STABILISED GEL SYSTEM AND PRODUCTION THEREOF

Description

[0001] This invention relates to a stabilised gel system for supporting finely divided particulate matter in suspension, to detergent compositions and abrasive preparations based on such a stabilised gel system, and to the production thereof.

[0002] In recent years, mainly for reasons of manufacturing economics, heavy duty built liquid detergents have made in-roads into the spray-dried washing powder market with the result that much work has taken place both on the physics and on the chemistry of product formulation.

[0003] Each type of preparation contains the same basic ingredients and in both cases it has been necessary to incorporate materials which can only be regarded as inert diluents of the active compounds in the formulation. In the case of solid preparations the diluent has been alkali metal sulphates whilst in the case of the liquid it has simply been water.

[0004] Herein lies the problem in the case of the heavy duty built liquid detergents because the desired performance in a washing machine requires the presence of high percentages of alkaline materials (builders) along with percentages of surface active agents in the region of 9% to 20% (active ingredients). At these concentrations the chemical groupings are incompatible as far as homogeneity of the product is concerned. Such surface active ingredients normally include an anionic surfactant or tenside and may further include one or more non-ionic surfactants. Examples of anionic surfactants include the sodium salts of alkyl benzene sulphonic acids and of alkyl sulphonic acids. As examples of non-ionic surfactants there can be mentioned polyalkylene oxide ethers of alkyl alcohols or alkylphenols, as well as the monoethanolamides of fatty acids, such as coconut fatty acid monoethanolamide.

[0005] It follows therefore that conventional heavy duty laundry detergents are composed of two physical phases and consist essentially of saturated solutions of the builders, with excess builder particles present in the liquid mass as a dispersion, and an aqueous solution of surfactant micelles some of which have been salted-out by the electrolytic action of the saturated solution of the builders.

[0006] Such a complex mixture of materials with their own interactions and incompatibilities poses a problem to the detergent formulator.

[0007] US-A-3708428 and US-A-3899447 teach detergent compositions containing silica colloids. The colloidal silica is formed in situ as a sol by the reaction of a preheated solution of a water-soluble or dispersible alkali silicate with a preheated anionic, detergent-forming organic acid. These documents do not disclose any compositions in which relatively large quantities of particulate builders are held in suspension and, in fact, it is expressly taught that builders such as complex phosphates (e.g. sodium tripolyphosphate) should be restricted to levels of concentration of the order of 4.0% by weight or lower.

[0008] EP-A-0191372 relates to two-component alkaline cleaners having a pH of 11 or greater. The cleaners are said to be suitable for cleaning rigid materials such as metal and glass. One of the components of the system is an aqueous silicic acid dispersion which contains detergent builder. The component containing the silicic acid dispersion also requires the presence of from 0.3 to 3% by weight of a stabiliser, which is usually based on xanthan.

[0009] In order to produce a smooth, pourable, homogeneous product for entry into the market place a very large amount of experimental work has been undertaken by laboratories throughout the world and some of the relevant teachings are to be found, for example, in US-A-3351557, US-A-3574122, CA-A-917631, GB-A-948617 and GB-A-2153839. Reference can also be made to GB-B-2123846, EP-B-086614, EP-B-0170091, EP-B-0151884, GB-B-2153380 and EP-A-0295021. In all cases the aim has been to produce some sort of structured liquid system which can hold the excess inorganic builder particles in a thixotropic suspension. This has been accomplished in various ways such as by an emulsion technique, by micronising, or by ball-milling. Typically such a conventional liquid built detergent composition has a storage life of at least several months. However, upon centrifuging at 800g for 17 hours at 25°C such compositions normally separate into two or more phases. Although such compositions have good storage properties, it would be desirable to provide liquid built detergent compositions with even better storage characteristics.

[0010] It is apparent that in such heavy duty built systems the builders and the surfactants physically interact so that each is above the limits of its water solubility.

[0011] In the case of the builders the system is saturated with respect to the soluble salts and the excess must be homogeneously held in stable suspension, while in the case of the surfactants the tenside micelles are either forced to contract from a linear conformation to gathered-up bundles, or at the limit, to be salted out of solution as high strength surfactant hydrates. Overall, therefore, the separated phases are in equilibrium with their own moieties in the continuous aqueous system. Normally, upon salting out, anionic surfactants give rise to formation of solid hydrates. The presence of such solid anionic surfactant hydrates can give rise to formation of a composition in which the presence of spherulites of surfactant hydrate can be detected or in which the composition contains the surfactant as a lamellar liquid crystal or solid hydrate interspersed with an aqueous phase containing dissolved electrolyte. On the other hand non-ionic surfactants do not, generally speaking, form hydrates, although they may be salted out of solution due to the presence of high concentrations of dissolved electrolyte.

[0012] There is accordingly a need in the art to provide an improved system for supporting finely divided particulate matter, such as builders or abrasives, in suspension. There is also a need for an improved liquid built detergent formulation which is stable under normal storage conditions for extended periods. There is a further need in the art to provide a liquid built detergent composition, and a process for making same, in which the problems of the prior art are substantially obviated.

[0013] The present invention accordingly seeks to provide an improved liquid built detergent composition and a process for making same in which the problems encountered in the prior art are substantially obviated. It also seeks to provide an improved system for supporting finely divided particulate matter in suspension.

[0014] According to the present invention there is provided the use of a stabilised gel system for supporting finely divided particulate matter in suspension, the stabilised gel system comprising a hydrosol of silicic acid stabilised by entanglement with micelles of a tenside. Preferably the tenside is one containing one or more sulphonate groups. Such a stabilised gel system can conveniently be produced by at least partially neutralising a sodium silicate solution with a tenside-forming acid containing one or more sulphonic acid groups. Such a stabilised gel system is normally acidic or near neutral in character. Typically the pH of a liquid support system in accordance with the invention lies in the range of from 1.0 to 9.0. Normally it will have a pH of not more than 8.0, e.g. in the range of from 4.0 to 7.5.

[0015] In another aspect of the invention there is provided a liquid built detergent composition comprising a stabilised gel system comprising a hydrosol of silicic acid stabilised by entanglement with micelles of a tenside and particles of a builder substantially uniformly distributed therein.

[0016] Also provided in accordance with the present invention is an abrasive preparation comprising a hydrosol of silicic acid stabilised by entanglement with micelles of a tenside in which are dispersed finely divided particles of an abrasive material. Preferably the tenside in such an abrasive preparation is one containing one or more sulphonate groups. Such an abrasive composition can be formulated as an oven cleaner, for example, or as a cleaner for hard surfaces.

[0017] There is further proposed, according to a still further aspect of the invention, a process for the production of a stabilised gel system for supporting finely divided particulate matter in suspension which comprises neutralising a solution of an alkali metal silicate to a pH in the range of from 1.0 to 7.0 in the presence of a tenside thereby to produce a hydrosol of silicic acid stabilised by entanglement with tenside micelles.

