[0001] The present invention relates to the use of an ethoxylated aliphatic alcohol containing
at least 25 ethylene oxide groups to improve dissolution and/or dispersion in the
wash liquor of a particulate detergent composition. The invention is of especial applicability
to particulate detergent compositions, containing no, or low levels of, phosphate
builder and to compositions of high bulk density.
[0002] In recent years there has been a trend to reduce or eliminate phosphate builders
in particulate detergent compositions. The replacement of sodium tripolyphosphate
as a builder in detergent powders by a crystalline aluminosilicate (zeolite), has
led to a number of difficulties with the structure and physical properties of powders.
One such problem that has been encountered, is the tendency of zeolite-built powders
to dispense less well in automatic washing machines than do their phosphate-built
counter-parts; a higher proportion of the powder dosed into the washing machine is
left in the dispenser, in the washing process leading to product wastage and clogging.
The problem is especially marked at low water inlet temperatures.
[0003] The tendency towards poor dispensing has been exacerbated by the recent trend in
the detergent industry towards higher bulk density powders. Detergent powders of high
bulk densities from 600 to 1100 kg/m
3, preferably from 700 to 1100 kg/m
3, are attractive to the customer. Because the capillary diameter of the high bulk
density powder is smaller than in low bulk density powders, the water penetration
into the particle is slower. As a consequence, when the powder is wetted by water
flowing through the dispenser the detergent particles may stick together resulting
in considerable residues of wetted and adhering powder left behind in the drawer.
Similar problems may be encountered when applying a detergent dosing device as described
in EP-A-253,419, for indrum dosing of high density detergent powder.
[0004] Detergent powders typically comprise anionic and/or nonionic surfactants. Nonionic
surfactants are particularly effective in removing hydrophobic soils such as hydrocarbon
oils, complex fats and other long-chain unsaturated and saturated glycerides. However,
when detergent powders containing nonionic surfactants come into contact with aqueous
solutions, the nonionic surfactant may form a viscous phase which may impede dissolution.
Nonionic surfactants having a low degree of ethoxylation, generally employed because
of their oily soil detergency, are especially problematic in this respect.
[0005] It has now surprisingly been found that the problem of poor dissolution and/or dispersion
in the wash liquor of such a powder can be overcome by incorporating in the powder
a relatively small amount of an ethoxylated aliphatic alcohol containing at least
25 ethylene oxide groups.
[0006] Accordingly, the present invention provides the use set out in Claim 1.
[0007] Suitably the granular detergent composition has a bulk density from 600 to 1100 kg/m
3, preferably from 700 to 1100 kg/m
3. Various postdosed ingredients, such as sodium carbonate, bleach material and foam
depressing agent, may be added to the composition as desired. The composition may
be prepared by spray-drying optionally followed by mixing or by dry-mixing/agglomeration.
For obtaining high bulk densities, the composition is preferably prepared by dry-mixing/agglomeration.
[0008] As essential ingredients, the composition contains surfactant system, builder material
and a dissolution aid. It is preferred that the dissolution aid is present in the
composition of the invention as a separate granular component. Preferably the dissolution
aid is substantially pure ethoxylated aliphatic alcohol containing at least 25 ethylene
oxide groups.
[0009] Preferably, the dissolution aid contains at least 50 ethylene oxide groups, more
preferably at least 80 ethylene oxide groups.
[0010] The dissolution aid is suitably present at a level of from 0.01 to 1% by weight,
preferably from 0.05 to 0.5% by weight based on the composition.
[0011] The surfactant system present in the detergent composition suitably contains alkoxylated
nonionic surfactants having an average degree of alkoxylation of at most 11. Suitable
nonionic surfactants include condensation products of ethylene oxide with an aliphatic
alcohol having from 8 to 15 carbon atoms and an average degree of ethoxylation from
2 to 10.
[0012] A preferred surfactant system comprises a mixture of two C
8-15 nonionic surfactants having an average degree of ethoxylation respectively of 2 to
5, preferably 2.5 to 4 and 6.5 to 10, preferably 6.5 to 8 which, suitably, are present
in a weight ratio of 1 to 25:5. In order to obtain particularly beneficial dissolution
properties it is especially preferred that the proportion of nonionic surfactant having
a branched aliphatic alcohol is in the range from 10 to 60% by weight for example
about 55% by weight based on the total amount of nonionic surfactant in the composition.
[0013] Nonionic detergent-active compounds and the dissolution aid together are suitably
present in the compositions in a total amount of from 2 to 50% by weight, preferably
from 5 to 30% by weight.
