EP3167040A1

EP3167040A1 - Washing liquid and washing method

Info

Publication number: EP3167040A1
Application number: EP15735698.1A
Authority: EP
Inventors: Peter Schmiedel; Michael Dreja; Christian Nitsch; Arnd Kessler; Benoit Luneau; Reinhard Strey; Anna KLEMMER; Thorsten Bastigkeit; Thomas Müller-Kirschbaum; Nicole BODE; Iwona Spill
Original assignee: Henkel AG and Co KGaA
Current assignee: Henkel AG and Co KGaA
Priority date: 2014-07-09
Filing date: 2015-07-08
Publication date: 2017-05-17
Anticipated expiration: 2035-07-08
Also published as: EP3167040B1; US10513675B2; DE102014213314A1; US20190352586A1; US20170114310A1; WO2016005462A1

Abstract

The invention relates to an aqueous washing liquid in a device for cleaning soiled textile substrates containing a plurality of water-insoluable solid particles and a liquid phase, which contains a microemulsion, and to a textile washing method using said type of washing liquid.

Description

WASHPLOTTE AND WASHING PROCESS

The present invention relates to a textile washing process, which is carried out to form a microemulsion or a microemulsion system, and the washing liquor used for this purpose.

There is a long felt need to be able to effectively remove fatty soiling. Therefore, as a rule, each washing process aims at at least hydrophobic portions of the

Remove soiling. In order then to record the hydrophobic parts of the

To cause soiling in the wash liquor must be a thermodynamically attractive

Environment are created for these soiling.

The state of the art offers different solutions for this purpose. A process for the purification and impregnation of functional textiles is described in international patent application WO 2006/066986 A1, in which first the textiles are treated with a so-called short liquor, i. a liquor, which has a ratio of the weight of the amount of dry textile to the weight of the amount of water greater than 1: 8, are wetted and then washed a predetermined amount of a hydrophobic agent by means of water from the detergent reservoir in the tub and brought into contact with the moistened textiles becomes. According to WO 2010/031675, the finishing composition is sprayed on the pre-moistened items of laundry in the form of fine droplets (spray).

From WO 2005/003268 a washing process is known in which the detergent is dispersed in less water than in conventional processes and the laundry is thus contacted at a greater ratio of the amount of dry textile to the amount of water with a less dilute wash liquor. The detergent formulation itself has no special requirements. The ratio of the weight of the dry laundry amount to the weight of the water amount is 1: 2 to 4: 1.

From WO 2013/134168 A, a washing process is known in which, in at least two successive sub-washing cycles, the laundry in the first sub-washing cycle is treated with a more concentrated detergent composition than in a second Under wash cycle. A wash cycle is the period from the creation of a wash liquor to the removal of the wash liquor from the washing machine. A wash cycle can be done in

Sub-washing cycles be subdivided, wherein at the end of the first sub-washing cycle, the wash liquor is not removed, but at the beginning of the second cycle but new, additional water is fed into the existing wash liquor. It is preferred that the first

Sub-wash cycle lasts longer than the second. The detergent formulation itself has no special requirements.

WO 2012/04891 1 A discloses a washing method in a washing machine, wherein the cleaning agents and optionally various cleaning agents or components thereof are sprayed into the interior of the washing machine. The process and control of the machine are designed to consume significantly less water during cleaning and flushing than conventional processes. Further requirements for the cleaning agents, with the exception of the property that they must be sprayable, are not provided.

It is known that microemulsions are thermodynamically stable emulsions and have extremely low interfacial tensions. The skilled person also knows that for the removal of dirt, the interfacial tension between water and the fat component of

Pollution must be lowered.

WO 2013/1 10682 A describes cleaning agents, in particular for the manual

Dishwashing, but also for the pretreatment of laundry, said compositions containing 1 to 50 wt .-% of anionic surfactants and 1 to 36 wt .-% salts and which spontaneously form a microemulsion on contact with oils and / or fats. Furthermore, microemulsions are described, which 1 to 50 wt .-% anionic surfactants, 1 to 36 wt .-% salts, 10 to 80 wt .-% water and 10 to 80 wt .-% of at least one triglyceride or a mixture of a triglyceride and a or more components from the group consisting of waxes, lipids, terpenes, triterpenes and fatty acids. The formation of the microemulsion takes place in situ with the triglycerides or triglyceride-containing mixtures present on the surface to be cleaned.

US Pat. No. 6,112,120 discloses acidic cleaning agents for hard

Surfaces known, which may be in the form of a microemulsion. An application of such emulsions in a washing machine is not recommended.

The patent applications EP 0160762 A and WO 95/27035 A propose O / W microemulsions as detergents. German patent application DE 10129517 A proposes microemulsions of water, one or more hydrophobic components and sugar-based nonionic surfactants as stain pretreatment agents for textiles or for cleaning hard surfaces

Apply surfaces. The suitability of these microemulsions for use in

Washing machines is not described.

EP-A-1371718 discloses polymeric nanoparticles having an average particle diameter of 1 to 10 nm which are useful as fabric care additives in detergent formulations for improving the

Properties such as softening, wrinkle resistance, dirt and stain removal, soil release, dye transfer, dye fixation, static control and anti-foaming are suitable. The nanoparticles can interact with silicone compounds in the

Detergent formulation can be used, or can be functionalized with silicone groups to extend significantly different textile care properties of the preparations.

US-A-4655952 teaches a detergent and a process for its preparation, the detergent for textile surfaces, in particular textile floor coverings. The product contains a powdered, porous carrier of a foamed, plasticized urea-formaldehyde resin foam enriched with detergent and contains a hydrous surfactant which adheres to the carrier material, with the water in the carrier material remaining completely homogeneous.

JP-A-04241 165 relates to the treatment of a dyed natural fiber material having an appearance similar to that of a stone-washed fabric while avoiding the deficiencies of the stone-wash treatment and discloses the treatment of indigo-dyed denim clothing by stirring and washing in water or in water an aqueous solution of a detergent in frictional contact with solid rubber balls and 10-50% by weight of an abrasive such as MgO having a particle size of 60-200 mesh.

DE-A-1 900 002 discloses solid detergents and cleaners, surface-active substances, washing, non-surface-active cleaning salts and laundry additives which contain polymers of vinyl compounds with an average particle size of less than 1 mm.

WO-A-01/71083 discloses a washing machine having a drum for receiving articles to be washed, the drum having at least two rotatable drum sections and a drive, the drum comprising a plurality of different drum modes including a mode in which the rotatable drum parts are driven to effect relative rotation between them. A controller controls the device to a Run variety of different washing programs, each washing program has an associated drum mode.

WO 2010/094959 A1 relates to the cleaning of substrates using a

Solvent-free cleaning system that requires the use of only small amounts of water. More particularly, the document is concerned with the cleaning of textile fibers using such a system, and provides an apparatus for use in this context.

WO-A-2007/128962 enables the efficient separation of the substrate from the polymer particles upon completion of the cleaning process and describes a design for using two internal drums.

Finally, WO 201 1/073062 A discloses bicontinuous microemulsion systems which are suitable as stain pretreatment agents and which are capable of dissolving solid and solidified fatty stains in the main wash at neutral pH.

Users of washing and cleaning processes, both private and commercial, have an intuitive knowledge that using a concentrated cleaning solution with subsequent dilution is a better way to remove heavy soiling

Cleaning result leads to the immediate application of a diluted detergent solution. The examples are numerous:

1 . To wash hair, shampoo is given in concentrated form in the hair. Only after the action of the concentrated solution is diluted and rinsed out.

2. To wash heavily soiled hands, hand wash products (eg jellies or pastes, also liquid soap) are offered on the market, which are rubbed in concentrated form. Only when the cleaning product has intimately mixed with the (oily) soiling is diluted. These products can not exert their effect when used in the same diluted form, e.g. be put in a sink.

