
Publication of EP0451894B1 publication Critical patent/EP0451894B1/de
Application granted granted Critical
Publication of EP0451894B2 publication Critical patent/EP0451894B2/de
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/06—Powder; Flakes; Free-flowing mixtures; Sheets
    • C11D17/065—High-density particulate detergent compositions
    • 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
    • C11D10/00—Compositions of detergents, not provided for by one single preceding group
    • C11D10/04—Compositions of detergents, not provided for by one single preceding group based on mixtures of surface-active non-soap compounds and soap
    • 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 ; Methods for using cleaning compositions
    • 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
    • C11D3/02—Inorganic compounds ; Elemental compounds
    • C11D3/12—Water-insoluble compounds
    • C11D3/124—Silicon containing, e.g. silica, silex, quartz or glass beads
    • C11D3/1246—Silicates, e.g. diatomaceous earth
    • C11D3/128—Aluminium silicates, e.g. zeolites
    • 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
    • C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02—Anionic compounds
    • C11D1/12—Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/14—Sulfonic acids or sulfuric acid esters; Salts thereof derived from aliphatic hydrocarbons or mono-alcohols
    • 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
    • C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/66—Non-ionic compounds
    • C11D1/72—Ethers of polyoxyalkylene glycols

Definitions

  • the present invention relates to granular detergent compositions having a high bulk density and good dispensing properties. Moreover, it relates to a process for the preparation of such detergent compositions, and more in particular, to a process for their continuous preparation.
  • JP-A-61 069897 discloses a process in which a spray-dried detergent powder containing a high level of anionic surfactant and a low level of builder (zeolite) is subjected successively to pulverizing and granulating treatments in a high-speed mixer/granulator, the granulation being carried out in the presence of an "agent for improving surface properties" and optionally a binder.
  • the spray-dried powder is initially broken down to a fine state of division; the surface-improving agent and optional binder are then added and the pulverized material granulated to form a final product of high bulk density.
  • the surface-improving agent which is a finely divided particulate solid such as fine sodium aluminosilicate, is apparently required in order to prevent the composition from being formed into large balls or cakes.
  • the process described in this Japanese patent application is essentially a batch process and is therefore less suitable for the large scale production of detergent powders.
  • GB-A-1 517 713 discloses' a batch process in which spray-dried or granulated detergent powders containing sodium tripolyphosphate and sodium sulphate are densified and spheronized in a "marumerizer" (Trade Mark).
  • This apparatus comprises a substantially horizontal, roughened, rotatable table positioned within, and at the base of, a substantially vertical, smooth-walled cylinder.
  • GB-A-1 453 697 discloses the use of a "marumarizer” (Trade Mark) for granulating together detergent powder components in the presence of a liquid binder to form a granular detergent composition.
  • This apparatus produces powders or granules having a rather wide particle size distribution, and in particular containing a relatively high proportion of oversize particles.
  • Such products exhibit poor dissolution and dispersion characteristics, particularly in low-temperature short duration machine washes as used in Japanese and other far-eastern washing machines. This can be apparent to the consumer as deposits on washed fabrics, and in machine washing leads to a high level of wastage.
  • EP-A-327 963 (HENKEL) describes a continuous process for increasing the bulk density of a spray-dried detergent powder by treating it in a mixing apparatus consisting of a substantially horizontal static hollow cylinder and a rotating shaft in the middle, the shaft having several different types of blades mounted thereon.
  • Example 1 discloses a densified detergent powder having a bulk density of 595 g/l, containing a ternary active system consisting of an anionic surfactant, nonionic surfactants and soap, the amount of soap being about 13% of the active system.
  • the formulation further contains a builder system consisting of 10% zeolite and 20% sodium tripolyphosphate, whereby the latter is likely to account for the claimed favorable dispensing properties.
  • the related EP-A-337 330 (HENKEL) describes a variant of the previous process, whereby liquid nonionic surfactant is sprayed onto a spray-dried base powder.
  • the base powder is a low-phosphate base powder and comprises conventional ingredients in the usual amounts. The process results in a moderate increase in bulk density of at most 100 g/l.
