GB2190921A - Granular detergent composition - Google Patents

Granular detergent composition Download PDF

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Publication number
GB2190921A
GB2190921A GB08612838A GB8612838A GB2190921A GB 2190921 A GB2190921 A GB 2190921A GB 08612838 A GB08612838 A GB 08612838A GB 8612838 A GB8612838 A GB 8612838A GB 2190921 A GB2190921 A GB 2190921A
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GB
United Kingdom
Prior art keywords
clay
microns
granular
particle size
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.)
Withdrawn
Application number
GB08612838A
Other versions
GB8612838D0 (en
Inventor
Graham Andrew Catton
Paul Michael Hill
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
Original Assignee
Unilever PLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Unilever PLC filed Critical Unilever PLC
Priority to GB08612838A priority Critical patent/GB2190921A/en
Publication of GB8612838D0 publication Critical patent/GB8612838D0/en
Publication of GB2190921A publication Critical patent/GB2190921A/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions
    • C11D11/02Preparation in the form of powder by spray drying
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/06Powder; Flakes; Free-flowing mixtures; Sheets
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/12Water-insoluble compounds
    • C11D3/124Silicon containing, e.g. silica, silex, quartz or glass beads
    • C11D3/1246Silicates, e.g. diatomaceous earth
    • C11D3/1253Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite
    • C11D3/126Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite in solid compositions

Abstract

A process for preparing a granular detergent composition, especially for fabric washing, comprises mixing a first granular component containing more than 8% nonionic detergent and more than 20% inorganic salt with a second granular component which is particles of a fabric softening clay agglomerated with water. Both components have a particle size of 150-2000 microns. The clay particles are less than 150 microns in size. The first component may be made by spray drying and the inorganic salt may be a detergency builder. The clay is preferably a smectite. The process reduces the negative effect of the detergent on the performance of the clay.