3. When washing dishes such as greasy pans, the user can intuitively add a few drops of pure detergent to the sponge or directly into the pan. The cleaning result is then better or easier than in the diluted application in the sink. 4. In commercial cleaning processes, such as a motor vehicle engine wash the (oil) soiled object is first sprayed with a cleaner concentrate, which is then diluted after thorough mixing with the oil of the soiling, for example with a high pressure cleaner and removed.

The situation is different with conventional textile washing. Here, the wash liquor is used immediately in relatively high dilution. The advantage in the cleaning performance, which results from the action of a concentrated surfactant solution is not used here.

Without wishing to be bound by theory, the colloid and interfacial chemical background is the higher cleaning performance of a concentrated surfactant solution in the US Pat

Phase behavior of water / surfactant / oil mixtures and the resulting

To look for interfacial tension between water and oil phases. As shown in unpublished DE 10 2014 202 990, certain surfactant systems can form W / O emulsions (Winsor II systems) at higher concentrations. When diluted, a

Run through three-phase region with a microemulsion, an excess oil phase and an excess water phase, which is characterized by an extremely low interfacial tension and thus by a high fat solubility. Upon further dilution, the emulsion type changes to an O / W emulsion (Winsor I system). In this condition is usually a dilute wash liquor.

In the teaching of the aforementioned document, a considerable saving in surfactant has already been achieved by using the Winsor II system instead of a single-phase microemulsion.

Of course, the same cleaning performance can be achieved by a single-phase microemulsion, but then with a much higher input of surfactants.

Here, a concentrate is proposed as a sales product, which results in a certain dilution to a so-called "short liquor" a Winsor II system, and thus results in an improved washing performance of greasy soils. This Winsor II system can act on and intimately mix with the greasy soils in an early stage of the wash cycle, in a manner of "full area pretreatment" with little textiles moistening and without the presence of free wash liquor. It is then further diluted in a later stage of the wash cycle while passing through the three-phase area to a Winsor I system which serves to flush away the solubilized greasy soil. The

A technical challenge in the implementation of this doctrine is that the small amount of liquid of the "short liquor" evenly on the textiles in a wash load to distribute. In previous prototypes, this short liquor was sprayed onto the washload with a spray device. However, such machines are not commercially available.

Recently, however, alternative methods are available to evenly apply a small amount of liquid to a textile load. As an example, polyamide flakes are to be mentioned, which are characterized by a high dirt holding capacity and which are able to redistribute a small amount of liquid in the wash load.

The object of the present invention is therefore to provide a wash liquor which can be redistributed in the form of a short liquor by water-insoluble solid particles.

Further, it is an object of the present invention by the combination of these means to make a washing cycle using the water-insoluble particles more efficient, in particular to reduce water consumption.

Surprisingly, it has been found that microemulsions in conjunction with redistribution by means of water-insoluble solid particles can advantageously be used as wash medium in a wash cycle. The particles avoid the usual disadvantages of microemulsions, e.g. the high demand for surfactants or the difficult redistribution of a small amount of liquid in the wash load.

Surprisingly, it has now been found that compared to a market

Detergent gives a higher washing effect when the washing solution applied in conjunction with the water-insoluble solid particles (the "short liquor") is a microemulsion or contains a surfactant system capable of spontaneously forming a microemulsion with oil.

A microemulsion is understood in the specialist literature to be a thermodynamically stable mixture of water, oil (s) and amphiphile (s). The microstructure may be O / W or W / O as usual for emulsions. In microemulsions, moreover, bicontinuous structures are also found. Most microemulsions are clear because their droplet size in the nm range is well below the wavelength of visible light. The clarity is in the context of the present invention also as an indicator of the presence of a microemulsion in a

Water / oil / amphiphile mixture scored. According to Winsor, microemulsion systems consisting of a water component, an oil component and an amphiphile can be subdivided into 4 types according to their phase equilibria.

In a Winsor Type I microemulsion system, the surfactant is primarily soluble in water and in an O / W microemulsion form. It consists of a surfactant-rich aqueous phase (O / W microemulsion) and an excess but low-surfactant oil phase.

In a Winsor Type II microemulsion system, the surfactant is especially soluble in an oil phase and in a W / O microemulsion form. It consists of a surfactant-rich oil phase (W / O microemulsion) and an excess but low-surfactant aqueous phase.

A Winsor Type III microemulsion system is a frequently bicontinuous microemulsion, also called a mid phase microemulsion, of a surfactant rich middle phase which coexists with a low surfactant aqueous phase as well as a low surfactant oil phase.

A Winsor Type IV microemulsion system, on the other hand, is a single phase homogeneous mixture and, in contrast to Winsor types I to III consisting of 2 or 3 phases, of which only one phase is a microemulsion, is a total microemulsion High surfactant concentrations to achieve this single phase, while in Winsor Type I and Type II microemulsion systems, significantly lower surfactant concentrations are required to achieve stable phase equilibrium. For this reason, although Winsor Type IV microemulsions are frequently described in the patent literature, they are rarely or not used in domestic machine washing processes. The large amount of surfactant required makes such a process uneconomical and is not least environmentally friendly.

In conjunction with the water-insoluble, solid particles, the required

Liquid quantity and the use of such a system, however, significantly reduced, so that the latter disadvantages are overcome and a single-phase microemulsion (Winsor IV) in conjunction with the water-insoluble solid particles is a preferred embodiment of the present invention.

According to Bancroft, the type of emulsion depends both on the emulsifier and on the phase in which the emulsifier, for example a surfactant or various surfactants, dissolves. If water-soluble, ie hydrophilic, emulsifiers, for example anionic surfactants, are used, O / W emulsions are formed. But anionic surfactants may be due to the addition of electrolytes Electrostatic shielding of the hydrophilic head group of anionic surfactants are made hydrophobic, so that W / O emulsions are achieved. It is thus possible to carry out a phase inversion by addition of salts and to convert an O / W emulsion with anionic surfactant as emulsifier into a W / O emulsion. This can then with the grease and oil-like dirt in

Interaction, mix with the dirt on the fiber, causing the

Surface tension between the existing greasy and oily stains and the water phase is lowered. Dilution of the emulsion then lowers the salt concentration, weakens the shielding of the ionic head group of the anionic surfactant and makes the anionic surfactant more hydrophilic. The grease and oil-like dirt can be better separated from the textile together with the microemulsion and dispersed in the aqueous liquor and ultimately transported away with the aqueous liquor.

Likewise, the behavior of the emulsifiers is influenced by the temperature.

If hydrophobic emulsifiers, for example nonionic surfactants, are used, W / O emulsions are formed. An addition of salt is not required. By higher

At application temperatures, the nonionic surfactants become more hydrophobic and can interact even better with greasy and oily soils. If the temperature is reduced again during dilution of the liquor, the nonionic surfactants become hydrophilic again, the grease and oily soils can be better detached from the textile and dispersed in the aqueous liquor and ultimately transported away with the aqueous liquor.

Thus, by temperature controls and / or addition of salts targeted phase inversions can be achieved.

In the context of the present invention, a surfactant system capable of forming a microemulsion is understood as meaning an aqueous surfactant system which is capable of solubilizing a larger amount of oil without cloudiness being detectable. In the context of the present invention, such a system contains less than 5% by weight of amphiphile, preferably less than 4% by weight of amphiphile, more preferably less than 3% by weight of amphiphile and is capable of more than 0.25% by weight. %, preferably more than 0.5 wt .-%, more preferably more than 1 wt .-% of an oil to solubilize clearly. Usually, such systems are characterized by a particularly low interfacial tension against the oil in question. Preferred are

Interfacial tensions <5 mN / m, more preferably <3 mN / m and most preferably <1 mN / m.

The microemulsion according to the invention contains Surfactants: nonionic surfactants, anionic surfactants, cationic surfactants and / or amphoteric surfactants. In a particular embodiment, the surfactant system of

Microemulsion linear alkyl benzene sulfonate. The concentrations are less than 5 wt .-%, preferably less than 4 wt .-%, more preferably less than 3 wt .-%. The lower the concentration required to form a microemulsion, the more efficient the surfactant system and hence the more advantageous.

