The present invention relates to a process for manufacturing a detergent portion unit, comprising a solid gel.
Continuously changing requirements are placed on the forms of manufacture and supply of washing and cleaning agents. The main focus has, for quite some time, been on the convenient dosing of detergents and cleaning agents by the consumer and the simplification of the work steps necessary for carrying out a washing or cleaning method. One technical solution is provided by pre-portioned washing or cleaning agents, for example, water-soluble containers having one or more receiving compartments for powdered or liquid detergents or cleaning agents. A further technical solution is provided by detergent tablets which can have a single-phase or multi-phase design.
To produce the water-soluble containers, water-soluble polymers are generally deformed to form receiving chambers, which are subsequently filled with a detergent or cleaning agent and finally closed. The receiving chambers can be produced, for example, from water-soluble polymer films by means of deep-drawing methods. In an alternative embodiment of the method, a water-soluble polymer is deformed by means of injection molding to form a receptacle.
The water-soluble packaging material used for packaging the filled detergent portion units is generally hygroscopic. In the context of the production, packaging, storage, and subsequent use by the consumer, the water absorption tendency and water absorption capacity of the packaging means can cause the portion units to adhere to surfaces of machines or packaging means and not be able to be conveyed optimally, or adjacent portion units, e.g., in a common outer packaging, to adhere to one another. To avoid this adhesion tendency of the water-soluble portion units, it is possible to modify the surface properties thereof by applying a powder agent. The powdering of the water-soluble detergent portion units in turn requires an additional method step.
The water-soluble packaging materials used are generally not washing active or cleaning active, i.e., do not contribute to the product performance. The reduction in the amount of packaging with respect to the total weight of the detergent portion units would thus not result in loss of performance and would be welcomed on the grounds of sustainability and economic efficiency.
Finally, the washing performance provided by the detergent portion unit is directly related to the dissolution properties of the portion unit. Particularly with regard to the increasing use of cold washing methods, it is preferred to keep the thickness of the water-soluble film material contained in the detergent portion unit as low as possible in order to accelerate the dissolution process. However, the reduction in the thickness of the surrounding film material simultaneously requires a reduced mechanical stability of the portion units. Overcoming this apparent dichotomy of mechanical stability and dissolution rate of detergent portion units packaged using water-soluble films is still a relevant aspect in the development of water-soluble detergent portion units.
Detergent tablets, in which, however, sufficient mechanical stability and a high dissolution rate are irreconcilably opposed in a similar manner as in the case of the sachets, offer an alternative to the previously described sachets.
Multi-phase detergent portion units, for example in the form of core tablets, which in addition to a tableted body comprise wax or gel phases, offer an alternative to completely compressed detergent tablets. Thus, European patent EP 1 032 642 B1 describes, for example, detergent tablets comprising a compressed phase and an uncompressed gel phase and a method for the manufacturing thereof.
Against the background of the prior art described above, the object of the application was that of providing efficient methods for manufacturing fast-dissolving detergent portion units that have high product and storage stability, can be prepared in a simple manner using minimal amounts of packaging materials, and appeal to the consumer with an attractive olfactory, visual, and tactile experience. The detergent portion units should have a high product performance and be easy and safe to handle for the consumer.
A first subject of the application is a method for manufacturing a detergent portion unit comprising
The term “detergent portion unit” describes a supply form in which a measured portion of a detergent or cleaning agent is present. Detergent portion units consequently refer both to supply forms for textile laundry and to supply forms for cleaning hard surfaces such as ceramics, glass, metal, or tiles. The detergent portion unit preferably has a weight of 14 g to 42 g, preferably of 18 g to 38 g, in particular of 20 g to 34 g.
The detergent portion unit comprises a solid gel. The detergent portion unit can consist of the solid gel. In this case, the solid gel preferably has a weight of 14 g to 42 g, more preferably of 18 g to 38 g, in particular of 20 g to 34 g. If the detergent portion unit comprises further constituents in addition to the solid gel, the weight of the solid gel is preferably 10 g to 28 g, preferably 12 g to 23 g and in particular 15 g to 20 g.
Bodies which exhibit elastic deformation behavior under the action of force are referred to as gel bodies. Bodies are considered dimensionally stable if they have an inherent dimensional stability that enables them to assume a non-disintegrating three-dimensional shape under the usual conditions of manufacture, storage, transport and handling by the consumer, this three-dimensional shape also not changing under the conditions mentioned over an extended period of time, preferably 4 weeks, particularly preferably 8 weeks and in particular 32 weeks, i.e., under the usual conditions of manufacture, storage, transport and handling by the consumer, the body remains in the three-dimensional geometric shape created during manufacture, i.e., it does not dissolve.
