Field of the invention
[0001] The present invention is in the field of fabric conditioners, in particular fabric
conditioners suitable for towels and sportswear.
Background of the invention
[0002] Fabric conditioners have traditionally been designed for generic fabrics, allowing
consumers to treat all fabrics with the same composition. However consumers have different
requirements for different fabrics. The needs of the consumers are not met by fabric
conditioners designed for generic fabrics.
[0003] There is a need for fabric conditioner compositions tailored for specific fabrics.
One particular group of fabrics which would benefit from specifically design product
are fabrics which are required to absorb moisture. In particular, towels and sportswear.
These fabrics would benefit from products which enhance water absorption and/or have
improved perfume performance. For towels, the enhanced water absorption would improve
their effectiveness at drying the user and improved perfume performance would cue
freshness for longer. For sportswear, improved water absorption, specifically sweat
absorption, enables the fabric to transport sweat away from the surface of the skin,
making the wearer feels drier and fresher. Improved perfume performance will mask
any unpleasant odours which are common to sportswear.
[0004] In has surprisingly been found that the compositions described herein, with fabric
softening actives comprising carbon chains from rice bran fatty acids and enriched
with C16 fatty acid chains provide enhanced water absorption and/or improved perfume
performance.
Summary of the invention
[0005] In a first aspect of the present invention is provided a fabric conditioner composition
comprising;
- a. Ester linked quaternary ammonium compounds; and
- b. 0.1 to 30 wt.% perfume materials;
wherein the ester linked quaternary ammonium compounds comprise carbon chains derived
from fatty acids; the fatty acids have an iodine value of 0 to 75; and the fatty acids
comprise non-edible rice bran fatty acids and; wherein the ester linked quaternary
ammonium compounds comprise of 35 to 65 % C16 fatty acid chains and 35 to 65 % C18
fatty acid chains, by weight of total fatty acid chains.
[0006] In a second aspect of the present invention is provided a method of improving the
water absorbency of fabric and/or the perfume performance of fabric, by treating a
fabric with ester linked quaternary ammonium compounds, wherein the ester linked quaternary
ammonium compounds comprise carbon chains derived from fatty acids; the fatty acids
have an iodine value of 0 to 75; and the fatty acids comprise non-edible rice bran
fatty acids and; wherein the ester linked quaternary ammonium compounds comprise of
35 to 65 % C16 fatty acid chains and 35 to 65 % C18 fatty acid chains, by weight of
total fatty acid chains.
[0007] In a third aspect of the present invention is provided a use of a composition as
described herein to improve the water absorbency of fabric and/or the perfume performance
of fabric.
Description
[0008] These and other aspects, features and advantages will become apparent to those of
ordinary skill in the art from a reading of the following detailed description and
the appended claims. For the avoidance of doubt, any feature of one aspect of the
present invention may be utilised in any other aspect of the invention. The word "comprising"
is intended to mean "including" but not necessarily "consisting of" or "composed of."
In other words, the listed steps or options need not be exhaustive. It is noted that
the examples given in the description below are intended to clarify the invention
and are not intended to limit the invention to those examples per se. Similarly, all
percentages are weight/weight percentages unless otherwise indicated. Except in the
operating and comparative examples, or where otherwise explicitly indicated, all numbers
in this description indicating amounts of material or conditions of reaction, physical
properties of materials and/or use are to be understood as modified by the word "about".
Numerical ranges expressed in the format "from x to y" are understood to include x
and y. When for a specific feature multiple preferred ranges are described in the
format "from x to y", it is understood that all ranges combining the different endpoints
are also contemplated.
Fabric softening active
[0009] The compositions described herein comprise esterquats (ester linked quaternary ammonium
compounds) which comprise carbon chains derived from fatty acids, the fatty acids
have an iodine value of 0 to 75; and the fatty acids comprise non-edible rice bran
fatty acids produced as a by-product in rice bran processing. In addition to the carbon
chains derived from non-edible rice bran fatty acids, the esterquats also comprise
additional C16 carbon chains.
[0010] The ester linked quaternary ammonium compounds comprise of 35 to 65 % C16 fatty acid
chains and 35 to 65 % C18 fatty acid chains, by weight of total fatty acid chains,
preferably 35 to 55 % C16 chains and 35 to 60 % C18 chains. These numbers include
both saturated and unsaturated C16 or C18 chains.
[0011] The esterquats described herein comprise rice bran fatty acids. Natural variation
will occur; however rice bran fatty acids generally have a chain length distribution
of 20 to 35 % C16 fatty acid chains, 60 to 75 % fatty acid C18 chains, by weight of
total fatty acid chains. Additional C16 fatty acid chains are added to the mix of
fatty acids to obtain the chains length distribution described herein. This provides
the benefits of enhanced water absorption and/or improved perfume performance.