Description

SPECIFICATION Processforpreparing a detergent composition This invention relates to a process for preparing a detergent composition, in particular a detergentcomposition for washing fabrics and providing said fabrics with a softening benefit.
It is common practice to wash fabrics in detergent compositions which contain a detergent active material for removing soil from the fabrics. With some fabrics, especially of natural origin, repeated washing can lead to fabric harshness, giving the fabric an unpleasantfeel. Forsome years fabric conditioning products have been available, intended interalia for alleviating thisfabric harshness by softening the fabrics in a post washing step, eg in the rinse step of a fabric laundering process. There has been a desire to provide a single detergent composition which would be capable of both washing and softening fabrics to overcome the inconvenience of using separate products.
According to GB 1 400898 (Procter & Gamble) a possible solution to this problem isto include inthe detergent composition a three-layer smectite clay containing material having a cation exchange capacity of at least 50 meq/l OOg together with an anionic or similar detergent active material.
According to GB 1 462484 (Procter & Gamble), such clays are almost ineffective in the presence of significant amounts of nonionic detergents, and that such clays should therefore be replaced by modified clays which carry a proportion of quaterniary ammonium cations. Such modified clays are generally more costly than their un-modified counterparts and have not been widely used.
However, detergent compositions containing significant amounts of nonionic detergent active material can be beneficial. Thus, for example, such compositions generally generate less foam in use. They arethere- fore more suitableforuse in automatic washing machines and the need to include foam control agents in such compositions is reduced or removed. Further, compositions containing high levels of nonionic detergent active material are especially effective on removing greasy or oily soils from fabrics.
It is therefore an object of the present invention to provide a process for preparing detergent compositions containing high levels of nonionic detergent active material and clay as a fabric softener, while reducing or overcoming the negative effects ofthe nonionic active on the performance ofthe clay. We have nowsurprisingly discovered that this object can be achieved by preparing the composition in such a manner as to keep the nonionic detergent active material and the clay separate from each other. While one might suppose that in a wash liquorformed by adding such a composition to water, the nonionic detergent active material and the clay could interact, we have found that this does not occur, at least not to a significant extent within the time period of the washing process.
Thus according to the invention there is provided a process for preparing a granular detergent composi- tion comprising the steps of: (i) preparing afirst granularcomponent having a particle size of from 150 to 2000 microns comprising more than 8% byweightofa nonionic detergent active material and more than 20% by weight of an inorganic salt, said percentages being based on theweightofthefinal composition; (ii) preparing a second granular component by agglomerating a fabric softening clay containing material having a particle size of less than 150 microns with water to form agglomerates having a particle size offrom 150to2000 microns;; (iii) mixing said first and second granular components in the substantial absence of water.
Thefirstgranularcomponent may be made by granulation but a process involving spray drying is prefer.
red.
A preferred particle size is 200 to 1000 microns. The term "particle size" as used herein means the weight average particle size as measured by sieve analysis and preferably the majority of particles have a size falling within the given range.
The level of nonionic detergent active inthefirst granularcomponent is preferably less than 15%, such as from 8.5 to 12% by weight, based on the final composition.
Suitable nonionic detergent compounds which may be used include in particularthe reaction products of compounds having a hydrophobic group and a reactive hydrogen atom, for example aliphaticalcohols, acids, amides or alkyl phenols with alkylene oxides, especially ethylene oxide either alone or with propylene oxide.
Specific nonionic detergent compounds are alkyl (C6-C22) phenols-ethylene oxide condensates, generally upto 25 EO, ie 25 units of ethylene oxide per molecule,thecondensation products of aliphatic(C8-C18) primary or secondary linear or branched alcohols with ethylene oxide, generally upto40 EO, and products may by condensation of ethylene oxide with the reaction products of propylene oxide and ethylendiamine.
Other so-called nonionic detergent compounds include long chain tertiary amine oxides, long chain tertiary phosphine oxides and dialkyl sulphoxides.
The inorganicsaltwhich is required to be present in thefirstgranularcomponentwill normally beconstituted by a detergency builder material, but other salts more usually known in the role of buffering agents (such as sodium silicate) orfillers (such as sodium sulphate) may also be used.
The detergency builder, when present, may be any material capable of reducing the level of free clacium 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 dispersion ofthe fabric softening clay material. The level ofthe detergency builder may be from 20% to 70% by weight, most preferably from 25% to 50% by weight.
Examples of detergency builders include precipitating builders such as the alkali metal carbonates, bicarbonates, ortho phosphates, sequestering builders such as the alkali metal tripolyphosphates or in exhange builders such as the amorphous alkalimetal aluminosilicates or the zeolites. Organic detergency builders, such as alkali metal citrates or nitrilotriacetates may be present in the first granular component.
The clay containing material may be any such material capable of providing a fabric softening benefit.
Usually these materials will be of natural origin containing a th ree-layer swel lable smectite clay which is ideally of the calcium and/or sodium montmorillonite type. It is preferable to exchange the natural calcium clays to the sodium form by using sodium carbonate, either before or during granulation, as described in GB 2 138037 (Colgate). The effectiveness of a clay containing material as afabricsoftenerwill depend interalia on the level of smectite clay. Impurities such as calcite, feldspar and silica will often be present. Relatively impure clays can be used provided that such impurities are tolerable in the composition.
The second granular component is prepared by agglomerating a clay containing material with water. The naturally occurring clay containing material is first milled to a particle size of less than 150 microns, preferably from 30 to 100 microns. At this stage any non-clay gritty material in the clay containing material may be removed. The fine particles are then agglomerated to the required size with water. Pure water is suitable, there being no necessity to add further binding agents. However,the presence of up to about 1% inorganic salts, including those derived from water hardness, in the water may be tolerated.
The level of the fabric softening clay material in the composition should be sufficient to provide a softening benefit, such as from 1.5% to 35% by weight, most preferably from 4% to 15% by weight, calculated on the basis ofthe clay material perse, and therefore the level of agglomerated clay containing material should be chosen accordingly.
The particle sizes of the first and second granular components should preferably be approximatelythe same so as to prevent undue segregation after mixing. Thus it is preferred that the ratio ofthe particle sizes of the two components is within 2:1 to 1 :2, most preferably within 1.5:1 to 1:1.5.
The two granular components should be mixed in the substantial absence of water. Thus the first granular component should not have a free-water content which is so high as to cause the particles thereof to be sticky, i.e. when mixing occurs the first granular component should be in the form of a free flowing powder.
The clay granules preferably have a moisture content of less than 15%, preferably less than 12%, where the term "moisture" is that water which is lost on drying the clay granules to 1 35"C. In particular it is most desirable not to add any free water during the mixing step. The mixing may be carried out at room temperature or at a temperature not significantly higherthan the melting point of the nonionic detergent active material, such as less than about50"C.
Apart fro the ingredients already mentioned a number of optional ingredients may aiso be present, either in the first component or added separately to the compositions.
In particular other detergent active materials may be present. Despite the advantages of the nonionic detergent active, some additional benefits may be derived from the presence of low levels, ie up to about 1.5% by weight, of an anionic detergent active. The preferred anionic detergent compounds aresodium (Cii-Ci5) alkyl benzene sulphonates and sodium (C16-Cr8) alkyl sulphates.
Examples of other additives which may be present in the composition include the lather boosters such as alkanolamides, particularly the monoethanolamides derived from palm kernel fatty acids and coconutfatty acids, lather depressants, oxygen-releasing bleaching agents such as sodium perborate and sodium percarbonate, peracid bleach precursors, chlorine-releasing bleaching agents such as tricloroisocyanuric acid, inorganic salts such as sodium sulphate, and, usually present in very minor amounts, flourescent agents, perfumes, enzymes such as proteases and amylases, germicides and colourants.
The invention will now be illustrated by the following non-limiting examples: Example 1 Afirstgranulewas prepared according tothe following formulation: Ingredient Parts by weight Anionic detergent active 1.5 Nonionic detergent active 8.5 Alkaline sodium silicate 7.5 Sodiumtripolyphosphate 20.0 Sodium sulphate 10.0 Minor ingredients 2.2 The nonionic active used was Dobanol 25-7EO (Trade Mark) (ex Shell). The anionic active was sulphonated Dobane 113 (exShell). This granulewas prepared by spray drying a slurry containing the listed ingredients, to an average particle size of 500 microns and a total water content of 7.5 parts.
To these granules were added 10 parts of agglomerated bentonite having an average particle size of 700 microns and a moisture content of 1.2 parts (12%). The clay used was sodium bentonite ex Steetley.Also added at this stage were 16 parts of sodium perborate tetrahydrate, 9 parts of sodium carbonate, 3.75 parts of neutral sodium orthophosphate, about 3.75 parts of sodium sulphate and 0.3 parts enzymes making a total product of 100 parts by weight.
Terry towelling cotton test cloths were then washed in an automatic washing machine using a dosage of 1 20g product (the machine capacity was 20 1). The water hardness was 26 FH (equivalent to 26 x 104 molar free calcium ions). The washing temperature was 95"C and the washing time was 55 minutes. Afterwashing and rinsing, the fabrics were line dried at 60% RH constant humidity and 21and assessed for softness.
The experiment was repeated with various modifications asfollows: (a) the clay was processed in the slurry together with other components of the first granule (b)theclaywasommitted (c) the clay was omitted and the ratio of anionic to nonionic active was increased to 6:4.
In all cases the softness of the fabrics was found to be significantly better with the composition of Example 1 compared with any of alternatives (a), (b) or (c).
When these experiments were repeated at 4000 using a wash time of 20 minutes, similar conclusions could be drawn from the results.

