| (19) |
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(11) |
EP 1 751 265 B1 |
| (12) |
EUROPEAN PATENT SPECIFICATION |
| (45) |
Mention of the grant of the patent: |
|
18.02.2009 Bulletin 2009/08 |
| (22) |
Date of filing: 28.05.2004 |
|
| (51) |
International Patent Classification (IPC):
|
| (86) |
International application number: |
|
PCT/EP2004/050963 |
| (87) |
International publication number: |
|
WO 2005/118767 (15.12.2005 Gazette 2005/50) |
|
| (54) |
PASTE-LIKE CONCENTRATE SUITABLE TO FORM STABLE (NON SEPERATING) ALKALINE CLEANING
AND DETERGENT SOLUTIONS
GEEIGNETES PASTENFÖRMIGES KONZENTRAT ZUR HERSTELLUNG VON STABILEN, SICH NICHT ENTMISCHENDEN
ALKALISCHEN REINIGUNGS- UND WASCHMITTELLÖSUNGEN
CONCENTRE EN PATE POUVANT FORMER DES SOLUTIONS DETERGENTES ET DE LAVAGE, ALCALINES
ET STABLES (PAS DE SEPARATION)
|
| (84) |
Designated Contracting States: |
|
AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PL PT RO SE SI SK TR
|
| (43) |
Date of publication of application: |
|
14.02.2007 Bulletin 2007/07 |
| (73) |
Proprietor: ECOLAB INC. |
|
St. Paul MN 55102-2233 (US) |
|
| (72) |
Inventor: |
|
- SHAMAYELI, Khalil
40225 Düsseldorf (DE)
|
| (74) |
Representative: Polypatent |
|
Postfach 11 07 51482 Overath 51482 Overath (DE) |
| (56) |
References cited: :
WO-A-95/29282 US-B1- 6 329 333
|
US-B1- 6 187 739
|
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| |
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| |
|
| Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
|
[0001] The present invention refers to a paste-like thixotropic detergent or cleaning concentrate
which is able to form a stable (non separating) alkaline parent lye for use as cleansing
agent or detergent, preferably for the machine cleaning of textiles, a parent lye
containing said concentrate and to a method for washing textiles using said concentrate
in diluted form as a parent lye.
[0002] In industrial laundries nowadays the single washing machines are centrally supplied
with the solution of a detergent or cleaning agent, the so called parent lye, to maximize
the capacity of the laundry and the machinery and to optimise the course of the process.
Generally, the central supply proceeds using a parent lye which contains 5 to 15 wt.-%
of the cleaning agent or detergent and which is distributed from a reservoir to the
single washing machines, in most cases without further diluting. Accordingly, a cleaning
agent or detergent suitable for use in industrial laundries must be capable to form
a stable (non separating) alkaline cleaning or detergent solution to ensure a constantly
excellent cleaning or washing performance.
[0003] Cleaning and detergent compositions formulated in particulate form are well known
to form stable (non separating) alkaline cleaning or detergent solutions. However,
generally large amounts of parent lye are prepared and stored in a reservoir to be
subsequently distributed to the single washing machines. This means a corresponding
amount of solid detergent or cleaning agent, respectively, has to be dissolved to
form the parent lye, which takes a lot of time and effort.
[0004] Moreover, large amounts of solid, especially particulate, detergents show problems
with respect to homogeneity if they are stored before being used to form the parent
lye and not consumed at one go. This is because the single components in the detergent
exhibit different volumes and densities which results in the active components migrating
to the bottom of the reservoir upon storage. Accordingly, if the parent lyes are prepared
using a detergent powder stored in a reservoir, this migrating process may take place
therein while consuming the parent lye. The following parent lyes may then exhibit
a more and more decreased cleaning performance due to the more and more decreasing
content of active agent in the solid detergent. The parent lye formed from the detergent
on the bottom of the reservoir, where the active ingredient accumulated, then again
exhibits excellent cleaning performance.
[0005] Accordingly there is a need to provide stable homogenous paste-like detergent or
cleaning concentrates which are easily batched and dissolved to form a stable parent
lye and exhibit excellent cleaning properties, especially in laundry application.
[0006] US 6187739 discloses paste-form washing and cleaning agents comprising nonionic surfactants
selected from ethoxylated and optionally propoxylated alcohols.
[0007] Yet, the actually known paste-like detergent and cleaning concentrates do not exhibit
this combination of properties. In particular, a large amount of a non-ionic surfactant
blend is required as liquid component to provide those concentrates with a viscid
to highly viscous consistency. Accordingly, when forming a parent lye, those concentrates
generally show poor solubility and do not form stable (non separating) solutions.
Even the use of emulsifiers in large amounts which increases costs and complicates
the disposal of the resulting waste water, did not provide a homogenous, stable parent
lye. This results in the requirement of vigorous stirring in the vessel during storage
of the parent lye to ensure a more or less homogenous distribution of the detergent
concentrate. In most cases not even vigorous stirring provides a homogenous parent
lye.