Optional oils in concentrations <10 wt .-%, preferably <5 wt .-%, particularly preferably <3 wt .-%. Oils are to be understood here essentially water immiscible oils. They serve in particular to solve greasy soiling. Alkanes can be used, preferably biodegradable oils with ether or ester groups. The use of terpenes is also possible. A preferred oil is e.g. Dioctyl.

Conventional perfume oils that are added with the aim of scenting the laundry, should not be considered here as an oil component in the context of the invention.

Optional salts in concentrations of 0 to 10 wt .-%, preferably from 0 wt .-% to 5 wt .-%, particularly preferably from 0 to 3 wt .-%

Optional cosurfactants. Cotensides are amphiphiles that, due to their molecular structure, do not themselves form surfactant-specific micelles, but are incorporated into the micellar structure of common surfactants and influence their morphology and interfacial properties. Cosurfactants are, for example, medium long chain fatty alcohols (pentanol to dodecanol), low EO aliphatic or aromatic alcohol ethoxylates (e.g., fatty alcohol ethoxylates containing 1 -3 EO, phenoxyetanol), monoglycerides or glycerol ethers, (e.g., ethylhexylglyceride), etc.

Optional amphiphilic polymers. These serve to increase the efficiency of the surfactant system, i. its minimum concentration above which a microemulsion can be formed.

Other common detergent ingredients, especially enzymes, bleach,

Builders, complexing agents, water-soluble solvents, optical brighteners, fragrances etc.

Auxiliaries e.g. Stabilizers, rheology modifiers, dyes etc.

In a particular embodiment, the microemulsion according to the invention contains salts, but no cosurfactant.

In a further particular embodiment, the microemulsion according to the invention contains cosurfactant but no salts apart from the customary amounts contained in detergents. In a further particular embodiment, the microemulsion according to the invention contains both salts and cosurfactants. The present invention thus relates to an aqueous wash liquor in a device for cleaning soiled textile substrates containing a plurality of

water-insoluble solid particles and a liquid phase, characterized in that the liquid phase contains a microemulsion.

Further embodiments can be found in the independent claims and in the dependent claims.

Although the addition of an oil component in the present invention is advantageous but optional, the term "microemulsion" in this context always means that the system is capable of producing a microemulsion with the fat and oil components of the soiling, ie a " microemulsible "system. The washing medium as such may in this case also be regarded as a "microemulsion without oil component", in particular if an optionally sufficient amount of oil is already present in the wash liquor coming from the textile substrate.

For the sake of convenience one would not give the consumer a direct one

Give microemulsion to the hand. Although this contains a considerable concentration of surfactant, but still a large amount of water, so that the consumer would have to carry large containers, which would also require a high packaging costs. Therefore, one would give the consumer a low-water concentrate in hand, which is diluted in the preparation of water, for example in a corresponding dilution device in the machine in such a way that a single-phase microemulsion is formed.

For the purposes of the present invention, it is thus preferable to use a concentrate which contains the following constituents:

5 to 80% by weight of surfactants

• Optionally a cosurfactant. Cotensides are amphiphilic compounds that due to their

low solubility or other properties in the binary system do not form micelles, but are incorporated into the micelles and interfacial films of a conventional surfactant system and alter their properties. Examples are fatty alcohols,

Protonated fatty acids, partial glycerides, low ethoxylated nonionic surfactants

Optional salts in amounts from 0% to 70% by weight

Optionally 0 to 60% by weight of an oil component

• Water

• Other common detergent ingredients and which when diluted with water by a factor of 2 to 20 a single-phase

Microemulsion yields.

To overcome the disadvantages of the single-phase microemulsion, i. the high surfactant input, also in

Combination with water-insoluble solid particles can also be used in the context of the present invention, the teaching of the above, not yet published patent application DE 10 2014 202 990, i. E. it is not the use of a single-phase microemulsion required, but a two-phase system of the type Winsor II, which on dilution

Three-phase system undergoes (Winsor II) and finally ends in a two-phase system of the Winsor I type.

Essential within the meaning of the present invention is therefore the use of a system of the Winsor II type according to the teaching of said patent application of the compound with water-insoluble solid particles in a wash cycle.

Analogous to single-phase microemulsions, it is also the case here that a water-leaner concentrate is advantageous as a sales product.

Accordingly, a concentrate is composed of

1 to 80 wt .-%, in particular 2 to 35 wt .-% surfactant

optionally a cosurfactant

Salts in amounts from 20% to 70% by weight

From 2 to 60% by weight of an oil component

water

other common detergent ingredients

particularly preferred.

However, especially in the field of commercial laundry, the direct use of

Microemulsions or Winsor II systems, which together with the water-insoluble, solid ponds form the wash liquor according to the invention, readily possible. The advantage of the direct use of the microemulsion is that no defined dilution of the concentrate according to the invention has to take place in the washing machine. The typical disadvantage that a large amount of water has to be transported, may not play such an important role in commercial laundry, as there suitable conveying and transport media are available and handling larger amounts of liquid in tanks, barrels or cans readily possible. Of course, especially in the field of commercial laundry, the

Dilution of the concentrate according to the invention to the actual inventive

Microemulsion, which forms the wash liquor according to the invention together with the water-insoluble, solid ponds, in an external, spatially separated from the actual washing machine device, and the microemulsion or the Winsor II system are then introduced into the laundry treatment room of the washing machine.

Another aspect of the present invention includes a method of cleaning a soiled textile substrate, the method including treating the substrate with a formulation comprising a plurality of water-insoluble solid particles, wherein the particles are optionally regenerated with or without the use of

microemulsions according to the invention are reused in further purification processes according to the method.

The substrate comprises textile substrates, each optionally of a variety of materials, which may be either a natural fiber such as cotton or synthetic textile fibers such as nylon 6,6 or a polyester.

The water-insoluble solid particles may be inorganic or organic in nature. For the solid particles, for example, zeolites, clays or ceramics are particularly preferred. The particles may have some hydrophilicity to allow wetting with the wash liquor.

The organic water-insoluble solid particles may be any of a variety

different polymers. Particularly preferred are polyalkenes such as polyethylene and polypropylene, polyesters and polyurethanes. However, preferred are the polymer particles of polyamide, more particularly particles of nylon, most preferably in the form of nylon chips. The polyamides are particularly effective for aqueous stain / soil removal, while polyalkenes are particularly useful for removing oily stains. Optionally, copolymers of the above polymeric materials may be used for the purposes of the invention.

Various nylon homo- or co-polymers can be used, including nylon 6 and nylon 6,6. Preferably, the polyamide comprises nylon 6,6 homopolymer having a weight average molecular weight in the range of 5,000 to 30,000 daltons, preferably 10,000 to 20,000 daltons, most preferably 15,000 to 16,000 daltons. The water-insoluble solid particles or granules, particles or moldings are of such a shape and size that enables good flowability and close contact with the textile substrate. Preferred forms of the particles include spheres and cubes, but the preferred particle shape is cylindrical. The particles are preferably sized to each have an average weight in the range of 20-50 mg, preferably 30-40 mg. In the case of the most preferred cylindrically shaped particles, the preferred average particle diameter is 1.5 to 6.0 mm, more preferably 2.0 to 5.0 mm, most preferably 2.5 to 4.5 mm, while the length of the cylindrical particles is preferably in the range of 2.0 to 6.0 mm, more preferably 3.0 to 5.0 mm, and most preferably in the range of 4.0 mm.

Before cleaning, the textile substrate, preferably by wetting with water or directly with the microemulsion according to the invention, be moistened to an additional

To provide improvement for the wash liquor and thereby improve the

To allow transport characteristics within the system (pretreatment). As a result, a more efficient transfer of washing-active substances or the inventive

Achieving microemulsion on the substrate and facilitating the removal of stains and stains from the substrate Preferably, the wetting treatment is performed to achieve a substrate to liquid phase weight ratio of 1: 0, 1 to 1: 5; more preferably the ratio is between 1: 0.2 and 1: 2, with particularly favorable results being achieved in ratios such as 1: 0.2, 1: 1 and 1: 2. However, in some cases, successful results with the substrate to liquid phase ratios of up to 1:50 can be achieved, although such ratios are not preferred in view of the substantial amounts of wastewater produced. The proportion of the liquid phase of the wash liquor is the proportion of the total wash liquor inclusive of the water-insoluble solid particles obtained by centrifuging 8 kg of the wash liquor containing the solid water-insoluble particles for 5 minutes in a centrifuge with the water-insoluble solid particles separated cylindrical rotating body of 515 mm inner diameter and 370 mm internal depth at 1400 revolutions per minute from the liquid portion.