[0014] In addition to the nonionic surfactants mentioned above, other detergent-active materials
may be present in the compositions. These additional detergent-active materials may
be anionic (soap or non-soap), cationic, zwitterionic, amphoteric surfactants, or
any combination of these surfactants.
[0015] Anionic detergent-active compounds may be present in an amount of from 0 to 40% by
weight, preferably from 0 to 20% by weight. It is preferred that the ratio of nonionic
surfactant and dissolution aid to anionic surfactant is within the range of 1:2 to
9:1.
[0016] Synthetic anionic surfactants are well known to those skilled in the art. Examples
include alkylbenzene sulphonates, particularly sodium linear alkylbenzene sulphonates
having an alkyl chain length of C
8-C
15; primary and secondary alkyl sulphates, particularly sodium C
12-C
15 primary alkyl sulphates, olefin sulphonates; alkane sulphonates; dialkyl sulphosuccinate;
and fatty acid ester sulphonates.
[0017] It may also be desirable to include one or more soaps of fatty acids. These are preferably
sodium soaps derived from naturally occurring fatty acids, for example the fatty acids
from coconut oil, beef tallow, sunflower or hardened rapeseed oil.
[0018] The total amount of surfactant in the composition is suitably from 5 to 50% by weight.
Of particular interest are high-performance compositions containing relatively high
levels of surfactant, preferably from 10 to 50% by weight and more preferably from
15 to 50% by weight.
[0019] Especially preferred compositions include surfactant systems consisting especially
of nonionic surfactant as described above in combination with linear alkylbenzene
sulphonate (LAS) or primary alcohol sulphate (PAS) or both.
[0020] Surfactant systems of especial interest consist essentially of
(i) from 40 to 100% by weight of ethoxylated nonionic surfactant, and
(ii) from 0 to 60% by weight of linear alkylbenzene sulphonate or primary C8-C18 alcohol sulphate.
[0021] The detergent powders contain one or more detergency builders, suitably in an amount
from 5 to 80% by weight, preferably from 20 to 60% by weight. The invention is especially
applicable to compositions containing alkali metal aluminosilicates as builders. Alkali
metal (preferably sodium) aluminosilicates may generally be incorporated in an amount
from 5 to 60% by weight (anhydrous basis) of the composition, preferably from 25 to
55% by weight, and suitably, in a heavy duty detergent composition, from 25 to 46%
by weight.
[0022] The alkali metal aluminosilicate may be either crystalline or amorphous or mixtures
thereof, having the general formula:
0.8-1.5 Na
2O. Al
2O
3. 0.8-6 SiO
2
[0023] These materials contain some bound water and are required to have a calcium ion exchange
capacity of at least 50 mg CaO/g. The preferred sodium aluminosilicates contain 1.5-3.5
SiO
2 units (in the formula above).
[0024] Suitable crystalline sodium aluminosilicate ion-exchange detergency builders are
described, for example, in GB 1,429,143 (Procter & Gamble). The preferred sodium aluminosilicates
of this type are the well-known commercially available zeolite A and X, and mixtures
thereof.
[0025] The zeolite may be the commercially available zeolite 4A now widely used in laundry
detergent powders. Alternatively, the zeolite builder incorporated in the composition
is maximum aluminium zeolite P (zeolite MAP) as described and claimed in EP-A-384,070
(Unilever). Zeolite MAP is defined as an alkali metal aluminosilicate of the zeolite
P type having a silicon to aluminium ratio not exceeding 1.33, preferably within the
range of from 0.90 to 1.33, and more preferably within the range of from 0.90 to 1.20.
The calcium binding capacity of zeolite MAP is generally at least 150 mg CaO per g
of anhydrous material.
[0026] Other builders may also be included in the detergent composition if necessary or
desired.
[0027] Inorganic builders that may be present include sodium carbonate, if desired in combination
with a crystallisation seed for calcium carbonate, as disclosed in GB 1,437,950 (Unilever).
Organic builders that may be present include polycarboxylate polymers such as polyacrylates,
acrylic/maleic copolymers, and acrylic phosphonates; monomeric polycarboxylates such
as citrates, gluconates, oxydisuccinates, glycerol mono-, di-and trisuccinates, carboxymethyloxysuccinates,
hydroxyethyliminodiacetates, alkyl- and alkenyl-malonates and succinates; and sulphonated
fatty acid salts. This list is not intended to be exhaustive.