[0008] Moreover, nowadays it is very important to provide cleaning agents and detergents
which do not only exhibit excellent cleaning properties but which are as well accessible
to the common waste water purification systems. If the waste water and/or a part of
the detergent solution accumulating after the washing process has been carried out
is treated by membrane filtration, many non-ionic surfactants cause considerable problems.
Depending on the choice of non-ionic surfactant, this may even lead to blocking-up
of the membranes. This point is to be deemed particularly critical in membrane filtration
processes in the course of which at least one reverse osmosis step occurs.
[0009] Therefore, the object of the present invention is to provide a cleaning or detergent
concentrate which on one hand forms a stable paste as such and on the other hand also
forms a stable (non separating) alkaline cleaning or detergent solution when dissolved
in water. Additionally, it should be possible to purify waste water resulting from
the cleaning or washing process and containing said concentrate on common membrane
filtration units, especially ones using one or more reverse osmosis steps, without
blocking the membrane or causing other damages.
[0010] Surprisingly, the underlying problem is solved by providing a paste-like, thixotropic,
alkaline detergent or cleaning concentrate comprising based on the whole concentrate
- a) 0,5 to 15 wt% of at least one first component selected from one or more compounds
represented by the general formula (I),
R1-(OC2H4)n-(OC3H6)m-OH (I)
wherein R1 represents an unbranched or branched alkyl or alkenyl group having 4 to 8, preferably
5 to 7, carbon atoms, and wherein the sum of the average degree of ethoxylation n
and propoxylation m ranges from 1 to 9, preferably from 3 to 7, with one of n and
m optionally being 0, and
- b) 5 to 90 wt% of at least one second component selected from one or more compounds
represented by the general formula (II),
R2-(OC2H4)0-(OC3H6)p-OH (II)
wherein R2 represents an unbranched or branched alkyl or alkenyl group having 9 to 22, preferably
10 to 16, carbon atoms, and wherein the sum of the average degree of ethoxylation
o and propoxylation p ranges from 1 to 9, preferably from 3 to 7, with one of o or
p optionally being 0,
- c) at least 1 wt% of at least one alkanolamine the cleaning concentrate exhibiting
at 25°C a viscosity of from 80 000 mPas to 250 000 mPas at 5 revolutions per minute
and a viscosity of from 20 000 mPas to 80 000 mPas at 50 revolutions per minute, each
measured using a Brookfield rotational viscometer (spindle no. 7) under otherwise
identical conditions.
[0011] In this context thixotropic means that the concentrate exhibits such a structural
viscosity that it does not flow under the influence of gravity. However, on shear
the viscosity tremendously decreases which enables the concentrate to flow under the
influence of gravity. The dosing of thixotropic composition is then preferably performed
by shearing the concentrate to reduce viscosity at first and afterwards dosing and
transmitting the free-flow concentrate using for example a feed pump. The above mentioned
viscosity values refer to reading after a detection time of 3 minutes to take the
time dependency of the thixotropic effect into account. The decrease of viscosity
on shear is to a great extent reversible, i. e. after having stopped the shear the
concentrate will return to its original physical condition without separation.
[0012] It has to be taken into account that the viscosity may change while an equilibrium
adjusts within the concentrate after its preparation. Accordingly, viscosity values
measured during the manufacturing process or directly afterwards may falsify the result.
Thus, the viscosities are determined after the equilibrium is adjusted and the final
viscosity is reached. Storing for one month is generally sufficient to obtain reliable
values.
[0013] In a preferred embodiment a mixture of two or more compounds represented by general
formula II is used wherein R
2 is C10, C13 and/or C12-14, o is 3, 4 and/or 5 and p is 0 or 5. In these cases it
is especially preferred to use at least one compound represented by the general formula
I wherein R
1 is C6, n is 5 and m is 0.
[0014] The preferred amount of the compound(s) represented by the general formula (I) is
in the range of from 1 to 10 wt.-% and most preferred from 2 to 5 wt.-% based on the
whole concentrate.
[0015] The one or more compounds represented by the general formula (II) should be present
in an amount of from 5 to 90 wt.-%, preferably from 15 to 70 wt.-% and most preferred
from 20 to 50 wt.-% based on the whole concentrate.
[0016] The alkalinity may be achieved using any compound known in the state of the art which
when dissolved in water shows an alkaline reaction, like for example alkali hydroxides,
especially sodium or potassium hydroxide, ammoniumhydroxide, alkaline-earth hydroxides,
alkali carbonates, like soda or mixtures thereof. The preferred alkalinity generating
compound is represented by soda.
[0017] In a further preferred embodiment amorphous alkali silicate may be added as alkalinity
source. Sodium meta silicate with a ratio of Na
2O: SiO
2 in the range of 1 : 0,8 to 1 : 1,3, preferably 1 : 1 is especially appropriate.