The weight ratio of the water-insoluble solid particles to the textile substrate is generally 0.1: 1 to 10: 1 parts by weight, especially 0.5: 1 to 5: 1 parts by weight. In this case, the proportion of water-insoluble solid particles as the weight of the particles in the dry state, ie after 24 hours of storage at 21 ° C and a relative humidity of 65%, determined. According to the invention, the water-insoluble solid particles can be coated prior to use with the concentrate described above according to methods known per se.

Another object of the present invention is a textile washing process in a washing machine using a wash liquor containing water-insoluble particles, as defined above, in particular in a washing machine with a washing cycle, which is characterized in that

the laundry item to be cleaned is placed in the laundry treatment room of the washing machine;

a concentrate according to the invention in a separate, spatially from the

Detergent storage space of the washing machine is given separate dilution device;

Alternatively, the concentrate according to the invention is added directly into the laundry treatment room of the washing machine, for example via a coating of the water-insoluble, solid particles

a dilution is made to a "short liquor" that is transported along with water-insoluble solid particles into the laundry treatment room of the washing machine, the short liquor being a single-phase microemulsion or a Winsor Type II biphasic system;

Alternatively, the microemulsion according to the invention or the Winsor II system according to the invention is used directly. #

an interaction of the short liquor (single-phase microemulsion or Winsor type II) and the particles with the debris present in the laundry, takes place, whereby a relaxation of the grease and oil-like dirt on the fiber is effected;

Dilution of the short liquor with water, the microemulsions or the Winsor II system in a Winsor I state pass with subsequent rinsing.

Removal of the particles.

The consumer product according to the invention, from which the wash liquor according to the invention, in particular in a washing machine, which has a Kurzflottenwaschtechnik, can be prepared, represents a single- or multi-phase concentrate, which at

Room temperature, for example, granular, liquid, gel or pasty but can also be in the form of a shaped body (piece, tablet OA). The teachings of the invention take advantage of the fact that the detergent composition used in the washing machine is intended to represent a single-phase microemulsion or a Winsor Type II microemulsion system, but the concentrate which constitutes the consumer product is not already in the form of a Winsor microemulsion or microemulsion system Type II must be present. For the Purpose of the invention, it is sufficient if the concentrate can be converted on dilution with water and in particular in a washing machine in a microemulsion system of Winsor type II. However, it may be advantageous if the concentrate already as

Microemulsion system of Winsor type II is present. It may likewise be preferred for the concentrate to be present as a Winsor type IV microemulsion if it can be converted into a Winsor Type II microemulsion system when the wash liquor is prepared. There a

Microemulsion system of Winsor type II is biphasic, it may be in the interest of a

uniform distribution of the short liquor on the laundry be expedient that the concentrate from a microemulsion system of Winsor type II when using not present macroscopically separated, but the application is carried out in such a way that a

Emulsion is applied from the two phases of the Winsor type II system. Such an emulsion can be made, for example, by appropriate mixing, in particular stirring of the microemulsion type before application to the laundry.

Under Kurzflottenwaschtechnik is in the context of the invention, the provision of a first

Unterwaschzyklus understood in which the first contact of the textile or Wäschepostens done with the wash liquor, wherein the ratio of the weight of the dry textile or

Laundry lot to the liquid phase of the wash liquor according to the invention is at least 1: 8, but preferably a short liquor is used, in which the ratio of the weight of the dry textile or laundry lot to liquid phase of the liquor is at least 1: 4, in particular not less than 1: 2, for example 1: 2 to 4: 1, advantageously 1: 2 to 2: 1. In the context of the present invention, the washing process which works with the wash liquor according to the invention consisting of a multiplicity of water-insoluble solid particles represents a very particularly preferred embodiment of the short liquor washing technique.

According to the invention, the aqueous liquor used in the first sub-wash cycle consists of a Winsor Type II single-phase microemulsion or microemulsion system. In preferred embodiments of the invention, the upper limit of the weight ratio of the dry fabric or laundry to the Winsor Type II aqueous liquor is limited should be that the entire batch of laundry during the first sub-washing cycle can be completely moistened. Only then is it ensured that the microemulsion can interact with all contaminants. The lower limit of the weight ratio of the dry textile or laundry lot to the liquid phase of the Winsor type II liquor or the single-phase microemulsion is given in preferred embodiments of the invention in that as little as possible "free liquor" when used in the washing machine, ie as little as possible excess liquor, which is not from the textile or the laundry item in the first sub-washing cycle can be absorbed and in

Laugensumpf the washing machine remains, is present. For this reason, a weight ratio of the dry textile or laundry lot to the aqueous liquor is very particularly preferably from 1: 2 to 1: 1, in particular not less than 1: 1.5.

The concentrate preferably contains surfactants which serve as emulsifiers after dilution in the single-phase microemulsion or the Winsor Type II microemulsion system.

In the concentrates and the microemulsions, preference is given to anionic and / or nonionic surfactants, with a combination of anionic and nonionic surfactants being particularly advantageous with regard to the removal of a wide variety of soiling. The content of the concentrates of surfactants and in particular of a combination of anionic and nonionic surfactants is preferably from 1 to 80% by weight, in particular from 5 to 30% by weight.

The microemulsions used in short liquor washing technology or

Typically, Winsor Type II microemulsion systems have at least 0.05% by weight of surfactants, particularly a combination of anionic and nonionic surfactants. Preference is given to contents of at least 0.2% by weight, preferably from 0.3 to not more than 15% by weight, in particular of a combination of anionic and nonionic surfactants.

Suitable anionic surfactants include alkylbenzenesulfonic acid salts, olefinsulfonic acid salts, C 12-18 alkanesulfonic acid salts, fatty alcohol sulfate, fatty alcohol ether sulfates, but also fatty acid soaps or a mixture of two or more of these anionic surfactants. Of these anionic surfactants, alkylbenzenesulfonic acid salts, fatty alcohol (ether) sulfates and mixtures thereof are particularly preferred.

As surfactants of the sulfonate type are preferably C9-i3-alkylbenzenesulfonates,

Olefin sulfonates, i. Mixtures of alkene and hydroxyalkanesulfonates and disulfonates, as obtained for example from Ci2-is-monoolefins with terminal or internal double bond by sulfonation with gaseous sulfur trioxide and subsequent alkaline or acidic hydrolysis of the sulfonation, into consideration. Also suitable are C 12 -is alkanesulfonates and the esters of α-sulfo fatty acids (ester sulfonates), for example the α-sulfonated methyl esters of hydrogenated coconut, palm kernel or tallow fatty acids.

Alk (en) ylsulfates are the salts of the sulfuric acid half esters of C 12-18 fatty alcohols, for example coconut fatty alcohol, tallow fatty alcohol, lauryl, myristyl, cetyl or stearyl alcohol or the C 10 -C 20 oxo alcohols and those half-esters of secondary alcohols of these chain lengths prefers. From a technical point of view, the Ci2-Ci6-alkyl sulfates and Ci2-Ci5-alkyl sulfates and Ci4-Ci5-alkyl sulfates are preferred. 2,3-alkyl sulfates are also suitable anionic surfactants.

Also, fatty alcohol ether sulfates, such as the sulfuric acid monoesters of straight-chain or branched C7-2i alcohols ethoxylated with from 1 to 6 mol of ethylene oxide, such as 2-methyl-branched C9-11 alcohols having on average 3.5 moles of ethylene oxide (EO) or C12- Fatty alcohols with 1 to 4 EO, in particular C 12-14 fatty alcohols with 2 EO are suitable.

