Note: Descriptions are shown in the official language in which they were submitted.
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COMPOSITIONS CONTAINING BENEFIT AGENT COMPOSITES PRE-
EMULSIFIED USING COLLOIDAL CATIONIC PARTICLES
CROSS-REFERENCE TO R.ELATED APPLICATION
[oool] The present application claims the benefit of priority of Proxisional
Patent
Application No. 6o/991,$o6 filed December 3, 2007. The entire text of the
priority
application is incorporated herein by reference in its entirety.
FIELD OF THE INVENTION
[0002] The present invention relates to compositions that allow increased
deposition and retention of benefit agents contained therein, onto a
substrate, for
example, a fabric; hair; skin; teeth, and other hard surfaces, while the
substrate is
being treated with these compositions. Cleansing products such as the
conditioning
shampoos, bodywashes, soaps, detergents, toothpaste, and counter or floor
cleaning
products, as well as surface-conditioning products such as fabric softeners
are some
of the exemplary product forms that these compositions represent. Silicone,
fragrance, emollient, ultraviolet (UV) ray absorbers, and antimicrobial agents
are
typical examples of the benefit agents.
[0003] Despite the large number of prior art methods and compositions for
enhancing the deposition of benefit agents (e.g., silicone, fragrance) from
cleansing
products, there is a need for substantially improving the deposition
efficiency. The
trends in consumer preference related to these products, for example,
conditioning
shampoos and moisturizing bodywashes, illustrate this void. Most commercial
conditioning shampoos (2-in-1 shampoos) contain a water-immiscible silicone
fluid
as a hair conditioning agent, with the silicone fluid remaining emulsified
(oil-in-
water O/W emulsion) in the water-based solution of a shampoo base. The shampoo
base further contains a water-soluble, high molecular weight, cationic polymer
as a
deposition-aid for silicone-deposition on the hair. Yet, most consumers
seeking
relatively high levels of hair-conditioning prefer conditioners, the products
that do
not rely on silicone-deposition for hair-conditioning, to the 2-in-1 shampoos.
[00041 LikextiTise, most commercial, moisturizing bodywash products contain
relatively high amounts of skin-moisturizing emollients such as petrolatum,
mineral
oil, and vegetable oils, along with a cationic polymer as a deposition-aid.
Despite
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this, consumers tend to rely on moisturizing lotions for skin-moisturizing,
likely
because of inadequate emollient-deposition on the skin from bodywash products.
[0005] Unexpectedlv, we have now found that the compositions disclosed herein
show considerably high levels of performance properties, namely, hair-
conditioning,
fabric softening, fragrance extension (i.e., long-lasting fragrance) and skin-
moisturizing, which is attributed to the specific additive-form in which the
benefit
agents are incorporated into these compositions, and in particular to the
composition
of this additive-form, hitherto not disclosed in the prior art. According to
the present
invention, the benefit agent is added to the claimed compositions, only after
it is
decidedlv bonded to a deposition-aid, utilizing physical interaction-mediated
bonding (i.e., not a chemical bond) between the two materials. Also, prior to
being
bonded to a deposition-aid, the benefit agent preferably undergoes a physical
change,
to serve multiple purposes critical to the object of the present invention.
[ooo6] In order to meet the object of the present invention, the
aforementioned
physical-modification of the benefit agent does not involve encapsulation of
the
benefit agent within a polymeric capsule-like enclosure, an approach revealed
in the
prior art. Rather, in one embodiment, it involves producing a composite
material
comprising a water-immiscible, hydrophobic liquid, and an exfoliated,
organophilic
smectite clay capable of thickening (increasing the viscosity) the hydrophobic
liquid.
The hydrophobic liquid itself can be a benefit agent and/or a solvent for a
benefit
agent. The organophilic (i.e., hydrophobic) smectite clay component of the
benefit
agent composite is such that a portion of the clay surface bears an anionic
charge,
and the hydrophobic modification of the clay surface is at a level wherein
exfoliated
clay platelets may remain adsorbed at an oil-water interface. In another
embodiment, it is a composite material comprising a hydrophobic liquid and an
exfoliated, organophilic smectite clay, with the composite material further
containing
a benefit agent dispersed homogeneously in the form of a particulate material
throughout the entire mass of the composite material. In yet another
embodiment,
the benefit agent is first entrapped in certain highly porous polymeric
microparticles
(which are insoluble in water and organic solvents), and the entrapped benefit
agent
is subsequently dispersed homogeneously in a composite material comprising a
hydrophobic liquid and an exfoliated, organophilic smectite clay.
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[0007] The resulting benefit agent composite is necessarily a highly viscous
material, having a sufficiently high viscosity for strongly opposing the "roll-
up"
mechanism, knowrn. in the art as being the mechanism by which surfactants
remove
"oily-soils" from a surface undergoing cleansing. Yet another beneficial
outcome of
the foregoing physical-modification of the benefit agent is that the Hamaker
constant, a direct proportionality factor for a measure of the van der Waals
attraction
between material bodies, of the composite material is significantly higher
than that of
the benefit agent taken individuallv. A further benefit is that the specific
gravity of
the benefit agent composite can be varied starting, for example, at a minimum
value
of about 1, which might be critical to achieving good stability against
settling/creaming (by virtue of density-matching between dispersed and
continuous
phases), when the benefit agent composite is dispersed in the claimed
compositions
whose solution phase could have a specific gravity of 1 or higher.
[ooo8] The deposition-aid material is not a low molecular weight surfactant
but
most preferably a cationic, colloidal (< 1- 2 micron in size), particulate
material
having a relatively high surface charge. The surface properties, including
hydrophobicity and surface charge (as defined and characterized bv methods
known
in the art), of these cationic particles and the benefit agent composite are
such that
the cationic particles can remain physically bonded to (adsorbed on) the
surface of
the benefit agent composite. Nonetheless, while remaining adsorbed on the
surface
of the composite, the cationic deposition-aid particles do not form any
continuous
film or capsule-wall around the composite. These cationic particles can
comprise
cationic polymers including the cationic deposition-aid polymers known in the
art.
The relatively high surface charge of the deposition-aid particles bound to
the benefit
agent composite, contributes to the dispersion-stability (i.e., against
flocculation and
coalescence) of the composite material, when the material is dispersed in
aqueous
solutions including surfactant solutions. In essence, these cationic
deposition-aid
particles also serve as a dispersing agent (an emulsifier system), when the
benefit
agent composite material is dispersed (emulsified) in water, in producing the
claimed
additive-form for the benefit agent.
[ooo9] The said additive-form of the benefit agent is a stable, cationic oil-
in-
water (O/W) emulsion, with the benefit agent contained in the oil phase
(comprising
the composite material described above) of the emulsion. The mean particle
size of
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the emulsion droplets is in the range of from 1 to about 300 microns,
preferably from
about 5 pm to about 150 ;um, more preferably from about 1.o pm to about l.oo
pm,
and most preferably from about 20 pm to about 50 pm. The resulting O/W
emulsion
is subsequently mixed into surfactant-laden final compositions of the present
invention, as is or in a dried form.
BACKGROUND OF THE INVENTION
[ooio] By design, detersive surfactants, generally present in excess in
products
such as shampoos, bodywashes, liquid soaps, laundry detergents, and
toothpaste, are
meant to remove dirt, oil, grease, and particulate matter from the hair, skin,
fabric,
and teeth. Nonetheless, it is desirable that one or more functional materials,
called
herein "benefit agent" or "active", contained in these cleansing products, can
be
deposited and retained at relatively high levels on the substrates being
cleaned, while
maintaining detergency and foaming properties of these products. These
actives,
having benefits related to hair-care or skin-care or fabric-care or dental-
care may
range from silicones used as hair-conditioning agents, to emollient oils and
fragrances, used as skin-moisturizing and aesthetic/sensory property-boosting
agents. Most of these benefit agents tend to be expensive, and hence can be
included
in the detersive products only at relatively low to moderate levels. Adequate
deposition and retention of these actives, therefore, is critical to realizing
their end-
use benefits, when they are to be delivered through shampoos, soaps, laundry
detergents, and toothpastes.
[ooil] The prior art includes numerous patents describing methods for
improving the deposition of hydrophobic or water-immiscible actives from
detersive
or wash-off product compositions, many of which involve the following:
i) the use of O/W emulsions of benefit agents, wherein a water-immiscible
liquid (e.g., silicone), used as a benefit agent, is emulsified in water using
an emulsifier selected from nonionic, anionic, and cationic surfactants;
ii) encapsulation of benefit agents within a polymeric capsule or shell, by
curing or hardening a polymeric film as a capsule wall over droplets
containing a benefit agent, or by encapsulating a benefit agent within a
capsule wall comprising a complex coascervate of polymers, e.g., a complex
coascerc-ate comprising a polycation and a polyanion.
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[ooi2] A majority of these reported inventions, for example, the ones
described in
U.S. patents 3,723,325, 5r085,857, 5,500,152, 5,543,074, 5,776,443, 5,853,707,
5,990,059, 5,935,561, 5,923,203, 6,126,954, 6,156,713, 6,277,361 Bi, 6,436,383
B2,
6,7o6,258 Bi, U.S. patent application 2005/0158266, and WO 98/11869 rely on
cationic polymers as a deposition-aid. Accordingly, these polymers are often
referred
to as deposition polymers in the art.
[0013] Despite the abundance of patents disclosing cationic polymer-aided
methods for enhancing the deposition of hydrophobic benefit agents from
surfactant-
laden compositions, there is a need for substantially improving the deposition
efficiency, given, for example, that most consumers who seek relatively high
levels of
hair-conditioning prefer conditioners, the non-detersive hair-conditioning
products,
to the detersive products like 2-in-1 shampoos which typically contain
cationic
polymers as a deposition-aid. A reason for this consumer preference is that,
with the
2-in-i shampoos, a substantial amount of the hair-conditioning agent,
silicone, is
rinsed away during shampooing, despite the deposition polymers contained
therein.