[0018] Moreover, one or more phosphates, can be used instead of or in addition to the amorphous
alkali silicate. However, this should only be in case that the use of phosphates does
not cause harm because of a phosphate eliminating waste water purification step following
the cleaning or washing steps.
[0019] The phosphates are preferably selected from at least one of primary orthophosphates
represented by the general formula M
IH
2PO
4 or M
II(H
2PO
4)
2, secondary orthophosphates represented by the general formula M
I2HPO
4 or M
IIHPO
4 or tertiary orthophosphates represented by the general formula M
I3PO
4 or M
II3(PO
4)
2, as well as condensed phosphates derived therefrom, the so called meta phosphates
and poly phosphates, with M being a metal cation, M
I preferably being an alkali metal and M
II preferably being an alkaline-earth metal.
[0020] In one especially preferred embodiment the phosphate is a tripolyphosphate, preferably
sodium tripolyphosphate (Na
5P
3O
10).
[0021] The content of the alkalinity source is chosen such that the pH value of a use solution
containing the inventive concentrate should advantageously be in the range of from
9 to 13, preferably 10 to 12. Correspondingly, the total amount of the alkalinity
source preferably ranges from 25 to 70 wt.-%, more preferably from 30 to 60 wt-% and
most preferred from 50 to 58 wt.-%, based on the whole concentrate.
[0022] In preferred embodiments soda is used in amounts of from 15 to 60 wt.-%, preferably
25 to 55 wt.-%. The amount of amorphous alkali silicate, especially sodium meta silicate,
with the above mentioned Na
2O : SiO
2 ratio, preferably ranges from 10 to 20 wt.-%, and especially is 15 wt.-%. The phosphor
compound should be contained in an amount of at most 40 wt.-%, preferably in an amount
of 30 wt.-% or below, especially in a range of from 20 to 30 wt.-% based on the whole
concentrate.
[0023] It is also possible to further add an alkaline compound in form of a solid or an
aqueous solution when diluting the concentrate before use. However, it is most preferred
to not add further alkaline compound when preparing the use solution from the inventive
concentrate.
[0024] The inventive concentrate comprises at least 1 wt.-% based on the whole concentrate
of at least one alkanolamine. Preferably the sum of alkanolamines contained in the
concentrate is contained in an amount above 2 wt.-% and lies within the range of from
2 to 10 wt-%, and in particular from 3 to 5 wt.-%, based on the whole concentrate.
[0025] In a preferred embodiment at least one of the alkanolamines is represented by the
general formula (III),

wherein R
3 represents a hydroxyalkyl group having 1 to 6 carbon atoms, and wherein R
4 and R
5 independent from each other are identical with R
3 or represent hydrogen. The most suitable alkanolamines are represented by mono-,
di- or triethanolamine or mixtures thereof.
[0026] Those compounds may function as solutizer and thus improve the homogeneity of the
inventive concentrate when diluted to form the use solution, for example the parent
lye. Moreover, alkanolamines additionally represent an alkalinity source. As they
are liquid they help to avoid the use of water to provide the paste-like concentrate.
[0027] The paste-like concentrate comprises a solid phase which is dispersed in a liquid
phase as homogeneous as possible. The composition according to the present invention
forming the above concentrate enables the water content to be reduced to an amount
preferably of less than 3 wt.-%, more preferred less than 2 wt.-%, and most preferred
less than 1 wt.-% based on the whole concentrate. Said water content is meant to refer
to free water only. Additional water may be present in form of water of crystallisation
or water of constitution. To improve the physical stability as well as the chemical
stability the concentrate may additionally comprise dehydration agents, for example
in form of salts which bind water of crystallisation like anhydrous sodium acetate,
calcium sulfate, calcium chloride, sodium hydroxide, magnesium silicate or metal oxides
like CaO, MgO, P
4O
10 or Al
2O
3 or mixtures thereof.
[0028] The concentrate may additionally contain at least one alkyl polyglucoside having
from 8 to 14 carbon atoms in the alkyl group and from 1 to 5 glucose moieties. The
amount of the alkyl polyglucosid should be in the range of from 1 to 6 wt.%, preferably
from 1,5 to 3 wt.%.
[0029] Such compounds have a strongly hydrophobic alkyl moiety and a strongly hydrophilic
glucosid moiety and, accordingly, are very much appropriate to function as stabilizer
of the paste-like concentrate.
[0030] Additionally, the concentrate may comprise one or more further additives generally
used in cleaning agents or detergents like further soil release agents, cobuilders,
optical brighteners, dyes and fragrances, small quantities of neutral salts such as
sulfates and chlorides in the form of their sodium or potassium salts, provided that
these do not impair the positive properties. Other suitable additives to the product
may be enzymes, foam regulators, redeposition inhibitors, soil release agents, bleaching
agents from the class of per compounds, which are conventionally used together with
activators, active chlorine compounds as well as dyes, dye transfer inhibitors or
dye intensifiers and fragrances.