[0018] Neutralisation may be effected by addition of an acid to a solution of an alkali metal silicate that contains also at least one surfactant. The acid may be selected from hydrochloric acid, sulphuric acid, sulphamic acid, phosphoric acid, formic acid, acetic acid, citric acid, and mixtures of two or more thereof. Alternatively neutralisation may be effected by titration of the solution of alkali metal silicate with a tenside-forming acid containing one or more sulphonic acid groups.

[0019] In another mode of production of a stabilised gel system for use according to the invention a solution having a pH of not more than 7.0 is produced by dissolving in an aqueous medium a tenside-forming acid containing one or more sulphonic acid groups and an alkali metal tripolyphosphate and a solution of an alkali metal silicate is added thereto.

[0020] The invention further relates to a process for the production of a liquid built detergent which comprises neutralising a solution of an alkali metal silicate such as sodium silicate, to a pH in the range of from 1.0 to 7.0 in the presence of a tenside thereby to produce a hydrosol of silicic acid stabilised by entanglement with tenside micelles and, either before or after completion of the neutralisation step, incorporating a builder in the composition. In such a process neutralisation can be effected by addition of an acid to a solution of an alkali metal silicate that also contains at least one surfactant and in which the builder is thereafter added. Alternatively neutralisation can be effected by titration of the solution of alkali metal silicate with a tenside-forming acid containing one or more sulphonic acid groups.

[0021] In another form of such a process a solution having a pH of not more than 7.0 is produced by dissolving in an aqueous medium a tenside-forming acid containing one or more sulphonic acid groups and an alkali metal tripolyphosphate and a solution of an alkali metal silicate is added thereto.

[0022] In the detergency technology of the prior art there are no examples disclosed, so far as is known, in which a pourable gel system, based on silicates, has been produced by a chemical reaction. The reason for this can be found in the fact that chemical theory does not indicate that such gel or colloidal systems are possible by this route. However, according to the present invention it is possible to produce a very stable, pourable gel or viscous colloidal system by the chemical interaction of an anionic surfactant with an alkali metal silicate constituent of the builder system.

[0023] Amongst the known effects of acids on solutions of alkali metal silicates it is known that:-

(1) When a strong acid is added to a sodium silicate solution a precipitate of silicic acid separates as a gelatinous mass (hydrogel) but some still remains in colloidal solution (hydrosol). It is possible to dialyse the hydrosol but a 5% solution of colloidal silica is about the maximum strength that can be obtained.

(2) The passage of silicic acid from the sol to the gel condition is retarded by the presence of a little acid, or hydroxide, but it is very much accelerated by the addition of sodium carbonate or of a phosphate; in fact the addition of one of the latter compounds invariably leads to rapid coagulation.

(3) When the pH value of a solution of sodium silicate is reduced from its normal value, which is typically in the range of from 11.0 to 13.0, to a value in the range of from 8.0 to 9.0 by the use of sodium hydrogen carbonate, the hydrosol produced is stable for a matter of hours, before coagulation occurs, and as such is used in water and sewage treatment as "activated silica".
In the new silicate chemistry work, which forms the basis of this invention, the following unexpected results can be disclosed:-

(4) When a strong solution of sodium silicate, for example one produced by a few dilutions of the 47% grade known as CRYSTAL 120 H, H, is titrated with an anionic detergent, in the free sulphonic acid form, to a pH value in the range of from 1.0 to 8.0, a soft gel is produced which can be diluted with water to give a stable syrup without precipitates.

(5) When a 5% solution of sodium metasilicate or sodium silicate soluble glass is titrated to pH 7.0 with a 10% w/w solution of dodecylbenzene sulphonic acid, a transparent syrup is produced which is stable for an extended period.

(6) When a quaternary ammonium chloride (QAC) such as a benzalkonium chloride is added to a sodium silicate solution and the pH value is reduced to 7.0 to 8.0, a transparent syrup is produced which is stable and does not precipitate silicic acid even though a mineral acid, such as hydrochloric acid, is used to neutralise the silicate solution. Such a syrup can be used as a stabilised gel system for supporting, for example, abrasive particles, to form an abrasive preparation such as an oven cleaner.

(7) Similar results to those summarised at (6) above were obtained when a sodium silicate solution containing a non-ionic surfactant, e.g. Synperonic A7 ™, was titrated to pH 7.0 to 8.0 using hydrochloric acid. Again, the resulting syrup can be used as a stabilised gel system for suspending finely divided particulate matter such as abrasive parties or builder particles.

[0024] From this work it can be seen that it is possible to interfere with normal hydrosol-hydrogel reactions of acidified sodium silicate solutions, as described above at (1), and thus force the separating silicic acid into a physical entanglement with the tenside micelles so that mutual stability is attained with respect to the colloidal silica and the surfactant moieties.

[0025] In particular it can be shown that it is not possible to precipitate hydrogels of silicic acid when sodium silicate is decomposed, even at pH 1.0, by detergent sulphonic acids. This result would not be chemically predictable. The resulting pourable colloidal viscous syrups are excellent media for uniting the separate phases of heavy duty laundry detergent liquids. During manufacture of these liquids little attention need be paid to the order in which the ingredients of a liquid detergent formulation are added, according to the teachings of this invention, so long as the sodium silicate in aqueous solution is first neutralised, or partly neutralised, by the tenside sulphonic acid, or acids, of the formulation or by neutralisation or partial neutralisation with non-tenside acids in the presence of tensides or surfactants.

[0026] Even though an anionic surfactant in the free sulphonic acid form, such as dodecyl benzene sulphonic acid, is a strong acid, a gelatinous precipitate of silicic acid, i.e. a hydrogel, is not produced when it is used to neutralise a sodium silicate solution. Instead a viscous solution, i.e. a hydrosol, is produced. This result is consistent with the theory that a stabilised gel system according to the invention comprises a hydrosol of silicic acid stabilised by entanglement with micelles of a tenside. Further evidence for such a structure is provided by electron microscopy studies on a liquid built detergent composition prepared from a stabilised gel system according to the invention. Such studies indicated that the liquid built detergent contained a largely featureless granular structure with crystals of builder distributed apparently at random. In particular such electron microscopy studies showed no sign of any spherulites and no sign of any lamellar structure. Hence there was no evidence that any of the surfactant was present as a lamellar liquid crystal or solid hydrate. Thus there did not appear to be any salting out of the anionic surfactant (i.e. sodium salt of dodecyl benzene sulphonic acid) despite the presence of large amounts of builder (i.e. sodium tripolyphosphate) in excess of its solubility limit. This is in contrast to the results reported in EP-B-0086614 and in GB-B-2123846, in which a vesicular, spherulitic or lamellar structure was apparent in a liquid built detergent composition containing comparable amounts of builder and of anionic surfactant added as a sodium salt.