The three-dimensional shape of the solid gel is basically freely selectable; its side surfaces can, for example, be designed to be convex, concave or planar. At the same time, however, certain spatial configurations have proven to be particularly advantageous against the background of the manufacturability, storage, and use of the solid gels.
In correspondingly advantageous detergent portion units, the solid gel comprises a flat underside, the largest diagonal of which is greater than the height of the solid gel. Not only can these bodies be manufactured in a simple manner, for example by means of casting methods, but they can also be packaged in a simple and space-saving manner and are suitable for dosing via the dosing or dispensing chambers of electronic cleaning devices. It is particularly preferred if the solid gel has a flat underside, the largest diagonal of which is more than 1.5 times, preferably more than twice the height of the solid gel.
For manufacturability, for example in relation to the removal of the solid gel from a casting mold, it has proven to be advantageous if the underside of the solid gel does not have any corners. Preferred solid gels are therefore characterized by oval undersides or alternatively by ellipsoidal or round, preferably round, undersides. Corresponding solid gels with non-angular undersides are also preferred by many consumers due to their optics. For example, such solid gels having an underside and an upper side which are connected to one another by a cylindrical lateral surface are therefore preferred.
Advantages in relation to the use of space during manufacture and packaging are realized by angular undersides. If the solid gels are molded, for example, in the form of plates, which are subsequently cut into solid gels, angular undersides are advantageous since such solid gels can be cut without any residual amounts occurring and can be packaged in a space-saving manner. In an alternative embodiment, preferred solid gels therefore have angular undersides, in particular triangular, square or hexagonal undersides. For further processing or packaging, it can be advantageous if the solid gel has an angular underside with rounded corners.
With regard to the manufacture, packaging, and use of the detergent portion units, it has also proven to be advantageous if the solid gels have an upper side plane parallel to the underside.
In a first preferred geometric embodiment, the solid gel has an underside and an upper side which have the same geometric shape, wherein the underside and the upper side have the same surface size. As already described above, corresponding solid gels can be produced in a simple manner, for example by casting plates and subsequently cutting the plates into individual solid gels. In addition, in any subsequent method steps, said solid gels can be spatially aligned during packaging or use by the user due to the geometric identity of the underside and upper side as solid gels with reduced body symmetry. This applies in particular to solid gels which at the same time have an upper side plane parallel to the underside. Examples of such solid gels are circular cylinders, elliptical cylinders, parallelepipeds, rhomboids, straight or oblique prisms, cuboids or cubes. The group of circular cylinders and elliptical cylinders in turn includes vertical circular cylinders and elliptical cylinders as well as the inclined circular cylinders and elliptical cylinders. Due to their simple production by isolation from a plate, solid gels in the form of vertical circular cylinders, vertical elliptical cylinders, straight prisms, straight cuboids or cubes are preferred.
In an alternative embodiment, the solid gel has an underside and an upper side which have the same geometric shape, wherein the underside and the upper side have different surface sizes. Corresponding solid gels can be preferred due to their attractive appearance or their optimized fit while simultaneously being comparatively simple to manufacture. Examples of such solid gels include circular cylinders or elliptical cylinders with a convex or concave underside and a planar upper side. Further examples include truncated cones or truncated pyramids.
In summary, preferred subject matters of the application can be characterized as detergent portion units comprising a solid gel having an underside and an upper side, wherein the surface of the upper side amounts to 80 to 100%, preferably 90 to 100%, and in particular 98 to 100% of the underside.
The method is suitable in particular for preparing solid gel having a high surfactant content. In preferred embodiments, the first flowable surfactant-containing composition contains, based on the total weight thereof, 30 to 70 wt. %, preferably 40 to 60 wt. %, and in particular 45 to 55 wt. %, surfactant.
In terms of the manufacturability and the subsequent dissolving power of the solid gels, it has proven advantageous for them to contain 15 to 35 wt. %, preferably 20 to 30 wt. %, of an aqueous organic solvent. The aqueous organic solvent of the solid gel is preferably introduced via the first and second flowable compositions. Thus, it is preferred if the second flowable gelling-agent-containing composition also contains an organic solvent. Particularly preferred flowable gelling-agent-containing compositions contain gelling agent and organic solvent in a total weight proportion above 50 wt. %, preferably above 70 wt. %, and in particular above 90 wt. %.