[0014] In light of the distinguishing features of the present invention over
the
prior art, it appears that one plausible cause for the inadequate performance
of the
cationic deposition polymers as used in the prior art is that these polymers
and the
benefit agents are added as separate ingredients in producing the final
detersive
compositions, i.e., the deposition polymer(s) is not pre-adsorbed or pre-
disposed to
bind onto the benefit agent(s) as these ingredients are incorporated into the
final
compositions. As described herein, in order for the cationic polymer to
function
adequately as a deposition-aid, it must first physically attach onto the
benefit agent.
Given that most cleansing products contain relatively high amounts of anionic
surfactants, and in contrast, relatively low levels of benefit agent(s) and a
deposition
polymer, binding of the deposition polymer onto the benefit agent may not be
possible when these ingredients are added separately as ingredients to the
detersive
compositions, for reasons such as the following:
i) factors such as high concentration of anionic surfactants, and strong
interaction (electrostatic) between an anionic surfactant and a cationic
polymer are likely to favor association between the anionic surfactants and
the cationic polymer over that between two weakly interacting, low-level
ingredients, the cationic polymer and the hydrophobic benefit agent,
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especially considering that the commonly used cationic deposition
polymers (for example, cationic cellulose and cationic guar derivatives) are
mostly hydrophilic polymers that tend to have a low affinity for
hydrophobic surfaces such as the surfaces of hydrophobic benefit agents;
ii) since the amount of an anionic surfactant likely to adsorb on the
hydrophobic benefit agent ~vould be much smaller than the amount of the
surfactant remaining dissolved (i.e., non-adsorbed) in the solution-phase,
the cationic deposition polymer is most likely to (associate) form
complexes (anionic complexes in anionic surfactant-rich solutions) with
the dissolved surfactant molecules rather than with any surfactant
molecules pre-adsorbed on the benefit agent;
iii) being present at a much higher concentration than any cationic polymer-
anionic surfactant complex that could possibly form, and having a
diffusivity much higher than that of such a complex, the anionic
surfactants might adsorb on the hydrophobic benefit agent far more easily
than the polymer-surfactant complex, implying that the cationic deposition
polymer may not be able to adsorb on the benefit agent to any considerable
extent, when these two materials are added separately as ingredients to
anionic surfactant-rich cleansing product compositions; and
iv) the hydrophobic benefit agent may simply dissolve in the surfactant-rich
solution.
[0015] In fact, it is often theorized in the art that association between the
cationic
deposition polymer and the hydrophobic benefit agent is achieved only when the
cleansing products get heavily diluted during the course of the rinsing
process.
Clearly, large portions of the added deposition polymer and the benefit agent
would
be rinsed off before this optimum dilution level is reached.
[oo16] Albeit, the prior art reveals approaches other than the use of cationic
deposition polymers, for example, as disclosed in the U.S. patents 5,726,138,
6,541,565 B2, and 6,667,029 B2, the commercial detersive products continue to
rely
on these polymers for the deposition of hydrophobic benefit agents. This is
likely
because the deposition polvmer-free approaches are not commercially viable
from
the standpoint of cost, product stability, and bulk manufacturing.
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[0017] The prior art also includes methods wherein hydrophobic benefit agents
are encapsulated within a capsule wall comprising a polymeric material. The
encapsulated benefit agent is subsequently mixed into a cleansing/wash-off
product
composition comprising one or more surfactants. This final composition may
further
contain a cationic polymer, with the cationic polymer coating the capsule
wall, as
disclosed in US 7,118,057 B2 and US 7,294,612 B2.
[oo18] The prior art also teaches that a cationic polymer may be an integral
part
of a capsule wall enclosing a benefit agent, with the capsule wall comprising
a
complex coascervate of a polycation and a polyanion, as revealed in WO
98/11870.
According to a disclosure in WO 98/11870, the cleansing composition may
further
contain a cationic polymer-based thickening agent which remains dissolved in
the
aqueous solution phase of the composition. The encapsulated droplets have a
particle size distribution such that at least io% by weight of the droplets
comprises
relatively large particles having a diameter of at least 1oo microns. As noted
in WO
98/11870, the efficacy of the claimed compositions relies heavily on
parameters such
as the relative hardness/softness and the thickness of the complex coascervate
capsule wall, as well as the size of the encapsulated droplets of hydrophobic
benefit
agents, which would be hard to control in a cost-effective manner, especially
during
bulk manufacturing. Furthermore, while it might be possible to use a
thickening
agent in certain cleansing products such as shampoo and body-wash, for
minimizing
gravity-separation of relatively large suspended droplets (particle size >> 1
micron)
from a product formulation, avoiding gravity-separation of a key ingredient,
might be
impossible for liquid detergents which are generally required to have a
relatively low
viscosity and hence have a relatively low particulate-suspending ability. In
addition
to these specific concerns regarding the compositions in WO 98/11870, one
skilled in
the art would be particularly wary about a major limitation that applies, in
general, to
any encapsulation approach, as discussed below.
[ooi9] In order to adequately realize the end-use benefits, for example, hair-
conditioning, fabric-softening, and fragrance-extension, of the hydrophobic
benefit
agents, while it is essential that there is substantial deposition of the
benefit agents
on the treated substrate, it is equally important that the benefit agents,
once
deposited on the substrate, are available in a physical form that is suitable
for
providing the desired end-use benefit. For example, deposition of a
hydrophobic
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substance such as silicone on hair or on a fabric causes hydrophobic-
modification of
the hair or the fabric surface, which in turn leads to effects that manifest
as hair-
conditioning or fabric-softening benefits. Nonetheless, if the silicone is
encapsulated
within a polymeric capsule, and should the encapsulated silicone droplet
deposit on a
substrate, it is the outer surface of the capsule wall and not the strongly
hydrophobic
surface of the silicone droplet, which would ultimately impart any effect in
the way of
modification of the substrate-surface. If the capsule wall is derived from
hydrophilic,
water-soluble polymers, as disclosed in US 7,118,057 B2, US 7,294,612, and WO
98/1187oB2, the outer surface of the capsule wall may not be able to provide
for
hydrophobic-modification of the hair or the fabric surface, essential to
delivering
benefits such as hair-conditioning and fabric-softening.
[0020] In other words, even after substantial deposition of a benefit agent,
it may
not be possible to realize the end-use benefits, if the benefit agent is
deposited in an
encapsulated form comprising a shell of a capsule wall and an inner core of
the
benefit agent. In that case, at best, one can hope to see only a partial
benefit of the
benefit agent, relying on diffusion of the benefit agent through the capsule
wall
and/or leakage of the same due to any breakage of the capsule wall (for which
hardness/softness and thickness of the capsule wall would be the efficacy
determining factors, as revealed in WO 98/11870). Such subdued or partial
availability of the benefit agent, despite its adequate deposition, may
provide for a
level of end-use benefit (e.g., fragrance emission) that may be sufficient,
for example,
for post-wash fragrance-extension, but too little for any appreciable hair-
conditioning and fabric-softening.
[0021] It is therefore an object of the present invention to provide a more
efficient
method than the methods described in the prior art, for the deposition and
retention
of hydrophobic or oil-based benefit agents from detersive and/or rinse-off
compositions. It is a further object that the compositions and methods
described
herein, do not involve encapsulation of benefit agents within any capsule
wall, are
relatively inexpensive, involve manufacturing steps that are easy to implement
or
control, and do not adversely affect the stability, detergency, and foaming
properties
of the cleansing product compositions. A related object is to provide stable,
low-cost,
compositions that allow significantly high deposition and retention of
hydrophobic
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benefit agents onto substrates being treated with the compositions, including
the
fabric, hair, and skin.
[0022] Furthermore, it would be highly convenient to have hydrophobic benefit
agents available in a form which can be incorporated easily into a final
product
composition. In that vein, it would be of much benefit, if such an additive-
form for
the benefit agent also served towards attaining an enhanced deposition of the
benefit
agent. Nonetheless, an important issue to be addressed in producing this
additive-
form is its long-term storage stability. It is therefore a further object of
the
compositions and methods to provide a highly stable additive-form for
hydrophobic
benefit agents, which, when incorporated into final product compositions,
leads to an
increased deposition of the benefit agents.
[0023] Several of the patents cited above, for example, U.S. patent 6,7o6,258
Bi,
describe the use of preformed oil-in-water (O/W) emulsions of hydrophobic
benefit
agents, wherein the oil-phase containing the benefit agent, is emulsified
using
(anionic, nonionic) surfactant-based emulsifiers. However, in the reported
inventions, wherein a cationic polymer-based deposition-aid was used in
conjunction
v6th a preformed emulsion of a hydrophobic benefit agent (or cvith a
hydrophobic
benefit agent alone), the cationic polymer additive and the preformed emulsion
(or a
hydrophobic benefit agent alone) were incorporated into the final detersive
composition as separately-added ingredients, i.e., no attempt was made therein
to
pre-adsorb or bind the cationic polymer additive onto the emulsion droplets
(or the
hydrophobic benefit agent) and subsequently mixing in the polymer-modified
emulsion droplets (or the hydrophobic benefit agent) as a whole ingredient in
producing the final detersive composition.
[0024] In fact, there is no known prior art document wherein a cationic
particle
and/or a cationic polymer-based additive was used as part of the emulsifier
system
used to produce a stable O/W emulsion of a hydrophobic benefit agent, that is
subsequently incorporated into a surfactant containing aqueous composition,
with
the composition exhibiting enhanced deposition of the hydrophobic benefit
agent
onto an intended site during use, along with good stability, and minimal
detrimental
effect on detergency and foaming properties, as in accordance with the
compositions
and methods described herein.