Builders, both inorganic and organic, are preferably present in alkali metal salt,
especially sodium salt, form.
[0028] Especially preferred supplementary builders are polycarboxylate polymers, more especially
polyacrylates and acrylic/maleic copolymers, suitably used in amounts of from 0.5
to 15% by weight, especially from 1 to 10% by weight; and monomeric polycarboxylates,
more especially citric acid and its salts, suitably used in amounts of from 3 to 20%
by weight, more preferably from 5 to 15% by weight.
[0029] The composition may contain alkali metal, preferably sodium, carbonate, to increase
detergency and to ease processing. Sodium carbonate may generally be present in amounts
ranging from 1 to 60%by weight, preferably from 2 to 40% by weight, and most preferably
from 2 to 13% by weight. However, compositions free of alkali metal carbonate may
also be used.
[0030] Preferred compositions preferably do not contain more than 5% by weight of inorganic
phosphate builders, and are desirably substantially free of phosphate builders.
[0031] Suitable fully formulated laundry detergent compositions may additionally contain
any suitable ingredients normally employed in detergent compositions, for example,
inorganic salts such as sodium silicate or sodium sulphate; organic salts such as
sodium citrate; antiredeposition aids such as cellulose derivatives and acrylate or
acrylate/maleate polymers; fluorescers; bleaches, bleach precursors and bleach stabilizers;
proteolytic and lipolytic enzymes; dyes; coloured speckles; perfumes; foam controllers;
fabric softening compounds.
[0032] The particulate detergent compositions may in principle be prepared by any of the
available tower (spray-drying), non-tower (granulation) or combination processes.
[0033] Of especial interest are compositions of high bulk density - at least 600 g/l, preferably
at least 700 g/l and most preferably at least 800 g/l - which may be prepared by processes
involving granulation and/or densification in a high-speed mixer/granulator.
[0034] One suitable method comprises spray-drying a slurry of compatible heat-insensitive
ingredients, including the zeolite MAP, any other builders, and at least part of the
detergent-active compounds; densifying the resulting base powder in a mixer/granulator;
and then spraying on or post-dosing those ingredients unsuitable for processing via
the slurry (for example bleaches and enzymes).
[0035] In another method, the spray-drying step can be omitted altogether, a high bulk density
base powder being prepared directly from its constituent raw materials, by mixing
and granulating in a high speed mixer/granulator, and then post-dosing bleach and
other ingredients as in the spray-drying/post-tower densification route.
[0036] The high-speed mixer/granulator, also known as a high-speed mixer/densifier, may
be a batch machine such as the Fukae (Trade Mark)FS, or a continuous machine such
as the Lodige (Trade Mark) Recycler CB30.
Processes using high-speed mixer/granulators are disclosed, for example, in EP-A-340,013,
EP-A-367,339, EP-A-390,251 and EP-A-420,317 (Unilever).
[0037] The dissolution aid may be included in the base powder but is preferably admixed
with the finished base powder. Nonionic surfactants having a lower degree of alkoxylation,
particularly those containing on average less than 11 ethylene oxide groups, may be
included in the base powder, post added, or both.
[0038] As mentioned above, use of the dissolution aid in detergent composition has been
found to improve dissolution properties in a washing process in a washing machine.
Additional benefits associated with use of the dissolution aid were found to be reduced
redeposition characteristics during the washing cycle and improved bleeding behaviour
upon storage.
EXAMPLES
[0039] The following non-limiting Examples illustrate the invention. Examples identified
by numbers are in accordance with the invention, those identified by letter are comparative.
Parts and percentages are by weight unless otherwise stated.
Examples 1-9, Comparative Example A
[0040] A particulate detergent composition having a bulk density of 830 kg/m
3 was prepared by spray-drying an aqueous slurry to form a base powder (including nonionic
surfactants as specified), densifying the base powder in a continuous Lodige high-speed
mixer/granulator, spraying-on further nonionic surfactants as specified, and then
admixing the remaining ingredients.
[0041] The general formulation, in weight percent, is shown in Table 1.