  • EP-A-220 024 discloses a process in which a spray-dried detergent powder containing a high level (30-85% by weight) of anionic surfactant is mixed with an inorganic builder (sodium tripolyphosphate, or sodium aluminosilicate and sodium carbonate) and compacted under high pressure using a roll compactor ("chilsonator"); the compacted material, after removal of oversize material and fines, is then granulated using conventional apparatus, for example a fluidized bed, tumble mixer, or rotating drum or pan.
  • an inorganic builder sodium tripolyphosphate, or sodium aluminosilicate and sodium carbonate
  • the present invention provides a granular detergent composition or component having a bulk density of at least 600 g/l, comprising from 10 to 70% by weight of a builder, the builder comprising amorphous alkali metal aluminosilicate or zeolite, at least 50% by weight of said builder being a non-phosphate material, and from 5 to 45% by weight of a ternary active system comprising one or more nonionic surfactants, anionic surfactants and soap, whereby the weight ratio of the anionic surfactant to the nonionic surfactant is less than 5 : 1 and the amount of soap is from 10 to 90% by weight of the active system., the composition further containing sodium silicate the amount of said sodium silicate being less than 5% by weight.
  • the invention provides a process for the preparation of the granular detergent composition or component of the invention, whereby a particulate starting material is treated
  • the granular detergent compositions according to the invention comprise 10 to 70% by weight of a builder system, the builder comprising amorphous alkali metal aluminosilicate or zeolite and 5 to 45% by weight of an active system.
  • the builder system of the compositions according to the invention may consist of a single detergency builder in a amount of from 10 to 70 % by weight of the total formulation. It may also be a mixture of two or more detergency builders. However, the invention is especially applicable for detergent powders wherein at least 50% by weight of the builder system is a non-phosphate material, because in such cases the dispensing properties of densified powders of conventional formulations are particularly poor.
  • the builder may be any material capable of reducing the level of free calcium ions in the wash liquor and will preferably provide the composition with other beneficial properties such as the generation of an alkaline pH, the suspension of soil removed from the fabric and the suspension of the fabric-softening clay material.
  • the level of the detergency builder is preferably from 15% to 60% by weight.
  • detergency builders which may also be used in the invention include precipitating builders such as the alkali metal carbonates, bicarbonates, orthophosphates, sequestering builders such as the alkali metal tripolyphosphates or nitrilotriacetates, or ion exchange builders such as the amorphous alkali metal aluminosilicates or the zeolites, or layered silicates, for example Na-SKS-6 from Hoechst.
  • the detergency builder is a non-phosphate builder such as zeolite.
  • the active system of the compositions according to the invention is a ternary detergent active system. consisting of an anionic surfactant, a nonionic surfactant and a soap. It is present in an amount of from 5 to 45 % by weight of the total formulation.
  • the weight ratio of the anionic to the nonionic surfactant is less than 5 : 1, preferably less than 4 : 1.
  • the amount of soap must at least be 10 % by weight and less than 90% by weight of the active system, in order to obtain the desired good dispensing properties.
  • the amount of soap is from 10 to 60% by weight of the active system.
  • the anionic surfactants of the ternary active system are usually water-soluble alkali metal salts of organic sulphates and sulphonates having alkyl radicals containing from about 8 to about 22 carbon atoms, the term alkyl being used to include the alkyl portion of higher acyl radicals.
  • suitable synthetic anionic detergent compounds are sodium and potassium alkyl sulphates, especially those obtained by sulphating higher (C 8 -C 18 ) alcohols, produced for example from tallow or coconut oil, sodium and potassium alkyl (C 9 -C 20 ) benzene sulphonates, particularly sodium linear secondary alkyl (C 10 -C 15 ) benzene sulphonates; and sodium alkyl glyceryl ether sulphates, especially those ethers of the higher alcohols derived from tallow or coconut oil and synthetic alcohols derived from petroleum.
  • the preferred anionic detergent compounds are sodium (C 11 -C 15 ) alkyl benzene sulphonates and sodium (C 16 -C 18 ) alkyl sulphates.
  • Suitable nonionic detergent compounds which may be used in the ternary active system include, in particular, the reaction products of compounds having a hydrophobic group and a reactive hydrogen atom, for example, aliphatic alcohols, acids, amides or alkyl phenols with alkylene oxides, especially ethylene oxide either alone or with propylene oxide.
  • Specific nonionic detergent compounds are alkyl (C 6 -C 22 ) phenols-ethylene oxide condensates, generally 3 to 25 EO, i.e. 3 to 25 units of ethylene oxide per molecule, and the condensation products of aliphatic (C 8 -C 18 ) primary or secondary linear or branched alcohols with ethylene oxide, averaging generally from 3 to 40 EO.
  • Alkoxylated fatty alcohols, more in particular ethoxylated alcohols are the preferred nonionic surfactants.
