TECHNICAL FIELD
[0001] The present invention relates to a slurry, which is suitable for use as a component
of liquid treatment compositions.
BACKGROUND OF THE INVENTION
[0002] In the preparation of liquid treatment compositions, it is an aim to improve technical
capabilities thereof and aesthetics. One method of improving the aesthetics of a liquid
treatment composition is to make it pearlescent.
[0003] Pearlescence can be achieved by incorporation of a pearlescent agent into the liquid
treatment composition. Pearlescent agents include inorganic natural substances, such
as mica, bismuth oxychloride and titanium dioxide, and organic compounds such as metal
salts of higher fatty acids, fatty glycol esters and fatty acid alkanolamides. The
present invention relates only to the use of inorganic pearlescent agents. The pearlescent
agent can be acquired as a powder, suspension of the agent in a suitable suspending
agent or, where the agent is a crystal, it may be produced in situ.
[0004] Detergent compositions and pearlescent dispersions comprising pearlescent agent fatty
acid glycol ester are disclosed in the following art;
US 4,717,501 (to Kao);
US 5,017,305 (to Henkel);
US 6,210,659 (to Henkel);
US 6,835,700 (to Cognis). Liquid treatment compositions containing pearlescent agents are disclosed in
US 6,956,017 (to Procter & Gamble). Liquid detergents for washing delicate garments containing
pearlescent agent are disclosed in
EP 520551 B1 (to Unilever).
[0005] The present invention relates to a slurry comprising inorganic pearlescent agent.
The slurry described in
WO2007/111899 A2 (to Procter & Gamble) uses water as the carrier for pearlescent agent. However, the
Applicants have discovered that using water as the carrier for pearlescent agent only
allows up to six weeks of physical stability, before the pearlescent agent starts
to settle.
[0006] The inorganic pearlescent agent slurry of
WO2007/11189 is prepared in a batch process. A measured quantity of the inorganic pearlescent
agent slurry is then added to the continuous process used to prepare liquid treatment
compositions. However, as discussed above, the inorganic pearlescent agents tend to
settle from the slurry suspension. This settling causes problems in the continuous
processing used to prepare the liquid treatment compositions, since there will be
points when there may be too much pearlecence or no pearlecence at all.
[0007] One potential solution to these problems may be to increase the viscosity of the
slurry. However the end products necessarily have relatively low viscosity, especially
at high shear, such that they may be poured or processed. Therefore components of
the liquid treatment composition, like the slurry, should not have too high viscosity.
Contrarily, if the slurry has low viscosity at low shear, the particulates have a
tendency to fall out of suspension and either float or sink upon storage. This results
in an undesired, non-homogenous slurry, wherein part of the slurry is pearly and part
of it is clear and homogeneous. Such a slurry clearly would have an undesirable effect
on the aesthetics of the final composition, which may have too much pearlecence or
no pearlecence at all. Hence the Applicant has found that simply varying the viscosity
of the slurry, does not adequately solve the problems as set out in the present invention.
[0008] Moreover, inorganic pearlescent agents are insoluble and without adequate solution,
behave like wet sand, causing problems in processing of the slurry. The wet sand behavior
makes the slurry difficult to mix and requires considerable effort from the equipment
used in the mixing process.
[0009] The present invention provides a slurry and a procedure to prepare the slurry suitable
for further processing into a liquid treatment compositions. The present invention
specifically relates to improving the physical stability and process lifetime of an
inorganic pearlescent agent slurry, and thereby improving the process of preparation
and quality of the liquid treatment composition. The present invention also relates
to the use of combination of solvent and rheology modifier in a slurry of inorganic
pearlescent agents to improve the physical stability and the process lifetime of the
slurry. The Applicants have discovered that replacing water by either glycerol or
sorbitol solvent increases the physical stability of the slurry, in that the slurry
remains physically stable 16 weeks. The present invention also relates to an optimized
the process of preparing the inorganic pearlescent agent slurry wherein the addition
of inorganic pearlescent agent is strictly controlled.
SUMMARY OF THE INVENTION
[0010] According to the present invention there is provided an inorganic pearlescent agent
slurry suitable for use in a liquid treatment composition comprising:
- a) inorganic pearlescent agent
- b) organic solvent, selected from the group consisting of glycerol, sorbitol and mixtures
thereof.
- c) rheology modifier.
wherein the inorganic pearlescent agent is mica.
[0011] The present invention also relates to a process of preparing an inorganic pearlescent
agent slurry, for use in liquid treatment compositions, comprising the steps of:
- a) combining organic solvent, selected from the group consisting of glycerol and sorbitol
and mixtures thereof and from 10% to 66% by weight of the 100% active inorganic pearlescent
agent wherein the inorganic pearlescent agent is mica;
- b) adding rheology modifier and mixing; and
- c) adding remaining inorganic pearlescent agent.
DETAILED DESCRIPTION OF THE INVENTION
[0012] In the present invention, the term slurry is used herein to mean a liquid composition
that is typically flowable at ambient temperature and contains water-insoluble solid
particulates or other solid matter.
[0013] The inorganic pearlescent agent slurry of the present invention is suitable for use
as a component of liquid treatment compositions suitable for laundry or house hold
care applications. By the term laundry treatment composition it is meant to include
all liquid compositions used in the treatment of laundry including cleaning and softening
or conditioning compositions. By the term hard surface treatment composition it is
meant to include all liquid compositions used in the treatment of hard surfaces, such
as kitchen or bathroom surfaces, as well as dish and cook ware in the hand or automatic
dishwashing operations.
[0014] The pearlescent agent slurry according to the present invention for this use comprises
from 30% to 60% water. However there is preferably no freely added water. Where water
does exist in the slurry, it is preferably present as a component of another ingredient
of the slurry, such as the rheology modifier premix.
[0015] The inorganic pearlescent agent slurry of the present invention preferably has viscosity
from 21000 to 65000 centipoises at 0.5 s
-1 and from 1000 to 3000 centipoises at 20s
-1. Viscosity can be determined by conventional methods. Viscosity according to the
present invention is however measured using an AR 550 rheometer from TA instruments
using a plate steel spindle at 40 mm diameter and a gap size of 500 µm. The high shear
viscosity at 20s
-1 and low shear viscosity at 0.5
-1 can be obtained from a logarithmic shear rate sweep from 0.1
-1 to 25
-1 in 3 minutes time at 21°C.
[0016] The slurry of the present invention preferably has a pH of from 7 to 11, more preferably
from 7 to 9 when measured directly from the slurry.
[0017] The temperature of the slurry and throughout the preparation and storage is preferably
below 35 °C. When the used rheology modifier is Hydrogenated Castor Oil (HCO), the
temperature is more preferably between 10 °C and 30 °C. HCO has a low melting point
and will lose the rheology modifier activity when melted and cause the instability
of the slurry.