TABLE 1
| Base powder |
|
| Linear alkylbenzene sulphonate |
8.60 |
| *Nonionic surfactant (i) |
1.92 |
| Zeolite 4A1 |
23.61 |
| Acrylic/maleic copolymer2 |
3.51 |
| Sodium carbonate |
7.49 |
| Minor ingredients3 |
1.35 |
| Moisture |
9.02 |
| |
55.50 |
| |
| Sprayed-on |
|
| **Nonionic surfactant (ii) |
4.68 |
| |
| Admixed |
|
| Zeolite 4A |
5.00 |
| Sodium Carbonate |
4.30 |
| Granular sodium silicate |
3.75 |
| TAED4 |
7.75 |
| Sodium perborate monohydrate |
15.00 |
| EDTMP5 |
0.37 |
| Antifoam granules6 |
2.00 |
| Enzyme granules |
1.00 |
| Perfume |
0.65 |
| |
100.00 |
wherein:
* nonionic ethoxylated alcohol, Synperonic A7 (containing 7 EO groups), ex ICI |
| ** nonionic ethoxylated alcohol, 1:1 mixture of Synperionic A3 and A7 (containing
3 and 7 EO groups), ex ICI |
| 1: Wessalith (Trade Mark) P powder ex Degussa: percentage is for anhydrous material,
the water of hydration being included in the figure for total moisture. |
| 2: Sokalan (Trade Mark) CP5, ex BASF. |
| 3: Fluorescer, sodium carboxymethylcellulose, salts, etc. |
| 4: Tetraacetylethylenediamine, as 83%wt granules. |
| 5: Ethylenediaminetetramethylenephosphonic acid, calcium salt: Dequest (Trade Mark)
2047 ex Monsanto (34%wt active). |
| 6: Antifoam granules in accordance with EP-B-266,863 (Unilever). |
[0042] To the thus prepared particulate detergent composition varying -minor- amounts of
several types of ethoxylated alcohol containing at least 25 ethylene oxide (EO) groups,
were postdosed, as specified in Table 2. Suitable commercially available nonionic
materials containing at least 25 EO groups include the LUTENSOL AT [Trade Mark] series
ex BASF and the BRIJ [Trade Mark] series ex ICI.
As can be seen, the type of the postdosed nonionic materials is indicated in this
Table by number of EO-groups present therein.
TABLE 2
| Example |
Postdosed high EO |
nonionic material |
| |
amount (parts) |
type |
| A |
0.000 |
-- |
| 1 |
0.50 |
25 EO |
| 2 |
0.125 |
25 EO |
| 3 |
0.50 |
50 EO |
| 4 |
0.125 |
50 EO |
| 5 (Comp.) |
1.00 |
80 EO |
| 6 |
0.50 |
80 EO |
| 7 |
0.25 |
80 EO |
| 8 |
0.125 |
80 EO |
| 9 |
0.0625 |
80 EO |
[0043] The delivery characteristics of the thus obtained powders were tested using a model
system which simulates the delivery of a powder in an automatic washing machine.
[0044] For this test a cylindrical vessel having a diameter of 4 cm and a height of 7 cm,
made of 600 micron pore size stainless steel mesh, and having a top closure made of
teflon and a bottom closure made of the above type of mesh, was used. In this top
closure, a 30 cm metal rod was inserted to act as a handle, and this handle was attached
in an agitator arm positioned above 1 litre water present in a container and having
a temperature of 20 C. By means of this agitator apparatus the cylindrical vessel
held at 45 degrees, could be rotated through a circle with a 10 cm radius during 2
seconds. Subsequently the vessel could be allowed to rest during 2 seconds before
the next rotation-rest cycle started.
[0045] A 50 grams powder sample was introduced in the cylindrical vessel. This vessel was
then closed and attached to the agitator arm which was subsequently moved down to
a position wherein the top of the cylindrical vessel was just below the water surface.
After a ten second delay, the rotation was started, and the apparatus then allowed
to operate for 15 rotation-rest cycles.
Subsequently, the cylindrical vessel and handle were removed from the water and the
vessel was detached. Surface water was carefully poured off, and any powder residues
transferred to a preweighed container. The container was then dried at 100°C for 24
hours, and the weight of dried residue as a percentage of the initial powder weight
calculated. The results are shown in Table 3.
TABLE 3
| Example |
Postdosed high EO nonionic material |
Residue |
| |
amount (parts) |
type |
(wt%) |
| A |
0.000 |
-- |
34 |
| 1 |
0.50 |
25 EO |
22 |
| 2 |
0.125 |
25 EO |
20 |
| 3 |
0.50 |
50 EO |
24 |
| 4 |
0.125 |
50 EO |
18 |
| 5 (Comp.) |
1.00 |
80 EO |
25 |
| 6 |
0.50 |
80 EO |
22 |
| 7 |
0.25 |
80 EO |
16 |
| 8 |
0.125 |
80 EO |
14 |
| 9 |
0.0625 |
80 EO |
21 |
[0046] It can be seen from Table 3 that the largest reduction of the powder residue as compared
to the residue found in example A, could be obtained when applying a detergent powder
composition comprising a minor amount of postdosed ethoxylated alcohol containing
80 ethylene oxide groups.