[0031] When preparing the inventive concentrate for practical reasons the liquid components
should be pre-mixed before the solid components and further ingredients are incorporated.
In case that the particulate solids are not fine enough to provide a homogeneous,
paste-like concentrate, they may be grinded one or more times before incorporation.
[0032] The inventive concentrate as described above can be used to prepare a stable parent
lye. Especially for usage in laundry applications the parent lye contains the inventive
concentrate in amounts of from 0,5 to 25 wt.-%, preferably 5 to 15 wt.-% based on
the detergent solution. Generally, the concentrate is dissolved in pure water to form
the parent lye. However, it is also possible to use water in which further additives,
like hydrophilic auxiliaries, are dissolved.
[0033] Although the main emphasis for the usage of the concentrate or the solution containing
the inventive concentrate, respectively, is on laundry detergents, it may as well
be applied as cleaning agent in warewashing, clean in place cleaners and sanitizers,
food an dairy formulations and other applications in which such alkaline cleaning
solutions may be applied. Preferably, the solution containing the concentrate is used
as parent lye for the industrial machine cleaning of textiles.
[0034] Moreover, the present invention provides a method for washing textiles comprising
one step in which a parent lye is prepared by diluting the concentrate according to
claims 1 to 12 such that the parent lye contains the concentrate in an amount of from
0,5 to 25 wt.-%, preferably of from 5 to 15 wt.-% based on the detergent solution.
[0035] The concentrate according to the invention is metered from a storage reservoir using
a metering equipment which is suitable to meter paste-like substances by influence
of shearing force. An appropriate equipment is described for example in
WO 95/09263. The required amount of the concentrate which then is free-flow is transmitted into
a further tank in which it is combined and dissolved with the appropriate amount of
solvent, which generally is water and may as well contain further additives or auxiliaries.
[0036] To accelerate the blending the mixture is advantageously agitated. The resulting
parent lye may than either directly be distributed to the single washing machines
or stored for usage in washing cycles to be performed later. Preferably, the parent
lye is shortly agitated after having been stored before it is distributed to the single
washing machines to guarantee a homogeneous distribution of the active agent in the
parent lye. When transmitted to the single washing machines the parent lye may be
further diluted depending on the desired detergent concentration.
[0037] It is also possible to pre-portion the paste-like concentrate, for example to wrap
it in foil bags. Since the concentrate essentially does not contain water the concentrate
may be wrapped in foils which are water soluble. In this case when preparing the parent
lye the required number of foil bags is poured into a tank, the appropriate amount
of water is added and after the foils are dissolved by the water the parent lye may
be obtained by stir ring.
[0038] A further advantage resulting from the composition of the concentrate is that it
allows the purification of the waste water which is accumulated during the cleaning
or washing process using common membrane filtration units without blocking them or
causing other damages. The membrane filtration may as well comprise at least one ultra
filtration and/or reverse osmosis step. Said purification processes succeed best with
a concentrate according to the invention which contains one or more phosphates.
Examples
[0039] The following table presents examples for appropriate compositions (C1 to C10) for
the inventive concentrate. The cited values refer to wt.-%, based on the whole concentrate.
The paste-like concentrates exhibited good storage stabilities, i. e. they did not
separate over a period of at least 12 months, provided stable parent lyes when being
stirred and optionally warmed up to 30-40°C, i. e. they essentially did not separate
over a period of at least 1 week, when diluted in water in an amount such that the
content of the concentrate was 10 wt.-% based on the parent lye. Generally, slightly
stirring was sufficient to obtain a stable parent lye. Moreover, the concentrate when
used as a 10 wt.-% aqueous parent lye exhibited excellent cleaning properties. Especially
when applying the concentrates in examples C3, C6, C7 and C9 the waste water accumulated
during the washing process could be purified by membrane filtration even using ultra
filtration steps.