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SUMMARY OF THE INVENTION
[0025] Described herein are compositions for use as cleansing and surface-
conditioning products like shampoos, bodywashes, liquid soaps, laundry
detergents,
fabric softeners, and toothpaste, which allow substantive retention on the
hair, skin,
fabric, and tooth/gum, of one or more hydrophobic benefit agents contained
therein.
According to the compositions and methods described herein, the hydrophobic
actives are incorporated into the compositions, as cationic oil-in-water (O/W)
emulsions. The compositions may further contain surfactants present either in
aqueous solutions or in powder/granular forms, polymers, and hydrophilic
solvents
selected from water, lower alcohols, glycols, and glycerine.
[0026] Although low molecular weight (molecular weight < 5,ooo Dalton)
cationic surfactants could be used as an emulsifier, as revealed in the U.S.
patent
5,306,434 involving non-detersive hair conditioner compositions, to produce
the
cationic surface charge of emulsion droplets, these surfactants are not
preferred for
the purpose of the compositions and methods described herein. With these low
molecular weight emulsifiers, the emulsion stability would be only modest,
while the
emulsifier dosage requirement would be relatively high. More importantly,
these low
molecular weight compounds may not be capable of aiding deposition of benefit
agents from detersive compositions.
[0027] Emulsions stabilized by particulate- and/or polymer-based emulsifiers
generally tend to exhibit a relatively high stability against flocculation and
coalescence. Considering this inherent advantage with the aforementioned
emulsifiers, the present invention embodies the use of these emulsifiers in
producing
cationic oil-in-water (O/W) emulsions of the hydrophobic benefit agents.
Unexpectedly, we have found now that these cationic emulsions greatly enhance
the
deposition of hydrophobic benefit agents from detersive compositions onto an
intended site during use, e.g., hair shaft, skin, fabric.
[0028] According to an important embodiment of the compositions and methods
described herein, a key component of the emulsifier system used in making the
claimed cationic emulsions of hydrophobic benefit agents is preferably a
cationic
particulate material, comprising an inorganic moiety, or an organic moiety, or
a
hybrid of inorganic and organic moieties. This particulate component of the
emulsifier system has a relatively high cationic surface charge (as determined
by
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methods known in the art), as characterized by a zeta potential value of at
least +25
millivolts, and a particle size of less than 1 - 2 microns, preferably much
less than 1
micron. Unexpectedly, it has been found that one way to produce the cationic
emulsifier particles that would serve the object of the present invention is
by
combining certain water-soluble cationic polymers with at least one water-
insoluble
anionic polymer, so long as certain material property, composition, and
processing
requirements are met during the manufacturing of the particles. These water-
insoluble, polymeric particles bear a relatively high cationic surface charge
which
stabilizes them against particle-to-particle aggregation. Ordinarily, these
particles do
not form any particulate network structures, being stable against aggregation,
and
are typically much smaller than 1 micron in size.
[0029] Yet another important embodiment requires that, preferably, medium to
very high molecular weight cationic polymers, more preferably, high molecular
weight cationic polymers having a molecular weight in the range of 300,000 -
1,ooo,ooo Dalton, and most preferably, certain combinations of high molecular
weight and ultra high molecular weight (molecular weight > 1,ooo,ooo Dalton)
cationic polymers are used as an emulsifier component to render the emulsion
droplets cationic. Nonetheless, in order for a cationic particulate material
or a
cationic polymer to serve as an emulsifier, it is required to adsorb at the
oil-water
interface.
[0030] One way to achieve good interfacial adsorption of cationic polymers is
to
use cationic, amphiphilic copolymers that have both hydrophilic and
hydrophobic
segments in the polymer chain. Such copolymers could adsorb at the oil-water
interface with their hydrophobic segments anchored onto the oil phase. Albeit,
such
copolymers might be functionally suitable for the present invention, they tend
to be
costly. The other type of cationic polymer that might be effective, are the
hydrophobically-modified cationic polymers which also tend to be expensive.
[0031] Hydrophilic cationic polymers are relatively low-cost materials, and
hence
are preferred for the compositions and methods described herein. These
polymers,
however, may not be sufficiently surface-active for adsorption at the oil-
water
interface. Therefore, according to an important embodiment of the present
invention, anionic polymers and surfactants that are capable of adsorbing at
the oil-
surface are used to facilitate the interfacial adsorption of the hydrophilic
cationic
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polymers. These anionic polymers or surfactants electrostatically attract,
onto
themselves, the cationic polymers, serving as a coupling agent for the
cationic
polymers to co-adsorb at the interface. In effect, the emulsifier system is a
combination of the hydrophilic cationic polymers and the surface-active
anionic
polymers or surfactants. Another embodiment of the compositions and methods
described is to have the ratio of weights of the anionic and cationic
components of
the emulsifier system such that the emulsion droplets are cationic. Yet
another
embodiment is to use Nvater-insoluble, hydrophobic, anionic polymers or
surfactants
as the anionic component of the emulsifier system.
[0032] As indicated above, the most preferred option for the cationic
component
of the emulsifier system is to use certain combinations of high molecular
weight
(molecular weight in the range of 50,000 - 1,ooo,ooo Dalton) and ultra high
molecular weight (molecular weight > 1,ooo,ooo Dalton) cationic polymers.
Since a
very high molecular weight polymer can flocculate emulsion droplets by what is
known as bridging flocculation, for the object of the present invention, it is
important
that the cationic charge of the emulsion droplets is relatively high, for
example,
Ntirherein the droplets show a cationic zeta potential of more than 25
millivolts, as
measured using the methods known in the art. Bridging flocculation of
suspended
particles occurs when a single polymer chain simultaneously adsorbs on more
than
one particle. Accordingly, before undergoing bridging flocculation by a
polymer
chain, two or more suspended particles must approach one another as closely as
where the particle-to-particle separation distance is equal to or less than
the length of
the polymer chain. Such close approach of the suspended particles may not be
possible if there is sufficient electrostatic repulsion between the particles
due to their
surface charge, inhibiting the prospects of bridging flocculation even by a
very high
molecular weight polymer.
[0033] It was found during the research leading to the compositions and
methods
described herein that concentrated emulsions of hydrophobic benefit agents
could be
produced more easily, using the aforementioned emulsifier system, if, prior to
emulsification, the oil phase was thickened using a specific type of a
particulate-
based thickener, with the thickener particles dispersed homogeneously in the
oil
phase. High-shear mixing was required to ensure good dispersion of the
particulate
thickener in the oil phase, in turn producing a viscous composite material
comprising
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a hydrophobic liquid and the dispersed thickener particles. In order to serve
the
object of the present invention, it is highly desirable that the Hamaker
constant, a
direct proportionality factor for a measure of van der Waals attraction
between
material bodies, of the particulate-based thickener is such that the Hamaker
constant
(as may be derived using methods described in the colloid chemistry
literature) of the
composite oil phase is significantly higher, at least 4% higher, than that of
a
hydrophobic benefit agent by itself.
[0034] The most widely used particulate-based thickeners include the layered
silicate materials such as the smectite clays, namely bentonite and hectorite
clays, as
well as fumed metal oxides, for example, silica. Layered silicate materials
are a class
of inorganic particulate materials that occur as stacks of individual, planar
silicate
layers referred to as platelets in the clay literature. These materials, as
well as fumed
silica, however, are hydrophilic in terms of surface property. Therefore,
unless their
surface is rendered hydrophobic, these materials can be used only as
thickeners for
water-based compositions but not for hydrophobic liquids. Various methods are
known in the art for hydrophobic surface-modification of these materials,
including
treating the materials with long-chain (C8 - C22) quaternary ammonium
compounds, amphiphilic copolymers, and silanes.
[0035] In order to achieve the full advantage of the compositions and methods
described herein, the specific type of particulate-based thickeners that are
suitable
include the hydrophobically-modified smectite clays for which only the face-
surfaces
of the clay platelets are rendered hydrophobic by the adsorption of long-chain
(C8 -
C22) onium ions, e.g., from quaternary ammonium compounds, while the edge-
surfaces remain hydrophilic and bears an anionic charge when wetted by an
aqueous
solution having a pH of greater than 3. Among the particulate-based
thickeners, the
materials that lend themselves easily to selective surface-modification are
the
smectite clays, because of the differences in the surface properties between
the face
surfaces and the edge surfaces of the clay platelets. The face-surfaces of
smectite
clays bear an anionic charge due to the isomorphic substitution of aluminum by
magnesium in the clay-crystal structure. On the other hand, the electrical
charge of
the edge-surfaces depends on the type (anionic or cationic) of potential
determining
ions that adsorb on the edge surfaces when the clay platelets are dispersed in
water
or in an electrolyte solution. Under controlled solution (water-based)
conditions,
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long-chain (C8 - C22) quaternary surfactants can be made to adsorb only on the
face-surfaces of clay platelets via ion-exchange, acting as counterions for
the anionic
platelet surface charge. The typical loading level for the quarternary
ammonium
compound can be in the range of about lo-8o % by weight based on the dry
weight of
the smectite clay.
[0036] An important feature of one embodiment of the compositions and
methods described herein relates to the final viscosity of the composite
material (oil
phase) containing the benefit agent, prior to the emulsification of the oil
phase. The
final (low shear-rate,e.g., 0.5 - 2 rpm of spindle speed in a Brookfield
viscometer)
viscosity of the composite is preferably greater than 500,000 cps, more
preferably
greater than 1,ooo,ooo cps, and most preferably greater than 5,000,000 cps,
with
the viscosity measured using a Brookfield viscometer. The viscosity of the
composite
is preferably so high that the oil phase takes on a "stiff' consistency. In
order to
achieve this final viscosity, the hydrophobically-modified smectite clay
thickener is
adequately exfoliated or delaminated (separation of clay platelets across
their face
surfaces, as described in the art) in the oil phase, using high-shear
dispersion
methods knoNvn in the art.