[0012] Esterquats are a class of cationic surfactants mainly used in laundry applications
such as fabric softeners. Esterquats generally contain a long chain fatty acid group
linked to a quaternary ammonium group via an ester linkage. In the fabric softening
active used in the present invention, the esterquats comprise the long chain fatty
acid groups sourced from non-edible rice bran fatty acids produced as a by-product
in rice bran processing and extraction of rice bran oil.
[0013] Rice bran oil is a by-product of rice bran processing; however the oil is categorized
as an edible product. Thus, food-grade oil is often wasted for non-food purposes,
when it is hydrolysed and used for the synthesis of esterquats. Therefore, the use
of rice bran oil for the manufacture of esterquats is undesirable. However there are
other sources of fatty acids from rice bran, other than from rice bran oil (via hydrolysis),
which do not fall under the edible category. During extraction of rice bran oil, a
substantial amount of oil undergoes degradation due to enzymatic activity, forming
fatty acids in the crude rice bran oil. This crude rice bran oil is non-edible. To
make the crude rice bran oil edible, the fatty acid by-product must be removed. The
crude rice bran oil is refined by separating the fatty acids by alkali refining or
steam distillation. The resultant rice bran fatty acids generated as the by-product
of rice bran oil extraction are non-edible and hence are more favourable for the production
of products unrelated to food. As used herein, 'non-edible rice bran fatty acids'
are fatty acids produced as a by-product during the extraction and purification of
rice bran oil.
[0014] Unless stated otherwise, the abbreviation RBFA and the term "rice bran fatty acids"
refer herein to rice bran fatty acids which stem from a non-edible source, i.e. fatty
acids which result from the enzymatic degradation of rice bran oil during processing
and are separated from crude rice bran oil.
[0015] The basic chemistry involved in the synthesis of esterquats using RBFA corresponds
with the prior art involving palm oil fatty acids.
[0016] The ester-linked quaternary ammonium compound described herein comprise carbon chains
sourced from rice bran fatty acids and additional C16 carbon chains, to raise the
percentage of C16 chains. The additional C16 carbon chains may be sourced from any
source, for example animal sources such as tallow or plant sources such as palm oil,
sunflower oil, rice bran oil etc. Preferably the additional C16 chains are sourced
from a plant source, more preferably rice bran oil, most preferably rice bran fatty
acids as described herein. The C16 chains are preferably fatty acids. Most natural
sources of carbon chains, particularly fatty acids comprise a mixture of different
chain lengths. The C16 chains may need to be separated from other carbon chain lengths.
The separation process may be any suitable method, such as distillation.
[0017] Particularly preferred esterquats are ester-linked triethanolamine (TEA) quaternary
ammonium compounds comprising a mixture of mono-, di- and tri-ester linked components.
[0018] Typically, TEA-based fabric softening compounds comprise a mixture of mono, di- and
tri ester forms of the compound where the di-ester linked component comprises no more
than 70 wt.% of the fabric softening compound, preferably no more than 60 wt.% e.g.
no more than 55%, or even no more that 45% of the fabric softening compound and at
least 10 wt.% of the monoester linked component.
[0019] A first group of ester-linked quaternary ammonium compounds suitable for use in the
present invention is represented by formula (I):

wherein each R is independently selected from a C5 to C35 alkyl or alkenyl group,
preferably at least one R is a carbon chain derived from rice bran fatty acids or
a C16 chain, more preferably all R groups are a carbon chain derived from rice bran
fatty acids or a C16 chain;
[0020] R1 represents a C1 to C4 alkyl, C2 to C4 alkenyl or a C1 to C4 hydroxyalkyl group;
T may be either O-CO. (i.e. an ester group bound to R via its carbon atom), or may
alternatively be CO-O (i.e. an ester group bound to R via its oxygen atom); n is a
number selected from 1 to 4; m is a number selected from 1, 2, or 3; and X- is an
anionic counter-ion, such as a halide or alkyl sulphate, e.g. chloride or methylsulfate.
Di-esters variants of formula I (i.e. m = 2) are preferred and typically have mono-
and tri-ester analogues associated with them. Such materials are particularly suitable
for use in the present invention.
[0021] A second group of ester-linked quaternary ammonium compounds suitable for use in
the invention is represented by formula (II):

wherein each R1 group is independently selected from C1 to C4 alkyl, hydroxyalkyl
or C2 to C4 alkenyl groups; and wherein each R2 is independently selected from a C5
to C35 alkyl or alkenyl group, preferably at least one R2 is a carbon chain derived
from rice bran fatty acids or a C16 chain, more preferably all R2 groups are a carbon
chain derived from rice bran fatty acids or a C16 chain; and wherein n, T, and X-
are as defined above.
[0022] Preferably, these materials also comprise an amount of the corresponding mono-ester.
[0023] A third group of ester-linked quaternary ammonium compounds suitable for use in the
invention is represented by formula (III):
(R
1)
2-N
+-[(CH
2)
n-T-R
2]
2X
- (III)
wherein each R1 group is independently selected from C1 to C4 alkyl, or C2 to C4 alkenyl
groups; and wherein each R2 is independently selected from a C5 to C35 alkyl or alkenyl
group, preferably at least one R2 is a carbon chain derived from rice bran fatty acids
or a C16 chain, more preferably all R2 groups are a carbon chain derived from rice
bran fatty acids or a C16 chain; and n, T, and X- are as defined above.