Preferred solid gels further contain dye.
Preferred solid gels are transparent. Such solid gels are referred to as “transparent” if they have a transmission above 50%, preferably above 60% and in particular above 80%, in the wavelength range of from 410 to 800 nm at at least one wavelength, preferably at 600 nm. The transmission is determined by means of VIS spectrometry at a sample temperature of 20° C. and with a cuvette length of 10 mm.
For the manufacture and later storage properties and transport properties of the solid gels, it has proven advantageous to use low-molecular-weight gelling agents having a molar mass of up to 2000 g/mol in the solid gel, wherein the weight proportion thereof with respect to the total weight of the solid gel is preferably less than 5 wt. %, preferably 0.1 to 5 wt. %, and particularly preferably 0.1 to 2.5 wt. %. Furthermore, the advantages of the method according to the invention are particularly evident in the processing of these low-molecular-weight gelling agents with their specific gelling properties.
In a preferred embodiment, the low-molecular-weight gelling agent has a solubility in water of less than 0.1 g/L (20° C.). The solubility of the organic gelator compound is determined at 20° C. in bidistilled, demineralized water.
Furthermore, gelling agents are preferably suitable which comprise a structure containing at least one hydrocarbon structural unit having 6 to 20 carbon atoms (preferably at least one carbocyclic, aromatic structural unit) and additionally an organic structural unit that is covalently bonded to the aforementioned hydrocarbon unit and has at least two groups selected from —OH, —NH—, or mixtures thereof.
Particularly preferred solid gels are characterized in that said solid gels contain at least one benzylidene alditol compound of formula (GB-I) as gelling agent
Due to the stereochemistry of the alditols, it should be mentioned that said benzylidene alditols according to the invention are suitable in the L configuration or in the D configuration or in a mixture of the two. Due to natural availability, the benzylidene alditol compounds are preferably used according to the invention in the D configuration. It has proven preferable if the alditol backbone of the benzylidene alditol compound according to formula (GB-I) contained in the shaped body is derived from D-glucitol, D-mannitol, D-arabinitol, D-ribitol, D-xylitol, L-glucitol, L-mannitol, L-arabinitol, L-ribitol or L-xylitol.
Particularly preferred are those solid gels which are characterized in that R1, R2, R3, R4, R5 and R6 according to the benzylidene alditol compound of formula (GB-I) mean, independently of one another, a hydrogen atom, methyl, ethyl, chlorine, fluorine, or methoxy, preferably a hydrogen atom.
n according to the benzylidene alditol compound of formula (GB-I) preferably represents 1.
m according to the benzylidene alditol compound of formula (GB-I) preferably represents 1.
The solid gel very particularly preferably contains at least one compound of formula (GB-I1) as the benzylidene alditol compound of formula (GB-I)
where R1, R2, R3, R4, R5 and R6 are as defined in formula (I). Most preferably, according to formula (GB-I1), R1, R2, R3, R4, R5 and R6 represent, independently of one another, a hydrogen atom, methyl, ethyl, chlorine, fluorine, or methoxy, preferably a hydrogen atom.
Most preferably, the benzylidene alditol compound of formula (GB-I) is selected from 1,3:2,4-di-O-benzylidene-D-sorbitol; 1,3:2,4-di-O-(p-methylbenzylidene)-D-sorbitol; 1,3:2,4-di-O-(p-chlorobenzylidene)-D-sorbitol; 1,3:2,4-di-O-(2,4-dimethylbenzylidene)-D-sorbitol; 1,3:2,4-di-O-(p-ethylbenzylidene)-D-sorbitol; 1,3:2,4-Di-O-(3,4-dimethylbenzylidene)-D-sorbitol or mixtures thereof.
Preferred solid gels contain at least one 2,5-diketopiperazine compound of formula (GB-II) as the gelling agent
It is preferred according to the invention if R3 and R4 according to formula (GB-II) represent a hydrogen atom. It is particularly preferred according to the invention if R2, R3 and R4 according to formula (GB-II) represent a hydrogen atom. Therefore, particularly preferred shaped bodies according to the invention contain at least one 2,5-diketopiperazine compound according to formula (GB-IIa)
where R1 and R5 are as defined under formula (GB-II) (vide supra).
