EP0430603B1 - Reinigungsmittel - Google Patents

Reinigungsmittel Download PDF

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Publication number
EP0430603B1
EP0430603B1 EP90312779A EP90312779A EP0430603B1 EP 0430603 B1 EP0430603 B1 EP 0430603B1 EP 90312779 A EP90312779 A EP 90312779A EP 90312779 A EP90312779 A EP 90312779A EP 0430603 B1 EP0430603 B1 EP 0430603B1
Authority
EP
European Patent Office
Prior art keywords
filler
detergent active
particulate
composition
anionic detergent
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.)
Revoked
Application number
EP90312779A
Other languages
English (en)
French (fr)
Other versions
EP0430603A3 (en
EP0430603A2 (de
Inventor
Nathan George John Davidson
Peter Cory Knight
Colin Sydney Fairclough
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=10666891&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0430603(B1) "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 EP0430603A2 publication Critical patent/EP0430603A2/de
Publication of EP0430603A3 publication Critical patent/EP0430603A3/en
Application granted granted Critical
Publication of EP0430603B1 publication Critical patent/EP0430603B1/de
Anticipated expiration legal-status Critical
Revoked legal-status Critical Current

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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
    • C11D17/0034—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
    • 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
    • C11D1/22—Sulfonic acids or sulfuric acid esters; Salts thereof derived from aromatic compounds
    • 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
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02—Inorganic compounds ; Elemental compounds
    • C11D3/12—Water-insoluble compounds
    • C11D3/14—Fillers; Abrasives ; Abrasive compositions; Suspending or absorbing agents not provided for in one single group of C11D3/12; Specific features concerning abrasives, e.g. granulometry or mixtures