Pearlescent Agent
[0018] The pearlescent agents according to the present invention is an inorganic crystalline
or glassy solids, transparent or translucent compounds capable of reflecting and refracting
light to produce a pearlescent effect. Typically, the pearlescent agents are crystalline
particles insoluble in the composition in which they are incorporated. Preferably
the pearlescent agents have the shape of thin plates or spheres. Spheres, according
to the present invention, are to be interpreted as generally spherical. Particle size
is measured across the largest diameter of the sphere. Plate-like particles are such
that two dimensions of the particle (length and width) are at least 5 times the third
dimension (depth or thickness). Other crystal shapes like cubes or needles or other
crystal shapes do not display pearlescent effect. Many pearlescent agents like mica
are natural minerals having monoclinic crystals. Shape appears to affect the stability
of the agents. The spherical, even more preferably, the plate-like agents being the
most successfully stabilised.
[0019] The mechanism of pearlescence is described by
R. L. Crombie in International Journal of Cosmetic Science Vol 19, page 205-214. Light reflected from pearl platelets or spheres, as they lie essentially parallel
to each other at different levels in the composition creates a sense of depth and
luster. Some light is reflected off the pearlescent agent, and the remainder will
pass through the agent. Thus light passing through the pearlescent agent, may pass
directly through or be refracted. Reflected, refracted light produces a different
colors, brightness and luster.
[0020] The smaller the particle size and distribution of the pearlescent agent, the more
easily they are suspended. However as the particle size of the pearlescent agent is
decreased, the efficacy of the agent is also decreased. It is therefore preferred
that in the present invention the pearlescent agent has particle size preferable between
5 and 32 micrometers and more preferably between 5 and 26 micrometers.
[0021] The slurry of the present invention preferably comprise from 1% to 35% by weight
of the slurry of a 100% active inorganic pearlescent agent. More preferably the slurry
comprises from 10 % to 30%, more preferably from 10% to 20%, by weight of the slurry
of the 100% active inorganic pearlescent agent.
[0022] The pearlescent agent of the present invention is inorganic. Inorganic pearlescent
agents provide both dynamic and static pearlescent effect. By dynamic pearlescence
it is meant that the composition exhibits a pearlescent effect when the composition
is in motion. By static pearlescence it is meant that the composition exhibits pearlescence
when the composition is static.
Inorganic Pearlescent Agents:
[0023] Inorganic pearlescent agents include those selected from the group consisting of
mica, metal oxide coated mica, silica coated mica, bismuth oxychloride coated mica,
bismuth oxychloride, myristyl myristate, glass, metal oxide coated glass, guanine,
glitter (polyester or metallic) and mixtures thereof.
[0024] Suitable micas include muscovite or potassium aluminum hydroxide fluoride. The platelets
of mica are preferably coated with a thin layer of metal oxide. Preferred metal oxides
are selected from the group consisting of rutile, titanium dioxide, ferric oxide,
tin oxide, alumina and mixtures thereof.
[0025] Pearlecence effect in these pearlescent agents develops through interference between
light rays reflecting at specular angles from the top and bottom surfaces of the metal-oxide
layer. The agents loose color intensity as viewing angle shifts to non-specular angles
and gives it the pearlescent appearance.
[0026] More preferably inorganic pearlescent agents are selected from the group consisting
of mica and bismuth oxychloride and mixtures thereof. More preferably inorganic pearlescent
agents are mica. More preferably the pearlescent agent is metal oxide coated mica,
more preferable titanium oxide coated mica, bismuth oxychloride coated mica or silica
coated mica and mixtures thereof. Commercially available suitable inorganic pearlescent
agents are available from Merck under the tradenames Iriodin, Biron, Xirona, Timiron
Colorona, Dichrona, Candurin and Ronastar. Other commercially available inorganic
pearlescent agent are available from BASF (Engelhard, Mearl) under tradenames Biju,
Bi-Lite, Chroma-Lite, Pearl-Glo, Mearlite and Eckart under the tradenames Prestige
Soft Silver and Prestige Silk Silver Star.
[0027] Inorganic pearlescent agents are preferably incorporated as a powder, and are used
to prepare the slurry without the need for any additional process steps. Process to
prepare the slurry will be described in more details later on.
Organic Solvent system
[0028] The solvent system in combination with the rheology modifier are essential in driving
physically stability in the slurry. Suitable solvents according to the present invention
are organic solvents, selected from the group consisting of glycerol and sorbitol
and mixtures thereof. Solvent is typically present at levels in the range from 10%
to 50%, preferably from 20% to 40% by weight of the slurry.
[0029] Glycerol is a colorless, odorless and viscous liquid. It is sweet-tasting and of
low toxicity. Glycerol has three hydroxyl groups that are responsible for its solubility
in water and its hydroscopic nature.
[0030] Sorbitol is a sugar alcohol, which has six hydroxyl groups that are responsible for
its solubility in water and its hydroscopic nature.
[0031] Without wishing to be bound by the theory it is believed that a synergy exits between
the solvent and rheology modifier. It is further believed that the system comprising
these two elements created more elasticity within the system. This elasticity appears
to mean the system or network is able to recover more quickly following shear.
Rheology Modifier
[0032] The slurry of the present invention comprises a rheology modifier. The overall objective
in adding such a rheology modifier to the slurry herein is to arrive at a slurry which
is suitably functional and aesthetically pleasing from the standpoint of slurry thickness,
pourability, physically stability, optical properties, and/or particles suspension
performance. Thus the rheology modifier will serve to establish appropriate rheological
characteristics of the slurry and will do so without imparting any undesirable attributes
to the product such as unacceptable optical properties or unwanted phase separation.
By rheological characteristics are meant characteristics of the flow of the slurry
under stress and strain.
[0033] The rheology modifier component of the pearlescent agent slurry herein can be characterized
as an "external" or "internal" rheology modifier. An "external" rheology modifier,
for the purposes of this invention, is a material which has as its primary function
that of providing rheological alteration of the liquid matrix. Generally, therefore,
an external rheology modifier will not, in and of itself, provide any significant
fabric cleaning or fabric care benefit or any significant ingredient solubilization
benefit. An external rheology modifier is thus distinct from an "internal" rheology
modifier which may also alter matrix rheology but which has been incorporated into
the liquid product for some additional primary purpose. Thus, for example, a preferred
internal rheology modifier would be anionic surfactants which can serve to alter rheological
properties of the slurry, but which have been added to the slurry primarily to act
as the cleaning ingredient in the final product.
[0034] The rheology modifier of the slurry of the present invention is used to provide a
liquid matrix for the pearlescent agent slurry which has certain rheological characteristics.