It has been found to be preferred if the functional group R1 according to formula (GB-II) and according to formula (GB-IIa) binds in the para position of the phenyl ring. Within the meaning of the present invention, shaped bodies according to the invention are therefore preferred which contain at least one 2,5-diketopiperazine compound according to formula (GB-IIb),
where R1 and R5 are as defined under formula (GB-II) (vide supra). By way of illustration, numbers 3 and 6 positioned at the ring atoms in formula (GB-IIb) only mark positions 3 and 6 of the diketopiperazine ring, as they are generally used in the scope of the invention for naming all 2,5-diketopiperazines according to the invention.
The 2,5-diketopiperazine compounds of formula (GB-II) have centers of chirality at least on the carbon atoms in positions 3 and 6 of the 2,5-diketopiperazine ring. The numbering of ring positions 3 and 6 was illustrated by way of example in formula (GB-IIb). The 2,5-diketopiperazine compound of formula (GB-II) of the composition according to the invention is preferably, based on the stereochemistry of the carbon atoms at the 3 and 6 position of the 2,5-diketopiperazine ring, the configuration isomer 3S,6S, 3R,6S, 3S,6R, 3R,6R, or mixtures thereof, particularly preferably 3S,6S.
Preferred solid gels contain at least one 2,5-diketopiperazine compound of formula (GB-II) as the gelling agent, selected from 3-benzyl-6-carboxyethyl-2,5-diketopiperazine, 3-benzyl-6-carboxymethyl-2,5-diketopiperazine, 3-benzyl-6-(p-hydroxybenzyl)-2,5-diketopiperazine, 3-benzyl-6-iso-propyl-2,5-diketopiperazine, 3-benzyl-6-(4-aminobutyl)-2,5-diketopiperazine, 3,6-di(benzyl)-2,5-diketopiperazine, 3,6-di(p-hydroxybenzyl)-2,5-diketopiperazine, 3,6-di(p-(benzyloxy)benzyl)-2,5-diketopiperazine, 3-benzyl-6-(4-imidazolyl)methyl-2,5-diketopiperazine, 3-benzyl-6-methyl-2,5-diketopiperazine, 3-benzyl-6-(2-(benzyloxycarbonyl)ethyl)-2,5-diketopiperazine or mixtures thereof. In turn, compounds having the aforementioned configuration isomers are preferably suitable for selection.
It is also possible for the solid gels according to the invention to contain at least one diarylamidocystine compound of formula (GB-III) as the gelling agent a)
Each of the stereocenters contained in the compound of formula (GB-III) can represent, independently of one another, the L or D stereoisomer. It is preferable according to the invention for the above-mentioned cystine compound of formula (GB-III) to be derived from the L stereoisomer of cysteine.
The above-mentioned solid gels can contain at least one compound of formula (GB-III), in which R1, R2, R3 and R4 represent, independently of one another, a hydrogen atom, a halogen atom, a C1-C4 alkyl group, a C1-C4 alkoxy group, a C2-C4 hydroxyalkyl group, a hydroxyl group, or R1 with R2 or R3 with R4 forms a 5-membered or 6-membered annulated ring, which in turn can each be substituted with at least one group from C1-C4 alkyl group, C1-C4 alkoxy group, C2-C4 hydroxyalkyl group, or hydroxyl group. In particular, shaped bodies which contain N,N′-dibenzoylcystine (R1═R2=R3═R4=hydrogen atom; X+═independently a hydrogen atom or an equivalent of a cation), in particular N,N′-dibenzoyl-L-cystine, as a diarylamidocystine compound of formula (GB-III), are particularly suitable.
The N—(C8-C24) hydrocarbylglyconamide compounds suitable as the gelling agent a) preferably have the formula (GB-IV)
In particularly preferred embodiments, the functional group
is one of a functional group derived from a glycuronic acid, in particular the glycuronic acid of a hexose (n=4). In particular, glucuronic acid should be mentioned as a preferred functional group. R1 is preferably H or a short-chain alkyl functional group, in particular methyl. R2 is preferably a long-chain alkyl functional group, for example a C8-C18 alkyl functional group.
Compounds of formula (GB-IV1) are therefore very particularly preferred
where R2 has the meanings given for formula (GB-IV).
In a particularly preferred embodiment, the at least one low-molecular-weight gelling agent of the second flowable gelling-agent-containing composition is selected from the group consisting of the group of cyclic dipeptides, cyclic dipeptide derivatives and dibenzylidene sorbitols. The at least one gelling agent of the second flowable gelling-agent-containing composition is particularly more preferably dibenzylidene sorbitol (DBS) because of its technical effect.