Further suitable anionic surfactants are fatty acid soaps. Suitable are saturated and unsaturated fatty acid soaps, such as the salts of lauric acid, myristic acid, palmitic acid, stearic acid, (hydrogenated) erucic acid and behenic acid, and in particular derived from natural fatty acids, for example coconut, palm kernel, olive oil or tallow fatty acids

Soap mixtures. Preferably, the content of the concentrates of fatty acid soaps 0 to 5 wt .-%.

The anionic surfactants including the fatty acid soaps may be in the form of their sodium, potassium or magnesium or ammonium salts. Preferably, the anionic surfactants are in the form of their sodium salts and / or ammonium salts. Amines which can be used for neutralization are preferably choline, triethylamine, monoethanolamine, diethanolamine, triethanolamine,

Methylethylamine or a mixture thereof, with monoethanolamine is preferred.

Suitable nonionic surfactants include alkoxylated fatty alcohols, alkoxylated oxo alcohols, alkoxylated fatty acid alkyl esters, fatty acid amides, alkoxylated fatty acid amides,

Polyhydroxy fatty acid amides, alkylphenol polyglycol ethers, amine oxides, alkyl polyglucosides and mixtures thereof.

The alkoxylated fatty alcohols used are preferably ethoxylated, in particular primary, alcohols having preferably 8 to 18 carbon atoms and an average of 2 to 12 moles of ethylene oxide (EO) per mole of alcohol, in which the alcohol radical is linear. In particular, alcohol ethoxylates having 12 to 18 C atoms, for example coconut, palm, tallow or oleyl alcohol, and on average 5 to 8 EO per mole of alcohol are preferred. Preferred ethoxylated alcohols include, for example, _Ci-2 -i4 alcohols having 2 EO, 3 EO, 4 EO or 7 EO, n-alcohol with 7 EO, C12-18 alcohols containing 3 EO, 5 EO or 7 EO, C 16 -is-alcohols with 5 EO or 7 EO and mixtures of these. In addition to these nonionic surfactants, fatty alcohols with more than 12 EO can also be used. Examples include tallow fatty alcohol with 14 EO, 25 EO, 30 EO or 40 EO. It is particularly preferred that a Ci2-is-alcohol, in particular a Ci2-Ci4-alcohol or a C13-alcohol with an average of 2 EO or 3 EO is used as a nonionic surfactant. In addition to the pure ethylene oxide adducts, however, corresponding propylene oxide adducts, in particular also EO / PO mixed adducts, are advantageous, with particular preference being given to C 16 -C 18 -alkylpolyglycol ethers having in each case 2 to 8 EO and PO units. In some embodiments, EO / BO mixed adducts and even EO / PO / BO mixed adducts are also preferred. Particularly preferred EO / PO mixed adducts include C 16-18 fatty alcohols having fewer PO than EO units, in particular C 16-18 fatty alcohols having 4 PO and 6 EO or C 16-18 fatty alcohols having 2 PO and 4 EO.

The stated degrees of alkoxylation (EO = ethylene oxide, PO = propylene oxide, BO = butylene oxide) represent statistical averages, which for a particular product may be an integer or a fractional number. Preferred alkoxylates have a narrow homolog distribution.

As already indicated above, inorganic salts are not absolutely necessary in order to be able to produce single-phase microemulsions or microemulsions of Winsor type II. However, concentrates, in particular anionic surfactant-containing concentrates, which contain one or more inorganic salts are preferred. Preferred inorganic salts are alkali metal sulfates and alkali metal halides, especially chlorides, and also alkali metal carbonates. Very particularly preferred inorganic salts are sodium sulfate, sodium hydrogen sulfate, sodium carbonate, sodium hydrogencarbonate and mixtures of these. The content of the concentrates of one or more inorganic salts is preferably 0 to 70% by weight. In the Winsor Type II microemulsions or microemulsion systems, the content of one or more inorganic salts is 0 to 20% by weight and preferably 5 to 15% by weight, wherein

Concentrations of 8 to 12 wt .-% have been found to be particularly preferred.

In preferred embodiments of the invention, the concentrates also contain one or more additional oils. In the context of the present invention, an additional oil which additionally and deliberately contains the fatty and oil-like substances present on the textiles to be washed

Stains is used, understood in principle any non-water-miscible or in combination with water 2 phases forming organic non-surfactant liquid, which itself has a fat dissolving power. In particular, such additional oils are preferred, which not only have a good fat dissolving power, but are also biodegradable and acceptable odor. Particularly preferred concentrates have as additional oil dioctyl ether, oleic acid, limonene, low molecular weight paraffins and / or low molecular weight silicone oils, for example, the well-known from chemical cleaning solvent cyclosiloxane D5 on. Also, aromatic solvents such as toluene are of course effective additive oils for the purposes stated herein; but they are usually omitted for toxicological reasons. Of the Content of the concentrates of one or more additional oils is preferably 0 to 60% by weight and in particular 2 to 50% by weight.

The use of one or more additional oils in the concentrate according to the invention has several advantages. At first, additional oils work as solvents for the fats, which are used in the

Application temperatures in the washing machine in solid form. In addition, the oil and grease-like dirt on the laundry is usually not well defined. It is therefore not known in advance which surfactants must be present in the W / O emulsion in order to actually interact with the soil in such a way that it becomes relaxed and can be flushed out of the textile. In addition, without the presence of additional oils, the grease and oily soils on the fabrics could unbalance the microemulsion system. But if an additional hydrophobic component as defined above (additive oil) is used from the outset in the concentrate, the influence of the grease and oil-like dirt on the laundry on the balance of the microemulsion is negligible and the likelihood of a desired interaction and relaxation of the dirt on the textile fiber is significantly increased.

In the single-phase microemulsions or microemulsion systems of Winsor type II to be prepared, the content of one or more additional oils is preferably 0 to 20% by weight and in particular 0.5 to 15% by weight, with concentrations of 1 to 12% by weight. % have been found to be particularly preferred.

In particular, microemulsion systems of Winsor type II can be prepared from the concentrates of the invention by dilution with water, containing from 0.1 to 5% by weight of surfactants, preferably 0.2 to 1% by weight of surfactants, with particular preference of less than 0.1 Wt .-% surfactants, and 0.5 to 5 wt .-%, advantageously 1 to 3 wt .-% additional oils. With further preference, the aforementioned Winsor 2 microemulsion systems have from 80 to 94.6% by weight of water and from 0 to 15% by weight of inorganic salts, preferably from 1 to 12% by weight of inorganic salts, in particular from 5 to 10% by weight. % inorganic salts on.

In further embodiments, it is preferred that the concentrates have inorganic salts and / or additive oils. It has proven to be particularly advantageous, especially when anionic and nonionic surfactants are contained in the concentrates that the

Concentrates have one or more inorganic salts as well as one or more additional oils. The weight ratio of inorganic salt to additional oil can vary within a wide range, depending on the surfactants used. Particularly preferred additional oils, which in Combination with inorganic salts are di-ethers. Di-n-octyl ether is used with particular advantage.

In addition, the concentrate may further comprise at least one, preferably two or more, selected from the group consisting of builders, bleaches, electrolytes, nonaqueous but water miscible solvents, enzymes, pH modifiers, perfumes, perfume carriers, fluorescers, dyes, hydrotropes , Foam inhibitors, silicone oils,

Anti redeposition agents, grayness inhibitors, inlet preventer, anti-crease agents,

Color transfer inhibitors, antimicrobial agents, germicides, fungicides, antioxidants, preservatives, corrosion inhibitors, antistatic agents, bittering agents, ironing aids, repellents and impregnating agents, swelling and anti-slip agents, plasticizing components and UV absorbers.

As builders, which may be contained in the concentrate, in particular silicates, aluminum silicates (especially zeolites), carbonates, salts of organic di- and

To name polycarboxylic acids and mixtures of these substances.