  • the soaps which are used in the compositions of the present invention are sodium salts of fatty acids of natural or synthetic origin.
  • the alkyl groups of the fatty acids may be branched or straight alkyl groups comprising 8 to 22 carbon atoms, preferably from 12 to 20 carbon atoms.
  • Particularly referred ternary active systems are mixtures of a sodium salt of an alkyl benzene sulphonate, an ethoxylated alcohol and a sodium soap having 12-20 carbon atoms.
  • the detergent powder of the invention may contain any of the ingredients conventionally present in compositions intended for the washing of fabrics.
  • the powder of the invention contains sodium silicate.
  • High levels of silicate can in themselves have a beneficial effect on dispensing, as well as on powder structure and prevention of machine corrosion, but are undesirable in powders containing aluminosilicate because the two components react together to form insoluble siliceous species. Accordingly, the amount of sodium silicate is less that 5% by weight, more especially less than 2% by weight, of sodium silicate, which would be expected to have poor dispensing properties.
  • the granular detergent composition or component of the invention may be used as a detergent powder of its own right, but it can also be used as a base powder for formulating a complete fabric washing powder by adding other components.
  • examples of such components include inorganic salts such a sodium carbonate, sodium silicate, etc., bleaches, fluorescers, lather control agents, enzymes and perfumes.
  • the final product will usually comprise from 50 to 95% by weight of the base powder described above.
  • the granular detergent composition or component of the invention may be prepared by any suitable technique, whether batch or continuous, for obtaining detergent compositions having an increased bulk density of 600 g/l and above. According to a preferred process, a particulate starting material is treated
  • a particulate starting material is thoroughly mixed in a high-speed mixer/densifier for a relatively short time of about 5-30 seconds.
  • the particulate starting material may be prepared by any suitable method, such as spray-drying or dry-mixing.
  • the process is therefore very flexible with respect to the chemical composition of the starting material.
  • Phosphate-containing as well as zeolite-containing compositions, and compositions having either a low or a high active content may be used.
  • the process is also suitable for densifying calcite/carbonate-containing detergent compositions.
  • the first step is carried out in a high-speed mixer/densifier, preferably under conditions whereby the starting material is brought into, or maintained in, a deformable state, to be defined hereafter.
  • a high-speed mixer/densifier we advantageously used the Lödige (Trade Mark) CB 30 or CB 100 Recycler. These apparatus essentially consist of a large static hollow cylinder and a rotating shaft in the middle. The shaft has several different types of blades mounted thereon. It can be rotated at speeds between 100 and 2500 rpm, dependent on the degree of densification and the particle size desired.
  • the blades on the shaft provide a thorough mixing action of the solids and the liquids which may be admixed in this stage.
  • the mean residence time is somewhat dependent on the rotational speed of the shaft, the position of the blades and the weir at the exit opening. It is also possible to add solid material in the Lödige recycler.
  • the densified powder is dried and/or cooled.
  • This step can be carried out in a known way, for instance in a fluid bed apparatus (drying) or in an airlift (cooling). From a processing point of view, it is advantageous if the powder needs a cooling step only, because the required equipment is relatively simple.
  • the detergent material may still possess a considerable porosity such that a further increase in bulk density could be achieved.
  • a longer residence time in the high-speed mixer/densifier we found it to be particularly advantageous to subject the powder to a further densification step.
  • the process is then essentially the same as described in our co-pending not prepublished European patent application 367,339.
  • the detergent material is treated for 1-10 minutes, preferably for 2-5 minutes, in a moderate-speed granulator/densifier under such conditions that the powder is brought into, or maintained in, a deformable state.
  • the particle porosity will be further reduced.
  • the main differences with the first step reside in the lower mixing speed and the longer residence time of 1-10 minutes.
  • This further processing step can be successfully carried out in a Lödige (Trade Mark) KM 300 mixer, also referred to as Lödige Ploughshare.
  • This apparatus essentially consists of a hollow static cylinder having a rotating shaft in the middle. On this shaft various plough-shaped blades are mounted. It can be rotated at a speed of 40-160 rpm.
  • one or more high-speed cutters can be used to prevent excessive agglomeration.
  • Another suitable machine for this step is, for example, the Drais (Trade Mark) K-T 160.