[0027] Examples of anionic surfactants (named here, for convenience, as elsewhere in the specification, in the free acid form) which can be utilised in the present invention include alkyl benzene sulphonic acids, in which the alkyl group contains from 6 to 20 carbon atoms, for example from 10 to 14 carbon atoms, alkyl sulphonic acids containing from 10 to 26 carbon atoms, for example from 10 to 14 carbon atoms, and alpha-olefin sulphonic acids obtained by sulphonation of an alpha-olefin containing, for example from 10 to 22 carbon atoms, such as a C₁₆ to C₁₈ olefin or a mixture containing same. Besides a surfactant containing a sulphonate group there may also be present a sulphated fatty alcohol or a sodium salt thereof; typical sulphated fatty alcohols include those containing from 10 to 26 carbon atoms, for example a sulphated fatty alcohol mixture containing C₁₀, C₁₂, C₁₄, C₁₆ and C₁₈ fatty alcohols. Typical of such a fatty alcohol mixture is one containing alcohols in the following proportions: C₁₀ 3.0%, C₁₂ 57.0%, C₁₄ 20.0%, C₁₆ 9.0% and C₁₈ 11.0%.

[0028] Typically a liquid built detergent composition according to the invention contains from 2% w/w up to 30% w/w of anionic surfactant (calculated as sulphonic acid) based upon the total weight of the composition.

[0029] The composition of the invention may further include one or more non-ionic surfactants. Typical non-ionic surfactants include fatty acid monoethanolamides such as coconut fatty acid monoethanolamide, a typical formulation for which is a mixture of monoethanolamides of fatty acids as follows: C₆ 0.5%, C₈ 6.5%, C₁₀ 6.0%, C₁₂ 49.5%, C₁₄ 19.5%, C₁₆ 8.5%, C₁₈ (stearic) 2.0%, C₁₈ (oleic) 6.0%, and C₁₈ (linoleic) 1.5%. Other suitable non-ionic surfactants include polyoxyalkylene ethers of alkanols, typically polyoxyethylene ethers of alkanols containing from about 6 to about 20 ethylene oxide groups and based upon alkanols containing from about 6 to about 26 carbon atoms. Such alkanols and alkanol mixtures can be produced by hydrogenation of methyl esters produced by transesterification of naturally occurring vegetable oils such as coconut oil, sunflower oil, palm oil, rape seed oil, and the like, or of animal fats, such as tallow or lard. A typical polyoxyethylene ether of an alkanol is based upon lauryl alcohol condensed with approximately 8 moles of ethylene oxide.

[0030] Typically the concentration of non-ionic surfactant, if present, in the liquid built detergent composition ranges from 0.5% w/w up to 30% w/w based upon the total weight of the composition.

[0031] Other ingredients which may be included in the liquid built detergent composition of the invention include preservatives, optical brighteners, bleaches, fragrances, zeolites, foam depressants, foam boosters and/or stabilisers, soaps, dyes, buffers, corrosion inhibition agents, bleach activators, enzymes, humectants, enzyme stabilisers, and the like. Such minor ingredients do not usually comprise more than 5% w/w each of the total composition, mostly less than 1% w/w each of the total composition, and more usually do not together amount to more than 5% w/w in total based upon the weight of the composition.

[0032] As an example of a builder there can be mentioned in particular sodium tripolyphosphate. Potassium tripolyphosphate can alternatively be used. The pyrophosphates, metaphosphates, orthophosphates, tetraphosphate, phosphonates such as acetonodiphosphonates, aminotrismethylenephosphonates, ethylenediamine tetramethylene phosphonates, and carbonates of sodium and potassium have also been suggested as builders, as have also zeolites and organic sequestering agents, such as nitrilotriacetic acid, ethylene diamine tetraacetic acid, and polymeric carboxylic acids and their salts, such as polyacrylic acid and polymethacrylic acid.

[0033] A typical liquid built detergent composition according to the invention comprises from 5% w/w up to 40% w/w based upon the total weight of the composition of a builder or builders.

[0034] For further details of ingredients which can be included in a liquid built detergent composition reference may be made to GB-B-2123846.

[0035] Upon preparing a stabilised gel system according to the invention the pH is typically in the range of from 1.0 to 8.0, preferably about pH 4.0. Upon addition of the builder in the production of a liquid built detergent according to the invention a pH increase is often observed. In some cases the pH may rise above 7.0, when starting from a stabilised gel system at a pH of about 4.0; hence the final pH may be as high as 9.0 or even a little higher.

[0036] The liquid built detergents of GB-B-2123846 are characterised by the fact that, upon centrifuging at 800 times normal Earth gravity for 17 hours at 25°C, these compositions separate into a first, predominantly aqueous, liquid phase, containing dissolved electrolyte, and at least one other phase. It is an advantage of our invention that, if a stabilised gel system is prepared of sufficient strength, then this may be used to prepare a liquid built detergent composition which does not separate into two or more phases upon centrifuging at 800 times normal Earth gravity for 17 hours at 25°C. For this purpose it is desirable to formulate the liquid built detergent composition, if starting from sodium silicate as the precursor for the silicic acid hydrosol, from a mixture of ingredients that includes at least 3.0% by weight of sodium silicate (or an equivalent amount of another soluble silicate) up to 8% by weight based upon the total weight of the liquid built detergent composition. By selecting an appropriate quantity of sodium silicate (or equivalent) as an ingredient for manufacture of the liquid built detergent composition of the invention it is possible to support amounts as high as 25% or more of builder in a manner such that no separation of phases occurs upon centrifugation at 800 times normal Earth gravity at 25°C. In the course of our experiments we have produced liquid built detergent compositions that exhibit little or no separation of phases, even when centrifuged at 2000 times normal Earth gravity at 25°C for 17 hours. These experimental results indicate that our liquid built detergent compositions should exhibit superior storage stability to those of GB-B-2123846.

[0037] The invention is further illustrated in the following Examples in which all percentages are by weight.

Example 1

[0038] This describes preparation of a type of liquid which has been shown to be very stable in terms of time (shelf-life) and thermal cycling (environmental stability).

Linear Alkylbenzene Sulphonic Acid	11%
Coconut Fatty Acid Monoethanolamide	2%
Sodium Tripolyphosphate	20%
Sodium Silicate (47%) Syrup	6%
Sodium Carbonate Anhydrous	3%
Hydrotrope H-66 (trade mark)	2%
Optical Brightener	0.15%
Formaldehyde (40%) Solution	0.75%
Silicone Antifoam Emulsion	0.01%
Fragrance	0.50%
Water to produce on a W/W basis	100%

[0039] The alkylbenzene sulphonic acid, or mixture of alkylbenzene sulphonic acids, is dissolved in about twice its own weight of water and added to the sodium silicate which was previously diluted with three times its weight of water. To the resulting transparent syrup, with slow stirring, are added all the other ingredients to produce a shining white, or glossy, pourable syrup which is further diluted with water to give the full batch of product at 100% by weight basis. A suitable alkyl benzene sulphonic acid is dodecyl benzene sulphonic acid.