[0037] In addition to one or more particulate-based thickeners, the oil phase
may
further contain other particulate materials in the form of inorganic and
organic
solids or liquids. In other words, the oil phase itself can be a dispersion of
an
inorganic or an organic solid, or an emulsion of an inorganic or an organic
liquid,
comprising two or more immiscible liquids.
[0038] Yet another embodiment of the compositions and methods described
herein pertains to the hydrophobic or oil-based benefit agents that are
appreciably
soluble in concentrated solutions of detersive surfactants, typically used in
various
cleansing products. According to the compositions and methods described
herein,
such benefit agents are dissolved, dispersed, or diluted in one or more
hydrophobic
solvent or liquid that has a relatively low solubility in concentrated
surfactant
solutions, in order to minimize the dissolution of the benefit agent in the
detersive
surfactant solutions. These hydrophobic solvents have a solubility of less
than 2% by
weight in an aqueous surfactant solution containing at least 3% (preferably
3%) by
weight of one or more surfactant. The oil-phase, comprising one or more
benefit
agent and the hydrophobic solvent, is subsequently thickened using an
organophilic
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smectite clay of the type noted above, followed by emulsification of the
viscous,
composite oil-phase using the aforementioned emulsifier svstem. The increased
-viscosity of the composite oil phase, due to the formation of a particulate
network
structure of the exfoliated organophilic clay, is expected to provide an
addition
barrier to the diffusion of the benefit agent from the oil phase to the
surrounding
aqueous phase of the emulsion or of the final cleansing product composition.
The
concentrated emulsions thus produced are eventually mixed or diluted with
reagents
selected from surfactants, polymers, and/or hydrophilic solvents to produce
the
compositions described herein.
[0039] A further embodiment of the compositions and methods described herein
pertains to hydrophobic benefit agents, for example, water-immiscible
fragrances
and perfumes, that tend to evaporate or otherwise dissipate rapidly. According
to the
compositions and methods described herein, highly porous, adsorbent polymeric
microparticles are used as a carrier for such hydrophobic benefit agents,
wherein the
hydrophobic benefit agent is entrapped within the highly porous matrix of the
microparticles, in the form of a liquid or a solid. According to a critical
embodiment,
the porosity of these polymeric microparticles is sufficiently high for the
tap density
(as measured by the methods known in the art) of the microparticles to be _
0.5
gram per milliliter. Also, the heat transfer parameters (as can be determined
by the
methods known in the art) for the polymeric solid constituting these
microparticles,
are such that the evaporative loss of the benefit agent can be significantly
reduced
upon entrapping the benefit agent into the microparticles, despite the highly
porous
nature of the polymeric matrix of the microparticles. Furthermore, the
particle size
for these polymeric microparticles can be in the range of 1 - 200 microns.
These
polymeric microparticles, being highly porous, do not, in effect, encapsulate
the
benefit agent in a capsule-like fashion, as evident from a relatively high
rate of
partitioning (as can be determined by the methods known in the art) of the
entrapped benefit agent out of the microparticles into a surrounding liquid.
[004o] The microparticle-entrapment of the hydrophobic benefit agent is
subsequently dispersed in a water-immiscible, hydrophobic liquid which have a
solubility of less than 2% by weight in an aqueous surfactant solution
containing at
least 3% by weight of one or more surfactant. The oil-phase, comprising the
microparticle-entrapment of one or more benefit agents, dispersed in a water-
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immiscible, hydrophobic liquid, is subsequently thickened using an
organophilic
smectite clay of the type noted above, followed by emulsification of the
thickened oil-
phase using the aforementioned emulsifier system. The concentrated emulsions
thus
produced are eventually mixed or diluted w-ith reagents selected from
surfactants,
polymers, and hydrophilic solvents to produce the compositions described
herein.
[0041] According to one embodiment of the present invention, the claimed
compositions are produced upon mixing or diluting the foregoing cationic O/W
emulsions of the benefit agent with reagents selected from surfactants and
hydrophilic solvents including water, glycols, alcohols, and glycerol.
[0042] The resulting cationic emulsions of the benefit agents are highly
stable
against coalescence, the phenomenon that leads to the separation of the oil
phase
from the water phase in O/W emulsions. The stability (tested using methods
known
in the art) is retained even when the emulsions are diluted with water, for
example,
in the amount of 1 part by weight of emulsion ta 50 parts by weight of water.
[0043] In the aforementioned emulsions, the individual cationic emulsifier
particles remain adsorbed on the emulsion droplets in a manner such that these
particles are able to function as an emulsifier. The total amount of cationic
charge of
the particles adsorbed on individual oil droplets is sufficiently high for
offsetting any
anionic charge due to any anionic component contained in the oil phase, such
that
the net surface-charge of the emulsion droplets is strongly cationic
(characterized by
a zeta potential of at least +25 millivolts). The surface properties,
including
hydrophobicity and surface charge (as defined and characterized by methods
known
in the art), of these cationic particles and the benefit agent composite are
such that
the cationic particles can remain adsorbed on the surface of the benefit agent
composite. The enhanced substrate-deposition of the benefit agents from the
claimed compositions, to a large extent, is attributed to having the cationic
emulsifier
particles pre-adsorbed on the emulsion droplets containing the benefit agent.
[0044] In addition, by emulsifying the benefit agents using an emulsifier
system
comprising pre-formed, discrete particles that are highly stable against
coagulation,
and hence remain adsorbed at the oil-water interface as individual or
segregated
particles, the benefit agent is not subjected to encapsulation within any
capsule-like
enclosure. This allows full manifestation of the intended benefits (for
example,
fragrance emission and hair conditioning), once the benefit agents deposit
onto the
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substrates being treated by the compositions described herein. We now have
also
found that the foregoing cationic emulsions of the hydrophobic benefit agents
do not
adversely affect the foaming properties of surfactant-laden claimed
compositions to
any profound extent.
[0045] A distinguishing feature of the present invention over the prior art is
that
the emulsifier system used in producing the aforementioned additive-form for
the
benefit agent, is not a surfactant type of an emulsifier, but rather comprises
at least
two components: i) a cationic particle having a relatively high surface charge
(at least
+25 millivolts of zeta-potential) and a particle size of less than 1- 2
micron; and ii) a
surface-modified smectite clay that is dispersible in a water-immiscible
organic
liquid but not in ,tiTater, with the clay modified by the adsorption of onium
ions, e.g.,
obtained by dissolution of C8 - 22 alkyl ammonium compounds onto specific
sections of the clay surface. Also, in order for this emulsifier system to
vATork,
component (i) can be added only to the water phase and component (ii) only to
the
oil phase of the claimed O/W emulsions of benefit agents.
[0046] Another distinguishing feature is that the emulsified oil phase w-ith a
benefit agent contained therein, prior to emulsification, is a composite
material
providing for several beneficial features important to achieve certain objects
of the
present invention, such as: i) the composite material containing the benefit
agent is
considerably more viscous than the benefit agent itself, with the viscous
consistency
retained even upon heating; ii) the Hamaker constant of the composite material
is
considerably higher (at least 4% higher) than that of the benefit agent; and
iii) the
specific gravity of the composite material can be in the range of >_ 1.
[0047] A further distinguishing feature is that the benefit agent is not
encapsulated in its entirety within a capsule wall, and accordingly there is
no solid
shell-wall separating an inner core comprising the benefit agent, from the
surrounding solution phase of any cleansing or wash-off product composition
that
were to contain the benefit agent. Rather, the benefit agent composite is
bonded to a
particulate-based, cationic deposition-aid material that also serves as an
emulsifier
for the O/W emulsion of the composite material in water, without forming any
capsule-like enclosure around the composite.
[0048] An additional distinguishing feature of one embodiment of the
compositions and methods described herein is that a very high molecular weight
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polymer, with a weight average molecular weight exceeding l,ooo,ooo Dalton,
often
referred to in the prior art as deposition polymer, is an integral part of the
multi-
component emulsifier system used to emulsify the benefit agent-laden composite
oil
phase in a water phase, unlike in the prior art compositions wherein such a
deposition polymer is not pre-adsorbed or bound to any non-encapsulated
hydrophobic benefit agent emulsified in the water phase of these compositions.
DETAILED DESCRIPTION
[0049] The compositions described herein comprise the following ingredients:
= Reagents selected from the group consisting of surfactants and hydrophilic
solvents and mixtures thereof, with the surfactants selected from the group
consisting of anionic, nonionic, zwitterionic, and cationic surfactants, and
the hydrophilic solvents selected from water, alcohols, glycols, and
glycerine;
= Benefit agent selected from the group consisting of hydrophobic
compounds, oils, oil-soluble or dispersible compounds, and water-
immiscible compounds, offering hair-care, skin-care, fabric-care, and/or
aesthetic or sensory property-boosting benefits.
[005o] Depending on the type of final products in which they are used as,
i.e.,
shampoo, liquid soap, bodywash, laundry detergent, fabric softener,
toothpaste,
antiseptic ointments, these compositions may further contain ingredients
selected
from fatty alcohols having 8 to 22 carbon atoms, opacifiers or pearlescers
such as
ethylene glycol esters of fatty acids (e.g., ethylene glycol distearate),
viscosity
modifiers, buffering or pH adjusting chemicals, water-soluble polymers
including
cross-linked and non cross-linked polymers, foam boosters, perfumes, dyes,
coloring
agents or pigments, herb extracts, preservatives, hydrotopes, enzymes,
bleaches,
fabric conditioners, optical brighteners, antioxidants, stabilizers,
dispersants, soil
release agents, anti-wrinkle agents, chelants, anti corrosion agents, and
teeth
cleansing and whitening agents, and mixtures thereof.