  • small amounts of fine powdered solids such as zeolite, can be added in the high-speed mixer/densifier and/or the moderate speed granulator/densifier, such as disclosed in our co-pending European patent application 390,251.
  • Preferred for the first step and essential for the further processing step is the deformable state into which the detergent powder must be brought in order to get optimal densification.
  • This deformable state may be induced in a number of ways, for instance by operating at temperatures above 45 °C. When liquids such as water or nonionics are added to the particulate starting material, lower temperatures may be employed, for example 35 °C and above.
  • a spray-dried base powder leaving the tower at a temperature of above 45°C is fed directly into the process of the present invention.
  • the spray-dried powder may be cooled first, e.g. in an airlift, and subsequently be heated again after transportation.
  • the heat may be applied externally, possibly supplemented by internally generated heat, such as heat of hydration of water-free sodium tripolyphosphate.
  • the deformability of a detergent powder can be derived from its compression modulus, which in turn can be derived from its stress-strain characteristics.
  • a sample of the composition is compressed to form an airless prill of 13 mm diameter and height.
  • the compression modulus can now be derived from the slope of the stress - versus relative strain diagram during the first part of the compression process, which reflects the elastic deformation.
  • the compression modulus is expressed in MPa (mega Pascal).
  • the Instron apparatus can be equipped with a heatable sample holder.
  • the compression modulus as measured according to the above method was found to correlate well with the particle porosity decrease and the accompanying bulk density increase, under comparable processing conditions. This is further illustrated in the Examples.
  • the powder can be considered in a deformable state if the compression modulus as defined above is less than approximately 25, preferably less than 20 MPa. Even more preferably, the compression modulus is less than 15 MPa and values of less than 10 MPa are particularly preferred.
  • the deformability of a powder depends, among other things, on the chemical composition, the temperature and the moisture content. As to the chemical composition, the liquids to solids ratio and the amount of polymer proved to be important factors. Moreover, it was generally more difficult to bring phosphate-containing powders into a deformable state than it was for zeolite-containing powders.
  • the storage stability of the final detergent powder can be assessed by means of the Unconfined Compressibility Test.
  • the detergent powder is placed in a cylinder having a diameter of 13 cm and a height of 15 cm. Subsequently, a weight of 10 kg is placed on top of the powder. After 5 minutes the weight is removed and the walls of the cylinder are taken away. Then an increasing load is placed on top of the column of compressed detergent powder and the weight (in kg) is determined at which the column disintegrates. This value is a function of the stickiness of the detergent powder and proved to be a good measure for the storage stability.
  • Dispensing performance is assesssed by the following method. Dry powder (100 g) is placed in a dry dispenser tray of an automatic front-loading washing machine of the type Philips AWB 126/127 (shower-type dispenser). Mains water at a flow rate of 5 liters/min, supplied at a pressure of 0.5 bar, is allowed to flow through the dispenser for one minute. The temperature of the water is 10-20°C. The remaining undispensed powder is removed, dried at 100°C for 12 hours, and weighed. The dispensing residue is the residual dried powder expressed as a percentage of the initial sample. An average of 4 determinations is taken as the final result.
  • Detergent powders were prepared to the compositions given in Table 1 by spray-drying aqueous slurries.
  • Examples 1-3 relate to products produced within the scope of the invention, the examples 4 and 5 are comparative Examples. The amounts are parts by weight.
  • Example 1 2 3 4 5 LAS 6.4 8.0 8.4 9.0 7.2
  • Example 1 2 3 4 5 Bulk density (g/l) Moisture 440 444 443 474 458 content (%) Mean particle size 14.5 13.3 12.2 11.1 13.9 (microns) 646 758 682 527 590
  • the powders were fed directly into a Loedige Recycler CB continuous high speed mixer/densifier, described in more detail above.
  • the CB 30 unit was used for the low throughput described, and the CB 100 for the high throughput.
  • the units were usually operated at a mixer tip speed of 8-30 meters per second.
  • the comparative powder of example 5 was treated in a conventional rotating drum mixer. The residence time was in this case about 1 to 2 minutes.
  • the powders can be optionally passed through an additional moderate speed granulator/densifier. This was done with the powder of Example 3, to give the properties shown in Table 4.
  • Example 4 which lies outside the required detergent active specification because the soap content of the active system is too low, exhibits poor dispensing properties.
  • Example 5 The powder of example 5 was produced in a conventional drum without the densification step and has a bulk density of only 595 g/l.