Example 2

[0040] In this Example a stable colloidal syrup, or pourable gel, is obtained by acidification of alkali metal silicate solutions which contain surfactants before the titration is attempted. This method of production of heavy duty laundry detergents utilises the following ingredients:-

Sodium Alkyl Benzene Sulphonate	11%
Coconut Fatty Acid Monoethanolamide	2%
Sodium Tripolyphosphate	20%
Sodium Silicate (47%) Syrup	5.5%
Sodium Carbonate Anhydrous	3%
Optical Brightener	0.15%
Formaldehyde (40%) Solution	0.75%
Silicone Antifoam Emulsion	0.01%
Hydrotrope H-66 (trade mark)	2.00%
Fragrance	0.50%
Hydrochloric Acid (25%)	as required
Water to produce W/W	100%

[0041] The sodium alkylbenzene sulphonate (e.g. sodium dodecyl benzene sulphonate) is twice diluted with water and placed in a pan and to it is added the sodium silicate syrup which can, if desired, be diluted with three volumes of water before addition to the pan. The mixture is slowly stirred and the pH value of the solution reduced to 8.0 by the use of the correct aliquot of the 25% hydrochloric acid. Once the reaction is over, which is about two minutes after the last addition of hydrochloric acid, the remainder of the water is added followed by the addition of the other ingredients in any order. Final adjustment to the required weight is by the last addition of water. A product similar to that of Example 1 is obtained.

Example 3

[0042] A liquid built detergent composition is prepared from the following ingredients:

Dodecylbenzenesulphonic acid	10.0%
Sodium silicate (47%) syrup   about	6.5%
Coconut Fatty Acid Monoethanolamide	1.4%
Sodium carboxymethylcellulose	0.1%
Sodium tripolyphosphate	24.2%
Preservative	0.2%
Alcohol ethoxylate	1.3%
Hydrotrope H66	0.5%
Antifoam	0.2%
Fragrance	0.2%
Enzyme - Esperase	0.4%
Termamyl	0.4%
Optical brightener	0.1%
Water   To	100%

[0043] The alcohol ethoxylate used in this Example was a polyoxyethylene ether obtained by condensing 7 moles of ethylene oxide with a C_13/15 alcohol.

[0044] First of all the sodium carboxymethyl cellulose is dissolved in water. The coconut fatty acid monoethanolamide is also dissolved in hot water. Then the dodecylbenzene sulphonic acid is diluted with about twice its own weight of water. To this is added with vigorous stirring the sodium silicate syrup which has previously been diluted with about three times its own weight of water. Sufficient of this diluted sodium silicate syrup is added to give a pH of about 4.0. Then the sodium carboxymethyl cellulose solution is added, followed by the coconut fatty acid monoethanolamide solution, while continuing to stir. Next the sodium tripolyphosphate is added with stirring, followed by the other minor ingredients. Finally the composition is diluted to the desired strength with water.

[0045] The resulting composition is stable and does not separate out into separate layers even after several months storage. Moreover, upon centrifugation at 800g for 17 hours, no separation of phases can be detected. There is no sign of any formation of vesicles or spherulites, nor is there any evidence of any of the surfactant being present as a lamellar liquid crystal or solid hydrate. Hence, upon electron microscopic evaluation of the detergent composition of this Example, the observations recorded were consistent with a largely featureless granular structure with crystals of sodium tripolyphosphate distributed at random.

Example 4

[0046] A liquid built detergent composition is produced from the same ingredients as are used in Example 3 except that the addition of the sodium silicate syrup is delayed until after addition of the sodium tripolyphosphate. The sodium carboxymethyl cellulose and the coconut fatty acid monoethanolamide are each dissolved separately in hot water. Then the dodecylbenzene sulphonic acid is diluted with about twice its own weight of water. The sodium carboxymethyl cellulose solution and the coconut fatty acid ethanolamide solution are added in turn to the dodecylbenzene sulphonic acid solution with vigorous stirring to yield a solution having a pH of about 7.0 or lower, followed by the other minor ingredients. Lastly the sodium silicate syrup, which has previously been diluted with twice its own weight of water, is added whilst continuing to stir vigorously. Finally the composition is diluted with water to the desired strength.

[0047] The resulting liquid built detergent composition is similar to that of Example 3 except that it exhibits initially a somewhat lower viscosity. It does not separate into layers upon centrifugation at 800 g for 17 hours. It does not show any indication that any spherulites or vesicles are present, nor is there any evidence of any of the surfactant being present in the form of a lamellar liquid crystal or solid hydrate. Moreover, the results of electron microscopy evaluation indicate that the liquid built detergent composition of this Example has a largely featureless granular structure with randomly distributed crystals of sodium tripolyphosphate.

[0048] Although it is not required that this innovation be explained in terms of physical chemistry it is interesting to note that very concentrated hydrosols of silicic acid must be produced. without any tendency to coagulate or precipitate to rigid gels, because as the alkylbenzene sulphonic acid is titrated to the neutral point with silicate solution the electrical conductivity of the solution decreases due to the disappearance of hydroxonium ions as donated from the sulphonic acid. This type of tenside/silicic acid hydrosol reaction is not restricted in its application to the production of heavy duty laundry detergents.

[0049] In another example a soft anionic gel or syrup can be loaded with fine abrasive and used as an oven, or hard surface, cleaner.

[0050] Hence the invention is not restricted, in its application, to pourable gel systems in heavy duty laundry detergents.

Claims

1. The use of a stabilised gel system for supporting finely divided particulate matter in suspension, the stabilised gel system comprising a hydrosol of silicic acid stabilised by entanglement with micelles of a tenside.

2. The use according to claim 1, in which the pH of the stabilised gel system lies in the range of from 1.0 to 9.0.

3. The use according to claim 1 or claim 2, in which the pH of the stabilised gel system lies in the range of from 4.0 to 7.5.

4. The use according to any one of claims 1 to 3, in which the tenside of the stabilised gel system comprises an anionic surfactant selected from anionic surfactants derived from alkyl benzene sulphonic acids, anionic surfactants derived from alkyl sulphonic acids, and anionic surfactants derived from alpha-olefin sulphonic acids.

5. The use according to claim 4, in which the stabilised gel system further comprises at least one non-ionic surfactant.

6. The use according to claim 5, in which the at least one non-ionic surfactant comprises coconut fatty acid monoethanolamide.

7. The use according to any one of claims 1 to 6, in which the stabilised gel system has been prepared by a process which comprises neutralising a solution of an alkali metal silicate to a pH in the range of from 1.0 to 7.0 in the presence of a tenside thereby to produce a hydrosol of silicic acid stabilised by entanglement with tenside micelles.