[0051] In producing the claimed compositions, the benefit agents are
incorporated into the compositions as cationic oil-in-water (O/W) emulsions of
a
Nriscous composite material containing the benefit agent(s). The cationic
emulsion of
the benefit agent(s) is produced using a multicomponent, particulate-based
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emulsifier system comprising mixtures of certain hydrophilic cationic polymers
and
water-insoluble or surface-active anionic polymers. In effect, the benefit
agent(s) is
contained in these emulsions as part of a viscous, emulsified oil-phase, with
the
emulsion droplets bonded to interfacially-active, cationic particles serving
as
emulsifier, comprising the aforementioned polymers. By interfacially-active is
meant
the ability to adsorb at an interface, for example, oil-water and air-water
interfaces.
[0052] The benefit agents that have appreciable solubility in concentrated
(amount >_ 3% by weight) surfactant solutions, are first dissolved or
dispersed or
diluted in a suitable hydrophobic cosmetically acceptable liquid or solvent
that has a
low (<1% by tikt.) solubility in concentrated surfactant solutions. A
particularly useful
cosmetic-solvent is a triglyceride, while equally useful is a silicone fluid,
preferably a
dimethicone fluid.
[0053] The benefit agents that tend to evaporate or otherwise dissipate
rapidly
are first entrapped in certain highly porous adsorptive polymeric
microparticles that
have a tap density of <0.5 gram per milliliter, and a particle size in the
range of 1-
200 microns. The maximum adsorption capacity of these polymeric microparticles
for either hydrophobic or hydrophilic benefit agents may be in the range of 2 -
15 g
of adsorbate/gm of the dry polymer. These polymeric microparticles, being
highly
porous, do not, in effect, encapsulate the benefit agent in a capsule-like
fashion. The
microparticle-entrapment of the hydrophobic benefit agent is subsequently
dispersed
in a water-immiscible, hydrophobic liquid that has a relatively low solubility
in
concentrated surfactant solutions. A preferred hydrophobic, water-immiscible
liquid
is a silicone fluid, a dimethicone fluid having a viscosity of > 50
centistokes.
[0054] Preceding emulsification, the oil-phase, comprising a hydrophobic,
water-
immiscible liquid or solvent with the benefit agent(s) contained therein, is
thickened
using one or more organophilic smectite clay for which only the face-surface
of the
clay platelets is rendered hydrophobic, while the edge-surface remains
hydrophilic,
while capable of bearing an anionic surface charge when exposed to aqueous
solutions at a pH of _ 3. Upon thickening, the oil phase preferably has a
viscosity of
greater than 500,000 cps, as measured using a Brookfield RVT viscometer
operated
at 1 rpm (revolution per minute) of spindle speed with spindle number 7.
[0055] The various aspects of the aforementioned compositions are discussed in
greater detail below:
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Surfactants
[0056] Non-limiting examples of suitable anionic surfactants are the sodium,
ammonium, and mono-, di-, and tri-ethanolamine salts of alkyl sulfates, alkyl
ether
sulfates, alkaryl sulfonates, alkyl succinates, alkyl sulfosuccinate, N-alkoyl
sarcosinates, alkyl phosphates, alkyl ether phosphates, alkyl ether
carboxylates, and
a-olefin sulfonates. The alkyl groups generally contain from 8 to 18 carbon
atoms
and may be unsaturated. The alk-yl ether sulfates, alkyl ether phosphates, and
alkyl
ether carboxylates may contain from 1 to 1o ethylene oxide or propylene oxide
units
per molecule, and preferably contain 2 to 3 ethylene oxide units per molecule.
Examples of the most preferred anionic surfactants include sodium or ammonium
lauryl sulfate and sodium or ammoinium lauryl ether sulfate.
[0057] Suitable nonionic surfactants include, but not limited to, aliphatic,
primary or secondary linear or branched chain alcohols or phenols with
alkylene
oxides, generally ethylene oxide and generally 6-3o ethylene oxide groups.
Other
suitable nonionic surfactants include mono- or di-alkyl alkanolamides, alkyl
polyglucosides, and polyhydroxy fatty acid amides.
[0058] The amphoteric surfactants suitable for use in the present invention
include alkyl amine oxides, alkyl betaines, alkyl amidopropyl betaines, alkyl
sulfobetaines, alkyl glycinates, alkyl carboxyglycinates, alkyl
amphopropionates,
alkyl amidopropyl hydroxysultaines, acyl taurates, and acyl glutamates wherein
the
alkyl and acyl groups have from 8 to 18 carbon atoms.
[0059] Nonlimiting examples of suitable cationic surfactants include water-
soluble or water-dispersible or water-insoluble compounds containing at least
one
amine group which is preferably a quaternary amine group, and at least one
hydrocarbon group which is preferably a long-chain hydrocarbon group. The
hydrocarbon group may be hydroxylated and/or alkoxylated and may comprise
ester- andJor amido- and/or aromatic-groups. The hydrocarbon group may be
fully
saturated or unsaturated.
[oo6o] The level of surfactants may range from 0.5 to 95%, preferably from 2
to
9o%, and most preferably from 3 to go% by weight of the claimed compositions.
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Hydrophilic Solvents
[oo61] The hydrophilic solvents suitable for use include water and hydrophilic
organic liquids and mixtures thereof. Nonlimiting examples of preferred
hydrophilic
organic liquids include glycerol, ethanol, isopropanol, propylene glycol,
butylene
glycol, hexylene glycol, polyethylene glycol and mixtures thereof.
[oo62] The level of hydrophilic solvents may range from 0.1 to 95%, preferably
from 1 to go%, and most preferably from 3 to 9o o by weight of the claimed
compositions.
Benefit Agents
[oo63] In the compositions and methods described herein, benefit agents are
water-insoluble but oil-soluble/miscible/dispersible solids and liquids, as
well as oily
materials, that can provide a positive or beneficial effect to the substrate
being
treated, e.g., to the hair, skin, fabric, and teeth. Preferred benefit agents
include, but
not limited to, the following:
a) silicone oils, resins, and modifications thereof such as linear and cyclic
polydimethylsiloxanes, amino-modified, alkyl, aryl, and alkylaryl silicone
oils, which preferably have a viscosity >> 50,000 cst;
b) fragrance, perfumery, and essential oils and resins;
c) organic sunscreen actives, for example, octylmethoxy cinnamate;
d) antimicrobial agents, for example, 2-hydroxy-4,2,4-trichlorodiphenylether;
e) ester solvents; for example, isopropyl myristate;
f) lipids and lipid like substance, for example, cholesterol;
g) hydrocarbons such as paraffins, petrolatum, and mineral oil
h) fish and vegetable oils
i) hydrophobic plant extracts;
j) therapeutic and skin-care reagents;
k) hydroquinone
1) waxes; and
m) pigments including inorganic compounds with hydrophobically modified
surface and/or dispersed in an oil or a hydrophobic liquid.
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Polymeric Microparticles for the Entrapment of Rapidly Eva.porating
Benefit Agents
[oo64] One class of adsorbent polymeric microparticles is prepared by
suspension polymerization techniques, as set forth in U.S. Patent Nos.
5,677,407;
5,712,358; 5,777,054; 5,830,967; 5,834,577; 5,955,552; and 6,107,429, each
incorporated herein by reference (available commercially under the tradename
of
POLY-PORE* E200, INCI name, ally methacrylates crosspolvmer, from AMCOL
International, Arlington Heights, IL). Another class of adsorbent polymeric
microparticles is prepared by a precipitation polymerization technique, as set
forth in
U.S. Patent Nos. 5,830,96o; 5,837,790; 6,248,849; and 6,387,995, each
incorporated
herein by reference (available commercially under the tradename of POLY-PORE*
L200 from AMCOL International, Arlington Heights, IL).
[oo65] Another class of adsorbent polymeric microparticles prepared by a
precipitation polymerization technique is disclosed in U.S. Patent Nos.
4,962,170;
4,948,818; and 4,962,133, each incorporated herein by reference, and available
commercially under the tradename of POLYTRAP by AMCOL International (INCI
name of lauryl methacrylate / glycol dimethacrylate cross polymer).
[oo66] An additional adsorbent polymeric microparticle has been developed, as
disclosed in U.S. Patent Re. 33,429, incorporated herein by reference and sold
under
the tradename of MACROBEAD by AMCOL International (INCI name of lauryl
methacrylate / glycol dimethacrylate cross polymer). Other adsorbent polymers
that
are commercially available include, for example, MICROSPONGE@ (INCI name of
methyl methacrylate / glycol dimethylacrylate crosspolymer), as disclosed in
U.S.
Patent 4,69o,825, available from AMCOL International, and Poly-HIPE polymers
(e.g., a copolymer of 2-ethylhexyl acrylate, styrene, and divinylbenzene)
available
from Biopore Corporation, Mountain View, CA.
[oo67] The amount of the polymeric microparticle may range from about io% to
about loo% by weight of the benefit agent. The amount of the entrapped benefit
agent may range from about i% to about 6o % by weight of the emulsified oil
phase.