Examples 10,11, Comparative Example B
[0047] A particulate detergent composition was prepared in a very similar way and having
almost the same formulation as in the above-mentioned Example A, the only difference
being that in the present Examples the sprayed-on nonionic surfactant material fully
consists of Synperionic A3 (containing 3 EO groups) ex ICI.
[0048] To this detergent powder, varying amounts of ethoxylated alcohol containing 80 EO
groups were postdosed. The delivery characteristics of the thus obtained powders were
tested using the above-described model system and testing process. The results obtained
are shown in Table 4.
TABLE 4
| Example |
Postdosed high EO nonionic material |
Residue |
| |
amount (parts) |
type |
(wt%) |
| B |
0.000 |
-- |
68 |
| 10 |
0.50 |
80 EO |
55 |
| 11 |
0.125 |
80 EO |
42 |
[0049] It can be seen that the dissolution properties of the detergent powder of Example
B are inferior as compared to the powder cf Example A, and that also in this case
an improvement of the delivery characteristics could be obtained by post-dosing minor
quantities of ethoxylated alcohol containing 80 EO groups.
Comparative Examples C,D
[0050] To the detergent powder of Example A, varying -minor- amounts of polyethylene glycol
having a molecular weight of 4000 (PEG 4000) were postdosed.
The delivery characteristics of the thus obtained powders were tested using the above-described
model system and testing process. The results obtained are shown in Table 5.
TABLE 5
| Example |
Postdosed PEG 4000 |
Residue |
| |
amount (parts) |
(wt%) |
| A |
0.000 |
34 |
| B |
0.50 |
33 |
| C |
0.25 |
35 |
[0051] It can be seen that no improvement of the delivery characteristics of the detergent
powder of Example A could be obtained by post-dosing the above-indicated minor amounts
of PEG 4000.
Example 12 and Comparative Example E
[0052] A detergent composition having a bulk density of about 900 g/l was prepared by a
mixing/granulation process to produce a base powder to which further components were
post-dosed into the base powder as listed below.
| Base Powder |
|
| Sodium primary alkyl sulphate (PAS) |
5.81 |
| Zeolite MAP |
36.04 |
| Sodium carbonate |
0.96 |
| a*Synperonic A3 ex ICI |
7.15 |
| a*Synperonic A7 ex ICI |
5.81 |
| Stearic acid |
2.04 |
| b*Tallow 80EO |
0.20 |
| Sodium carboxymethyl cellulose |
0.89 |
| Moisture |
4.98 |
| |
63.88 |
| a About 55% branched. |
| b Ethoxylated tallow alcohol having an average degree of ethoxylation of 80. |
[0053] The nonionic materials (*) were mixed and then sprayed onto an adjunct comprising
PAS, carbonate and part of the zeolite, and sodium carboxymethyl cellulose and stearic
acid in a Lodige CB30 "Recycler" mixer. The stearic acid was neutralised by addition
of base. The mixture was then layered with the remaining zeolite and passed to a Lodige
KM300 "Ploughshare" mixer and then a fluid bed as described in EP-A-367 339 (Unilever)
to produce the base powder.
[0054] The following components were then admixed to the base powder (63.88 parts).
| Fluorescer |
3.00 |
| Sodium silicate |
2.90 |
| c TAED |
4.75 |
| d Manganete catalyst |
2.40 |
| Sodium Percarbonate |
20.50 |
| e DEQUEST 2047 ex Monsanto |
0.37 |
| Enzyme |
1.75 |
| Perfume |
0.45 |
| c tetraacetyl ethylene diamine |
| d as described in EP 458 397 (Unilever) |
| e sequestrant |
[0055] A comparative composition E was prepared by the same process and to the same composition
as Example 12 save that the Tallow 80EO in the base was replaced by 0.20 parts SYNPERONIC
A3.
[0056] The delivery characterisatics of the two powders were tested using the model system
described in Examples 1 to 9. The results are shown in Table 6.
TABLE 6
| Composition |
Residue (wt%) |
| 12 |
45 |
| E |
60 |
[0057] These results demonstrate that compositions containing a dissolution aid have significantly
superior delivery characteristics when compared to a similar composition which does
not contain a dissolution aid.