Claims (13)

  1. Gekörntes Waschmittel oder gekörnte Waschmittelkomponente mit einer Schüttdichte von mindestens 600 g/l, umfassend 10 bis 70 Gew.-% eines Builders, wobei der Builder amorphes Alkalimetallaluminosilicat oder Zeolith umfaßt, wobei mindestens 50 Gew.-% des Builders kein Phosphatmaterial sind, und 5 bis 45 Gew.-% eines ternären Aktivstoffsystems, umfassend ein oder mehrere nichtionische Tenside, anionische Tenside und Seife, wobei das Gewichtsverhältnis von dem anionischen Tensid zu dem nichtionischen Tensid weniger als 5:1 ist und die Seifenmenge 10 bis 90 Gew.-% des Aktivstoffsystems ist, wobei die Zusammensetzung weiterhin Natriumsilicat enthält, wobei die Menge an Natriumsilicat weniger als 5 Gew.-% beträgt.
  2. Gekörntes Waschmittel oder gekörnte Waschmittelkomponente nach Anspruch 1, wobei das Gewichtsverhältnis des anionischen Tensids zu dem nichtionischen Tensid weniger als 4:1 ist und die Seifenmenge 10 bis 60 Gew.-% des Aktivstoffsystems beträgt.
  3. Gekörntes Waschmittel oder gekörnte Waschmittelkomponente nach einem der vorangehenden Ansprüche mit einer Schüttdichte von mindestens 650 g/l.
  4. Gekörntes Waschmittel oder gekörnte Waschmittelkomponente nach einem der vorangehenden Ansprüche, wobei der Builder kein Phosphatbuilder ist.
  5. Gekörntes Waschmittel oder gekörnte Waschmittelkomponente nach Anspruch 4, wobei der Builder Zeolith ist.
  6. Gekörntes Waschmittel oder gekörnte Waschmittelkomponente nach einem der vorangehenden Ansprüche, enthaltend weniger als 2 Gew.-% Silicat.
  7. Gekörntes Waschmittel oder gekörnte Waschmittelkomponente nach einem der vorangehenden Ansprüche, im wesentlichen frei von Alkalimetallsulfaten.
  8. Waschpulver, umfassend 50 bis 95 Gew.-% des gekörnten Waschmittels oder der gekörnten Waschmittelkomponente nach einem der vorangehenden Ansprüche.
  9. Verfahren zur Herstellung eines gekörnten Waschmittels oder einer gekörnten Waschmittelkomponente nach den Ansprüchen 1 bis 7, wobei ein teilchenförmiges Ausgangsmaterial
    (i) in einem Hochgeschwindigkeitsmischer/Verdichter, bei einer mittleren Aufenthaltszeit von etwa 5 bis 30 Sekunden; und dann
    (ii) in einer Trocken- und/oder Kühlvorrichtung behandelt wird.
  10. Verfahren nach Anspruch 9, wobei das teilchenförmige Ausgangsmaterial in einen verformbaren Zustand gebracht oder gehalten wird, wie hierin definiert.
  11. Verfahren nach den Ansprüchen 9 bis 10, wobei der verformbare Zustand durch Verarbeiten bei Temperaturen oberhalb 45°C und/oder Flüssigzugabe zu dem teilchenförmigen Ausgangsmaterial bewirkt wird.
  12. Verfahren nach den Ansprüchen 9 bis 11, wobei nichtionische Tenside und/oder Wasser auf das teilchenförmige Ausgangsmaterial gesprüht werden.
  13. Verfahren nach den Ansprüchen 9 bis 12, wobei das teilchenförmige Ausgangsmaterial ein sprühgetrocknetes Waschmittelgrundpulver ist.
EP91200662A 1990-04-09 1991-03-25 Granulare Detergenszusammensetzungen mit hohem Schüttgewicht und Verfahren zu ihrer Herstellung Expired - Lifetime EP0451894B2 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB909008013A GB9008013D0 (en) 1990-04-09 1990-04-09 High bulk density granular detergent compositions and process for preparing them
GB9008013 1990-04-09

Publications (3)

Publication Number Publication Date
EP0451894A1 EP0451894A1 (de) 1991-10-16
EP0451894B1 EP0451894B1 (de) 1995-05-24
EP0451894B2 true EP0451894B2 (de) 2003-11-26

Family

ID=10674150

Family Applications (1)

Application Number Title Priority Date Filing Date
EP91200662A Expired - Lifetime EP0451894B2 (de) 1990-04-09 1991-03-25 Granulare Detergenszusammensetzungen mit hohem Schüttgewicht und Verfahren zu ihrer Herstellung

Country Status (8)

Country Link
EP (1) EP0451894B2 (de)
JP (1) JPH0798960B2 (de)
AU (1) AU7413391A (de)
BR (1) BR9101403A (de)
DE (1) DE69109922T3 (de)
ES (1) ES2072524T5 (de)
GB (1) GB9008013D0 (de)
ZA (1) ZA912621B (de)