[oo68] One or more of the foregoing benefit agents is included in the
compositions described herein in an amount varying from 0.05 to 99%,
preferablv
from 0.1 to 40%, and most preferably from 0.5 to 20% by weight of the
detersive
composition. The benefit agents are incorporated into the detersive
compositions by
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mixing or diluting concentrated emulsions of the benefit agents with detersive
surfactants, wherein in the preferred embodiment, the emulsions are produced
in
accordance with the following sequential steps (i) through (iii).
i) Unless the benefit agent is insoluble or only sparingly soluble in
surfactant solutions, for example, as with most silicones, the benefit agent
is dissolved or dispersed or diluted in a hydrophobic liquid or solvent
N-dth poor surfactant-phase solubility (herein defined as having a
solubility < 2% by weight in an aqueous detersive surfactant solution with
a surfactant content in the range of 3 - 25%). A preferred diluent is a
triglyceride, castor oil, or a silicone fluid, dimethicone fluid, having a
viscosity of >5o centistokes. The triglyceride- or dimethicone-content of
the resulting oil-phase is preferably at least 5o% by weight, e.g., 50 - 95%
by weight, while the amount of the benefit agent is the range of o.1 - 6o%.
ii) The oil-phase containing the benefit agent, or the silicone-based benefit
agent, is thickened using an organophilic smectite clay. Not all
commercially available organophilic smectite clays are ideal for obtaining
the full advantage of the compositions and methods described herein.
The preferred organophilic smectite clays are those for which only the
face surface is rendered hydrophobic by the adsorption of fatty
quaternary ammonium compounds with 8 to 22 carbon atoms in the alkyl
chain, while the edge-surface remains hydrophilic. Examples of suitable
organoclays include, but not limited to, the organophilic bentonite clays
available from Nanocor, a subsidiary of AMCOL International
Corporation. The amount of organoclay added to the oil- or silicone-
phase can be 3 - 6o a by weight, preferably 20 - 5o%, and ideally 25 -
45%, based on the weight of the oil- or silicone phase. In order to
enhance the thickening ability of the organoclay, one or more polar
materials such as propylene carbonate, ethanol, alkylene glycol, and
water and mixtures thereof may be added at the level of lo - 6o% by
weight, based on the weight of the organoclay. In producing the
thickened oil- or silicone-phase, the organoclay is dispersed in the
hydrophobic liquid using high-shear equipment such as rotor-stator
homogenizer and extruder.
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iii) The thickened oil- or silicone-phase is emulsified in water using an
emulsifier system comprising in part a cationic particle having a relatively
high cationic surface charge and a size of < 1 - 2 micron. According to a
preferred embodiment, the cationic particle component of the emulsifier
comprises three polymeric components, an anionic polymer and two
hydrophilic cationic polymers, as described in more detail to follow.
However, not all three of these polymeric components of the emulsifier
system are added to the emulsion batch at the same time. Two of the
three components, the anionic polymer, and one of the cationic polymers
are added to the batch prior to adding the third component. These two
components are collectively referred to herein as part A of the emulsifier
system. The third polymeric component, added at a later stage of the
emulsification process, is referred to herein as part B of the emulsifier
system. As the first step of the emulsification process, the water-phase of
the emulsion is prepared by combining in a given sequential fashion de-
ionized water, the anionic polymer of part A of the emulsifier system, and
a preservative, and subsequently homogenizing the mixture in a rotor-
stator homogenizer, for example. The next step is to add the cationic
polymer of part A of the emulsifier system, and subsequently
homogenizing the mixture under high shear. The subsequent step is to
add the thickened oil- or silicone-phase to the water-phase, while the
batch remains under agitation. Subsequently, the batch is homogenized
using high-shear agitation provided by an agitator. Once the emulsion
has formed and the composition looks uniform, part B of the emulsifier
system is added, and the emulsion is homogenized further.
[oo69] In addition to the aforementioned ingredients, the emulsion may further
contain ingredients such as one or more pH adjustment chemicals, buffering
chemicals, one or more water-phase thickener selected from non-ionic and
cationic
polymer-based thickeners, and one or more optical brightener pigments. The
amount of thickened oil- or silicone-phase in the emulsion may range from 1o
to 6o%
by weight of the final composition, but most preferably from 25 to 45%.
[0070] The concentrated emulsions of the benefit agents thus produced are
mixed or diluted with one or more detersive surfactants present either in
aqueous
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solutions or in powder/granular forms, in producing the detersive compositions
of
the present invention. The concentrated emulsions are incorporated into
surfactant-
containing aqueous compositions at levels varying from 1 to 6o % by weight of
the
final compositions. These emulsions are required to be such that the surface
charge
of the emulsion droplets is strongly cationic (as may be determined by
measuring the
zeta-potential of the emulsion droplets using a method knowm in the art -
typically,
after diluting the emulsion in DI water or in a dilute electrolyte solution to
a
suspended matter content of about o.o1 - o.1% by weight), prior to mixing the
emulsions with the detersive surfactants. In order to achieve the relatively
high
cationic charge of the emulsion droplets, the ratio of the weight of the
anionic
component to the weight of the cationic components of the emulsifier system
may
vary from 1:0.5 to 1:30, more preferably from 1:1 to 1:20, and most preferably
from
1:2 to 1:10, respectively. The ratio of the weight of the cationic polymer
comprising
part A of the emulsifier system to the weight of the cationic polymer
comprising part
B of the emulsifier system is in the range of 1:o.o1 - 1:1o, more preferably
in the
range of 1:0.05 -1:5, and most preferably in the range of 1:o.1-1:1.
Emulsifier System
[0071] As noted above, in accordance with the compositions and methods
described herein, the emulsifier system used in producing the concentrated,
cationic
emulsions of the benefit agents is comprised of three essential components:
(1) an
anionic polymer that is sufficiently surface-active for adsorption at the oil-
water
interface, and is preferably water-insoluble; (2) a medium-to-high molecular
weight,
hydrophilic, cationic polymer that is virtually insoluble (soluble less than
1.o% by
weight) in 3 weight% or higher anionic surfactant solutions; and (3) a high-to-
very
high molecular weight, hydrophilic, cationic polymer. In mixing components (1)
and
(2) to produce part A of the emulsifier system, the anionic polymer is
dissolved or
dispersed in water, prior to adding the cationic polymer (component 2). For
the
anionic polymers having weak-acid groups, for example, the phosphate and
carboxylate groups, a base is added prior to adding component (2), in order to
ensure
that these anionic groups are fully or partially dissociated, producing
anionic charge
sites on the polymer chain. Component (3) is preferably added at a later stage
of
emulsification. Although components (2) and (3) are both hydrophilic, cationic
polymers, they are preferably not interchangeable in terms of their order of
addition,
CA 02689552 2009-12-10
WO 2009/073729 PCT/US2008/085414
in order to achieve the full advantage of the compositions and methods
described
herein.
[0072] We have now found that Part A of the emulsifier system essentially
comprises a colloidally-stable particulate material having a relatively high
cationic
surface charge (as inferred from the zeta-potential of the dispersed
particles,
measured using a method known in the art), and colloidal (i.e., less than 1 -
2
micrometer) particle size (as measured, based on video microscopy, and using a
Malvern Zetasizer, Nano-ZS, particle size analyzer). Bv colloidal-stability is
meant
stability against particle aggregation or flocculation, which may be
determined using
methods (e.g., determining particle size as a function of time, stability
under large
centrifugal forces, measuring dispersion viscosity as a function of shear-
rate) knoxvn
in the art.
Component (1)
[0073] This is selected from water-soluble or water-dispersible anionic
polymers,
such as polyphosphate, polysulfonates (e.g., polyvinyl sulfonate,
lignosulfonates),
polycarboxylates (e.g. sodium polyacrylate), polysulfates (e.g., polyvinyl
sulfate), and
silicone polymers Arith a pendant anionic group selected from carboxylate,
sulfate,
and phosphate groups. The polymer is sufficiently surface-active for
adsorption at
the oil-water interface, capable of reducing the surface tension of water,
when added
at a level of 1% by weight, preferably reducing the surface tension by at
least 15%.
[0074] A preferred anionic polymer is a water-insoluble but oil-soluble,
liquid
copolymer of castor oil phosphate and 3-isocvanatomethyl-3,5,5-trimethyl
cyclohexyl
isocyanate, referred to herein as castor oil phosphate/IPDI copolymer. This
liquid
copolymer is preferred because of its relatively low solubility (2 weight% or
lower in
surfactant solutions containing 3 weight% or higher amount of surfactant) in
surfactant solutions, and because the liquid form is expected to yield less
rigid (i.e.,
softer) cationic particles used as the emulsifier in accordance with the
present
invention.
Component (2)
[0075] This is selected from hydrophilic, cationic poly-rners with a
relatively high
cationic charge content of least 6% by weight of cationic nitrogen group, and
having a
preferred molecular weight in the range of 50,000 - 6oo,ooo Dalton, more
preferably in the range of 2oo,ooo - 500,ooo Dalton, and most preferably in
the
26
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WO 2009/073729 PCT/US2008/085414
range of 300,000 -5oo,ooo Dalton. According to an important embodiment, the
polymer should be insoluble in concentrated solutions (amount at least 3% by
weight) of anionic surfactants. Insolubility is defined as soluble less than
i.o%,
preferably less than 0.5% by weight, in a 3% by weight or greater aqueous
anionic
surfactant solution. The most suitable polymer is poly(diallyldimethyl
ammonium
chloride) which will be referred to herein as Poly(DADMAC). It has a cationic
nitrogen content of about 8.67% by weight. Due to their relatively high
solubility in
concentrated surfactant solutions, examples of hydrophilic cationic polymers
which
may not be best suited to serve as component (2) of the aforementioned
emulsifier
system include copolymers of DADMAC and acrylamide monomers, also known as
polyquaternium-7, quaternized copolymers of vinylpyrrolidone and
dimethylaminomethylmethacryalte, also known as polyquaternium-11, copolymer of
vinylpyrrolidone and methacrylamidopropyltrimethylammonium chloride, also
known as polyquaternium 28, and cationic derivatives of natural polymers such
as
cellulose, starch, and guar gum. Some of these polymers, however, may be
suitable
as component (3) of the emulsifier system.