The principal characteristic is that the matrix must be "shear-thinning". A shear-thinning
fluid is one with a viscosity which decreases as shear is applied to the fluid. Thus,
at rest, i.e., during storage or shipping of the slurry the liquid matrix of the slurry
should have a relatively high viscosity. When shear is applied to the pearlescent
agent slurry, however, such as in the act of pouring, pumping or mixing the slurry
the viscosity of the matrix should be lowered to the extent that dispensing and mixing
of the slurry is easily and readily accomplished.
[0035] One type of rheological modifier agent which is especially useful in the slurry of
the present invention comprises non-polymeric (except for conventional alkoxylation),
crystalline hydroxy-functional materials which can form thread-like structuring systems
throughout the liquid matrix when they are crystallized within the matrix in situ.
Such materials can be generally characterized as crystalline, hydroxyl-containing
fatty acids, fatty esters or fatty waxes.
[0036] Specific examples of preferred crystalline, hydroxyl-containing rheology modifiers
include castor oil and its derivatives. Especially preferred derivatives are such
as hydrogenated castor oil (HCO) and hydrogenated castor wax. Commercially available,
castor oil-based, crystalline, hydroxyl-containing rheology modifiers include THIXCIN
® from Rheox, Inc. (now Elementis).
[0037] Alternative commercially available materials are those suitable for use as crystalline,
hydroxyl- containing rheology modifiers. An example of a rheology modifier of this
type is 1, 4- di- O- benzyl- D- Threitol in the R, R, and S, S forms and any mixtures,
optically active or not.
[0038] All of these crystalline, hydroxyl-containing rheology modifiers as hereinbefore
described are believed to function by forming thread-like structuring systems when
they are crystallized in situ within the liquid matrix of the slurry herein or within
a pre-mix which is used to form such a liquid matrix. Such crystallization is brought
about by heating an aqueous mixture of these materials to a temperature above the
melting point of the rheology modifier, followed by cooling of the mixture to room
temperature while maintaining the liquid under agitation.
[0039] Other types of rheology modifiers, besides the non-polymeric, crystalline, hydroxyl-containing
rheology modifiers described hereinbefore, may be utilized in the slurry herein. Polymeric
materials which will provide shear-thinning characteristics to the aqueous liquid
matrix may also be employed.
[0040] Suitable polymeric rheology modifiers include those of the polyacrylate, polysaccharide
or polysaccharide derivative type. Polysaccharide derivatives typically used as rheology
modifiers comprise polymeric gum materials. Such gums include pectine, alginate, arabinogalactan
(gum Arabic), carrageenan, gellan gum, xanthan gum and guar gum.
[0041] If polymeric rheology modifiers are employed herein, a preferred material of this
type is gellan gum. Gellan gum is a heteropolysaccharide prepared by fermentation
of Pseudomonaselodea ATCC 31461. Gellan gum is commercially marketed by CP Kelco U.S.,
Inc. under the KELCOGEL tradeneme. Processes for preparing gellan gum are described
in
U.S. Patent Nos. 4,326,052;
4,326,053;
4,377,636 and
4,385,123.
[0042] In an other preferred embodiment the rheology modifier is a polyacrylate of unsaturated
mono- or di-carbonic acid and 1-30C alkyl ester of the (meth) acrylic acid. Such copolymers
are available from Noveon Inc under the tradename Carbopol Aqua 30.
[0043] Preferably the rheology modifier of the present invention is an external rheology
modifier. The rheology modifier is selected from the group consisting of non-polymeric
crystalline, hydroxy-functional materials, polymeric rheology modifiers and mixtures
thereof. The rheology modifier imparts shear thinning characteristics to the slurry.
Crystalline, hydroxy-functional materials are rheology modifiers which form thread-like
structuring systems throughout the matrix of the composition upon in situ crystallization
in the matrix. Polymeric rheology modifiers are preferably selected from polyacrylates,
polymeric gums, other non-gum polysaccharides, and combinations of these polymeric
materials.
[0044] The pearlescent agent slurry of the present invention preferably comprise from 40%
to 80% by weight of the inorganic pearlescent agent slurry of rheology modifier. Preferably
from 40% to 60% by weight, more preferably from 40% to 50% by weight, of the inorganic
pearlescent agent slurry herein.
Detersives surfactants
[0045] The slurry may also comprise a surfactant. Said surfactant may be a component of
the rheology modifier or not. Surfactant is used in present invention as detersive
surfactant for soil suspension purposes.
[0046] Detersive surfactants utilized can be of the anionic, nonionic, zwitterionic, ampholytic
or cationic type or can comprise compatible mixtures of these types. More preferably
surfactants are selected from the group consisting of anionic, nonionic, cationic
surfactants and mixtures thereof. Preferably the compositions are substantially free
of betaine surfactants. Detergent surfactants useful herein are described in
U.S. Patent 3,664,961, Norris, issued May 23, 1972,
U.S. Patent 3,919,678, Laughlin et al., issued December 30, 1975,
U.S. Patent 4,222,905, Cockrell, issued September 16, 1980, and in
U.S. Patent 4,239,659, Murphy, issued December 16, 1980. Anionic and nonionic surfactants are preferred.
[0047] Useful anionic surfactants can themselves be of several different types. For example,
water-soluble salts of the higher fatty acids, i.e., "soaps", are useful anionic surfactants
in the compositions herein. This includes alkali metal soaps such as the sodium, potassium,
ammonium, and alkyl ammonium salts of higher fatty acids containing from about 8 to
about 24 carbon atoms, and preferably from about 12 to about 18 carbon atoms. Soaps
can be made by direct saponification of fats and oils or by the neutralization of
free fatty acids. Particularly useful are the sodium and potassium salts of the mixtures
of fatty acids derived from coconut oil and tallow, i.e., sodium or potassium tallow
and coconut soap.
[0048] Additional non-soap anionic surfactants which are suitable for use herein include
the water-soluble salts, preferably the alkali metal, and ammonium salts, of organic
sulfuric reaction products having in their molecular structure an alkyl group containing
from about 10 to about 20 carbon atoms and a sulfonic acid or sulfuric acid ester
group. (Included in the term "alkyl" is the alkyl portion of acyl groups.) Examples
of this group of synthetic surfactants are a) the sodium, potassium and ammonium alkyl
sulfates, especially those obtained by sulfating the higher alcohols (C
8-C
18 carbon atoms) such as those produced by reducing the glycerides of tallow or coconut
oil; b) the sodium, potassium and ammonium alkyl polyethoxylate sulfates, particularly
those in which the alkyl group contains from 10 to 22, preferably from 12 to 18 carbon
atoms, and wherein the polyethoxylate chain contains from 1 to 15, preferably 1 to
6 ethoxylate moieties; and c) the sodium and potassium alkylbenzene sulfonates in
which the alkyl group contains from about 9 to about 15 carbon atoms, in straight
chain or branched chain configuration, e.g., those of the type described in
U.S. Patents 2,220,099 and
2,477,383. Especially valuable are linear straight chain alkylbenzene sulfonates in which the
average number of carbon atoms in the alkyl group is from about 11 to 13, abbreviated
as C
11-C
13 LAS.
[0049] Preferred nonionic surfactants are those of the formula R
1 (OC
2H
4)
nOH, wherein R
1 is a C
10-C
16 alkyl group or a C
8-C
12 alkyl phenyl group, and n is from 3 to about 80. Particularly preferred are condensation
products of C
12-C
15 alcohols with from about 5 to about 20 moles of ethylene oxide per mole of alcohol,
e.g., C
12-C
13 alcohol condensed with about 6.5 moles of ethylene oxide per mole of alcohol.