8. A liquid built detergent composition comprising a stabilised gel system comprising a hydrosol of silicic acid stabilised by entanglement with micelles of a tenside and particles of a builder substantially uniformly distributed therein.

9. A liquid built detergent composition according to claim 8, in which the tenside comprises a tenside containing one or more sulphonate groups.

10. A liquid built detergent composition according to claim 9, which contains at least one anionic surfactant (calculated as sulphonic acid) based upon the total weight of the composition which is selected from anionic surfactants derived from alkyl benzene sulphonic acids, in which the alkyl group contains from 6 to 20 carbon atoms, anionic surfactants derived from alkyl sulphonic acids containing from 10 to 26 carbon atoms, alpha-olefin sulphonic acids containing from 10 to 22 carbon atoms, and mixtures thereof.

11. A liquid built detergent composition according to claim 10, in which the anionic surfactant is derived from dodecyl benzene sulphonic acid.

12. A liquid built detergent composition according to any one of claims 9 to 11, which further comprises a sulphated fatty alcohol or a sodium salt thereof.

13. A liquid built detergent composition according to any one of claims 9 to 12, which contains from 2% w/w up to 30% w/w of at least one anionic surfactant (calculated as sulphonic acid) based upon the total weight of the composition.

14. A liquid built detergent composition according to any one of claims 8 to 13, which further comprises from 0.5% w/w up to 30% w/w of at least one non-ionic surfactant.

15. A liquid built detergent composition according to claim 14, in which the at least one non-ionic surfactant comprises coconut fatty acid monoethanolamide.

16. A liquid built detergent composition according to claim 14 or claim 15, in which the at least one non-ionic surfactant comprises a polyoxyalkylene ether of an alkanol containing from about 6 to about 20 ethylene oxide groups and based upon an alkanol containing from about 6 to about 26 carbon atoms.

17. A liquid built detergent composition according to any one of claims 8 to 16, in which the amount of builder or builders comprises from 5% w/w up to 40% w/w based upon the weight of the composition.

18. A liquid built detergent composition according to any one of claims 8 to 17, in which the builder comprises sodium tripolyphosphate.

19. A liquid built detergent composition according to any one of claims 8 to 18, in which the amount of silicic acid corresponds to from 3% w/w up to 8% w/w (calculated as sodium silicate) based upon the weight of the composition.

20. A liquid built detergent composition according to any one of claims 8 to 19, which further comprises at least one material selected from preservatives, optical brighteners, bleaches, fragrances, zeolites, foam depressants, foam boosters, foam stabilisers, soaps, dyes, buffers, corrosion inhibition agents, bleach activators, enzymes, humectants, and enzyme stabilisers.

21. A liquid built detergent composition according to any one of claims 8 to 20, in which the pH is in the range of from 4.0 to 9.0.

22. A liquid built detergent composition according to any one of claims 8 to 21, which does not separate into two or more phases upon centrifuging at 800 times normal Earth gravity for 17 hours at 25°C.

23. An abrasive preparation comprising a stabilised gel system comprising a hydrosol of silicic acid stabilised by entanglement with micelles of a tenside and finely divided abrasive particles substantially uniformly distributed therein.

24. A process for the production of a liquid built detergent composition according to claim 8, which comprises neutralising a solution of an alkali metal silicate to a pH in the range of from 1.0 to 7.0 in the presence of a tenside thereby to produce a hydrosol of silicic acid stabilised by entanglement with tenside micelles and, either before or after completion of the neutralisation step, incorporating a builder in the composition.

25. A process according to claim 24, in which the amount of builder or builders comprises from 5% w/w up to 40% w/w based upon the weight of the composition.

26. A process according to claim 24 or claim 25, in which the builder comprises sodium tripolyphosphate.

27. A process according to any one of claims 24 to 26, in which neutralisation is effected by addition of an acid to a solution of an alkali metal silicate that contains also at least one surfactant.

28. A process according to claim 27, in which the acid is selected from hydrochloric acid, sulphuric acid, sulphamic acid, phosphoric acid, formic acid, acetic acid, citric acid, and mixtures of two or more thereof.

29. A process according to any one of claims 24 to 26, in which a solution having a pH of not more than 7.0 is produced by dissolving in an aqueous medium a tenside-forming acid containing one or more sulphonic acid groups and by adding thereto an alkali metal tripolyphosphate and then a solution of an alkali metal silicate is added.

30. A process according to any one of claims 24 to 26, in which neutralisation is effected by titration of the solution of alkali metal silicate with a tenside-forming acid containing one or more sulphonic acid groups.

31. A process according to any one of claims 24 to 30, in which the alkali metal silicate is sodium silicate.

32. A process according to any one of claims 24 to 31, in which the tenside is an anionic surfactant selected from anionic surfactants derived from alkyl benzene sulphonic acids, alkyl sulphonic acids, and anionic surfactants derived from alpha-olefin sulphonic acids.

33. A process according to any one of claims 24 to 32, in which there is further added at least one non-ionic surfactant.

34. A process according to claim 33, in which the non-ionic surfactant comprises coconut fatty acid monoethanolamide.

35. A process according to any one of claims 24 to 34, in which there is incorporated in the composition, either before or after the neutralisation step, a sulphated fatty alcohol or a sodium salt thereof.

36. A process according to any one of claims 24 to 35, in which there is used from 2% w/w up to 30% w/w of anionic surfactant (calculated as sulphonic acid) based upon the total weight of the composition.

37. A process according to any one of claims 24 to 36, in which there is incorporated in the composition, either before or after the neutralisation step, 0.5% w/w up to 30% w/w of at least one non-ionic surfactant comprising coconut fatty acid monoethanolamide, a polyoxyalkylene ether of an alkanol containing from 6 to 20 ethylene oxide groups and based upon an alkanol containing from 6 to 26 carbon atoms, or a mixture thereof.

38. A process according to any one of claims 24 to 37, in which there is used from 3% w/w up to 8% w/w of sodium silicate based upon the weight of the composition.

39. A process according to any one of claims 24 to 38, which further comprises incorporating in the composition, either before or after the neutralisation step, at least one material selected from preservatives, optical brighteners, bleaches, fragrances, zeolites, foam depressants, foam boosters, foam stabilisers, soaps, dyes, buffers, corrosion inhibition agents, bleach activators, enzymes, humectants, and enzyme stabilisers.

40. A process according to any one of claims 24 to 39, in which the pH of the resulting composition is in the range of from 4.0 to 9.0.

Ansprüche

1. Verwendung eines stabilisierten Gelsystems zur Unterstützung fein verteilter partikulärer Stoffe in Suspension, wobei das stabilisierte Gelsystem ein Kieselsäure-Hydrosol umfaßt, das durch Verknäuelung mit Micellen eines Tensids stabilisiert wird.