In step iii) of the method, the first and second flowable compositions are fed to the mold. In one embodiment of the method, the first flowable composition and the second flowable composition are fed to the mold in the same line. This embodiment of the method is characterized by reduced equipment. In this embodiment of the method, partial mixing of the first and second flowable compositions can already take place in the feed line leading to the mold. The disadvantages of this embodiment of the method are reduced control of the gelation process and, in the event of a production interruption, increased cleaning effort before the manufacturing equipment is restarted.
For the latter reasons, it is preferred to feed the first flowable composition and the second flowable composition to the mold in separate lines.
The materials known to a person skilled in the art for the production of casting molds, for example materials from the group of metals, polymers or rubbers, are suitable for the production of the mold. With regard to the removal of the solid gel from the mold, materials from the group of silicones have proven to be particularly suitable.
In step iv) of the method, the first and second flowable compositions are introduced into the mold. In one embodiment of the method, the first flowable composition and the second flowable composition are introduced into the mold by means of a common injector. As in the case of the previously described common supply line, this embodiment of the method is characterized by reduced equipment. In addition, in this case too, partial mixing of the first and second flowable compositions can already take place in the common injector. The disadvantages of this embodiment of the method, however, are, albeit to a lesser extent than in the case of the common feed line, reduced control of the gelation process and, in the event of a production interruption, increased cleaning effort before the production equipment is restarted.
For the latter reasons, it is preferred to introduce the first flowable composition and the second flowable composition into the mold by means of separate injectors.
An injector is a device which is suitable for introducing a free-flowing composition into a mold. The injector is, for example, a filling spout or a nozzle.
In a preferred method variant, the first flowable composition and the second flowable composition are introduced into the mold simultaneously in step iv). This approach improves the desired mixing of the two compositions due to turbulent flow.
The embodiment of the method according to the invention is suitable particularly for processes in the course of which flowable compositions are mixed in weight proportions that differ greatly from one another. In the method according to the invention, the first flowable composition and the second flowable composition are preferably mixed in the mold in a weight ratio of 50:1 to 5:1, preferably 35:1 to 8:1.
The first flowable composition and the second flowable composition are introduced into the mold preferably at a filling rate of 1 ml/s to 25 ml/s.
It has also proven advantageous for method efficiency if the dynamic mixing device is lowered before the first flowable composition and the second flowable composition are introduced into the mold. It is particularly preferred to introduce the first flowable composition and the second flowable composition into the effective region of the mixing element of the dynamic mixing device.
The mixers used can be, for example, impeller mixers. Preferred mixing devices have a gear as a mixing element. It is very particularly preferred that a dynamic mixing device is used which comprises two intermeshing gears as a mixing element. An appropriate arrangement of the mixing elements not only enables the homogeneous mixing of the two flowable compositions but at the same time ensures uninterrupted cleaning of the two gears used as a mixing element.
The mixing element preferably fills only 1 to 10 vol. %, preferably 2 to 8 vol. %, of the internal volume of the mold. It is preferably placed in the centroid of the volume of the mold. It is also preferred to position the mixing element in the mold such that it is close to the bottom, as this allows the effect of the mixing element on the two compositions to begin early.
To assist the mixing process, the mixing element and the mold can be moved relative to each other in step v). Such a relative movement can be realized by the movement of the mixing element, the movement of the mold or the movement of the mixing element and the mold. By means of the relative movement, the mixing of the two compositions in the mold can be improved.
A preferred method variant that is technically easy to implement provides for moving the mixing element in the mold in step v). The movement can occur in the mold in the horizontal or the vertical or the horizontal and the vertical direction. In the case of a horizontal movement, the direction of movement of the mixing element is parallel to the opening area of the mold; in the case of a vertical movement, the direction of movement is orthogonal to this area.
Alternatively or in conjunction with the movement of the mixing element, the mold can be moved in step v). A corresponding relative movement can result, for example, from the transport of the mold on a conveyor belt or from a shaking movement of the mold. The movement of the mold can also occur in the horizontal or the vertical or the horizontal and the vertical direction. In the case of a horizontal movement, the direction of movement of the mold is parallel to the opening area of the mold; in the case of a vertical movement, the direction of movement is orthogonal to this area.
The mixing of the first flowable composition and the second flowable composition in step v) is preferably carried out over a time period of 1 to 20 seconds, more preferably 2 to 10 seconds.