[0050] The inorganic pearlescent agent slurry of the present invention may comprise from
about 6% to 13% by weight of the slurry of a surfactant. Surfactant is a particularly
preferred ingredient of the slurry when the rheology modifier is Hydrogenated Castor
Oil.
LIQUID TREATMENT COMPOSITION
[0051] The inorganic pearlescent agent slurry is preferably used as a component of a liquid
treatment composition. It is therefore preferable that the slurry meets requirements
of the liquid treatment composition and is processable with other components thereof.
Suitable components of the liquid treatment composition are listed and discussed in
detail below.
The Inorganic Pearlescent Slurry
[0052] The slurry is described and discussed in detail above.
Rheology Modifier
[0053] The liquid treatment composition preferably comprises rheology modifier, in addition
to that used in the pearlescent agent slurry. The function and choice of rheology
modifier in the liquid treatment composition is the same as is already described with
respect to the slurry.
Detersive Surfactants
[0054] The liquid treatment composition preferably comprises detersive surfactant, in addition
to that used in the pearlescent agent slurry. The function and choice of detersive
surfactant in the liquid treatment composition is the same as is already described
with respect to the slurry.
Optional Ingredients of the Liquid Treatment Composition
[0055] The liquid treatment composition may comprise other ingredients selected from the
list of optional ingredients set out below. Unless specified herein below, an "effective
amount" of a particular laundry adjunct is preferably from 0.01%, more preferably
from 0.1%, even more preferably from 1% to 20%, more preferably to 15%, even more
preferably to 10%, still even more preferably to 7%, most preferably to 5% by weight
of the detergent compositions.
Fabric Care Benefit Agents
[0056] According to a preferred embodiment of the compositions herein there is comprised
a fabric care benefit agent. As used herein, "fabric care benefit agent" refers to
any material that can provide fabric care benefits such as fabric softening, color
protection, pill/fuzz reduction, anti-abrasion, anti-wrinkle, and the like to garments
and fabrics, particularly on cotton and cotton-rich garments and fabrics, when an
adequate amount of the material is present on the garment/fabric. Nonlimiting examples
of fabric care benefit agents include cationic surfactants, silicones, polyolefin
waxes, latexes, oily sugar derivatives, cationic polysaccharides, polyurethanes, fatty
acids and mixtures thereof. Fabric care benefit agents when present in the treatment
composition are suitably at levels of up to about 30% by weight of the composition,
more typically from 1% to 20%, preferably from 2% to 10% in certain embodiments.
Builder
[0057] The liquid treatment compositions may optionally comprise a builder. Suitable builders
are discussed below:
[0058] Suitable polycarboxylate builders include cyclic compounds, particularly alicyclic
compounds, such as those described in
U.S. Patents 3,923,679;
3,835,163;
4,158,635;
4,120,874 and
4,102,903.
[0059] Other useful detergency builders include the ether hydroxypolycarboxylates, copolymers
of maleic anhydride with ethylene or vinyl methyl ether, 1, 3, 5-trihydroxy benzene-2,
4, 6-trisulphonic acid, and carboxymethyloxysuccinic acid, the various alkali metal,
ammonium and substituted ammonium salts of polyacetic acids such as ethylenediamine
tetraacetic acid and nitrilotriacetic acid, as well as polycarboxylates such as mellitic
acid, succinic acid, oxy-disuccinic acid, polymaleic acid, benzene 1, 3, 5-tricarboxylic
acid, carboxymethyloxysuccinic acid, and soluble salts thereof.
[0060] Citrate builders, e.g., citric acid and soluble salts thereof (particularly sodium
salt), are polycarboxylate builders of particular importance for heavy duty liquid
detergent formulations due to their availability from renewable resources and their
biodegradability. Oxydisuccinates are also especially useful in such compositions
and combinations.
[0061] Also suitable in the liquid treatment compositions are the 3,3-dicarboxy-4-oxa-1,6-hexanedioates
and the related compounds disclosed in
U.S. Patent 4, 566, 984, Bush, issued January 28, 1986. Useful succinic acid builders include the C5-C20 alkyl and alkenyl succinic acids
and salts thereof. A particularly preferred compound of this type is dodecenylsuccinic
acid. Specific examples of succinate builders include: laurylsuccinate, myristylsuccinate,
palmitylsuccinate, 2-dodecenylsuccinate (preferred), 2-pentadecenylsuccinate, and
the like. Laurylsuccinates are the preferred builders of this group, and are described
in
EP-A-0 200 263, published November 5, 1986.
[0062] Specific examples of nitrogen-containing, phosphor-free aminocarboxylates include
ethylene diamine disuccinic acid and salts thereof (ethylene diamine disuccinates,
EDDS), ethylene diamine tetraacetic acid and salts thereof (ethylene diamine tetraacetates,
EDTA), and diethylene triamine penta acetic acid and salts thereof (diethylene triamine
penta acetates, DTPA).
[0063] Other suitable polycarboxylates are disclosed in
U.S. Patent 4,144,226, Crutchfield et al, issued March 13, 1979 and in
U.S. Patent 3,308,067, Diehl, issued March 7, 1967. See also
Diehl U.S. Patent 3,723,322. Such materials include the water-soluble salts of homo-and copolymers of aliphatic
carboxylic acids such as maleic acid, itaconic acid, mesaconic acid, fumaric acid,
aconitic acid, citraconic acid and methylenemalonic acid.
Bleach system
[0064] Bleach system suitable for use in liquid treatment compositions contain one or more
bleaching agents. Nonlimiting examples of suitable bleaching agents are selected from
the group consisting of catalytic metal complexes, activated peroxygen sources, bleach
activators, bleach boosters, photobleaches, bleaching enzymes, free radical initiators,
and hyohalite bleaches.