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2083331C (en) * 1991-11-26 1998-08-11 Johannes H. M. Akkermans Detergent compositions
GB9125035D0 (en) * 1991-11-26 1992-01-22 Unilever Plc Detergent compositions and process for preparing them
DE4211699A1 (de) * 1992-04-08 1993-10-14 Henkel Kgaa Verfahren zur Erhöhung des Schüttgewichts sprühgetrockneter Waschmittel
EP0660873B2 (de) † 1992-09-01 2006-05-31 The Procter & Gamble Company Granuliertes reinigungsmittel von hoher dichte
WO1994005767A1 (en) * 1992-09-08 1994-03-17 Unilever Plc Detergent composition and process for its production
US5739097A (en) * 1993-02-11 1998-04-14 Henkel Kommanditgesellschaft Auf Aktien Process for the production of surfactant granules
DE4320851A1 (de) * 1993-06-23 1995-01-05 Henkel Kgaa Waschmittel mit verfärbungsinhibierenden Eigenschaften
USH1604H (en) * 1993-06-25 1996-11-05 Welch; Robert G. Process for continuous production of high density detergent agglomerates in a single mixer/densifier
US5486303A (en) * 1993-08-27 1996-01-23 The Procter & Gamble Company Process for making high density detergent agglomerates using an anhydrous powder additive
US5733862A (en) * 1993-08-27 1998-03-31 The Procter & Gamble Company Process for making a high density detergent composition from a sufactant paste containing a non-aqueous binder
GB9324129D0 (en) * 1993-11-24 1994-01-12 Unilever Plc Detergent compositions and process for preparing them
US5431857A (en) * 1994-01-19 1995-07-11 The Procter & Gamble Company Process for producing a high density detergent composition having improved solubility by agglomeration of anionic surfactants and an agglomerating agent
US5565137A (en) * 1994-05-20 1996-10-15 The Proctor & Gamble Co. Process for making a high density detergent composition from starting detergent ingredients
TW326472B (en) * 1994-08-12 1998-02-11 Kao Corp Method for producing nonionic detergent granules
US5496487A (en) * 1994-08-26 1996-03-05 The Procter & Gamble Company Agglomeration process for making a detergent composition utilizing existing spray drying towers for conditioning detergent agglomerates
US5489392A (en) * 1994-09-20 1996-02-06 The Procter & Gamble Company Process for making a high density detergent composition in a single mixer/densifier with selected recycle streams for improved agglomerate properties
US5516448A (en) * 1994-09-20 1996-05-14 The Procter & Gamble Company Process for making a high density detergent composition which includes selected recycle streams for improved agglomerate
US5691297A (en) * 1994-09-20 1997-11-25 The Procter & Gamble Company Process for making a high density detergent composition by controlling agglomeration within a dispersion index
WO1996025482A1 (en) * 1995-02-13 1996-08-22 The Procter & Gamble Company Process for producing detergent agglomerates in which particle size is controlled
US5574005A (en) * 1995-03-07 1996-11-12 The Procter & Gamble Company Process for producing detergent agglomerates from high active surfactant pastes having non-linear viscoelastic properties
US5569645A (en) * 1995-04-24 1996-10-29 The Procter & Gamble Company Low dosage detergent composition containing optimum proportions of agglomerates and spray dried granules for improved flow properties
US5707959A (en) * 1995-05-31 1998-01-13 The Procter & Gamble Company Processes for making a granular detergent composition containing a crystalline builder
US5565422A (en) * 1995-06-23 1996-10-15 The Procter & Gamble Company Process for preparing a free-flowing particulate detergent composition having improved solubility
US5554587A (en) * 1995-08-15 1996-09-10 The Procter & Gamble Company Process for making high density detergent composition using conditioned air
US5665691A (en) * 1995-10-04 1997-09-09 The Procter & Gamble Company Process for making a low density detergent composition by agglomeration with a hydrated salt
US5576285A (en) * 1995-10-04 1996-11-19 The Procter & Gamble Company Process for making a low density detergent composition by agglomeration with an inorganic double salt
US5668099A (en) * 1996-02-14 1997-09-16 The Procter & Gamble Company Process for making a low density detergent composition by agglomeration with an inorganic double salt
WO1998006816A1 (en) * 1996-08-14 1998-02-19 The Procter & Gamble Company Process for making high density detergent
JP2000501453A (ja) * 1996-08-26 2000-02-08 ザ、プロクター、エンド、ギャンブル、カンパニー 変性ポリアミンポリマーの予備混合を含む洗剤組成物を製造する為の凝集法
ATE207108T1 (de) * 1996-08-26 2001-11-15 Procter & Gamble Sprühtrocknungsverfahren zur herstellung von waschmittelzusammensetzungen unter vormischung eines modifizierten polyamins
US5914307A (en) * 1996-10-15 1999-06-22 The Procter & Gamble Company Process for making a high density detergent composition via post drying mixing/densification
GB9711350D0 (en) * 1997-05-30 1997-07-30 Unilever Plc Granular detergent compositions and their production
GB9711359D0 (en) 1997-05-30 1997-07-30 Unilever Plc Detergent powder composition
GB9711356D0 (en) * 1997-05-30 1997-07-30 Unilever Plc Particulate detergent composition
WO1998054289A1 (en) 1997-05-30 1998-12-03 Unilever Plc Free-flowing particulate detergent compositions
US6610645B2 (en) 1998-03-06 2003-08-26 Eugene Joseph Pancheri Selected crystalline calcium carbonate builder for use in detergent compositions
DE69930738T2 (de) * 1998-06-04 2007-01-04 Kao Corporation Oberflaechenaktive zusammensetzung