Component (g)
[0076] This is selected from high-to-very high molecular cationic polymers
having molecular weight preferably in the range of greater than 6oo,ooo
Dalton,
more preferably in the range of 2,000,000 - 6,ooo,ooo Dalton, and most
preferably
in the range of 1,ooo,ooo - 4,ooo,ooo Dalton. The cationic charge content of
these
polymers is preferably in the range of 0.1 - 4.5% by weight of cationic
nitrogen
group. Examples of such polymers include cationic copolymers of acrylamide,
and
cationic derivatives of natural polymers such as cellulose ether polymers,
guar gum,
and starch. The most preferred component (3)-polymer are the cationic
derivatives
of cellulose, guar, and starch.
[0077] The following examples will more fully illustrate the preferred
embodiments within the scope of the present invention. These examples are
solely
for the purpose of illustration and are not to be construed as limitations of
the
present invention as many variations thereof are possible without departing
from the
purview and spirit of the compositions and methods described herein.
27
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EXAMPLE I
[0078] This example shows the thickened compositions of some benefit agents
that could be used in producing the detersive compositions of the present
invention.
In producing the thickened fragrance composition (shown in Table I), the
fragrance
material(s) was first mixed writh a triglyceride, castor oil. The organoclay
was added
to this mixture in small portions, while the batch remained under mixing in a
rotor-
stator homogenizer (Silverson). Once the entire amount of the organoclay was
added, the homogenizer speed was gradually increased to about 8,ooo - Io,ooo
rpm, and the batch was homogenized until lump-free and viscous. The silicone-
and
castorlatum-based benefit agents were thickened following a procedure similar
to the
one above, except that these benefit agents were not diluted in a triglyceride
prior to
undergoing thickening. Also, once the composition appeared to be lump-free, a
polar
activator, propylene carbonate, was added, and the batch was subsequently
homogenized further until it looked uniform and viscous. The organophilic
smectite
clay used in Mix Nos. 1, 3, and 5 is an organophilic sodium bentonite clay
from
AMCOL International Corporation, while a mixture of two different organophilic
sodium bentonite clays was used in Mix No. 4.
TABLE I
Ingredient Weight %
Mix I Mix 2 Mix 3 Mix 4 Mix 5
Benefit Benefit Benefit Benefit Benefit
Agent: Agent: Agent: Agent: Agent:
Fragrance Castorlatum Silicone Silicone Silicone
Triglyceride: 48.13
Castor Oil
Fragrance 24.07
Castorlatum 72, 71
1
Dimethicone 29=35 11=58
Fluid,
6o,ooo cst
Dimethicone 15.05 15.19
Fluid,
10,000 cst
28
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WO 2009/073729 PCT/US2008/085414
Dimethicone, 22.17
5,000 cst
Dimethicone, 46.24 38.61
350 est
Dimethicone, 20.48 19.31
Gum 2
Phenyl 7.72
Trimethicone
Bentonite 15=78
Clay 3
Organophilic 27.8 25.67 14=38 1$=53
Bentonite
Clay 4
Fatty 8.61 (6.46 -
Quaternary active)
Ammonium
Compound 5
Propylene 2.9 7.76 3.71 4.25
Carbonate
1: A proprietary blend of castor oil and hydrogenated castor oil from CasChem
2: SF 76 from General Electric Silicones
3: Sodium Bentonite clay from AMCOL International Corporation
4: Organo-34 from AMCOL, Bentone 34 from Elementis
5: Q2C from Tomah products, 75% active
EXAMPLE II
[0079] This example presents the typical composition and manufacturing
procedure for the cationic emulsions of benefit agents, produced in accordance
with
the present invention. The cationic polymer for the part A of the emulsifier
system is
poly(DADMAC), Zetag 7122 (20% active), received from Ciba Specialty Chemicals.
The anionic polymer for the part A of the emulsifier system is castor oil
phosphate/IPDI copolymer, Polyphos PPI-CO, received from Alzo International
Inc..
The cationic polymer for the part B of the emulsifier system is cationic
hydroxyethyl
cellulose, Ucare Polymer JR 3oM, received from Amerchol Corporation.
29
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WO 2009/073729 PCT/US2008/085414
[oo8o] In producing the part A of the emulsifier system, the anionic polymer
(wate-insoluble) -was dispersed (resulting in a pale white-colored dispersion)
in de-
ionized water after adding a 50% solution of sodium hydroxide to the water,
using a
rotor-stator homogenizer (Silverson). Zetag 7122 was added next, slowly, while
the
batch was being homogenized at a speed of abaut 5,000 - 7,ooo rpm. Once the
addition of Zetag 7122 was complete, the batch was homogenized at a speed of
7,000
- 8,ooo rpm, while maintaining ambient temperature (2o-25oC) for the batch by
applying cooling. Typically, when the batch comprised a total weight of about
1.5 - 2
kg, based on the above ingredients, it was homogenized for a period of about
1o
minutes. During the course of this homogenization process, the dispersion
batch
exhibited a milky white appearance. Subsequently, a small amount of a
preservative,
phenonip, received from Clariant, was added to the batch, folloxving which the
batch
was homogenized for an additional 1o minutes. The resulting dispersion would
typically exhibit the follow-ing characteristics in terms of particle size: i)
when
diluted by about 2.8X with water, the dilute dispersion would filter through a
Whatman grade No. 40 filter paper under an applied suction, leaving virtually
no
solid residue on the filter paper; ii) the particle size, as measured based on
video-
microscopy or on a Malvern Zetasizer particle size analyzer would indicate
that the
particle size is in the colloidal range, i.e., less than 1- 2 micron; and iii)
the particles
are sufficiently small for to be able to resist centrifugal separation (i.e.,
virtually no
separation of the dispersed material) when the dispersion (having a Brookfield
viscosity of < 200 cps for the spindle-speed range of 1-ro rpm) is centrifuged
at
4,5oo rpm for a period of 30 minutes.
[oo81] Once the part A of the emulsifier system was produced as described
above,
the thickened benefit agent composite phase was added to the batch in small
portions, while keeping the batch under high-speed agitation using a
dispersion
blade agitator. The mixture was homogenized adequately under high-shear
agitation
to form a homogeneous emulsion. Polymer JR 30M was added next in the form of
an aqueous solution containing 2% by weight of the polymer. The emulsion was
homogenized further, following the addition of the polymer solution. The
composition for the resulting final emulsion is presented in Table II, wherein
the
Brookfield viscosity of the final emulsion is at least 1o,ooo cps at 1 rpm of
spindle
speed.
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TABLE II
Phase Ingredient Weight %
(within o.oi%)
Part A of the Emulsifier System
Water Deionized water 1.8.45
50% Sodium Hydroxide 0.12
Castrol Oil Phosphate/IPDI Copolymer o.69
Zetag 7122 (20 wt.% active) 17.00 (3.4 active)
Phenonip 0.41
Thickened Benefit Agent
Oil Thickened Benefit Agent 39.10
Part B of the Emulsifier System
Water 2 % Polymer JR-3oM Solution (2 wt.% 24.25 (0.49
active) active)
EXAMPLE III
[oo82] This example describes the composition, manufacturing procedure, and
performance properties of the detersive compositions produced in accordance
with
the preferred embodiments.
Composition
[oo83] Conditioning (i.e., 2-in-1 type) shampoos, Shampoo Nos. 1 and 2, were
manufactured using a dimethicone (silicone) emulsion prepared as per the
specifications in EXAMPLE II, wherein the thickened silicone composition
corresponds to Mix No. 5 in Table I of EXAMPLE I. The thickened silicone
compositions used in producing the dimethicone emulsions contained in Shampoo
No. 3 and in Bodywash No. 1, as per the specifications in EXAMPLE II,
correspond to
Mix Nos. 4 and 3, respectively, in Table I. Bodywash No. 2 contained a
castorlatum
emulsion produced as per the specifications in EXAMPLE II, using the thickened
castorlatum composition of Mix No. 2 in Table I.
TABLE III
Phase Ingredients Shampoo 1 Shampoo 2 Shampoo 3 Bodywash 1 Bodywash 2
A Deionized 23.150 2o.650 24.480 1.575 11.480
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Phase Ingredients Shampoo L Shampoo 2 Shampoo 3 Bodywash 1 Bodywash 2
Water
A Hydroxyethyl 10.000 (2% 10.000 (2% 8.92 (2.5% 2.000 (i% 4.400 (2.5%
Cellulosel active) active) active) active) active)
Solution
B Ammonium 35-725 35=725 35-725 33=750
Laureth-3
Sulfate (28%
active)
B Ammonium 21.425 21.425 21.425 11.250
Lauryl Sulfate
(28% active)
B Cocamidopropyl 17.420
Betaine (31%
active)
B Ammonium 47.100
Laureth-2
Sulfate (25.5%
active)
B Disodium 21.875
Laureth
Sulfosuccinate
(32% active)
C Cocamide MEA. l..ooo 1.000 1.000 3.000
(92% active)
C Ethylene Glycol 1.500 1.500 1.500 1.500 1.500
Distearate
C Ammonium 1.000 1.000 1.000 1.000
Chloride
C Sodium 1.000
Chloride
D Preservative 2 0.200 0.200 0.200 0.200 0.200
D Color Solution 0.500 0.500 1.500 1.500 0.500
D Fragrance 0.500 0.500 0.500 1.000 0.500
E Benefit Agent 5.000 (1.5% 2.500 (0.75% 3.750 (1=2% z9.25o (5% i8.ooo
32
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Phase Ingredients Shampoo 1 Shampoo 2 Shampoo 3 Bodywash 1 Bodytivash 2
Emulsion Dimethicone) Dimethicone) Dimethicone) Dimethicone) (5.15f
Castorlatum)
1: Cellosize Polymer PCG-lo from Amerchol Corporation
2: DMDM Hydantoin (Tradename: Glydant) from Lonza
Manufacturing Procedure
[0084] Combine the Phase A ingredients under gentle agitation.