Definitions

  • This invention relates to the particulate detergent compositions containing relatively high levels of detergent active and furthermore where the detergent comprises a high level of anionic detergent, at least 30% by weight of the composition.
  • Such compositions may in particular be suitable for cleaning fabrics, although they may be intended for other uses.
  • This invention also relates to the production of such compositions.
  • Detergent compositions containing lower levels of anionic detergent active are commonplace, and are often prepared by spray drying as is well known. At first sight it might be supposed that there would be no difficulty in making compositions with higher concentrations of anionic detergent because many anionic detergent active materials can be prepared in more or less solid form consisting of substantially pure anionic detergent, or at least containing a very high percentage of anionic detergent.
  • US 4213874 discloses the production of aluminosilicates which have an oil absorbtion of at least 75ml/100gram. It is disclosed that they may be used to absorb nonionic detergents in detergent products.
  • US 4707290, GB 1485371 and GB 1591518 disclose the use of absorbent solids to act as carriers for nonionic detergents.
  • Nonionic detergents are a different problem to anionic detergents in that the nonionic materials are generally liquids (which need to be made into solid form) whereby anionic detergents are generally solids in their own right.
  • this invention provides a particulate detergent composition, the particles of which contain at least 30% by weight of anionic detergent active and also contain a particulate filler with an oil absorption value of at least 100ml/100g, this filler being distributed within the particles of the composition in intimate mixture with the detergent active, the amount of the particulate filler being such that the weight ratio of the filler to anionic detergent active lies in the range from 1:10 to 1:1, more preferably 1:8 to 2:3.
  • This ratio range signifies that the amount of filler is not greater than the amount of anionic detergent active.
  • the filler has a mean particle size not greater than 20 micrometres.
  • the invention provides a process of preparing a detergent composition which process comprises incorporating a particulate filler into a fluid or semi-solid composition containing anionic detergent active so that the filler is intimately mixed with the anionic detergent, which particulate filler has an oil absorbtion value in excess of 100ml/100gram, and forming the resultant mixture into a particulate composition with the filler distributed within the particles of the composition, the amounts of anionic detergent active and filler being such that the composition contains at least 30 wt% of anionic detergent and has a weight ratio of filler to detergent active ranging from 1:10 to 1:1.
  • the present invention contains particulate filler with an oil absorption value which is equal to, or exceeds, a minimum value.
  • the oil absorption value of the filler is to be determined by the following test which is in accordance with British Standard 3483 : Part B7 : 1982.
  • the test for oil absorption is performed by placing a weighed sample of the test powder on a plate and then adding linseed oil from a burette. The oil is added a few drops at a time. After each addition the powder is mixed vigorously with the oil using a palette knife. Addition of oil is continued until a paste of smooth consistency is formed. The paste should just spread without cracking or crumbling.
  • the oil absorption value is expressed as the volume (ml) of oil absorbed per 100 gram of powder.
  • a detergent composition according to the invention may be marketed directly as a washing product. Alternatively it can be mixed with other particulate material to form a finished product.
  • a particulate detergent composition according to the invention may be mixed with a second particulate composition which contains other constituents of a final detergent composition, such as detergency builders.
  • a second composition which contains other constituents of a final detergent composition, such as detergency builders.
  • Admixing the composition in accordance with the invention would then serve to increase the overall proportion of detergent active.
  • admixing a composition in accordance with this invention did not increase the overall proportion of detergent active - for instance by achieving beneficial physical properties or by enhancing overall production from available process plant.
  • compositions in accordance with this invention may be accomplished by conventional routes for the manufacture of particulate detergent compositions with a high level of detergent active, provided there is a stage when the detergent active is in a fluid or semi-solid form.
  • the particulate filler is mixed with the detergent active at this stage and leads to an improvement in the properties of the particulate composition which is produced. In some instances a particulate state would not be achieved without the filler.
  • the filler can be mixed with the acid form of the detergent active before neutralization.
  • the filler may even be used as a base to neutralise the acid form of the detergent active, i.e. part of the material used as filler may serve to effect neutralisation. Another possibility is to neutralise the active and mix the filler with the resulting neutralised paste before this becomes solid.
  • a fluid or semi-solid mixture containing the detergent active and the filler may be dried to solidify it, for example by means of a drum dryer.
  • a viscous dough may be produced with a formulation such that the dough can be extruded but will then solidify into a hard solid which can be comminuted to desired particle size.
  • compositions of this invention is by neutralizing an acid form of an anionic detergent active with an alkali metal oxide, hydroxide or carbonate (which may be a true carbonate, bicarbonate or sesquicarbonate) to produce a viscous dough, mixing the particulate filler with this dough, allowing the dough to harden to a solid and comminuting the solid.
  • Neutralization may be effected in the presence of little or no added water.
  • the amount of water added is not more than 10%, more preferably not more than 5%, by weight based on the total weight of acid detergent and carbonate.
  • Such neutralization and admixing of filler can be carried out in various types of high shear mixer.
  • One possibility is a Z-blade mixer
  • another possibility is a cavity transfer mixer whose use as a chemical reactor is disclosed in our European patent application 194812
  • yet another possibility is a twin screw extruder.
  • Other intensive mixers which may be used consist of vessels which contain rotating blades for mixing and high speed knives for dispersing, manufactured for example by Lödige (Trade Mark) ex Morton Machine Co Ltd, Scotland.
  • detergent active may also be mixed in.