In step vi) of the method, the surfactant-containing and gelling-agent-containing mixture solidifies in the mold to form a dimensionally stable solid gel. To accelerate the solidification process, the surfactant-containing and gelling-agent-containing mixture can be cooled in step vi). The cooling preferably takes place under defined climatic conditions in which, in addition to the temperature, the humidity in the process chamber is also controlled and regulated, for example.
Finally, the dimensionally stable solid gel can be removed from the mold.
In order to manufacture detergent portion units which comprise further components in addition to the solid gel, a procedure is suitable in which the solid gel is bonded to a prefabricated shaped body.
In a first preferred approach, the mold into which the first and second flowable preparations are introduced in step iv) is partially filled with a prefabricated shaped body. The prefabricated shaped body covers the bottom surface of the mold into which the first and second flowable preparations are introduced in step iv), preferably at least partially, particularly preferably completely.
In a second preferred approach used as an alternative or used in conjunction with the previously described approach, the surfactant-containing and gelling-agent-containing mixture is covered with a prefabricated shaped body before, while or after the surfactant-containing and gelling-agent-containing mixture is allowed to solidify in step vi) in the mold. In this case, it is preferred that the surface of the surfactant-containing and gelling-agent-containing mixture that is visible in the mold is completely covered with a prefabricated shaped body.
If the surfactant-containing and gelling-agent-containing mixture is introduced into the mold onto a first prefabricated shaped body and the side opposite the side covered with the first prefabricated shaped body is covered with a second prefabricated shaped body, a sandwich-like detergent portion unit which is particularly advantageous in terms of handling and appearance is obtained.
A particularly preferred method variant for producing a detergent portion unit comprising
Preferred shaped bodies fill 5 to 45 vol. %, preferably 10 to 25 vol. %, of the mold.
The shaped body can be packaged in different ways. The use of cast bodies has proven to be technically easy to implement. The manufacture of the shaped body using casting processes has the advantage that a wide variety of geometries can be produced. The casting bodies are particularly preferably solidified melts.
Due to their ease of manufacture on an industrial scale, extruded bodies, in particular tablets, are particularly preferred as shaped bodies.
Irrespective of the method used for its manufacture, the shaped body preferably has a breaking strength of 50 N to 300 N, in particular of 50 N to 150 N. This breaking strength ensures, on the one hand, that the shaped body is sufficiently stable during production, transport and handling by the consumer and, on the other hand, ensures a satisfactory dissolution behavior of the shaped body in an aqueous liquor. The hardness of the shaped body is measured by deformation until fracture, wherein the force acts on the side surfaces of the shaped body and the maximum force that it withstands is determined. In order to determine the level of shaped body hardness, a tablet testing apparatus from the company Sotax is suitable, for example.
Preferred shaped bodies have an imprint.
If the solid gel is combined with a shaped body as previously described, the dimensionally stable solid gel partially covered by a shaped body is finally removed from the mold. The solid gel and the shaped body are preferably adhesively bonded to one another.
In a preferred embodiment of the detergent portion units, the shaped body also contributes to the active washing and active cleaning effect. Corresponding detergent portion units comprise a shaped body which, based on its total weight, contains more than 40 wt. %, preferably more than 60 wt. %, particularly preferably more than 80 wt. %, of active washing or active cleaning ingredient.
Fragrances form a first group of active washing or active cleaning ingredients integrated in the shaped body. Their incorporation into the shaped body ensures a fragrance experience that can be perceived by the consumer and which cannot be ensured in the same way when the fragrances are incorporated into the solid gel.
Builders, in particular the citrates, zeolites, silicates, and carbonates, especially preferably in particular the citrates and zeolites, constitute a further group of active washing or active cleaning ingredients preferably incorporated in the casing substance. The proportion by weight of said active ingredients with respect to the total weight of the casing substance is preferably 5 to 60 wt. %, in particular 10 to 50 wt. %. Casing substances which contain, based on the total weight thereof, 5 to 60 wt. %, in particular 10 to 50 wt. %, of citrate and/or zeolite are particularly preferred. These active substances not only contribute to the washing and cleaning effect as intended, but also improve the contour sharpness and resistance of the imprinted image in the event of the shaped body surface being imprinted.
The use of an active substance from the group of polymeric active washing or active cleaning ingredients, preferably from the group of celluloses and cellulose derivatives and anionic or nonionic aromatic polyesters, preferably from the group of celluloses, microcrystalline celluloses and carboxymethyl celluloses and anionic or nonionic aromatic polyesters, is also advantageous for the contour sharpness and durability of the imprinted image. The proportion by weight of said cellulose-based active ingredients with respect to the total weight of the casing substance is preferably 2 to 50 wt. %.