Organic builders which may be present in the concentrate are, for example, the polycarboxylic acids which can be used in the form of their sodium salts, polycarboxylic acids meaning those carboxylic acids which carry more than one acid function. For example, these are citric acid, adipic acid, succinic acid, glutaric acid, malic acid, tartaric acid, maleic acid, fumaric acid, sugar acids, aminocarboxylic acids, and mixtures of these. Preferred salts are the salts of polycarboxylic acids such as citric acid, adipic acid,

Succinic acid, glutaric acid, tartaric acid, sugar acids and mixtures thereof.

As builders further polymeric polycarboxylates are suitable. These are, for example, the alkali metal salts of polyacrylic acid or polymethacrylic acid, for example, those having a molecular weight of 600 to 750,000 g / mol. Suitable polymers are in particular polyacrylates, which preferably have a molecular weight of from 1,000 to 15,000 g / mol. Because of their superior solubility, this group can again be the short-chain polyacrylates, the molecular weights of 1,000 to 10,000 g / mol, and particularly preferably from 1,000 to

5,000 g / mol, be preferred.

Also suitable are copolymeric polycarboxylates, in particular those of acrylic acid with methacrylic acid and of acrylic acid or methacrylic acid with maleic acid. To improve the water solubility, the polymers may also contain allylsulfonic acids, such as allyloxybenzenesulfonic acid and methallylsulfonic acid, as a monomer. In the liquid detergents but preferably soluble builders, such as citric acid, or acrylic polymers having a molecular weight of 1 .000 to 5,000 g / mol are used.

In addition to the additional oils, non-aqueous solvents that are miscible with water can be added to the microemulsion systems or the concentrate used to produce the microemulsions. Suitable non-aqueous solvents include monohydric or polyhydric alcohols, alkanolamines or glycol ethers. For example, the solvents are selected from ethanol, n-propanol, i-propanol, butanols, glycol, propanediol, butanediol, methylpropanediol, glycerol, diglycol, propyldiglycol, butyldiglycol, hexylene glycol,

Ethylene glycol methyl ether, ethylene glycol ethyl ether, ethylene glycol propyl ether, ethylene glycol mono-n-butyl ether, diethylene glycol methyl ether, diethylene glycol ethyl ether, propylene glycol methyl ether, propylene glycol ethyl ether, propylene glycol propyl ether, dipropylene glycol monomethyl ether,

Dipropylene glycol monoethyl ether, methoxytriglycol, ethoxytriglycol, butoxytriglycol, 1-butoxyethoxy-2-propanol, 3-methyl-3-methoxybutanol and mixtures of these solvents. It should be noted, however, that the type and amount of non-aqueous, but water-miscible solvents must be selected so that when creating the short fleet a

Microemulsion system of Winsor type II can arise.

In a further embodiment of the invention, anhydrous or at least nearly anhydrous concentrates are used, in which essentially only substantially as much water is contained as is introduced by the raw materials used for their preparation, without actively adding water. In the context of the present invention, anhydrous is understood to mean that the content of water in the concentrates is not more than 2% by weight, preferably not more than 1% by weight. In a preferred embodiment of the invention, the concentrates are in the form of an anhydrous paste which contains surfactants, in particular a mixture of anionic and nonionic surfactants.

Advantageously, the surfactant content, in particular the mixture of anionic and nonionic surfactants, in the anhydrous pastes in the same areas as in the aqueous concentrates. The same applies to the other constituents of the concentrates. In place of water, the paste may have additional fine-particle solids, for example, aluminosilicates such as zeolites or smectites or bentonites, silicic acids or, in preferred embodiments, for example, include the type of Aerosils ^®. These finely divided additives affect the phase boundaries and stability of the pastes to be made from the pastes

Winsor type II microemulsion systems are not essential.

The concentrates of the invention may be prepared by any method known in the art. It is also preferred to offer the concentrates according to the invention in the form of disposable portions. These include in particular containers of water-soluble materials which are filled with the concentrates according to the invention. Particular preference is given to single-chamber or multi-chamber containers, in particular of polyvinyl alcohol or polyvinyl alcohol derivatives or copolymers with vinyl alcohol or vinyl alcohol derivatives as monomer. These disposable portions ensure that the correct amount of the present invention is sufficient for the preparation of the Winsor Type II microemulsion system and for the corresponding performance associated therewith

Concentrate is used in the first sub-washing cycle. Optionally, depending on the amount of textile or laundry to be washed, multiple disposable portions may also be used.

A further embodiment of the invention provides that the concentrates are in granulated form on a carrier. Suitable carrier materials are the carrier materials known from the prior art for detergents. Particular preference is given to ingredients of detergents such as builders and alkali metal, for example alkali metal carbonates or zeolites, or bleaching agents such as percarbonates or enzyme granules, but also sodium sulfates or silicates and in particular those substances which have a high absorption capacity for liquids, for example silicic acids. Such granulated products may also be powdered with finely divided materials known in the art for this purpose. Particular preference is given to silicic acids, zeolites or other aluminosilicates, but also mixtures of silicic acids and zeolites.

Another object of the invention is the use of a concentrate as described above to form a short liquor of a Winsor Type II microemulsion system. All facts and embodiments described for the concentrates are also valid for use.

In a preferred embodiment of the textile washing process according to the invention, a washing machine, in particular a domestic washing machine, is used with a washing cycle with at least two successive sub-washing cycles, wherein

in the first sub-wash cycle, there is a short liquor in the laundry treatment room of the washing machine,

an interaction of the short liquor with the dirt present in the laundry lot takes place in the first sub-wash cycle, whereby the interfacial tension between the existing grease and oil-like soils and the water phase is lowered, subsequently, in at least one further sub-washing cycle, the liquor is diluted with water until a long liquor is formed,

- while the dirt from the laundry item is released and

- At the end of the last sub-washing cycle, the dirt is removed together with the long liquor from the laundry treatment room.

This embodiment of the method provides that a washing cycle is carried out with at least 2 consecutive sub-washing cycles. A wash cycle is the period from the creation of a first wash liquor to the removal of the wash liquor from the washing machine. The washing cycle is subdivided into at least two sub-washing cycles, whereby the washing liquor is not removed at the end of the first to penultimate sub-washing cycle. In the preferred embodiment, a washing cycle with 2 consecutive

Underwashing cycles, the short liquor is formed in the form of a microemulsion or Winsor type II microemulsion system at the beginning of the first sub-washing cycle or retained in the case where the concentrate already used as Winsor type II microemulsion system, while at the beginning of the second sub-washing cycle new , Additional water is fed into the existing wash liquor to form a long fleet. At this dilution, which may also be considered as a first rinse step, breakage of the single-phase microemulsion or phase inversion of the Winsor II system occurs and typically a Winsor I emulsion is formed.

A method according to the invention is preferably carried out in a washing machine which allows a short liquor washing technique. The statements already made above regarding the short liquor washing technology and the short liquor apply accordingly. The machines in question allow the use of concentrates or granulated concentrates to create a short liquor in the machine. Particular preference is given here

Washing machines in which the short liquor is redistributed by a large number of water-insoluble, solid particles.

Since a Winsor Type II microemulsion system is biphasic, a method is preferred which, in the interest of uniform distribution of the short liquor on the laundry, provides that the Winsor Type II microemulsion system is not macroscopically separate during application but as an emulsion of the two phases in the

Laundry treatment room introduced and applied to the laundry items. This temporary emulsion can be formed, for example, by vigorous mixing, in particular by stirring. In a particular embodiment, the machine measures the weight of the dry fabric or laundry load and supplies the amount of water required to form the short liquor. This is mixed with the concentrates according to the invention in the above-mentioned mixing device or directly in the laundry treatment space of the machine to form a single-phase microemulsion or a Winsor Type II microemulsion system. Likewise, in a particular embodiment, the water-insoluble, solid particles which together with the short liquor form the wash liquor according to the invention, with the inventive

Concentrates be pre-coated. The amount of water required to form the microemulsion system is then metered in or outside the washing drum. In order to be able to produce a temporary emulsion of the Winsor Type II, in principle, two-phase microemulsion system, it may be preferred for the machine to provide a space in which a temporary emulsion can be formed from the concentrate and the water supplied. This can be supported by the provision of a mixing device, preferably a stirring device in this mixing chamber. In this case, the mixing space for producing a temporary emulsion may be the dispensing rinsing chamber of a washing machine, in particular a domestic washing machine, but also an additional space in the machine, in particular the household washing machine.