  • some preneutralised detergent active or nonionic detergent active may be mixed in.
  • a surface coating of a flow-improving aid which may itself be a particulate solid having the oil absorption property required for the filler used in this invention.
  • a surface coating is conventional. The examples below demonstrate that it does not, by itself, achieve the results achieved by the invention.
  • compositions according to this invention must contain at least 30% by weight of active detergent. Preferably they contain more, e.g. at least 40% or even at least 55%.
  • the amount of detergent active present may range as high as 90% by weight of the composition.
  • anionic detergent actives may be utilized, selected from the conventional categories of anionic, nonionic, cationic and amphoteric.
  • anionic detergent active predominates; even if detergent active from another category is present the anionic detergent active may itself provide 30%, 40% or even 55% or more of the composition.
  • anionic detergent actives useful in this invention are: linear and branched alkyl benzene sulphonates, alkane sulphonates, secondary alcohol sulphates, primary alcohol sulphates, alpha olefin sulphonates, alkyl ether sulphates, fatty acyl ester sulphonates, and mixtures of these.
  • the invention is particularly applicable when at least part of the detergent active is alkyl benzene sulphonate, or a mixture thereof with fatty acyl ester sulphonate or primary alcohol sulphate.
  • the filler should have an oil absorbency, measured according to the test stated, of at least 100ml/100g. Preferably it is higher such as at least 150ml/100g, better at least 200ml/100g and most preferably at least 300ml/100g.
  • the filler may be water soluble but is more likely to be water insoluble.
  • the mean particle size of the filler is not over 20 micrometres, better not over 10 micrometres.
  • a small particle size is especially desirable for an insoluble filler, since it facilitates rinsing the filler away after a detergent composition has been used. Small particle size increases the speed of dissolution of a soluble filler.
  • An alternative way to state desirable particle size is that the particle size distribution includes substantially no particles larger than 50 micrometres. These particles however will generally be aggregates of smaller particles, typically having a size in the range from 5 to 200 nanometres and predominantly (or even wholly) in the narrower range 10 nanometres to 100 nanometres. Such smaller particles can be distinguished by electron microscopy.
  • Suitable inorganic materials tend to be finely divided solids obtained by precipitation.
  • Materials can be produced in such form include silica, aluminosilicates, calcium silicates, magnesium silicates and calcium carbonate.
  • Other materials which can be suitable, subject to testing their oil absorbency, are diatomaceous earths and finely divided cellulosic fillers.
  • the amount of filler included in the composition will generally range from 3% to 50% by weight, usually 5% to 40%.
  • detergent active and specified filler may be included in addition to the detergent active and specified filler, for example detergency builder, alkaline salts or other filler of lesser oil absorbency. A small quantity of moisture will almost always be present.
  • compositions and comparative compositions were prepared using a standard procedure as follows.
  • Linear alkyl benzene sulphonic acid with an average C13 alkyl chain length was charged to a Z-blade mixer. Temperature was maintained at 80°C. Sodium carbonate was added over ten minutes with continuous mixing during which time carbon dioxide was evolved. A particulate filler was then added over a period of 15 minutes and mixing continued for 5 minutes.
  • the dough produced by this procedure was removed from the mixer and cut into pellets. These were allowed to cool to ambient temperature, hardening as they did so.
  • the pellets were milled into a powder. This was mixed with 2% by weight of a conventional flow aid which coated the surfaces of the powder particles.
  • the mean particle size, bulk density and dynamic flow rate of the resulting powders were tested. Their content of sodium alkyl benzene sulphonate was checked analytically and found to be approximately 60% by weight, except in Example 5 where the content was approximately 52% by weight.
  • the dynamic flow rate, in ml/s, was measured using a cylindrical glass tube having an internal diameter of 35mm and a length of 600mm. The tube was securely clamped with its longitudinal axis vertical. Its lower end was terminated by means of a smooth cone of polyvinyl chloride having an internal angle of 15° and a lower outlet orifice of diameter 22.5mm. A beam sensor was positioned 150mm above the outlet, and a second beam sensor was positioned 250mm above the first sensor.
  • the outlet orifice was temporarily closed, for example, by covering with a piece of card, and powder was poured into the top of the cylinder until the powder level was about 100mm above the upper sensor. The outlet was then opened and the time t (seconds) taken for the powder level to fall from the upper sensor to the lower sensor was measured electronically. The result is the tube volume between the sensors, divided by the time measured.
  • Caking resistance of the particles and their hardness after exposure to air was tested by the following procedure: The powder was spread in a thin layer in a dish and exposed to atmosphere at 37°C and 70% relative humidity. After exposure for one week the powder was graded for feel. Also a sample of the powder which had been exposed was compressed under a standard load in a 2cm diameter cylindrical die to form a pellet. The hardness of the material in this pellet was tested with a cone penetrometer. The cone had an angle of 9° 10′ and was applied under 100 gram load for 10 seconds.
  • compositions of these examples and comparative examples are set out in Tables 1 and 2 below.
  • comparative example A an increased quantity of sodium carbonate was used rather than a separate particulate filler.
  • the sodium carbonate was added over a period of 15 minutes in view of the greater quantity used.
  • Sodium primary alcohol sulphate paste or sodium alkyl benzene sulphonate paste was charged to a Z-blade mixer. Temperature was maintained at 80°C. Sodium carbonate was added over five minutes with continuous mixing. A particulate filler was then added over a period of 15 minutes and mixing continued for 5 minutes.
  • the dough produced by this procedure was removed from the mixer and cut into pellets. These were dried and allowed to cool to ambient temperature, hardening as they did so. Excepting pellets from Example E, which could not be milled as they were too soft, the pellets were milled into a powder. This was mixed with 2% by weight of a conventional flow aid (Alusil ET).
  • Examples 7 and E are an instance where a particulate solid was not achieved without the filler.