2. Verwendung nach Anspruch 1, worin der pH des stabilisierten Gelsystems im Bereich zwischen 1,0 und 9,0 liegt.

3. Verwendung nach Anspruch 1 oder 2, worin der pH des stabilisierten Gelsystems im Bereich zwischen 4,0 und 7,5 liegt.

4. Verwendung nach einem der Ansprüche 1 bis 3, worin das Tensid des stabilisierten Gelsystems ein anionisches Tensid (Anion-Tensid) umfaßt, das aus folgendem ausgewählt wird: Anion-Tensiden, die sich von Alkylbenzolsulfonsäuren herleiten, Anion-Tensiden, die sich von Alkylsulfonsäuren herleiten und Anion-Tensiden, die sich von α-Olefinsulfonsäuren herleiten.

5. Verwendung nach Anspruch 4, worin das stabilisierte Gelsystem überdies mindestens ein nichtionisches Tensid (Niotensid) umfaßt.

6. Verwendung nach Anspruch 5, worin das mindestens eine Niotensid Kokosfettsäure-Monoethanolamid umfaßt.

7. Verwendung nach einem der Ansprüche 1 bis 6, worin das stabilisierte Gelsystem durch ein Verfahren hergestellt wurde, welches das Neutralisieren einer Lösung von einem Alkalimetallsilikat auf einen pH im Bereich zwischen 1,0 und 7,0 in der Gegenwart eines Tensids umfaßt, um dadurch ein Kieselsäure-Hydrosol herzustellen, das durch Verknäuelung mit Tensid-Micellen stabilisiert wird.

8. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung, die ein stabilisiertes Gelsystem umfaßt, das ein Kieselsäure-Hydrosol umfaßt, das durch Verknäuelung mit Micellen eines Tensids und Teilchen eines Gerüststoffes (Builders), die im wesentlichen gleichförmig darin verteilt sind, stabilisiert wird.

9. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach Anspruch 8, worin das Tensid ein Tensid umfaßt, das eine Sulfonatgruppe oder mehrere Sulfonatgruppen enthält.

10. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach Anspruch 9, die folgendes enthält: Ab mindestens einem Anion-Tensid (berechnet als Sulfonsäure) basierend auf dem Gesamtgewicht der Zusammensetzung, das aus folgendem ausgewählt wird: Anion-Tensiden, die sich von Alkylbenzolsulfonsäuren herleiten, worin die Alkylgruppe zwischen 6 und 20 Kohlenstoffatome enthält; Anion-Tensiden, die sich von Alkylsulfonsäuren herleiten, die zwischen 10 und 26 Kohlenstoffatome enthalten; α-Olefinsulfonsäuren, die zwischen 10 und 22 Kohlenstoffatome enthalten und Gemischen davon.

11. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach Anspruch 10, worin sich das Anion-Tensid von Dodecylbenzolsulfonsäure herleitet.

12. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 9 bis 11, die überdies einen sulfatierten Fettalkohol oder ein Natriumsalz davon umfaßt.

13. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 9 bis 12, die von 2 Gew.-% bis zu 30 Gew.-% mindestens eines Anion-Tensids (berechnet als Sulfonsäure) basierend auf dem Gesamtgewicht der Zusammensetzung enthält.

14. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 8 bis 13, die überdies von 0,5 Gew.-% bis zu 30 Gew.-% mindestens eines Niotensids umfaßt.

15. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach Anspruch 14, worin das mindestens eine Niotensid Kokosfettsäure-Monoethanolamid umfaßt.

16. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach Anspruch 14 oder 15, worin das mindestens eine Niotensid folgendes umfaßt: Einen Polyoxyalkylenether eines Alkanols, der zwischen circa 6 und circa 20 Ethylenoxidgruppen enthält und auf einem Alkanol basiert, das zwischen circa 6 und circa 26 Kohlenstoffatome enthält.

17. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 8 bis 16, worin die Menge an Gerüststoff oder Gerüststoffen von 5 Gew.-% bis zu 40 Gew.-% basierend auf dem Gewicht der Zusammensetzung umfaßt.

18. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 8 bis 17, worin der Gerüststoff Natriumtripolyphosphat umfaßt.

19. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 8 bis 18, worin die Kieselsäuremenge von 3 Gew.-% bis 8 Gew.-% (berechnet als Natriumsilikat) basierend auf dem Gewicht der Zusammensetzung entspricht.

20. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 8 bis 19, die überdies mindestens ein Material umfaßt, das aus folgendem ausgewählt wird: Konservierungsmitteln, optischen Aufhellern, Bleichmitteln, Duftstoffen, Zeolithen, Schaumdämpfern, Schaumboostern, Schaumstabilisatoren, Seifen, Farbstoffen, Puffern, Korrosionsinhibitoren, Bleichaktivatoren, Enzymen, Feuchthaltemitteln und Ezymstabilisatoren.

21. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 8 bis 20, worin der pH im Bereich zwischen 4,0 und 9,0 liegt.

22. Flüssig aufgebaute Wasch- und Reinigungsmittelzusammensetzung nach einem der Ansprüche 8 bis 21, die sich beim Zentrifugieren für die Dauer von 17 Stunden bei 25°C bei 800mal der normalen Erdschwerkraft nicht in zwei oder mehr Phasen auftrennt.

23. Schleifmittel, das ein stabilisiertes Gelsystem umfaßt, das ein Kieselsäure-Hydrosol umfaßt, das durch Verknäuelung mit Micellen eines Tensids und fein aufgeteilten abrasiven Partikeln, die im wesentlichen gleichförmig darin verteilt sind, stabilisiert wird.

24. Verfahren für die Herstellung einer flüssig aufgebauten Wasch- und Reinigungsmittelzusammensetzung nach Anspruch 8, die das Neutralisieren einer Lösung von einem Alkalimetallsilikat auf einen pH im Bereich zwischen 1,0 und 7,0 in Gegenwart eines Tensids umfaßt, um dadurch ein Kieselsäure-Hydrosol herzustellen, das durch Verknäuelung mit Tensid-Micellen und entweder vor oder nach Abschluß des Neutralisationsschrittes durch Inkorporation eines Gerüststoffes in die Zusammensetzung stabilisiert wird.

25. Verfahren nach Anspruch 24, worin die Menge an Gerüststoff oder Gerüststoffen von 5 Gew.-% bis zu 40 Gew.-% basierend auf dem Gewicht der Zusammensetzung umfaßt.

26. Verfahren nach Anspruch 24 oder 25, worin der Gerüststoff Natriumtripolyphosphat umfaßt.

27. Verfahren nach einem der Ansprüche 24 bis 26, worin die Neutralisation durch Zugabe einer Säure zu einer Lösung eines Alkalimetallsilikats bewirkt wird, die auch mindestens einen grenzflächenaktiven Stoff enthält.