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT337325B (de) * 1973-08-31 1977-06-27 Henkel & Cie Gmbh Verfahren zum waschen, bleichen oder reinigen von festen werkstoffen, insbesondere von textilien, sowie mittel zur durchfuhrung des verfahrens
GB1517713A (en) * 1974-10-31 1978-07-12 Unilever Ltd Preparation of detergent formulations
NZ201212A (en) * 1981-07-15 1985-08-16 Unilever Plc Detergent additives and compositions
GB8334017D0 (en) * 1983-12-21 1984-02-01 Unilever Plc Detergent composition
GB8415302D0 (en) * 1984-06-15 1984-07-18 Unilever Plc Fabric washing process
DE3444960A1 (de) * 1984-12-10 1986-06-12 Henkel KGaA, 4000 Düsseldorf Koerniges adsorptionsmittel
GB8603667D0 (en) * 1986-02-14 1986-03-19 Unilever Plc Detergent composition
DE3635313A1 (de) * 1986-10-17 1988-04-28 Bayer Ag Verfahren zur herstellung von granulaten
JPH0816236B2 (ja) * 1986-12-18 1996-02-21 ライオン株式会社 高嵩密度洗剤組成物の製造方法
DE3803966A1 (de) * 1988-02-10 1989-08-24 Henkel Kgaa Verfahren zur erhoehung der dichte spruehgetrockneter waschmittel
DE3812530A1 (de) * 1988-04-15 1989-10-26 Henkel Kgaa Verfahren zur erhoehung der dichte spruehgetrockneter, phosphatreduzierter waschmittel
CA1323277C (en) * 1988-04-29 1993-10-19 Robert Donaldson Process for preparing detergent compositions
GB8817386D0 (en) * 1988-07-21 1988-08-24 Unilever Plc Detergent compositions & process for preparing them
JP2547444B2 (ja) * 1988-05-12 1996-10-23 旭電化工業株式会社 濃縮高比重衣料用粉末洗剤
JP2800162B2 (ja) * 1990-03-16 1998-09-21 ライオン株式会社 洗浄剤組成物

Also Published As

Publication number Publication date
DE69109922T2 (de) 1995-10-05
ES2072524T3 (es) 1995-07-16
BR9101403A (pt) 1991-11-26
EP0451894B1 (de) 1995-05-24
DE69109922T3 (de) 2004-04-29
ES2072524T5 (es) 2004-07-01
DE69109922D1 (de) 1995-06-29
AU7413391A (en) 1991-10-10
JPH0798960B2 (ja) 1995-10-25
GB9008013D0 (en) 1990-06-06
JPH04227700A (ja) 1992-08-17
ZA912621B (en) 1992-12-30
EP0451894A1 (de) 1991-10-16

Similar Documents

Publication Publication Date Title
EP0451894B2 (de) Granulare Detergenszusammensetzungen mit hohem Schüttgewicht und Verfahren zu ihrer Herstellung
EP0390251B1 (de) Detergens-Zusammensetzungen und Verfahren zu ihrer Herstellung
US5133924A (en) Process for preparing a high bulk density granular detergent composition
US4925585A (en) Detergent granules from cold dough using fine dispersion granulation
US5164108A (en) Process for preparing high bulk density detergent compositions
JP2644038B2 (ja) 洗剤組成物およびその製造方法
CA2028204A1 (en) Detergent compositions
CA2242420C (en) Process for the production of a detergent composition
CZ284628B6 (cs) Prací prostředky
US5736502A (en) Process for preparing detergent compositions
EP0430328B1 (de) Verfahren zur Herstellung von Ton enthaltenden Reinigungspulvern hoher Dichte
EP0436240B2 (de) Verfahren zur Herstellung von Reinigungsmitteln hoher Dichte mit verbesserten Verteilungseigenschaften
US5990073A (en) Process for the production of a detergent composition
GB2283756A (en) Particulate detergent composition
AU739651B2 (en) Process for the production of a detergent composition

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

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): CH DE ES FR GB IT LI NL SE

17P Request for examination filed

Effective date: 19910829

RAP3 Party data changed (applicant data changed or rights of an application transferred)

Owner name: UNILEVER N.V.