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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)
  • Inorganic Chemistry (AREA)
  • Detergent Compositions (AREA)

Claims (9)

  1. Teilchenförmiges Waschmittelgemisch, umfassend
    (i) Teilchen, die mindestens 30 Gew.-% eines anionischen Waschmittelaktivstoffs enthalten und ebenfalls einen teilchenförmigen Füllstoff mit einem Ölabsorptionswert von mindestens 100 ml/100 g enthalten, wobei dieser Füllstoff innerhalb der Teilchen des Mittels in inniger Vermischung mit dem Waschmittelaktivstoff verteilt ist und das Gewichtsverhältnis von dem Füllstoff zu anionischem Waschmittelaktivstoff im Bereich von 1:10 bis 1:1 liegt, und
    (ii) weiteres festes teilchenförmiges Material.
  2. Gemisch nach Anspruch 1, wobei der Füllstoff einen Ölabsorptionswert von mindestens 200 ml/100 g aufweist.
  3. Gemisch nach Anspruch 1 oder 2, wobei der Füllstoff eine mittlere Teilchengröße von nicht mehr als 20 »m aufweist.
  4. Gemisch nach Anspruch 3, wobei der Füllstoff wasserunlöslich ist.
  5. Gemisch nach einem der vorangehenden Ansprüche, wobei die Teilchengrößenverteilung des Füllstoffs derart ausgelegt ist, daß im wesentlichen keine Füllstoffteilchen eine Größe von mehr als 50 »m aufweisen.
  6. Gemisch nach einem der vorangehenden Ansprüche, umfassend den Füllstoff in einer Menge von 3 bis 50 Gew.-% des Gesamtgemisches.
  7. Verfahren zur Herstellung eines teilchenförmigen Waschmittelgemisches, wobei das Verfahren umfaßt
    (i) Herstellen eines teilchenförmigen Mittels durch Einmischen eines teilchenförmigen Füllstoffes in ein flüssiges oder halbfestes Mittel, das einen anionischen Waschmittelaktivstoff enthält, so daß der Füllstoff innig mit dem anionischen Waschmittelaktivstoff vermischt wird, wobei der teilchenförmige Füllstoff einen Ölabsorptionswert oberhalb von 100 ml/100 g aufweist und Formen des erhaltenen Gemisches zu einem teilchenförmigen Mittel mit dem Füllstoff, der innerhalb der Teilchen des Mittels verteilt wird, wobei die Mengen an anionischem Waschmittelaktivstoff und Füllstoff derart ausgelegt sind, daß das Mittel mindestens 30 Gew.-% anionischen Waschmittelaktivstoff enthält und ein Gewichtsverhältnis von Füllstoff zu anionischem Waschmittelaktivstoff im Bereich von 1:10 bis 1:1 aufweist, und
    (ii) Vermischen des Mittels mit weiterem festen teilchenförmigen Material.
  8. Verfahren nach Anspruch 7, wobei die Herstellung des Mittels Neutralisieren der Säureform des anionischen Waschmittelaktivstoffs mit einem Alkalimetallcarbonatsalz unter Herstellung eines halbfesten Mittels, enthaltend den neutralisierten Waschmittelaktivstoff, einschließt, wobei der Füllstoff dann zu dem Mittel zugegeben wird und das Verfahren anschließend Härtenlassen des erhaltenen Gemisches und Zerkleinern umfaßt.
  9. Verfahren nach Anspruch 8, wobei die Menge an Wasser (falls vorliegend) zu der Säureform des anionischen Waschmittelaktivstoffs zugegeben wird und das Alkalimetallcarbonatsalz nicht mehr als 10 Gew.-%, bezogen auf die Gesamtmenge an Säure und Carbonatsalz, ausmacht.
EP90312779A 1989-11-24 1990-11-23 Reinigungsmittel Revoked EP0430603B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB898926644A GB8926644D0 (en) 1989-11-24 1989-11-24 Detergent composition
GB8926644 1989-11-24