It is further preferred that after determining the weight of the laundry item, the machine displays its weight in a readable manner for the consumer or the industrial user so that the consumer can dose the appropriate amount of the concentrate. The corresponding metered amounts of the concentrates depending on the weight of the Wäschepostens, which are required for the formation of the microemulsion system of Winsor type II, can from

Consumers are read on the outer packaging of the concentrates and / or are specified in a corresponding programmable machine by the machine itself.

Since a free wash liquor, so fleet that can not be absorbed by the laundry items or is in the interstices of water-insoluble, solid particles and remains in Laugensumpf the machine an unnecessary dilution of the system and possibly even a deterioration of the washing result would result Inventive method that creates as little as possible free liquor. It has proved to be advantageous if, in the first sub-washing cycle, a ratio of the weight of the dry textile or linen lot to the short liquor is at least 1: 8, preferably at least 1: 4, in particular not less than 1: 2, for example 1: 2 to 4: 1 is formed. In particular, it is preferable that in the first sub-washing cycle, a ratio of the weight of the dry fabric or the laundry lot to the short liquor is not less than not less than 1: 1.5. In particular, this ratio may be 1: 1, 2 to 1, 2: 1, ideally 1: 1. The even distribution of the short liquor on the laundry is done in the

Washing machine by the large number of water-insoluble, solid particles, which are circulated together with the liquid and the laundry items. For introducing the short liquor into the laundry treatment space, an injection, spraying or pumping system, for example a circulating pump, may also be used.

In a preferred embodiment of the invention, a method is proposed, which provides a ratio of the weight of the dry textile or laundry lot to short liquor of 1: 2 to 1: 1, 5, whereby the distribution of the short liquor takes place by means of a circulating pump.

At the end of the first sub-washing cycle, in a preferred embodiment, the

Washing liquor, which according to the invention includes the water-insoluble solid particles, not removed.

In a further preferred embodiment, at the end of the first sub-wash cycle, a possibly existing free liquor, i. a fleet that is not bound in the textiles or interstices of the water-insoluble solid particles, but not the particles themselves.

In a further preferred embodiment, at the end of the first sub-washing cycle, the water-insoluble solid particles are removed from the laundry treatment space of the machine and brought into a reservoir outside the laundry treatment space.

In a further preferred embodiment, at the end of the first sub-washing cycle, the water-insoluble solid particles are removed from the laundry treatment space and replaced by others which are not exposed to the short liquor. In this way, parts of the short fleet can be used multiple times.

At the beginning of the second sub-wash cycle, additional feed of water occurs, ultimately leading to the formation of a liquor known from conventional washing processes. In the context of the present invention, this most dilute liquor is called a long liquor for better distinction from the short liquor. Within the meaning of the present invention, the long liquor can also be produced as the result of a first rinse cycle. The liquor, which includes the dilution stages of the short liquor up to a long liquor, is called a diluent liquor in the context of the present invention. During the dilution of the short liquor to the formation of the long liquor, the concentration of the detergent in the liquor is reduced. In addition, in a preferred embodiment, the dilution of the Concentration of the preferred salt increases the hydrophilicity and water solubility of a preferably contained nonionic surfactant. As a result, a phase inversion is caused, wherein first a microemulsion system of Winsor type III and lastly, with further dilution, an emulsion system of Winsor type I is formed. Without wishing to be bound by theory, the Applicant believes that the training of the

Winsor Type III microemulsion system for improved separation of the Winsor Type III

Microemulsion system of Winsor type II relaxed dirt is responsible. Of the

The expert knows that the interfacial tension in the three - phase region of the

Microemulsion system of Winsor type III is very low. It is also known that low interfacial tensions promote the detachment of fat. Another advantage of the low interfacial tensions of the Winsor Type III microemulsion systems is that the better fat solubility can use less surfactant than single-type Winsor Type IV microemulsions, making the process more eco-friendly. The interplay of the Winsor Type II microemulsion system in the short liquor in the first sub-wash cycle and the Winsor Type III and Winsor Type I microemulsion systems in the second sub-wash cycle or sub-wash cycles then results in particularly good wash results.

However, also wash liquors consisting of the water-insoluble solid particles and a single-phase liquid phase Winsor type IV are the subject of the present invention, since the combination with the particles overcomes many disadvantages of the single-phase Winsor IV microemulsion in a conventional washing process.

As already described, the second sub-washing cycle is started by the supply of water, whereby the short liquor is diluted. If the remaining addition of the water until the final dilution and thus training the long liquor without further temporal

Interruption, phase inversion occurs via the Winsor Type III microemulsion system to the Winsor Type I microemulsion system in the second sub-wash cycle.

However, it may be advantageous if the dilution of the short liquor to the long liquor takes place in individual stages, that is, with interruptions of the addition of water. In a particularly preferred embodiment of the invention, therefore, a textile washing process is carried out as described above, wherein the phase inversion during the second

Underwashing cycle or during the other sub-washing cycles, wherein first a microemulsion system of Winsor type III and last of the Winsor type I is formed.

Particularly preferred is a method which is characterized by the passage of at least 3 sub-washing cycles, wherein the second sub-washing cycle, the production of a The Winsor Type III microemulsion system as a dilution liquor and the third sub-wash cycle comprises the long liquor washing process, ie the final amount of water introduced, optionally until the long liquor has been removed. The second sub-wash cycle may comprise multiple stages representing different levels of dilution, but at all stages there is a Winsor Type III microemulsion system. Once the dilution has progressed to phase inversion to Winsor Type I, the third begins

Under wash cycle. Further addition of water in this third sub-wash cycle is of course possible, but not required for performance reasons, nor desirable for environmental or economic reasons and therefore not preferred.

In a further preferred embodiment of the method, in the first sub-washing cycle and in particular only in the first sub-washing cycle, the heating of the machine is switched on, while the heating in the second sub-washing cycle and, if present, further

Sub-washing cycles and in optionally subsequent rinsing cycles is preferably switched off.

Alternatively, the machine may also be supplied with water heated by an internal or external heater to produce the short liquor microemulsion systems which cools during the first sub-wash cycle. The dilution to the long liquor is then preferably carried out with cold water. This is particularly advantageous when the single-phase microemulsion or the Winsor Type II microemulsion system in the short liquor contains nonionic surfactants. Nonionic surfactants become more hydrophobic with increasing temperature, and more hydrophilic with decreasing temperature. The heated nonionic surfactants provide higher hydrophobicity of the short liquor, thereby improving the interaction with grease and oily soils and their relaxation on the fabrics, while the nonionic surfactants in the cooling dilution liquor and the colder long liquor become more hydrophilic and coalesce from the water Rinse better with the dirt and have it removed. In this preferred method, therefore, the breaking of the microemulsion or the phase inversion from the Winsor II system to the Winsor I system, which are otherwise triggered only by the dilution, even by the

Temperature control of the process supported.

In a preferred embodiment of the method it is therefore provided that the first sub-washing cycle is carried out at temperatures of 10 to 60 ° C, preferably of at least 20 to 40 ° C.

In addition, the method has the advantage that heating energy as opposed to

conventional method is consumed only in the first sub-washing cycle. Because the first Subwash cycle involves only a short fleet, this is in contrast to conventional methods in which a long liquor, so a larger amount of aqueous liquor to be heated, energy saved.

Finally, the dirt along with the long liquor optionally after

Passing through further sub-washing cycles removed and removed from the laundry treatment room of the washing machine.

Another embodiment of the invention is a device for cleaning soiled textile substrates comprising a plurality of water-insoluble solid particles, a reservoir for receiving the particles inside or outside the device and a wash liquor according to the invention.