The composition of some preferred detergent portion units can be found in the following tables (amounts given in wt. % based on the total weight of the solid gel or the casing substance, unless otherwise indicated).
In summary, the following subjects, inter alia, are provided by this application:
1. A method for manufacturing a detergent portion unit comprising
2. The method according to point 1, wherein the solid gel has a weight of 14 g to 42 g, preferably of 18 g to 38 g, in particular of 20 g to 34 g.
3. The method according to one of the preceding points, wherein the solid gel comprises a flat underside, the largest diagonal of which is greater than the height of the solid gel.
4. The method according to one of the preceding points, wherein the solid gel has a flat underside, the largest diagonal of which is more than 1.5 times, preferably more than twice the height of the solid gel.
5. The method according to one of the preceding points, wherein the solid gel has an oval underside.
6. The method according to one of the preceding points, wherein the solid gel has an ellipsoidal or round, preferably round, underside.
7. The method according to one of the preceding points, wherein the solid gel has an angular underside.
8. The method according to one of the preceding points, wherein the solid gel has a triangular, square or hexagonal underside.
9. The method according to one of the preceding points, wherein the solid gel has an angular underside with rounded corners.
10. The method according to one of the preceding points, wherein the solid gel has an upper side which is plane parallel to the underside.
11. The method according to one of the preceding points, wherein the solid gel has an underside and an upper side which have the same geometric shape and wherein the underside and the upper side have the same surface size.
12. The method according to one of the preceding points, wherein the solid gel has an underside and an upper side which have the same geometric shape and wherein the underside and the upper side have different surface sizes.
13. The method according to one of the preceding points, wherein the solid gel has an underside and an upper side which are connected to one another by a cylindrical lateral surface.
14. The method according to one of the preceding points, wherein the solid gel has an underside and an upper side and the surface of the underside amounts to 80 to 100%, preferably 90 to 100%, and in particular 98 to 100% of the upper side.
15. The method according to one of the preceding points, wherein the first flowable composition and the second flowable composition are fed to the mold in separate lines.
16. The method according to one of the preceding points, wherein the mold is produced of a material from the group of metals, polymers or rubbers.
17. The method according to one of the preceding points, wherein the mold is produced of a material from the group of silicones.
18. The method according to one of the preceding points, wherein the first flowable composition and the second flowable composition are introduced into the mold by means of a common injector.
19. The method according to one of the preceding points, wherein the first flowable composition and the second flowable composition are introduced into the mold by means of separate injectors.
20. The method according to one of the preceding points, wherein the first flowable composition and the second flowable composition are introduced into the mold simultaneously.
21. The method according to one of the preceding points, wherein the first flowable composition and the second flowable composition are mixed in the mold in a weight ratio of 50:1 to 5:1, preferably 35:1 to 8:1.
22. The method according to one of the preceding points, wherein the first flowable composition and the second flowable composition are introduced into the mold at a filling rate of 1 ml/s to 25 ml/s.
23. The method according to one of the preceding points, wherein the mixing element of the dynamic mixing device is lowered before the first flowable composition and the second flowable composition are introduced into the mold.
24. The method according to one of the preceding points, wherein the first flowable composition and the second flowable composition are introduced into the effective region of the mixing element of the dynamic mixing device.
25. The method according to one of the preceding points, wherein the dynamic mixing device has a gear as a mixing element.
26. The method according to one of the preceding points, wherein the dynamic mixing device comprises two intermeshing gears as a mixing element.
27. The method according to one of the preceding points, wherein the mixing element fills 1 to 10 vol. %, preferably 2 to 8 vol. %, of the internal volume of the mold.
28. The method according to one of the preceding points, wherein the mixing element of the dynamic mixing device is located at the center of volume of the mold.
29. The method according to one of the preceding points, wherein in step v) the mixing element and the mold are moved relative to each other.
30. The method according to one of the preceding points, wherein in step v) the mixing element is moved in the mold.
31. The method according to one of the preceding points, wherein in step v) the mixing element is moved in the mold in the horizontal and/or the vertical direction.
32. The method according to one of the preceding points, wherein in step v) the mold is moved.
33. The method according to one of the preceding points, wherein in step v) the mold is moved in the horizontal and/or the vertical direction.
34. The method according to one of the preceding points, wherein the mixing of the first flowable composition and the second flowable composition in step v) is carried out over a time period of 1 to 20 seconds, preferably 2 to 10 seconds.