Perfume
[0065] Perfumes are preferably incorporated into the liquid treatment compositions. The
perfume ingredients may be premixed to form a perfume accord prior to adding to the
detergent compositions of the present invention. As used herein, the term "perfume"
encompasses individual perfume ingredients as well as perfume accords. More preferably
the liquid treatment compositions comprise perfume microcapsules. Perfume microcapsules
comprise perfume raw materials encapsulated within a capsule made of materials selected
from the group consisting of urea and formaldehyde, melamine and formaldehyde, phenol
and formaldehyde, gelatine, polyurethane, polyamides, cellulose ethers, cellulose
esters, polymethacrylate and mixtures thereof, most preferably the perfume is encapsulated
with a shell of melamine and formaldehyde. Encapsulation techniques can be found in
"
Microencapsulation": methods and industrial applications edited by Benita and Simon
(marcel Dekker Inc 1996).
[0066] Exemplary perfume ingredients and perfume accords are disclosed in
U.S. Pat. 5,445,747;
U.S. Pat. 5,500,138;
U.S. Pat. 5,531,910;
U.S. Pat. 6,491,840; and
U.S. Pat. 6,903,061.
Solvent system of liquid treatment composition
[0067] The solvent system in the liquid treatment compositions, by contrast with that of
the slurry, can be a solvent system containing water alone or mixtures of organic
solvents with water. Preferred organic solvents include 1,2-propanediol, ethanol,
glycerol, dipropylene glycol, methyl propane diol and mixtures thereof. Other lower
alcohols, C
1-C
4 alkanolamines such as monoethanolamine and triethanolamine, can also be used. Solvent
systems can be absent, for example from anhydrous solid embodiments of the invention,
but more typically are present at levels in the range of from 0.1% to 98%, preferably
at least 10% to 95%, more usually from 25% to 75%.
Fabric substantive and Hueing Dye
[0068] Dyes are conventionally defined as being acid, basic, reactive, disperse, direct,
vat, sulphur or solvent dyes, etc. For the liquid treatment compositions direct dyes,
acid dyes and reactive dyes are preferred, direct dyes are most preferred. Direct
dyes are a group of water-soluble dye taken up directly by fibers from an aqueous
solution containing an electrolyte, presumably due to selective adsorption. In the
Color Index system, directive dye refers to various planar, highly conjugated molecular
structures that contain one or more anionic sulfonate group. Acid dyes are a group
of water soluble anionic dyes that is applied from an acidic solution. Reactive dyes
are a group of dyes containing reactive groups capable of forming covalent linkages
with certain portions of the molecules of natural or synthetic fibers. From the chemical
structure point of view, suitable fabric substantive dyes useful herein may be an
azo compound, stilbenes, oxazines and phthalocyanines.
[0069] Suitable fabric substantive dyes for use herein include those listed in the Color
Index as Direct Violet dyes, Direct Blue dyes, Acid Violet dyes and Acid Blue dyes.
[0070] The hueing dye is included in the laundry detergent composition in an amount sufficient
to provide a tinting effect to fabric washed in a solution containing the detergent.
Encapsulated composition
[0071] The treatment composition, and thus the slurry, of the present invention, may be
encapsulated within a water-soluble film. The water-soluble film may be made from
polyvinyl alcohol or other suitable variations, including carboxy methyl cellulose,
cellulose derivatives, starch, modified starch, sugars, PEG, waxes, or combinations
thereof.
[0072] In another embodiment the water-soluble film may include other adjuncts such as co-polymer
of vinyl alcohol and a carboxylic acid.
US patent 7,022,656 B2 (Monosol) describes such film compositions and their advantages.
[0073] The water-soluble film may further comprise additional co-monomers. Suitable additional
co-monomers include sulphonates and ethoxylates. An example of preferred sulphonic
acid is 2-acrylamido-2-methyl-1-propane sulphonic acid (AMPS). A suitable water-soluble
film for use in the context of the present invention is commercially available under
tradename M8630™ from Mono-Sol of Indiana, US. The water-soluble film herein may also
comprise ingredients other than the polymer or polymer material. For example, it may
be beneficial to add plasticisers, for example glycerol, ethylene glycol, diethyleneglycol,
propane diol, 2-methyl-1,3-propane diol, sorbitol and mixtures thereof, additional
water, disintegrating aids, fillers, anti-foaming agents, emulsifying/dispersing agents,
and/or antiblocking agents. It may be useful that the pouch or water-soluble film
itself comprises a detergent additive to be delivered to the wash water, for example
organic polymeric soil release agents, dispersants, dye transfer inhibitors. Optionally
the surface of the film of the pouch may be dusted with fine powder to reduce the
coefficient of friction. Sodium aluminosilicate, silica, talc and amylose are examples
of suitable fine powders. The encapsulated pouches can be made using any convention
known techniques. More preferably the pouches are made using horizontal form filling
thermoforming techniques.
Other adjuncts
[0074] Examples of other suitable cleaning adjunct materials include, but are not limited
to, alkoxylated benzoic acids or salts thereof such as trimethoxy benzoic acid or
a salt thereof (TMBA); enzyme stabilizing systems; chelants including aminocarboxylates,
aminophosphonates, nitrogen-free phosphonates, and phosphorous- and carboxylate-free
chelants; inorganic builders including inorganic builders such as zeolites and water-soluble
organic builders such as polyacrylates, acrylate / maleate copolymers and the likescavenging
agents including fixing agents for anionic dyes, complexing agents for anionic surfactants,
and mixtures thereof; effervescent systems comprising hydrogen peroxide and catalase;
optical brighteners or fluorescers; soil release polymers; dispersants; suds suppressors;
dyes; colorants; filler salts such as sodium sulfate; hydrotropes such as toluenesulfonates,
cumenesulfonates and naphthalenesulfonates; photoactivators; hydrolysable surfactants;
preservatives; anti-oxidants; anti-shrinkage agents; anti-wrinkle agents; germicides;
fungicides; color speckles; colored beads, spheres or extrudates; sunscreens; fluorinated
compounds; clays; luminescent agents or chemiluminescent agents; anticorrosion and/or
appliance protectant agents; alkalinity sources or other pH adjusting agents; solubilizing
agents; processing aids; pigments; free radical scavengers, and mixtures thereof.
Suitable materials include those described in
U.S. Patent Nos. 5,705,464,
5,710,115,
5,698,504,
5,695,679,
5,686,014 and
5,646,101. Mixtures of adjuncts - Mixtures of the above components can be made in any proportion.
Slurry Preparation
[0075] The slurry of the present invention is prepared by mixing the ingredients together.
However the order and quantity of addition of inorganic pearlecent agent is important
and the inorganic pearlescent agent should be added in two parts. Said process comprises
the steps of
- a) combining organic solvent, selected from the group consisting of glycerol, sorbitol
and mixtures thereof and from 10% to 66% by weight of the 100% active inorganic pearlescent
agent wherein the inorganic pearlescent agent is mica
- b) adding rheology modifier and mixing; and
- c) adding remaining inorganic pearlescent agent.