[0085] Add the Phase B ingredients to the batch and start heating the batch to
about 75 - 85oC, while the batch remains under gentle agitation.
[oo86] Once the temperature reaches about 6ooC, add the Phase C ingredients
under continued gentle agitation.
[0087] Start cooling the batch, once the solids dissolve and the batch looks
uniform.
[oo88] Upon cooling the batch to about 30 - 35oC, add the phase D ingredients.
[oo89] Add phase E and continue mixing until homogeneous.
Performance Evaluation
Shampoo
[oo9o] A primary function or benefit of a hair-conditioning agent is to reduce
the
hair- combining strength, especially when the hair is wet. The silicone
deposition
efficiency of the shampoo compositions of the present invention was evaluated
by
conducting panel testing. Shampoo No. 1 of Table III was tested against a
reference
product comprising a leading commercial conditioner product that is rated by
the
manufacturer to yield a good hair-conditioning level of 5 on a scale of 1 to
1o (the
higher the number, the greater the level of conditioning). The panel testing
wTas
carried out at Cantor Research Laboratories, New York, wherein a panel of ten
panelists was convened at two different times, i.e., a total of twenty
panelists were
involved in evaluating Shampoo No. 1. The test protocol followed is as
follows. A
technical staff from Cantor Laboratories washed the panelist's hair first with
a
clarifying shampoo free of silicone and any other hair-conditioning agent, in
order to
wash off any residual hair-conditioning agent from prior use. This washing
process
33
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WO 2009/073729 PCT/US2008/085414
was repeated (typically 2-3 times) until the panelist and the technician
individually
rated the ease of combing for the wet hair at the score of 2-3 on a scale of 1-
lo (the
higher the number, the greater the ease of combing). The washed hair was dried
and
the dried hair was tested again for ease of combing individually by the
panelist and
the technician, following the same scoring protocol as noted above.
Subsequently,
the panelist's hair was split into two halves. Shampoo No. 1 was applied on
one half,
and the leading conditioner on the other half of the hair. Following complete
rinsing
of the two treated halves of the hair with water, the panelist and the
technician
evaluated the ease of combing of the wet hair using the above scoring
protocol. This
evaluation was repeated after the hair was dried. The panelist and the
technician
also rated the smoothness and the shine for the tvo halves of the dried hair.
The
composite average (averaged over all panelist scores and technician scores for
all
panelists) rating provided by the twenty panelists and the technician is
presented in
Table IV, wherein the term "enhancement" denotes the difference in score for a
conditioning property between post-clarifying shampoo and post-shampoo 1 or
post-
conditioner (i.e., Score after shampoo No. 1 treatment or the conditioner
treatment -
Score after clarifying shampoo treatment), wherein a positive value for the
"enhancement" score signifies an improvement in the hair-conditioning
property;
the higher the "enhancement" value, the greater the improvement). Following
the
panel testing method described above, the leading conditioner was tested
(involving
the same twenty panelists) also against a leading commercial conditioning (2-
in-1
type) shampoo that is rated by the manufacturer to yield deep conditioning.
Based
on certain findings, this 2-in-1 shampoo appears to resemble shampoo No. 1
considerably, in terms of levels of detersive surfactants and the conditioning
agents.
The leading 2-in-1 shampoo contains a cationic deposition polymer, cationic
hydroxyethyl cellulose. The average ratings for the two products are also
presented
in Table IV (Test 2).
TABLE IV
Enhancement Shampoo 1 Leading Leading 2- Leading
of (2-in-i type) Conditioner in-i Conditioner
Conditioning (Test i) (Test i) Shampoo (Test 2)
Property (Test 2)
34
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WO 2009/073729 PCT/US2008/085414
Wet Combing 3.25 3.15 1.38 3.5
Dry Combing 2.93 4.25 2.18 4.05
Smoothness 3.08 3.98 2.3 3.73
Shine 1.88 1.98 1.63 2.18
[oo9i.] As evident from Table IV, the conditioning shampoo, Shampoo No. 1, an
example of one embodiment of the present invention, came considerably close to
matching the hair conditioning performance of a leading conditioner. In
contrast,
the leading commercial conditioning shampoo fell much short of the leading
conditioner in providing for hair-conditioning. Based on similar panel testing
as
described above, it was also found that Shampoo No. 2 in Table III provided
slightly
better hair-conditioning, as compared to the leading commercial 2-in-1 shampoo
(containing 1.2 wt.% dimethicone plus two additional conditioning oils), even
though
Shampoo No. 2 had a significantly lower level (0.75 wt.% dimethicone) of
conditioning agent(s). Furthermore, the conditioning shampoo compositions
described herein showed good foaming properties, no worse than the .leading
commercial conditioning shampoo. The test method used for evaluating the
foaming
property involves 2oX dilution of the shampoo with water in a loo-mL graduated
centrifuge tube, under mixing in a rotary mixer for 5 minutes, followed by
noting the
volume of the resulting foam in the centrifuge tube.
Bodywash
[0092] Skin moisturization, resulting from silicone deposition on the skin
from
Bodywash No. 1 in Table III, was evaluated by measuring the trans epidermal
water
loss (TEWL) before and after treatment of the skin with the bodywash, using a
method known in the art. The panel testing (writh six panelists) involving
TEWL
measurements, was carried out at Cantor Research Laboratories, New York. In
order
to put the results into a perspective, a leading commercial bodywash that
contains
cationic hydroxyethyl cellulose, presumably as a cationic deposition polymer,
was
tested alongside Anrith Bodywash No. 1. The leading commercial bodywash
product
likely has a much higher (potentially as much as about 3X) level of a skin-
moisturizing emollient, petrolatum, as compared to Bodywash No. 1, containing
silicone as the skin-moisturizing agent. The reduction in the TEWL rate (a
sign of
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skin moisturization) was about 2.7 unit with the leading commercial bodywash,
closely followed by the 2.1 unit reduction in the TEWL rate with Bodywash No.
1.
EXAMPLE IV
[0093] This example presents the typical composition and manufacturing
procedure for the cationic emulsions of benefit agents, wherein the benefit
agents are
fragrances entrapped in a highly porous polymeric microparticle (INCI name:
methyl
methacrylate/glycol dimethylacrylate crosspolymer), available from AMCOL
International. Table V shows the typical compositions of the benefit agent-
laden oil-
phase of the emulsions.
TABLE V
Phase Ingredient Composition Composition Composition
1, Weight % 2, Weight % 3, Weight %
A Polyrneric 14=95 21=31 22.22
Microparticle
A Lavender Fragrance, 29.91
28% Fragrance Active,
(Supplier: Bell Flavor
and Fragrances)
A Lavender Fragrance, 28.41
18% Fragrance Active,
High Specific Gravity
(Supplier: Bell Flavor
and Fragrances)
A Lavendet Fragrance, 8.89
loo% Fragrance
Active (Supplier: Bell
Flavor and
Fragrances)
A Hydrogenated 17.78
36
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WO 2009/073729 PCT/US2008/085414
Polydecene
B Dimethicone Fluid, 44.48 42.61 44-44
100,000 cst
C Organophilic 8.895 6.39 5.56
Bentonite Clay
D Propylene Carbonate 1.765 1.28 1.11
Manufacturin-g Procedure
[0094] Combine the Phase A ingredients, mixing the liquid components first,
and
subsequently adding the polymeric microparticle. Mix well until lump-free or
uniform.
[0095] Add the Phase B ingredient to the batch and mix well until homogeneous.
[oo96] Add the Phase C ingredient and continue to shear the batch, until
homogeneous.
[0097] Add the Phase D ingredient and continue to shear the batch until
uniform
or viscous.
[oo98] Table VI shows the typical compositions of the emulsions, comprising
the
oil phase compositions noted in Table V, and produced using a manufacturing
procedure similar to the one described in EXAMPLE I.
TABLE VI
Phase Ingredient Emulsion Emulsion Emulsion
with Oil Phase with Oil Phase with Oil Phase
Composition Composition Composition
1, Weight % 2, Weight % 3, Weight %
A Deionized Water 10.52 16.69 18.77
A Preservative (DMDM o.o6 o.o6 o.o6
Hydantoin)
A 50% Sodium Hydroxide 0.10 0.11 0.10
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A Castrol Oil 0.59 o.64 0.57
Phosphate/IPDI
Copolymer
B Zetag 7122 (20% Active) 13.25 14.33 12.75
C Oil Phase 37=74 40=82 42=34
D 3% Cationic Guar 37=74 27=35 25-41
Solution, Jaguar C-17
(Rhodia)
[oo99] Together with a commercial liquid laundry detergent (ALL, 3X, High
Efficiency), the emulsion with oil-phase composition 1 was tested for fabric
softening
and fragrance extension (post-drying in a dryer), using a front-load washer
and
cotton towels. The test parameters are noted in Table VII.
TABLE VII
Sample Weight of Weight of Weight of Washing Drying
Towels, kg Laundry Fragrance Cycle Cycle
Detergent, Active/Wash
g load,g
Control 2.5 30 r(added as is) Normal, Normal,
Warm-cold, Medium-
High-speed heat
Spin
Test Sample 2.5 30 1 (added Normal, Normal,
- Emulsion through the Warm-cold, Medium-
with Oil- emulsion) High-speed heat
phase Spin
Composition
1
38
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WO 2009/073729 PCT/US2008/085414
[oioo] Panel testing of the washed towels for the two samples showed
significant
softening and a much higher intensity of post-dryer fragrance perception
('smell")
NAith the test sample, as compared to the control.
39