35. The method according to one of the preceding points, wherein the surfactant-containing and gelling-agent-containing mixture is cooled in step vi).
36. The method according to one of the preceding points, wherein the dimensionally stable solid gel is removed from the mold following step vi).
37. The method according to one of the preceding points, wherein the mold into which the first and second flowable preparations are introduced in step iv) is partially filled with a prefabricated shaped body.
38. The method according to point 37, wherein the bottom surface of the mold into which the first and second flowable preparations are introduced in step iv) is at least partially, preferably completely, covered with a prefabricated shaped body.
39. The method according to one of the preceding points, wherein the surfactant-containing and gelling-agent-containing mixture is covered with a prefabricated shaped body before, while or after the surfactant-containing and gelling-agent-containing mixture is allowed to solidify in step vi).
40. The method according to point 39, wherein the surface of the surfactant-containing and gelling-agent-containing mixture is completely covered with a prefabricated shaped body.
41. The method according to one of points 37 to 40, wherein the prefabricated shaped body fills 5 to 45 vol. %, preferably 10 to 25 vol. %, of the mold.
42. The method according to one of points 37 to 41, wherein the shaped body is in the form of a cast body.
43. The method according to one of points 37 to 41, wherein the shaped body is in the form of a pressed body, preferably a tablet.
44. The method according to one of points 37 to 43, wherein the shaped body has a breaking strength of 30 N to 300 N, preferably of 50 N to 150 N.
45. The method according to one of points 37 to 44, wherein the shaped body has an imprint.
46. The method according to one of points 37 to 45, wherein the dimensionally stable solid gel partially covered by a shaped body is removed from the mold following step vi).
47. The method according to one of the preceding points, wherein the first flowable surfactant-containing composition contains, based on the total weight thereof, 30 to 70 wt. %, preferably 40 to 60 wt. %, and in particular 45 to 55 wt. %, surfactant.
48. The method according to one of the preceding points, wherein the dimensionally stable solid gel contains, based on the total weight thereof, 15 to 35 wt. %, preferably 20 to 30 wt. %, aqueous organic solvent.
49. The method according to one of the preceding points, wherein the second flowable gelling-agent-containing composition contains low-molecular-weight gelling agent having a molar mass of up to 2000 g/mol, wherein the weight proportion of said gelling agent with respect to the total weight of the solid gel is preferably less than 5 wt. %, preferably 0.1 to 5 wt. %, particularly preferably 0.1 to 2.5 wt. %.
50. The method according to one of the preceding points, wherein the second flowable gelling-agent-containing composition contains low-molecular-weight gelling agent selected from the group of cyclic dipeptides, cyclic dipeptide derivatives and dibenzylidene sorbitols.
51. The method according to one of the preceding points, wherein the second flowable gelling-agent-containing composition contains dibenzylidene sorbitol as a low-molecular-weight gelling agent.
52. The method according to one of the preceding points, wherein the second flowable gelling-agent-containing composition also contains an organic solvent.
53. The method according to one of the preceding points, wherein the second flowable gelling-agent-containing composition contains gelling agent and organic solvent in a total weight proportion above 50 wt. %, preferably above 70 wt. %, and in particular above 90 wt. %.
54. The method according to one of points 37 to 53, wherein the shaped body contains, based on its total weight, more than 40 wt. %, preferably more than 60 wt. %, particularly preferably more than 80 wt. %, active washing or active cleaning ingredient.
55. The method according to one of points 37 to 54, wherein the shaped body contains an active washing or active cleaning ingredient from the group of fragrances.
56. The method according to one of points 37 to 55, wherein the shaped body contains an active washing or active cleaning ingredient from the group of builders, in particular at least one active substance from the group of citrates, zeolites, silicates, and carbonates, preferably from the group of citrates and zeolites.
57. The method according to one of points 37 to 56, wherein the shaped body contains a polymeric active washing or active cleaning ingredient, preferably a polymeric active washing or active cleaning ingredient from the group of celluloses and cellulose derivatives and anionic or nonionic aromatic polyesters, preferably from the group of celluloses, microcrystalline celluloses and carboxymethyl celluloses and anionic or nonionic aromatic polyesters.
58. The method according to one of points 37 to 57, wherein the solid gel and the shaped body are adhesively bonded to one another.
Number | Date | Country | Kind |
---|---|---|---|
10 2022 203 705.7 | Apr 2022 | DE | national |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2023/051060 | 1/18/2023 | WO |