Publications (3)

Publication Number Publication Date
EP0430603A2 EP0430603A2 (de) 1991-06-05
EP0430603A3 EP0430603A3 (en) 1991-11-27
EP0430603B1 true EP0430603B1 (de) 1995-01-25

Family

ID=10666891

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90312779A Revoked EP0430603B1 (de) 1989-11-24 1990-11-23 Reinigungsmittel

Country Status (10)

Country Link
EP (1) EP0430603B1 (de)
JP (1) JPH03177499A (de)
AU (1) AU629429B2 (de)
BR (1) BR9005872A (de)
CA (1) CA2030306C (de)
DE (1) DE69016374T2 (de)
ES (1) ES2067699T3 (de)
GB (1) GB8926644D0 (de)
NO (1) NO176405C (de)
ZA (1) ZA909423B (de)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2721616A1 (fr) 1994-06-22 1995-12-29 Hoechst France Compositions de tensioactifs anioniques en poudre, en perles ou en granulés, leur procédé de préparation et leur utilisation dans les produits de nettoyage et d'entretien.
DE4440621A1 (de) * 1994-11-14 1996-05-15 Henkel Kgaa Scheuerpulver mit verbesserter Rieselfähigkeit und Verfahren zu ihrer Herstellung
GB9825558D0 (en) 1998-11-20 1999-01-13 Unilever Plc Granular detergent components and particulate detergent compositions containing them
DE19961687A1 (de) * 1999-12-21 2001-07-05 Henkel Kgaa Wirkstoffkombination zur Einarbeitung in Wasch- und Reinigungsmittel
WO2014198034A1 (en) * 2013-06-13 2014-12-18 The Procter & Gamble Company Granular laundry detergent
US9828569B2 (en) 2013-06-13 2017-11-28 The Procter & Gamble Company Granular laundry detergent
EP3022279B1 (de) 2013-07-18 2019-03-27 Galaxy Surfactants Ltd. Fliessfähige, feste und hochaktive alkylethersulfate
WO2016145643A1 (en) * 2015-03-19 2016-09-22 The Procter & Gamble Company Structured detergent particles and granular detergent compositions containing the same

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL200200A (de) * 1954-09-06
US4049586A (en) * 1974-09-27 1977-09-20 The Procter & Gamble Company Builder system and detergent product
ES441319A1 (es) * 1974-09-27 1977-07-01 Procter & Gamble Procedimiento para preparar granulos conteniendo carbonato calcico.
GB1583081A (en) * 1977-05-18 1981-01-21 Unilever Ltd Production of detergent compositions
ES8607378A1 (es) * 1984-08-06 1986-05-16 Kao Corp Una composicion detergente en polvo de gran densidad
US4919847A (en) * 1988-06-03 1990-04-24 Colgate Palmolive Co. Process for manufacturing particulate detergent composition directly from in situ produced anionic detergent salt

Also Published As

Publication number Publication date
GB8926644D0 (en) 1990-01-17
NO905080L (no) 1991-05-27
ES2067699T3 (es) 1995-04-01
DE69016374D1 (de) 1995-03-09
CA2030306C (en) 1998-12-22
NO176405B (no) 1994-12-19
EP0430603A3 (en) 1991-11-27
BR9005872A (pt) 1991-09-24
AU6689990A (en) 1991-05-30
ZA909423B (en) 1992-07-29
CA2030306A1 (en) 1991-05-25
NO905080D0 (no) 1990-11-23
DE69016374T2 (de) 1995-05-24
AU629429B2 (en) 1992-10-01
NO176405C (no) 1995-03-29
JPH03177499A (ja) 1991-08-01
EP0430603A2 (de) 1991-06-05

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