[0076] The inorganic pearlescent agents are insoluble and without adequate solution, behave
like wet sand, causing problems in processing of the slurry. The wet sand behavior
makes the slurry difficult to mix and requires considerable effort from the equipment
used in the mixing process. By adding the inorganic pearlescent agent in two parts
will produce processable and homogenous slurry. In first inorganic pearlescent agent
addition from 10% to 66% by weight of the inorganic pearlescent agent is added in
steps and mixed.
[0077] Hydrogenated castor oil is a preferred rheology modifier. When hydrogenated castor
oil is used as the rheology modifier, it is preferred that a premix of the hydrogenated
castor oil and surfactant are prepared in a batch process. The water is heated from
80 °C to 98 °C. The surfactant is then added into the solution and pH is adjusted
to 7-8 by using a suitable pH adjusting agent e.g. NaOH and buffer. The hydrogenated
castor oil rheology modifier is dispersed in solution, at the temperature above the
melting point of rheology modifier and the mixture is emulsified. The premix is then
crystallized by cooling the emulsion down by 1°C/min ±0.2°C/min to an end point of
25 °C.
[0078] The remaining inorganic pearlescent agent is added in steps and mixed.
[0079] The mixing speed of the pearlescent agent slurry depends on the composition of the
slurry; higher percentage proportion of pearlescent agent requires faster mixing speed
compared to lower percentage of pearlescent agent. Adequate and constant mixing speed
is required to ensure blending and incorporation of pearlescent agent. However the
shear stress on the process should be kept to a minimum to avoid destroying the network
created by the rheology modifier.
EXAMPLES
[0080] The following nonlimiting examples are illustrative of the present invention. Percentages
are by weight unless otherwise specified.
[0081] Viscosity according to the present invention is measured using an AR 550 rheometer
from TA instruments using a plate steel spindle at 40 mm diameter and a gap size of
500 µm. The high shear viscosity (HSV) at 20s
-1 and low shear viscosity (LSV) at 0.5
-1 can be obtained from a logarithmic shear rate sweep from 0.1
-1 to 25
-1 in 3 minutes time at 21°C.
Example 1
[0082] In an example 1, examples A-D are examples of the slurry of the present invention.
| |
A |
B |
C |
D |
| Mica |
10.00 |
10.00 |
25.00 |
30.00 |
| Water |
30.40 |
48.64 |
30.40 |
30.40 |
| Glycerol |
50.00 |
26.00 |
35.00 |
30.00 |
| Rheology modifier |
1.60 |
2.56 |
1.60 |
1.60 |
| Surfactant |
6.40 |
10.24 |
6.40 |
6.40 |
| NaOH (50%) |
1.60 |
2.56 |
1.60 |
1.60 |
| Total |
100.00 |
100.00 |
100.00 |
100.00 |
| |
|
|
|
|
| LSV, cPs |
21013 |
29934 |
32681 |
31386 |
| HSV, cPs |
1101 |
1297 |
1756 |
1821 |
Slurry A
[0083] Detailed example of the process of making the slurry A is described in the table
below. The table set outs the process through time. Addition of inorganic pearlescent
agent in two main steps is indicated in the table as follows: 1
st mica addition (10% - 66% of the weight of the inorganic pearlescent agent) in steps
and 2
nd mica addition (remaining weight of the inorganic pearlescent agent) also in steps.
[0084] A batch size is 1100g and beaker diameter is 140 mm. Impeller type is pitched blade
turbine and impeller diameter is 100 mm. The clearance C (mm) is the distance from
the bottom of the beaker to the impeller and it can be measured with any measuring
device i.e. meter or ruler.
| Step |
time (min) |
Mixing speed (rpm) |
Clearance C (mm) |
Amount compound added (g) |
Addition rate (kg/min/m^2) |
| glycerol addition |
0 |
|
|
|
|
| 1st mica addition |
1 |
200 |
10 |
6 |
0.39 |
| increase rpm |
1.5 |
400 |
10 |
|
|
| 1st mica addition |
2 |
400 |
10 |
12.24 |
0.80 |
| 1st mica addition |
3 |
400 |
10 |
12.56 |
0.82 |
| 1st mica addition |
3.5 |
400 |
10 |
6.04 |
0.78 |
| blending |
3.5 |
400 |
10 |
|
|
| blending |
4 |
100 |
10 |
|
|
| Rheology modifier addition |
5.5 |
200 |
10 |
|
|
| increase rpm |
6.5 |
250 |
10 |
|
|
| Rheology modifier addition |
7.5 |
250 |
10 |
|
|
| blending |
8 |
200 |
10 |
|
|
| blending |
9 |
250 |
10 |
|
|
| 2nd mica addition |
10 |
250 |
10 |
13.6 |
0.88 |
| 2nd mica addition |
11 |
300 |
10 |
16.4 |
1.07 |
| 2nd mica addition |
12 |
300 |
10 |
15.5 |
1.01 |
| 2nd mica addition |
12.5 |
300 |
10 |
15 |
1.95 |
| 2nd mica addition |
13.5 |
300 |
10 |
13.25 |
0.86 |
| blending |
14 |
250 |
10 |
|
|
| blending |
17 |
250 |
10 |
|
|
Slurry B
[0085] Detailed example of the process of making the slurry B is described in the table
below. The table set outs the process through time. Addition of inorganic pearlescent
agent in two main steps is indicated in the table as follows: 1
st mica addition (10% - 66% of the weight of the inorganic pearlescent agent) in steps
and 2
nd mica addition (remaining weight of the inorganic pearlescent agent) also in steps.
[0086] A batch size is 1100g and beaker diameter is 140 mm. Impeller type is pitched blade
turbine and impeller diameter is 100 mm. The clearance C (mm) is the distance from
the bottom of the beaker to the impeller and it can be measured with any measuring
device i.e. meter or ruler.
| Step |
time (min) |
Mixing speed (rpm) |
Clearance C (mm) |
Amount compound added (g) |
Addition rate (kg/min/m^2) |
| glycerol addition |
|
|
|
|
|
| 1st mica addition |
1 |
200 |
10 |
13.1 |
0.85 |
| 1st mica addition |
2 |
300 |
10 |
15.3 |
0.99 |
| 1st mica addition |
2.5 |
300 |
10 |
8.3 |
1.08 |
| Rheology modifier addition |
3.5 |
300 |
10 |
|
|
| Rheology modifier addition |
5.5 |
300 |
10 |
|
|
| blending |
6 |
200 |
10 |
|
|
| blending |
7 |
200 |
10 |
|
|
| increase rpm |
7.5 |
350 |
|
|
|
| 2nd mica addition |
8 |
300 |
10 |
14.7 |
0.95 |
| 2nd mica addition |
9 |
400 |
10 |
14.3 |
0.93 |
| 2nd mica addition |
10 |
400 |
10 |
17.4 |
1.13 |
| 2nd mica addition |
11 |
400 |
10 |
13.4 |
0.87 |
| 2nd mica addition |
12 |
400 |
10 |
13.9 |
0.90 |
| blending |
13 |
300 |
10 |
|
|
| blending |
15 |
300 |
10 |
|
|
Slurry C
[0087] Detailed example of the process of making the slurry C is described in the table
below. The table set outs the process through time. Addition of inorganic pearlescent
agent in two main steps is indicated in the table as follows: 1
st mica addition (10% - 66% of the weight of the inorganic pearlescent agent) in steps
and 2
nd mica addition (remaining weight of the inorganic pearlescent agent) also in steps.