Table 1: Composition of paste-like concentrates which are suitable to form stable
(non separating) alkaline cleaning and detergent solutions
| Component |
C1 |
C2 |
C3 |
C4 |
C5 |
C6 |
C7 |
C8 |
C9 |
C10 |
C11 |
| Fatty alcohol ethoxylate, C12-14, 5 EO |
|
10 |
|
|
|
|
|
|
|
|
|
| Fatty alcohol ethoxylate and -propoxylate, C12-14, 5 EO, 4 PO |
|
5 |
|
|
|
12 |
|
5 |
|
|
12 |
| Fatty alcohol ethoxylate, C13, 5 EO |
|
|
11 |
|
5 |
|
|
|
|
|
|
| Fatty alcohol ethoxylate, C13, 7 EO |
14,5 |
|
|
9,5 |
|
|
11 |
14,5 |
|
14 |
|
| Guerbet alcohol ethoxylate, C10, 5 EO |
5 |
5 |
10 |
5 |
5 |
12 |
6 |
5 |
12 |
5 |
12 |
| Fatty alcohol alkoxylate |
|
|
|
5 |
9,5 |
|
5 |
|
12 |
5 |
|
| |
| Isolauryl alcohol |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
| Fatty alcohol ethoxylate, C6, 5 EO |
1,5 |
2 |
1 |
1,5 |
2 |
1 |
2 |
1,5 |
1 |
2 |
|
| Foam regulating agents |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
|
| Anorganic surfactants |
2 |
2 |
2 |
2 |
2 |
1,5 |
1,5 |
1,5 |
1,5 |
1,5 |
3,5 |
| Triethanol amine |
3 |
4 |
3 |
3 |
2,5 |
3 |
5 |
3 |
3 |
3 |
3 |
| |
| Optical brightners |
1 |
1 |
1 |
1 |
1 |
|
|
1 |
1 |
1 |
|
| Organic builders |
10,15 |
10,15 |
10,15 |
10,15 |
10,15 |
7,2 |
7,2 |
10,55 |
7,2 |
10,55 |
7,2 |
| Graying inhibitors |
1 |
1 |
1 |
1 |
1 |
|
|
|
|
|
|
| Na-metasilicate |
15 |
15 |
15 |
15 |
|
|
|
|
|
|
|
| Na-carbonate |
40,85 |
38,85 |
18,2 |
40,85 |
35,85 |
27,3 |
26,3 |
51,95 |
26,3 |
31,95 |
30,3 |
| Tripolyphosphate- Na, Na5P3O10 |
|
|
26 |
|
|
30 |
30 |
|
30 |
|
28 |
| Ethylenediaminetetraacetic acid |
|
|
|
|
6 |
|
|
|
|
6 |
|
| Perborate monohydrate-Na |
|
|
|
|
14 |
|
|
|
|
14 |
|
| |
C1 |
C2 |
C3 |
C4 |
C5 |
C6 |
C7 |
C8 |
C9 |
C10 |
C11 |
| EO = -(OC2H4)-, PO = -(OC3H6)- |
1. Paste-like, thixotropic, alkaline detergent or cleaning concentrate comprising based
on the whole concentrate
a) 0,5 to 15 wt-% of at least one first component selected from one or more compounds
represented by the general formula (I),
R1-(OC2H4)n-(OC3H6)m-OH (I)
wherein R1 represents an unbranched or branched alkyl or alkenyl group having 4 to 8, preferably
5 to 7, carbon atoms, and wherein the sum of the average degree of ethoxylation n
and propoxylation m ranges from 1 to 9, preferably from 3 to 7, with one of n and
m optionally being 0, and
b) 5 to 90 wt-% of at least one second component selected from one or more compounds
represented by the general formula (II),
R2-(OC2H4)0-(OC3H6)p-OH (II)
wherein R2 represents an unbranched or branched alkyl or alkenyl group having 9 to 22, preferably
10 to 16, carbon atoms, and wherein the sum of the average degree of ethoxylation
o and propoxylation p ranges from 1 to 9, preferably from 3 to 7, with one of o or
p optionally being 0,
c) at least 1 wt.-% of at least one alkanolamine,
the cleaning concentrate exhibiting at 25°C a viscosity of from 80 000 mPas to 250
000 mPas at 5 revolutions per minute and a viscosity of from 20 000 mPas to 80 000
mPas at 50 revolutions per minute, each measured using a Brookfield rotational viscometer
(spindle no. 7) under otherwise identical conditions.
2. Concentrate according to claim 1, characterized in that component a) is contained in an amount of from 1 to 10 wt.-% based on the whole concentrate.
3. Concentrate according to claims 1 or 2, characterized in that component b) is contained in an amount of from 15 to 70 wt.-% based on the whole
concentrate.
4. Concentrate according to claim 1, characterized in that the sum of alkanolamines contained in the concentrate is in the range of from 2 to
10 wt.-%, preferably of from 3 to 5 wt.-% based on the whole concentrate.
5. Concentrate according to claims 1 or 4,
characterized in that at least one of the alkanolamines is represented by the general formula (III),

wherein R
3 represents a hydroxyalkyl group having 1 to 6 carbon atoms, and wherein R
4 and R
5 independent from each other are identical with R
3 or represent hydrogen.
6. Concentrate according to claims 1, 4 ,5 , characterized in that the concentrate comprises mono-, di- or triethanolamine or mixtures thereof.
7. Concentrate according to claims 1 to 6, characterized in that the concentrate comprises one or more phosphates.
8. Concentrate according to claim 7, characterized in that the phosphates are selected from at least one of primary orthophosphates represented
by the general formula MIH2PO4 or MII(H2PO4)2, secondary orthophosphates represented by the general formula MI2HPO4 or MIIHPO4 or tertiary orthophosphates represented by the general formula MI3PO4 or MII3(PO4)2, as well as condensed phosphates derived therefrom, the so called meta phosphates
and poly phosphates, with M being a metal cation , M' preferably being an alkali metal
and M" preferably being an alkaline-earth metal.
9. Concentrate according to claims 7 or 8, characterized in that the phosphate is a tripolyphosphate, preferably sodium tripolyphosphate (Na5P3O10).