Owner name: UNILEVER PLC

17Q First examination report despatched

Effective date: 19940929

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): CH DE ES FR GB IT LI NL SE

ITF It: translation for a ep patent filed

Owner name: JACOBACCI & PERANI S.P.A.

REF Corresponds to:

Ref document number: 69109922

Country of ref document: DE

Date of ref document: 19950629

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2072524

Country of ref document: ES

Kind code of ref document: T3

ET Fr: translation filed
PLBQ Unpublished change to opponent data

Free format text: ORIGINAL CODE: EPIDOS OPPO

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PLBF Reply of patent proprietor to notice(s) of opposition

Free format text: ORIGINAL CODE: EPIDOS OBSO

26 Opposition filed

Opponent name: PROCTER & GAMBLE EUROPEAN TECHNICAL CENTER N.V.

Effective date: 19960223

Opponent name: HENKEL KOMMANDITGESELLSCHAFT AUF AKTIEN

Effective date: 19960222

NLR1 Nl: opposition has been filed with the epo

Opponent name: PROCTER & GAMBLE EUROPEAN TECHNICAL CENTER N.V.

Opponent name: HENKEL KOMMANDITGESELLSCHAFT AUF AKTIEN

PLBF Reply of patent proprietor to notice(s) of opposition

Free format text: ORIGINAL CODE: EPIDOS OBSO

PLBF Reply of patent proprietor to notice(s) of opposition

Free format text: ORIGINAL CODE: EPIDOS OBSO

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19970228

Year of fee payment: 7

PLAW Interlocutory decision in opposition

Free format text: ORIGINAL CODE: EPIDOS IDOP

APAC Appeal dossier modified

Free format text: ORIGINAL CODE: EPIDOS NOAPO

APAE Appeal reference modified

Free format text: ORIGINAL CODE: EPIDOS REFNO

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 19980217

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19980320

Year of fee payment: 8

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980331

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980331

APAC Appeal dossier modified

Free format text: ORIGINAL CODE: EPIDOS NOAPO

PLBQ Unpublished change to opponent data

Free format text: ORIGINAL CODE: EPIDOS OPPO

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

R26 Opposition filed (corrected)

Opponent name: HENKEL KOMMANDITGESELLSCHAFT AUF AKTIEN * 960223 P

Effective date: 19960222

APAE Appeal reference modified

Free format text: ORIGINAL CODE: EPIDOS REFNO

NLR1 Nl: opposition has been filed with the epo

Opponent name: PROCTER & GAMBLE EUROPEAN TECHNICAL CENTER N.V.

Opponent name: HENKEL KOMMANDITGESELLSCHAFT AUF AKTIEN

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19990326

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991001

EUG Se: european patent has lapsed

Ref document number: 91200662.4

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19991001

EUG Se: european patent has lapsed

Ref document number: 91200662.4

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

APAC Appeal dossier modified

Free format text: ORIGINAL CODE: EPIDOS NOAPO

PLAW Interlocutory decision in opposition

Free format text: ORIGINAL CODE: EPIDOS IDOP

PLAW Interlocutory decision in opposition

Free format text: ORIGINAL CODE: EPIDOS IDOP

PUAH Patent maintained in amended form

Free format text: ORIGINAL CODE: 0009272

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

Free format text: STATUS: PATENT MAINTAINED AS AMENDED

27A Patent maintained in amended form

Effective date: 20031126

AK Designated contracting states

Kind code of ref document: B2

Designated state(s): CH DE ES FR GB IT LI NL SE

REG Reference to a national code

Ref country code: ES

Ref legal event code: DC2A

Date of ref document: 20040119

Kind code of ref document: T5

ET3 Fr: translation filed ** decision concerning opposition
APAH Appeal reference modified

Free format text: ORIGINAL CODE: EPIDOSCREFNO

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20100326

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20100406

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20100326

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20100329

Year of fee payment: 20

Ref country code: IT

Payment date: 20100329

Year of fee payment: 20

REG Reference to a national code

Ref country code: DE

Ref legal event code: R071

Ref document number: 69109922

Country of ref document: DE

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

Expiry date: 20110324

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20110324

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20120604

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20110326

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20110325