[0088] A batch size is 1100g and beaker diameter is 140 mm. Impeller type is pitched blade
turbine and impeller diameter is 100 mm.
| Step |
time (min) |
Mixing speed (rpm) |
Clearance C (mm) |
Amount compound added (g) |
Addition rate (kg/min/m^2) |
| glycerol addition |
0 |
|
|
|
|
| 1st mica addition |
1 |
250 |
10 |
16.6 |
1.08 |
| 1st mica addition |
2 |
250 |
10 |
14.7 |
0.95 |
| 1st mica addition |
3 |
250 |
10 |
14.0 |
0.91 |
| 1st mica addition |
4 |
250 |
10 |
16.3 |
1.06 |
| 1st mica addition |
5 |
250 |
10 |
11.4 |
0.74 |
| 1st mica addition |
6 |
250 |
10 |
20.6 |
1.34 |
| blending |
6 |
300 |
10 |
|
|
| blending |
6.5 |
250 |
10 |
|
|
| Rheology modifier addition |
7.5 |
300 |
10 |
|
|
| Rheology modifier addition |
8.5 |
300 |
10 |
|
|
| blending |
9 |
300 |
10 |
|
|
| blending |
9.5 |
200 |
10 |
|
|
| blending |
10 |
200 |
10 |
|
|
| 2nd mica addition |
11 |
250 |
10 |
16.8 |
1.09 |
| 2nd mica addition |
12 |
250 |
10 |
17.5 |
1.14 |
| 2nd mica addition |
13 |
300 |
10 |
11.8 |
0.77 |
| 2nd mica addition |
14 |
300 |
10 |
13.8 |
0.90 |
| 2nd mica addition |
15 |
300 |
10 |
13.6 |
0.88 |
| 2nd mica addition |
16 |
300 |
10 |
15.3 |
0.99 |
| 2nd mica addition |
17 |
300 |
10 |
16.6 |
1.08 |
| 2nd mica addition |
18 |
350 |
10 |
14.3 |
0.93 |
| 2nd mica addition |
19 |
350 |
10 |
13.6 |
0.88 |
| 2nd mica addition |
20 |
350 |
10 |
16.4 |
1.07 |
| 2nd mica addition |
21 |
350 |
10 |
10.8 |
0.70 |
| 2nd mica addition |
22 |
350 |
10 |
22.4 |
1.45 |
| blending |
22.5 |
400 |
10 |
|
|
| blending |
23.5 |
300 |
10 |
|
|
| blending |
25 |
200 |
10 |
|
|
| blending |
26 |
200 |
10 |
|
|
Slurry D
[0089] Detailed example of the process of making the slurry D is described in the table
below. Addition of inorganic pearlescent agent in two main steps is indicated in the
table as follows: 1
st mica addition (10% - 66% of the weight of the inorganic pearlescent agent) in steps
and 2
nd mica addition (remaining weight of the inorganic pearlescent agent) also in steps.
[0090] A batch size is 30 kg and tank diameter is 390 mm. Impeller type is pitched blade
turbine and impeller diameter is 250 mm. The clearance C (mm) is the distance from
the bottom of the tank to the impeller and it can be measured with any measuring device
i.e. meter or ruler.
| Step |
Mixing speed (rpm) |
Clearance C (mm) |
Amount compound added (g) |
Addition rate (kg/min/m^2) |
| glycerol addition |
100 |
60 |
|
|
| 1st mica addition |
100 |
60 |
2980 |
0.80 |
| blending |
100 |
60 |
|
|
| Rheology modifier addition |
100 |
60 |
|
|
| blending |
150 |
100 |
|
|
| 2nd mica addition |
190 |
150 |
5600 |
1.20 |
| blending |
190 |
150 |
|
|
[0091] The dimensions and values disclosed herein are not to be understood as being strictly
limited to the exact numerical values recited. Instead, unless otherwise specified,
each such dimension is intended to mean both the recited value and a functionally
equivalent range surrounding that value. For example, a dimension disclosed as "40
mm" is intended to mean "about 40 mm".
1. Anorganische Perlglanzmittel-Aufschlämmung, geeignet zur Verwendung in einer flüssigen
Behandlungszusammensetzung, die Folgendes umfasst:
a) anorganisches Perlglanzmittel,
b) organisches Lösungsmittel, ausgewählt aus der Gruppe bestehend aus Glycerin, Sorbit
und Mischungen davon,
c) Rheologiemodifikator,
wobei das anorganische Perlglanzmittel Glimmer ist.
2. Aufschlämmung nach Anspruch 1, wobei der Rheologiemodifikator ausgewählt ist aus der
Gruppe bestehend aus nicht-polymerem kristallinem, hydroxyfunktionalem Material, Polyacrylat,
polymerem Gummi, anderen Nichtgummi-Polysaccharid-Rheologiemodifikatoren und Mischungen
davon.
3. Aufschlämmung nach einem der vorstehenden Ansprüche, ferner umfassend ein anionisches
Tensid, ausgewählt aus der Gruppe bestehend aus C11-C18-Alkylbenzolsulfonaten (LAS), C10-C20-verzweigtkettigen und regellosen Alkylsulfaten (AS), C10-C18-Alkylethoxysulfaten (AExS), wobei x von 1-30 ist, mittelkettenverzweigten Alkylsulfaten, mittelkettenverzweigten
Alkylalkoxysulfaten, C10-C18-Alkylalkoxycarboxylaten, umfassend 1-5-Ethoxyeinheiten, modifizierten Alkylbenzolsulfonaten
(MLAS), C12-C20-Methylestersulfonat (MES), C10-C18-alpha-Olefinsulfonat (AOS), C6-C20-Sulfosuccinaten und Mischungen davon.
4. Zusammensetzung nach einem der vorstehenden Ansprüche, ferner umfassend ein nichtionisches
Tensid ausgewählt aus der Gruppe bestehend aus C9-C18-Alkylethoxylaten, C6-C12-Alkylphenolalkoxylaten, C12-C18-Alkohol- und C6-C12-Alkylphenol-Kondensaten mit Ethylenoxid/Propylenoxid-Blockpolymeren, C14-C22-mittelkettenverzweigten Alkoholen, C14-C22-mittelkettenverzweigten Alkylalkoxylaten, Alkylpolyglycosiden, Polyhydroxyfettsäureamiden,
etherverkappten, poly(oxyalkylierten) Alkoholen, Fettsäure-(C12-18)-Sorbitanestern und Mischungen davon.