Detergency
[0058] The detergencies of the powders of Examples A,D (comparative) and 7 (according to
the invention) were compared by means of a washing machine test. The machine used
was a Siemens Siwamat (Trade Mark) Plus 3700 front-loading automatic washer.
[0059] 3 kg soiled loads containing white cotton interlock test cloth monitors (which monitors
have been pre-washed) were washed at 40°C using the half load main wash programme.
The powder samples (104 g dose) predissolved in 250 ml water were introduced via the
machine's dispenser. Detergency results (reflectance loss after 10 washes at 460 nm
of the test cloth monitors) were as follows:
| Composition of |
Reflectance loss after 10 washes |
| Example A |
2.1 |
| Example D |
1.9 |
| Example 7 |
1.4 |
[0060] These results demonstrate the additional benefit associated with the invention, of
reduced redeposition.
Bleeding
[0061] The bleeding characteristics of the powders of Examples A,D (comparative) and 7 (according
to the invention) were compared. To that end, Standard VC2 cardboard packs (having
a volume of 1.5 litre) were filled up to 80% of their total volume with samples of
the above mentioned respective powders. Subsequently the filled cardboard packs were
stored at a temperature of 37°C and a relative humidity of 70%, for two months. The
part of the total cardboard interior surface which was stained and had obtained a
darker colour due to nonionic migration (bleeding) during this two months storage
period, was recorded as a percentage, as is shown below:
| Composition of |
stained part of cardboard pack interior surface (in %) |
| Example A |
18 |
| Example D |
19 |
| Example 7 |
8 |
[0062] It can be derived from these results that a further benefit associated with the invention,
is significantly improved (i.e. reduced) bleeding behaviour of detergent compositions.
1. Verwendung eines ethoxylierten aliphatischen Alkohols mit wenigstens 25 Ethylenoxidgruppen
als Auflösungshilfe zur Verbesserung der Auflösung und/oder Dispersion einer partikulären
Reinigungsmittelzusammensetzung in der Waschflüssigkeit, wobei die partikuläre Reinigungsmittelzusammensetzung
eine Schüttdichte von wenigstens 600 g/l hat und ein Tensidsystem mit einem oder mehreren
nichtionischen Tensid(en), einem oder mehreren anionischen Tensid(en) und wenigstens
einem Aufbaustoff umfasst, wobei das Tensidsystem in einer Menge zwischen 10 und 50
Gew.-% der Zusammensetzung vorliegt, wobei die Auflösungshilfe in einer Menge zwischen
0,05 und 1 Gew.-%, berechnet auf die Zusammensetzung, vorliegt und das Gewichtsverhältnis
zwischen nichtionischem Tensid und Auflösungshilfe größer als 10:1 ist, vorausgesetzt,
die partikuläre Reinigungsmittelzusammensetzung umfasst kein Alkylglycosid der allgemeinen
Formel R-O-(G)x, wobei R eine gerade Primärkette oder ein verzweigter, aliphatischer 2-Methyl-Rest
mit 8 bis 22 Kohlenstoffatomen ist, G eine Glykosekette mit 5 bis 6 Kohlenstoffatomen
ist und der Oligomerisierungsgrad x zwischen 1 und 10 liegt.
2. Verwendung nach Anspruch 1, wobei die Auflösungshilfe wenigstens 50 Ethylenoxidgruppen
enthält.
3. Verwendung nach einem der vorherigen Ansprüche, wobei das Tensidsystem zwei nichtionische
Tenside umfasst, die Kondensationsprodukte von Ethylenoxid mit einem aliphatischen
C8-C15 Alkohol sind, mit jeweils einem durchschnittlichen Ethoxylierungsgrad von 2 bis 5
und von 6,5 bis 10.
4. Verwendung nach einem der vorherigen Ansprüche, wobei die Reinigungsmittelzusammensetzung
zwischen 0,05 und 0,5 Gew.-% der Auflösungshilfe, berechnet auf die Zusammensetzung,
umfasst.
5. Verwendung nach einem der vorherigen Ansprüche, wobei das Tensidsystem im Wesentlichen
Folgendes umfasst:
(i) 40 bis 100 Gew.-% des Tensidsystems an ethoxyliertem, nichtionischem Tensid, und
(ii) 0 bis 60 Gew.-% an linearem Alkylbenzolsulfonat oder C8-C18 Primäralkoholsulfat.
6. Verwendung nach einem der vorherigen Ansprüche, wobei die Reinigungsmittelzusammensetzung
im Wesentlichen frei von Phosphaten ist.