10. Concentrate according to claims 7 to 9, characterized in that the one or more phosphates are contained in an amount of at most 40 wt.-%, preferably
in an amount of 30 wt.-% or below based on the whole concentrate.
11. Concentrate according to claims 1 to 10, characterized in that the concentrate additionally contains at least one alkyl polyglucosides having from
8 to 14 carbon atoms in the alkyl group and from 1 to 5 glucose moieties.
12. Concentrate according to claims 1 to 11, characterized in that the concentrate contains less than 3 wt.-%, preferably less than 2 wt.-% water based
on the whole concentrate.
13. Use of the concentrate according to claims 1 to 12for the preparation of a stable
parent lye.
14. Stable parent lye containing the concentrate according to claims 1 to 11 in an amount
of from 0,5 to 25 wt.-%, preferably from 5 to 15 wt.-% based on the whole parent lye.
15. Use of the parent lye according to claims 13 and 14 as a cleansing agent or a detergent,
preferably for the machine cleaning of textiles.
16. Method for washing textiles comprising one step in which a parent lye is prepared
by diluting the concentrate according to claims 1 to 12 such that the parent lye contains
the concentrate in an amount of from 0,5 to 25 wt.-%, preferably of from 5 to 15 wt.-%
based on the parent lye.
17. Method according to claim 16, characterized in that the waste water accumulated during the whole washing process or parts thereof is
purified using a membrane filtration unit.
18. Method according to claim 17, characterized in that the membrane filtration process comprises at least one ultrafiltration and/or reverse
osmosis step.
1. Pastenartiges thixotropes alkalisches Waschmittel- oder Reinigungskonzentrat, das
bezogen auf das gesamte Konzentrat
a) 0,5 bis 15 Gew.-% wenigstens einer ersten Komponente, die ausgewählt ist aus einer
oder mehreren Verbindungen, dargestellt durch die allgemeine Formel (I):
R1-(OC2H4)n-(OC3H6)m-OH (I)
worin R1 eine unverzweigte oder verzweigte Alkyl- oder AlkenylGruppe mit 4 bis 8, vorzugsweise
5 bis 7 Kohlenstoff-Atomen bedeutet und die Summe des mittleren Ethoxylierungsgrads
n und Propoxylierungsgrads m im Bereich von 1 bis 9, vorzugsweise 3 bis 7 liegt, wobei
eines der n und m gegebenenfalls 0 ist, und
b) 5 bis 90 Gew.-% wenigstens einer zweiten Komponente, die ausgewählt ist aus einer
oder mehreren Verbindungen, dargestellt durch die allgemeine Formel (II):
R2-(OC2H4)o-(OC3H6)p-OH (II)
worin R2 eine unverzweigte oder verzweigte Alkyl- oder AlkenylGruppe mit 9 bis 22, vorzugsweise
10 bis 16 Kohlenstoff-Atomen bedeutet und die Summe des mittleren Ethoxylierungsgrads
o und Propoxylierungsgrads p im Bereich von 1 bis 9, vorzugsweise 3 bis 7 liegt, wobei
eines der o oder p gegebenenfalls 0 ist,
c) wenigstens 1 Gew.-% wenigstens eines Alkanolamins umfasst,
wobei das Reinigungskonzentrat bei 25°C eine Viskosität von 80 000 mPas bis 250 000
mPas bei 5 Umdrehungen pro Minute und eine Viskosität von 20 000 mPas bis 80 000 mPas
bei 50 Umdrehungen pro Minute aufweist, jeweils gemessen unter Einsatz eines Brookfield-Rotationsviskosimeters
(Spindel Nr. 7) unter ansonsten gleichen Bedingungen.
2. Konzentrat nach Anspruch 1, dadurch gekennzeichnet, dass die Komponente a), bezogen auf das gesamte Konzentrat, in einer Menge von 1 bis 10
Gew.-% enthalten ist.
3. Konzentrat nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass die Komponente b), bezogen auf das gesamte Konzentrat, in einer Menge von 15 bis
70 Gew.-% enthalten ist.
4. Konzentrat nach Anspruch 1, dadurch gekennzeichnet, dass die Summe der im Konzentrat enthaltenen Alkanolamine, bezogen auf das gesamte Konzentrat,
im Bereich von 2 bis 10 Gew.-%, vorzugsweise 3 bis 5 Gew.-% liegt.
5. Konzentrat nach Anspruch 1 oder 4,
dadurch gekennzeichnet, dass wenigstens eines der Alkanolamine dargestellt wird durch die allgemeine Formel (III):

worin R
3 eine Hydroxyalkyl-Gruppe mit 1 bis 6 Kohlenstoff-Atomen bedeutet und R
4 und R
5 unabhängig voneinander identisch mit R
3 sind oder für Wasserstoff stehen.