An essential feature of the device according to the invention is the presence of the abovementioned water-insoluble solid particles, and a reservoir for the particles

The apparatus of the invention typically includes a trap door in a housing to allow access to the interior of the washing tub to provide a substantially closed system. Preferably, the door includes a window of the stationary cylindrical drum rotatably supported in another drum while the rotatably supported cylinder drum is mounted vertically inside the housing. Consequently, a

Front loading device preferred. Alternatively, the stationary cylindrical drum may be mounted vertically within the housing and the access device located in the top of the device.

The device is suitable for contact of the particles and the invention

Provide wash liquor with the soiled substrate. Ideally, these particles should be efficiently circulated to promote effective purification.

According to the invention, the device comprises at least one reservoir, in particular with a corresponding control, for the water-insoluble solid particles, for example located inside the washing machine and suitable for controlling the flow of particles within the washing machine and containing the particles for regeneration.

In addition, it has been found that the measures of the process according to the invention make it possible to regenerate the water-insoluble solid particles, and the particles can be satisfactorily reused in the purification process, although some deterioration in performance generally after three uses of the particles can be observed. Re-use of the particles will give optimum results when re-coated with the concentrate before reuse.

The regeneration of the water-insoluble solid particles can be carried out in a manner known per se, as described, for example, in WO 2012 / 035342A1. In the context of the present invention, the regeneration is carried out by introducing the particles optionally with the detergent into the decolorizing device, for example in a separate rinse, optionally by adding cleaning agents, which may also be of an aggressive nature. The temperature of the regeneration step is independent of the washing temperature when the textile substrate has been removed from the washing machine before regeneration. Furthermore, the usual detergent raw materials can be used.

Examples:

Example 1 :

In Table 1 (recipe numbers 2 to 7) are microemulsions and for the formation of

Microemulsions capable surfactant systems which can be used together with water-insoluble solid particles in a textile washing process according to the invention:

Table 1 :

Cetio DOE: dicapryl ether

Dehydol® LT7: nonionic surfactant, C12 / 18 + 7EO, BASF

Maranil® A55: Linear Alkylbenzenesulfonate (LAS)

The amounts are given in percent by weight based on the total agent and refer to the active ingredient content (% AS) of the ingredients mentioned.

In these systems, the cosurfactant hexanol serves to get into the single-phase microemulsion phase. Salt is not required here. The oil component is Cetiol® OE. These formulations, which are obtained from a concentrate according to the invention by dilution with water, are used directly in a washing cycle together with polyamide particles as

Cleaning medium used. They are also single-phase and clear in the presence of the oil, which is considered in the context of the present invention as an indicator of the presence of a microemulsion. As a non-inventive comparative example is used in the above table, the recipe 1 without cosurfactant. This contains only a traditional surfactant mixture consisting of LAS and a nonionic surfactant.

Claims

claims

1. Aqueous wash liquor in a device for cleaning soiled textile substrates, containing a plurality of water-insoluble solid particles and a

Liquid phase, characterized in that the liquid phase contains a microemulsion.

2. wash liquor according to claim 1, characterized in that the liquid phase

a) consists of a microemulsion or

b) is two or more phases.

3. wash liquor according to one of claims 1 to 2, characterized in that the liquid phase

a) comprises or consists of a 2-phase Winsor II phase

b) includes or consists of a Winsor Ill phase.

4. wash liquor according to one of claims 1 to 3, characterized in that the liquid phase of the wash liquor is prepared by dilution of a mono- or multiphase concentrate.

5. wash liquor according to claim 4, characterized in that the concentrate

a) surfactants, in particular a combination of anionic and nonionic surfactants, preferably in amounts of 1 to 80 wt .-%, contains, and / or

b) one or more inorganic salts, preferably sodium sulfate, in particular in

Amounts up to 70 wt .-%, and / or

c) one or more additional oils, preferably di-ethers, in particular di-n-octyl ether,

especially in amounts up to 60 wt .-%, contains.

6. wash liquor according to one of claims 1 to 5, characterized in that the concentrate comprises a substantially anhydrous paste and surfactants, in particular a mixture of anionic and nonionic surfactants containing.

7. wash liquor according to one of claims 1 to 6, characterized in that the concentrate can be converted by dilution with water in a single-phase microemulsion or in a microemulsion system of Winsor type 2, which 0.5 to 5 wt .-% surfactants and 0 contains up to 5% by weight of additional oils and preferably 80 to 94.6% by weight of water and 0 to 15% by weight of inorganic salts.

8. Washing liquor according to one of claims 1 to 7, characterized in that the weight ratio of textile substrate to liquid phase in the range of 1: 0, 1 to 1: 5.

9. wash liquor according to one of claims 1 to 8, characterized in that the water-insoluble solid particles

a) inorganic nature, in particular zeolites, clays and / or ceramic include, and / or

b) are organic in nature, in particular polymer particles include.

10. wash liquor according to claim 9, characterized in that the polymer particles

Polyalkanes, polyesters, polyurethanes and / or polyamides including their copolymers, in particular a nylon 6.6 homopolymer having an average molecular weight of 5,000 to 30,000 daltons.

1 1. wash liquor according to one of claims 1 to 10, characterized in that the water-insoluble solid particles each have an average weight in the range of 20 to 50 mg.

12. textile washing process in a washing machine using a wash liquor, as defined in any one of claims 1 to 1 1.

13. textile washing method according to claim 12, characterized in that in one

Washing cycle is introduced with at least two consecutive sub-washing cycles of the laundry items to be cleaned in the laundry room of the washing machine, the concentrate is placed in a detergent storage room of the washing machine and in the first sub-washing cycle with simultaneous formation of a short fleet in the

Laundry room of the washing machine transported, in particular sprayed or pumped, being as a short liquor a single-phase microemulsion or a

A Winsor Type 2 microemulsion system is formed or maintained to interact with the Winsor Type 2 short liquor with the debris present in the laundry in the first sub-wash cycle, thereby causing the fat and oily debris to relax on the fiber, and subsequently in at least one other Sub-wash cycle dilute the liquor with water and continue to dilute with water until the formation of a long liquor, the dirt is released from the laundry items, and at the end of the last sub-wash cycle, the dirt is transported together with the long liquor from the laundry treatment room.

14. textile washing method according to claim 12, characterized in that the

Microemulsion system of Winsor type 2 is not present macroscopically separated during the application, but introduced as an emulsion of the two phases of the microemulsion system of Winsor type 2 in the laundry room of the machine and applied to the laundry items

15. textile washing method according to claim 13 or 14, characterized in that in the first sub-washing cycle, a weight ratio of the soiled dry textile substrate or laundry lot to the short liquor of not less than 1: 2, in particular not less than 1: 1, 5 is formed.

16. A textile washing process according to any one of claims 12 to 15, characterized in that during the first sub-washing cycle sub-washing cycle or following the first sub-washing cycle further sub-washing cycles, a phase inversion, wherein first a microemulsion system of Winsor type 3 and last of the Winsor type 1 is trained.

17. A textile washing process according to any one of claims 12 to 16, characterized in that at least 3 sub-washing cycles are passed, wherein the second sub-washing cycle, the production of a microemulsion system of Winsor type 3 as dilution liquor and the third sub-washing cycle the washing process with the long liquor, so the final amount the water introduced, if necessary, until the removal of the long fleet.

18. Use of a plurality of water-insoluble solid particles and a detergent comprising a single- or multi-phase non-solid concentrate for use as a laundry detergent, wherein the concentrate is suitable, when diluting in a short liquor, a single-phase microemulsion or a microemulsion system from Winsor Type 2, for cleaning soiled textile substrates by contacting the detergent and the particles with the textile substrate.

19. Use according to claim 18, characterized in that one dilutes the wash liquor with water in a separate step or as a first rinsing step.

A process for regenerating a plurality of contaminated water insoluble solid particles as defined in any one of claims 9 to 11 using a single phase

A microemulsion, a Winsor Type II microemulsion system or a concentrate as defined in any one of claims 4 to 7, by contacting the particles with the concentrate.