5. Aufschlämmung nach einem der vorstehenden Ansprüche, wobei das Gewicht des Lösemittels
in einer Konzentration von 10 % bis 50 % des Gewichts der anorganischen Perlglanzmittel-Aufschlämmung,
mehr bevorzugt von 20 % bis 40 % des Gewichts der anorganischen Perlglanzmittel-Aufschlämmung
vorhanden ist.
6. Aufschlämmung nach einem der vorstehenden Ansprüche, wobei das anorganische Perlglanzmittel
in einer Konzentration von 1 % bis 35 % des Gewichts der anorganischen Perlglanzmittel-Aufschlämmung,
mehr bevorzugt von 10 % bis 30 % und mehr bevorzugt von 10 % bis 20 % des Gewichts
der anorganischen Perlglanzmittel-Aufschlämmung vorhanden ist.
7. Aufschlämmung nach einem der vorstehenden Ansprüche, wobei der Rheologiemodifikator
in einer Konzentration von 40 % bis 80 % des Gewichts der anorganischen Perlglanzmittel-Aufschlämmung,
mehr bevorzugt von 40 % bis 60 % und mehr bevorzugt von 40 % bis 50 % des Gewichts
der anorganischen Perlglanzmittel-Aufschlämmung vorhanden ist.
8. Aufschlämmung nach einem der vorstehenden Ansprüche, wobei der Rheologiemodifikator
als eine Vormischung aus gehärtetem Rizinusöl und Tensid vorhanden ist, und wobei
das Tensid vorzugsweise in einer Konzentration von 6 % bis 13 % des Gewichts der Rheologiemodifikator-Vormischung
vorhanden ist.
9. Verfahren zum Herstellen der Aufschlämmung nach einem der vorstehenden Ansprüche zur
Verwendung in Waschmittelzusammensetzungen, das folgende Schritte umfasst
i) Kombinieren von organischem Lösemittel, ausgewählt aus der Gruppe bestehend aus
Glycerin, Sorbit und Mischungen davon, und von 10 % bis 66 % des Gewichts des 100
% aktiven anorganischen Perlglanzmittels, wobei das anorganische Perlglanzmittel Glimmer
ist;
ii) Hinzufügen des Rheologiemodifikators und Vermischen;
iii) Hinzufügen von restlichem anorganischem Perlglanzmittel.
1. Bouillie d'agent nacrant inorganique appropriée pour une utilisation dans une composition
de traitement liquide comprenant :
a) un agent nacrant inorganique,
b) un solvant organique, choisi dans le groupe constitué de glycérol, sorbitol et
des mélanges de ceux-ci,
c) un agent modifiant la rhéologie,
dans lequel l'agent nacrant inorganique est le mica.
2. Bouillie selon la revendication 1, dans laquelle l'agent modifiant la rhéologie est
choisi dans le groupe constitué d'un matériau cristallin non polymère, à fonction
hydroxy, de polyacrylate, de gomme polymère, d'autres agents modifiant la rhéologie
polysaccharide non-gomme et des mélanges de ceux-ci.
3. Bouillie selon l'une quelconque des revendications précédentes, comprenant en outre
un agent tensioactif anionique, choisi dans le groupe constitué d'alkylbenzène sulfonates
(LAS) en C11 à C18, alkylsulfates (AS) à chaîne ramifiée et aléatoires en C10 à C20, alkyl-éthoxy-sulfates en C10 à C18 (AExS) où x va de 1 à 30, alkylsulfates ramifiés à mi-chaîne, d'alkyl-alkoxy-sulfates
ramifiés à mi-chaîne, de carboxylates d'alkylalcoxy en C10 à C18 comprenant 1 à 5 motifs éthoxy, alkylbenzène sulfonates modifiés (MLAS), sulfonates
de méthylester (MES) en C12 à C20, alpha-oléfinesulfonates (AOS) en C10 à C18, sulfosuccinates en C6 à C20, et des mélanges de ceux-ci.
4. Composition selon l'une quelconque des revendications précédentes, comprenant en outre
un agent tensioactif non ionique choisi dans le groupe constitué d'alkyl-éthoxylates
en C9 à C18, alkyl-phénol alcoxylates en C6 à C12, condensats d'alcool en C12 à C18 et d'alkyl-phénol en C6 à C12 avec des polymères séquencés oxyde d'éthylène/oxyde de propylène, alcools ramifiés
à mi-chaîne en C14 à C22, alkyl-alcoxylates ramifiés à mi-chaîne en C14 à C22, alkylpolyglycosides, amides d'acide gras polyhydroxyle, alcools poly(oxyalkylés)
à coiffe éther, esters de sorbitan d'acide gras en (C12 à 18), et des mélanges de ceux-ci.
5. Bouillie selon l'une quelconque des revendications précédentes, dans laquelle le poids
du solvant est présent à un taux allant de 10 % à 50 % du poids de la bouillie d'agent
nacrant inorganique, plus préférablement de 20 % à 40 % du poids de la bouillie d'agent
nacrant inorganique.
6. Bouillie selon l'une quelconque des revendications précédentes, dans laquelle l'agent
nacrant inorganique est présent à un taux allant de 1 % à 35 % du poids de la bouillie
d'agent nacrant inorganique, plus préférablement de 10 % à 30 % et plus préférablement
de 10 % à 20 % du poids de la bouillie d'agent nacrant inorganique.
7. Bouillie selon l'une quelconque des revendications précédentes, dans laquelle l'agent
modifiant la rhéologie est présent à un taux allant de 40 % à 80 % du poids de la
bouillie d'agent nacrant inorganique, plus préférablement de 40 % à 60 % et plus préférablement
de 40 % à 50 % du poids de la bouillie d'agent nacrant inorganique.
8. Bouillie selon l'une quelconque des revendications précédentes, dans laquelle l'agent
modifiant la rhéologie est présent en tant que prémélange d'huile de ricin hydrogénée
et d'agent tensioactif et dans laquelle l'agent tensioactif est de préférence présent
à un taux allant de 6 % à 13 % du poids du prémélange d'agent modifiant la rhéologie.
9. Procédé de préparation de la bouillie selon l'une quelconque des revendications précédentes
pour une utilisation dans des compositions détergentes, comprenant les étapes consistant
à
i) combiner un solvant organique, choisi dans le groupe constitué de glycérol, sorbitol
et des mélanges de ceux-ci et de 10 % à 66 % du poids de l'agent nacrant inorganique
à 100 % d'agent actif dans lequel l'agent nacrant inorganique est le mica;
ii) ajouter l'agent modifiant la rhéologie et mélanger ;
iii) ajouter l'agent nacrant inorganique restant.