6. Konzentrat nach den Ansprüchen 1, 4, 5, dadurch gekennzeichnet, dass das Konzentrat Mono-, Di- oder Triethanolamin oder Mischungen derselben umfasst.
7. Konzentrat nach den Ansprüchen 1 bis 6, dadurch gekennzeichnet, dass das Konzentrat ein oder mehrere Phosphate umfasst.
8. Konzentrat nach Anspruch 7, dadurch gekennzeichnet, dass die Phosphate ausgewählt sind aus wenigstens einem der primären Orthophosphate, dargestellt
durch die allgemeine Formel MIH2PO4 oder MII(H2PO4)2, sekundären Orthophosphate, dargestellt durch die allgemeine Formel MI2HPO4 oder MIIHPO4, oder tertiären Orthophosphate, dargestellt durch die allgemeine Formel MI3PO4 oder MII3(PO4)2, sowie der davon abgeleiteten kondensierten Phosphate, die sogenannten Metaphosphate
und Polyphosphate, wobei M ein Metallkation ist, MI vorzugsweise ein Alkalimetall und M" vorzugsweise ein Erdalkalimetall ist.
9. Konzentrat nach Anspruch 7 oder 8, dadurch gekennzeichnet, dass das Phosphat ein Tripolyphosphat, vorzugsweise Natriumtripolyphosphat (Na5P3O10) ist.
10. Konzentrat nach den Ansprüchen 7 bis 9, dadurch gekennzeichnet, dass das eine oder die mehreren Phosphate, bezogen auf das gesamte Konzentrat, in einer
Menge von höchstens 40 Gew.-%, vorzugsweise in einer Menge von 30 Gew.-% oder darunter
enthalten ist/sind.
11. Konzentrat nach den Ansprüchen 1 bis 10, dadurch gekennzeichnet, dass das Konzentrat zusätzlich wenigstens eines der Alkylpolyglucoside mit 8 bis 14 Kohlenstoff-Atomen
in der Alkyl-Gruppe und 1 bis 5 Glucose-Einheiten enthält.
12. Konzentrat nach den Ansprüchen 1 bis 11, dadurch gekennzeichnet, dass das Konzentrat, bezogen auf das gesamte Konzentrat, weniger als 3 Gew.-%, vorzugsweise
weniger als 2 Gew.-% Wasser enthält.
13. Verwendung des Konzentrats nach den Ansprüchen 1 bis 12 zur Herstellung einer stabilen
Stammlauge.
14. Stabile Stammlauge, enthaltend das Konzentrat nach den Ansprüchen 1 bis 11 in einer
Menge von 0,5 bis 25 Gew.-%, vorzugsweise 5 bis 15 Gew.-%, bezogen auf die gesamte
Stammlauge.
15. Verwendung der Stammlauge nach den Ansprüchen 13 und 14 als Reinigungsmittel oder
Waschmittel, vorzugsweise zur maschinellen Reinigung von Textilien.
16. Verfahren zum Waschen von Textilien, umfassend einen Schritt, bei dem eine Stammlauge
hergestellt wird durch Verdünnen des Konzentrats nach den Ansprüchen 1 bis 12, so
dass die Stammlauge das Konzentrat in einer Menge von 0,5 bis 25 Gew.-%, vorzugsweise
5 bis 15 Gew.-% bezogen auf die Stammlauge enthält.
17. Verfahren nach Anspruch 16, dadurch gekennzeichnet, dass das während des gesamten Waschvorgangs angesammelte Abwasser oder ein Teil desselben
unter Einsatz einer Membranfiltrationseinheit gereinigt wird.
18. Verfahren nach Anspruch 17, dadurch gekennzeichnet, dass der Membranfiltrationsprozess wenigstens einen Ultrafiltrations- und/oder Umkehrosmose-Schritt
umfasst.
1. Concentré détergent ou nettoyant, alcalin et thixotropique, ayant la consistance d'une
pâte, comprenant, par rapport au concentré total,
a) de 0,5 à 15 % en poids d'au moins un premier composant choisi parmi un ou plusieurs
composés représentés par la formule générale (I)
R1-(OC2H4)n-(OC3H6)m-OH (I)
dans laquelle R1 représente un groupe alkyle ou alcényle ramifié ou non ayant de 4 à 8, de préférence
de 5 à 7 atomes de carbone, et dans laquelle la somme du degré moyen d'éthoxylation
n et de propoxylation m est comprise dans la plage allant de 1 à 9, de préférence
de 3 à 7, un de n et m étant facultativement égal à 0, et
b) de 5 à 90 % en poids d'au moins un deuxième composant choisi parmi un ou plusieurs
composés représentés par la formule générale (II)
R2-(OC2H4)0-(OC3H6)p-OH (II)
dans laquelle R2 représente un groupe alkyle ou alcényle ramifié ou non ayant de 9 à 22, de préférence
de 10 à 16 atomes de carbone, et dans laquelle la somme du degré moyen d'éthoxylation
o et de propoxylation p est comprise dans la plage allant de 1 à 9, de préférence
de 3 à 7, un de o et p étant facultativement égal à 0,
c) au moins 1 % en poids d'au moins une alcanolamine,
le concentré nettoyant présentant à 25°C une viscosité de 80 000 mPa.s à 250 000 mPa.s
à 5 tours par minute et une viscosité de 20 000 mPa.s à 80 000 mPa.s à 50 tours par
minute, chacune mesurée en utilisant un viscosimètre rotatif de Brookfield (mobile
n° 7) dans des conditions sinon identiques.