Claims (1)

1. A process for preparing a granular detergent comprising the steps of: (i) preparing a first granular component having a particle size of from 150 to 2000 microns comprising more than 8% by weight of a nonionic detergent active material and morethan 20% by weight of an inorganic salt, said percentages being based on the weight of the final composition; (ii) preparing a second granular component by agglomerating a fabric softening clay containing material having a particle size of less than 150 microns with water to form agglomerates having a particle size offrom 150 to 2000 microns; (iii) mixing said first and second granular components in the substantial absence of water.
GB08612838A 1986-05-27 1986-05-27 Granular detergent composition Withdrawn GB2190921A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB08612838A GB2190921A (en) 1986-05-27 1986-05-27 Granular detergent composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB08612838A GB2190921A (en) 1986-05-27 1986-05-27 Granular detergent composition

Publications (2)

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GB8612838D0 GB8612838D0 (en) 1986-07-02
GB2190921A true GB2190921A (en) 1987-12-02

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0353994A2 (en) * 1988-08-01 1990-02-07 Southern Clay Products, Inc. Coated clay granules
EP0362665A1 (en) * 1988-10-04 1990-04-11 Henkel Kommanditgesellschaft auf Aktien Process for preparing a particulate detergent composition
WO1991009101A1 (en) * 1989-12-20 1991-06-27 Henkel Kommanditgesellschaft Auf Aktien Process for producing a granular, softening detergent additive
WO1993025651A1 (en) * 1992-06-18 1993-12-23 Unilever N.V. Machine dishwashing composition
WO2000024859A1 (en) * 1998-10-26 2000-05-04 The Procter & Gamble Company Detergent particles and processes for making them
WO2000078908A1 (en) * 1999-06-21 2000-12-28 The Procter & Gamble Company Detergent particles and processes for making them
WO2000078914A1 (en) * 1999-06-21 2000-12-28 The Procter & Gamble Company Detergent particles and methods for making them
US6579844B1 (en) 2000-06-20 2003-06-17 The Procter & Gamble Co. Detergent particles and methods for making them
US6833346B1 (en) 1999-06-21 2004-12-21 The Procter & Gamble Company Process for making detergent particulates

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0353994A2 (en) * 1988-08-01 1990-02-07 Southern Clay Products, Inc. Coated clay granules
EP0353994A3 (en) * 1988-08-01 1990-10-17 Southern Clay Products, Inc. Coated clay granules
US5061397A (en) * 1988-08-01 1991-10-29 Ecc International Limited Coated clay granules
EP0362665A1 (en) * 1988-10-04 1990-04-11 Henkel Kommanditgesellschaft auf Aktien Process for preparing a particulate detergent composition
WO1990004015A1 (en) * 1988-10-04 1990-04-19 Henkel Kommanditgesellschaft Auf Aktien Process for producing particulate detergents
WO1991009101A1 (en) * 1989-12-20 1991-06-27 Henkel Kommanditgesellschaft Auf Aktien Process for producing a granular, softening detergent additive
WO1993025651A1 (en) * 1992-06-18 1993-12-23 Unilever N.V. Machine dishwashing composition
WO2000024859A1 (en) * 1998-10-26 2000-05-04 The Procter & Gamble Company Detergent particles and processes for making them
WO2000078908A1 (en) * 1999-06-21 2000-12-28 The Procter & Gamble Company Detergent particles and processes for making them
WO2000078914A1 (en) * 1999-06-21 2000-12-28 The Procter & Gamble Company Detergent particles and methods for making them
US6833346B1 (en) 1999-06-21 2004-12-21 The Procter & Gamble Company Process for making detergent particulates
US6579844B1 (en) 2000-06-20 2003-06-17 The Procter & Gamble Co. Detergent particles and methods for making them

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Publication number Publication date
GB8612838D0 (en) 1986-07-02

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