28. Verfahren nach Anspruch 27, worin die Säure aus Salzsäure, Schwefelsäure, Sulfaminsäure, Phosphorsäure, Ameisensäure, Essigsäure, Zitronensäure und Gemischen aus zwei oder mehreren davon ausgewählt wird.

29. Verfahren nach einem der Ansprüche 24 bis 26, worin eine Lösung mit einem pH von nicht mehr als 7,0 durch Lösen in einem wäßrigen Medium einer Tensid-bildenden Säure, die eine oder mehrere Sulfonsäuregruppen enthält und durch Zufügen eines Alkalimetalltripolyphosphats dazu hergestellt wird und dann eine Lösung von einem Alkalimetallsilikat zugefügt wird.

30. Verfahren nach einem der Ansprüche 24 bis 26, worin die Neutralisation durch Titration der Alkalimetallsilikat-Lösung mit einer Tensid-bildenden Säure bewirkt wird, die eine oder mehrere Sulfonsäuregruppen enthält.

31. Verfahren nach einem der Ansprüche 24 bis 30, worin das Alkalimetallsilikat Natriumsilikat ist.

32. Verfahren nach einem der Ansprüche 24 bis 31, worin das Tensid ein Anion-Tensid ist, das aus Anion-Tensiden ausgewählt wird, die sich von folgendem herleiten: Alkylbenzolsulfonsäuren, Alkylsulfonsäuren und Anion-Tensiden, die sich von α-Olefinsulfonsäuren herleiten.

33. Verfahren nach einem der Ansprüche 24 bis 32, worin überdies mindestens ein Niotensid zugefügt wird.

34. Verfahren nach Anspruch 33, worin das Niotensid Kokosfettsäure-Monoethanolamid umfaßt.

35. Verfahren nach einem der Ansprüche 24 bis 34, worin in die Zusammensetzung, entweder vor oder nach dem Neutralisationsschritt, ein sulfatierter Fettalkohol oder ein Natriumsalz davon inkorporiert wird.

36. Verfahren nach einem der Ansprüche 24 bis 35, worin von 2 Gew.-% bis zu 30 Gew.-% Anion-Tensid (berechnet als Sulfonsäure) basierend auf dem Gesamtgewicht der Zusammensetzung verwendet wird.

37. Verfahren nach einem der Ansprüche 24 bis 36, worin in die Zusammensetzung, entweder vor oder nach dem Neutralisationsschritt, 0,5 Gew.-% bis zu 30 Gew.-% mindestens eines Niotensids inkorporiert wird, das folgendes umfaßt: Kokosfettsäure-Monoethanolamid, einen Polyoxyalkylenether eines Alkanols, der zwischen 6 und 20 Ethylenoxidgruppen enthält und auf einem Alkanol basiert, das zwischen 6 und 26 Kohlenstoffatome enthält oder ein Gemisch davon.

38. Verfahren nach einem der Ansprüche 24 bis 37, worin von 3 Gew.-% bis zu 8 Gew.-% Natriumsilikat basierend auf dem Gewicht der Zusammensetzung verwendet wird.

39. Verfahren nach einem der Ansprüche 24 bis 38, das überdies die Inkorporation in die Zusammensetzung, entweder vor oder nach dem Neutralisationsschritt, mindestens eines Materials umfaßt, das aus folgendem ausgewählt wird: Konservierungsmitteln, optischen Aufhellern, Bleichmitteln, Duftstoffen, Zeolithen, Schaumdämpfern, Schaumboostern, Schaumstabilisatoren, Seifen, Farbstoffen, Puffern, Korrosionsinhibitoren, Bleichaktivatoren, Enzymen, Feuchthaltemitteln und Enzymstabilisatoren.

40. Verfahren nach einem der Ansprüche 24 bis 39, worin der pH der sich ergebenden Zusammensetzung im Bereich zwischen 4,0 und 9,0 liegt.

Revendications

1. Utilisation d'un système de gel stabilisé destiné à supporter une matière particulaire finement divisée en suspension, le système de gel stabilisé comprenant un hydrosol d'acide silicique stabilisé par enchevêtrement avec les micelles d'un tensioactif.

2. Utilisation selon la revendication 1, dans laquelle le pH du système de gel stabilisé est compris entre 1,0 et 9,0.

3. Utilisation selon la revendication 1 ou la revendication 2, dans laquelle le pH du système de gel stabilisé est compris entre 4,0 et 7,5.

4. Utilisation selon l'une quelconque des revendications 1 à 3, dans laquelle le tensioactif du système de gel stabilisé comprend un tensioactif anionique choisi parmi les tensioactifs anioniques dérivés des acides alkylbenzène-sulfoniques, les tensioactifs anioniques dérivés des acides alkyl-sulfoniques et les tensioactifs anioniques dérivés des acides alpha-oléfine-sulfoniques.

5. Utilisation selon la revendication 4, dans laquelle le système de gel stabilisé comprend en outre au moins un tensioactif non ionique.

6. Utilisation selon la revendication 5, dans laquelle ledit au moins un tensioactif non ionique comprend du monoéthanolamide d'acide gras de coco.

7. Utilisation selon l'une quelconque des revendications 1 à 6, dans laquelle le système de gel stabilisé a été préparé par un procédé qui comprend le fait de neutraliser une solution d'un silicate de métal alcalin à un pH compris entre 1,0 et 7,0 en présence d'un tensioactif, de manière à produire un hydrosol d'acide silicique stabilisé par enchevêtrement avec les micelles de tensioactif.

8. Composition de détergent liquide contenant un adjuvant comprenant un système de gel stabilisé comprenant un hydrosol d'acide silicique stabilisé par enchevêtrement avec les micelles d'un tensioactif et des particules d'un adjuvant distribué de façon sensiblement uniforme dans celui-ci.

9. Composition de détergent liquide contenant un adjuvant selon la revendication 8, dans laquelle le tensioactif comprend un tensioactif contenant un ou plusieurs groupes sulfonates.

10. Composition de détergent liquide contenant un adjuvant selon la revendication 9, qui contient* au moins un tensioactif anionique (calculé comme acide sulfonique) sur la base du poids total de la composition qui est choisi parmi les tensioactifs anioniques dérivés des acides alkylbenzène-sulfoniques, dans lesquels le groupe alkyle contient de 6 à 20 atomes de carbone, des tensioactifs anioniques dérivés des acides alkyl-sulfoniques contenant de 10 à 26 atomes de carbone, des acides alpha-oléfine-sulfoniques contenant de 10 à 22 atomes de carbone et des mélanges de ceux-ci.

11. Composition de détergent liquide contenant un adjuvant selon la revendication 10, dans laquelle le tensioactif anionique est dérivé de l'acide dodécylbenzène-sulfonique.

12. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 9 à 11, qui comprend en outre un alcool gras sulfaté ou un sel de sodium de celui-ci.

13. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 9 à 12, qui contient de 2 % p/p à 30 % p/p d'au moins un tensioactif anionique (calculé comme acide sulfonique) sur la base du poids total de la composition.

14. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 8 à 13, qui comprend en outre de 0,5 % p/p à 30 % p/p d'au moins un tensioactif non ionique.

15. Composition de détergent liquide contenant un adjuvant selon la revendication 14, dans laquelle ledit au moins un tensioactif non ionique comprend le monoéthanolamide d'acide gras de coco.

16. Composition de détergent liquide contenant un adjuvant selon la revendication 14 ou la revendication 15, dans laquelle ledit au moins un tensioactif non ionique comprend un éther polyoxyalkylénique d'un alcanol contenant d'environ 6 à environ 20 groupes oxyde d'éthylène et basé sur un alcanol contenant d'environ 6 à environ 26 atomes de carbone.

17. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 8 à 16, dans laquelle la quantité d'adjuvant ou d'adjuvants comprend de 5 % p/p à 40 % p/p sur la base du poids de la composition.

18. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 8 à 17, dans laquelle l'adjuvant comprend du tripolyphosphate de sodium.

19. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 8 à 18, dans laquelle la quantité d'acide silicique correspond à 3 % p/p à 8 % p/p (calculé comme silicate de sodium) sur la base du poids de la composition.

20. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 8 à 19, qui comprend en outre au moins un matériau choisi dans l'ensemble formé par les conservateurs, les azurants optiques, les agents de blanchiment, les parfums, les zéolites, les suppresseurs de mousse, les exalteurs de mousse, les stabilisateurs de mousse, les savons, les colorants, les tampons, les agents anticorrosion, les activateurs de blanchiment, les enzymes, les agents mouillants et les stabilisateurs enzymatiques.

21. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 8 à 20, dans laquelle le pH est compris entre 4,0 et 9,0.

22. Composition de détergent liquide contenant un adjuvant selon l'une quelconque des revendications 8 à 21, qui ne se sépare pas en deux ou plusieurs phases lors d'une centrifugation à 800 fois l'attraction terrestre normale pendant 17 heures à 25°C.

23. Préparation abrasive comprenant un système de gel stabilisé comprenant un hydrosol d'acide silicique stabilisé par enchevêtrement avec les micelles d'un tensioactif et les particules abrasives finement divisées distribuées de façon sensiblement uniforme dans celui-ci.

24. Procédé de fabrication d'une composition de détergent liquide contenant un adjuvant selon la revendication 8, qui comprend le fait de neutraliser une solution de silicate de métal alcalin à un pH compris entre 1,0 et 7,0 en présence d'un tensioactif de manière à produire un hydrosol d'acide silicique stabilisé par enchevêtrement avec les micelles de tensioactif et, soit avant soit après la fin de l'étape de neutralisation, le fait d'incorporer un adjuvant à la composition.

25. Procédé selon la revendication 24, dans lequel la quantité d'adjuvant ou d'adjuvants comprend de 5 % p/p à 40 % p/p sur la base du poids de la composition.

26. Procédé selon la revendication 24 ou la revendication 25, dans lequel l'adjuvant comprend le tripolyphosphate de sodium.

27. Procédé selon l'une quelconque des revendications 24 à 26, dans lequel la neutralisation est réalisée par addition d'un acide à une solution de silicate de métal alcalin qui contient également au moins un tensioactif.

28. Procédé selon la revendication 27, dans lequel l'acide est choisi dans l'ensemble formé par l'acide chlorhydrique, l'acide sulfurique, l'acide sulfamique, l'acide phosphorique, l'acide formique, l'acide acétique, l'acide citrique, et des mélanges de deux ou plusieurs de ceux-ci.

29. Procédé selon l'une quelconque des revendications 24 à 26, dans lequel une solution ayant un pH ne dépassant pas 7,0 est produite en dissolvant dans un milieu aqueux un acide formant un tensioactif contenant un ou plusieurs groupes acide sulfonique et en ajoutant à celui-ci un tripolyphosphate de métal alcalin, puis une solution de silicate de métal alcalin est ajoutée.

30. Procédé selon l'une quelconque des revendications 24 à 26, dans lequel la neutralisation est réalisée par titrage de la solution de silicate de métal alcalin avec un acide formant un tensioactif contenant un ou plusieurs groupes acide sulfonique.

31. Procédé selon l'une quelconque des revendications 24 à 30, dans lequel le silicate de métal alcalin est le silicate de sodium.

32. Procédé selon l'une quelconque des revendications 24 à 31, dans lequel le tensioactif est un tensioactif anionique choisi parmi les tensioactifs anioniques dérivés des acides alkylbenzène-sulfoniques, des acides alkyl-sulfoniques, et les tensioactifs anioniques dérivés des acides alpha-oléfine-sulfoniques.

33. Procédé selon l'une quelconque des revendications 24 à 32, dans lequel on ajoute en outre au moins un tensioactif non ionique.

34. Procédé selon la revendication 33, dans lequel le tensioactif non ionique comprend le monoéthanolamide d'acide gras de coco.

35. Procédé selon l'une quelconque des revendications 24 à 34, dans lequel on incorpore à la composition, soit avant soit après l'étape de neutralisation, un alcool gras sulfaté ou un sel de sodium de celui-ci.

36. Procédé selon l'une quelconque des revendications 24 à 35, dans lequel on utilise de 2 % p/p à 30 % p/p de tensioactif anionique (calculé comme acide sulfonique) sur la base du poids total de la composition.

37. Procédé selon l'une quelconque des revendications 24 à 36, dans lequel on incorpore à la composition, soit avant soit après l'étape de neutralisation, de 0,5 % p/p à 30 % p/p d'au moins un tensioactif non ionique comprenant le monoéthanolamide d'acide gras de coco, un éther polyoxyalkylénique d'un alcanol contenant de 6 à 20 groupes oxyde d'éthylène et basé sur un alcanol contenant de 6 à 26 atomes de carbone, ou un mélange de ceux-ci.

38. Procédé selon l'une quelconque des revendications 24 à 37, dans lequel on utilise de 3 % p/p à 8 % p/p de** silicate de sodium sur la base du poids de la composition.

39. Procédé selon l'une quelconque des revendications 24 à 38, qui comprend en outre le fait d'incorporer dans la composition, soit avant soit après l'étape de neutralisation, au moins un matériau choisi dans l'ensemble formé par les conservateurs, les azurants optiques, les agents de blanchiment, les parfums, les zéolites, les suppresseurs de mousse, les exalteurs de mousse, les stabilisateurs de mousse, les savons, les colorants, les tampons, les agents anticorrosion, les activateurs de blanchiment, les enzymes, les agents mouillants et les stabilisateurs enzymatiques.

40. Procédé selon l'une quelconque des revendications 24 à 39, dans lequel le pH de la composition résultante est compris entre 4,0 et 9,0.