2. Concentré selon la revendication 1, caractérisé en ce que le composant a) est contenu en une quantité de 1 à 10 % en poids, par rapport au
concentré total.
3. Concentré selon la revendication 1 ou 2, caractérisé en ce que le composant b) est contenu en une quantité de 15 à 70 % en poids, par rapport au
concentré total.
4. Concentré selon la revendication 1, caractérisé en ce que la somme des alcanolamines contenues dans le concentré est comprise dans la plage
allant de 2 à 10 % en poids, de préférence de 3 à 5 % en poids, par rapport au concentré
total.
5. Concentré selon la revendication 1 ou 4,
caractérisé en ce qu'au moins une des alcanolamines est représentée par la formule générale (III)

dans laquelle R
3 représente un groupe hydroxyalkyle ayant de 1 à 6 atomes de carbone, et dans laquelle
R
4 et R
5, indépendamment l'un de l'autre, sont identiques à R
3 ou représentent un atome d'hydrogène.
6. Concentré selon l'une quelconque des revendications 1, 4 et 5, caractérisé en ce que le concentré comprend une mono-, di- ou triéthanolamine ou des mélanges de celles-ci.
7. Concentré selon l'une quelconque des revendications 1 à 6, caractérisé en ce que le concentré comprend un ou plusieurs phosphates.
8. Concentré selon la revendication 7, caractérisé en ce que les phosphates sont choisis parmi au moins un des orthophosphates primaires représentés
par la formule générale MIH2PO4 ou MII(H2PO4)2, des orthophosphates secondaires représentés par la formule générale MI2HPO4 ou MIIHPO4, ou des orthophosphates tertiaires représentés par la formule générale MI3PO4 ou MII3 (PO4)2, ainsi que les phosphates condensés dérivés de ceux-ci, nommés métaphosphates et
polyphosphates, M étant un cation métallique, MI étant de préférence un métal alcalin et MII étant de préférence un métal alcalino-terreux.
9. Concentré selon la revendication 7 ou 8, caractérisé en ce que le phosphate est un tripolyphosphate, de préférence un tripolyphosphate de sodium
(Na5P3O10).
10. Concentré selon l'une quelconque des revendications 7 à 9, caractérisé en ce que le ou les phosphates sont contenus en une quantité d'au plus 40 % en poids, de préférence
en une quantité de 30 % en poids ou moins, par rapport au concentré total.
11. Concentré selon l'une quelconque des revendications 1 à 10, caractérisé en ce que le concentré contient en plus au moins un alkylpolyglucoside ayant de 8 à 14 atomes
de carbone dans le groupe alkyle et de 1 à 5 fragments glucoses.
12. Concentré selon l'une quelconque des revendications 1 à 11, caractérisé en ce que le concentré contient moins de 3 % en poids, de préférence moins de 2 % en poids
d'eau, par rapport au concentré total.
13. Utilisation du concentré selon l'une quelconque des revendications 1 à 12, pour la
préparation d'une lessive antériologue stable.
14. Lessive antériologue stable contenant le concentré selon l'une quelconque des revendications
1 à 11 en une quantité de 0,5 à 25 % en poids, de préférence de 5 à 15 % en poids,
par rapport à la lessive antériologue totale.
15. Utilisation de la lessive antériologue selon les revendications 13 et 14, en tant
qu'agent nettoyant ou détergent, de préférence pour le nettoyage en machine de textiles.
16. Procédé de lavage de textiles comprenant une étape dans laquelle une lessive antériologue
est préparée en diluant le concentré selon l'une quelconque des revendications 1 à
12 de sorte que la lessive antériologue contienne le concentré en une quantité de
0,5 à 25 % en poids, de préférence de 5 à 15 % en poids, par rapport à la lessive
antériologue.
17. Procédé selon la revendication 16, caractérisé en ce que les eaux usées accumulées pendant le procédé de lavage global ou des parties de celui-ci
soient purifiées en utilisant une unité de filtration sur membrane.
18. Procédé selon la revendication 17, caractérisé en ce que le procédé de filtration sur membrane comprend au moins une étape d'ultrafiltration
et/ou d'osmose inverse.
REFERENCES CITED IN THE DESCRIPTION
This list of references cited by the applicant is for the reader's convenience only.
It does not form part of the European patent document. Even though great care has
been taken in compiling the references, errors or omissions cannot be excluded and
the EPO disclaims all liability in this regard.
Patent documents cited in the description