[0024] A particular example of the fourth group of ester-linked quaternary ammonium compounds
is represented the by the formula:

[0025] A fifth group of ester-linked quaternary ammonium compounds suitable for use in the
invention are represented by formula:

[0026] R1 and R2 are each independently selected from a C5 to C35 alkyl or alkenyl group,
preferably at least one R1 or R2 is a carbon chain derived from rice bran fatty acids
or a C16 chain, more preferably both R1 and R2 groups are a carbon chain derived from
rice bran fatty acids or a C16 chain. X- is as defined above.
[0027] The iodine value of the fatty acids used in the production of the ester-linked quaternary
ammonium compound is from 0 to 75, this means that partial hydrogenation may have
occurred. Generally hydrogenation will be catalytic hydrogenation. More preferably
the iodine value is from 0 to 60, and most preferably from 0 to 45. The iodine value
may be chosen as appropriate. Essentially saturated material having an iodine value
of from 0 to 5, preferably from 0 to 1 may be used in the compositions of the invention.
Such materials are known as "hardened" quaternary ammonium compounds.
[0028] A further preferred range of iodine values is from 20 to 60, preferably 25 to 50,
more preferably from 30 to 45. A material of this type is a "soft" triethanolamine
quaternary ammonium compound, preferably triethanolamine di-alkylester methylsulfate.
Such ester-linked triethanolamine quaternary ammonium compounds comprise unsaturated
fatty chains.
[0029] If there is a mixture of ester-linked quaternary ammonium compound materials present
in the composition, the iodine value, referred to above, represents the mean iodine
value of the parent fatty acyl compounds or fatty acids of all the quaternary ammonium
materials present. Likewise, if there are any saturated ester-linked quaternary ammonium
compound materials present in the composition, the iodine value represents the mean
iodine value of the parent acyl compounds of fatty acids of all the quaternary ammonium
materials present.
[0031] A specific synthesis process for the preparation of esterquats from RBFA is described
in
WO 2020/011876.
[0032] In particular, esterquats for use in the present invention may preferably be produced
following the steps of:
- (i) esterification of a fatty acid or a mixture of fatty acids with an alkanolamine
to form an ester amine or a mixture of ester amines; and
- (ii) quaternisation of the amino group of the resultant ester amine or the amino groups
of the mixture of ester amines with a quaternising agent, preferably dimethyl sulphate,
wherein the fatty acid or mixture of fatty acids is based on a rice bran fatty acid
or a mixture of rice bran fatty acids from non-edible sources generated during refinement
of rice bran oil.
[0033] In the process, the esterification step (i) is typically carried out at temperatures
between 50 and 250 °C, preferably between 100 and 200 °C, more preferably between
130 and 180 °C. If the temperature is too low, the reaction is significantly slowed
down and thus is not applicable on an industrial scale. However, if the temperature
is too high, decomposition products occur at a high rate, thus limiting the usefulness
of the product mixture.
[0034] Preferably, the esterification step (i) is carried out under conditions in which
generated water is continuously removed from the reaction vessel. For example, water
removal may be accomplished by adding molecular sieves to the reaction mixture, by
attaching a Dean-Stark-apparatus or distillation apparatus to the reaction vessel,
or by applying vacuum to the reaction vessel. Preferably, the reaction is carried
out under vacuum or with a distillation apparatus attached.
[0035] The alkanolamine used in the process according to the invention may be any alkanolamine,
however tertiary alkanolamines are preferred. Even more preferred are trialkanolamines,
especially triethanolamine.
[0036] The rice bran oil, from the refinement from which the non-edible source of rice bran
fatty acids is generated, is not particularly limited. It is, however, desirable to
select rice bran oil that is a side product of rice bran processing. The rice bran
itself is also not limited to specific rice bran, but is preferably rice bran that
is a by-product of rice processing.
[0037] The rice bran fatty acids from non-edible sources are usually obtained as a mixture
of several fatty acids and often contain impurities that prevent the formation of
high quality esterquat composition products using conventional processes. Therefore
the rice bran fatty acids may preferably be separated and/or chemically processed
before they are subjected to the esterification step (i). Chemical processing may
include any chemical processing steps typically used for processing fatty acids, however
chemical processes for saturating unsaturated bonds are preferred. Exemplary means
of chemical processing of RBFA are halogenation, hydrohalogenation, hydroboration,
ozonolysis, Diels-Alder reactions, hydrogenation, and epoxidation. Preferred means
of chemical processing of the rice bran fatty acids from the non-edible source are
epoxidation and catalytic hydrogenation.
[0038] Separation techniques for rice bran fatty acids may include any known separation
techniques that are applicable for the separation of fatty acids from each other and/or
from further impurities. These separation techniques include, but are not limited
to crystallisation, winterisation, distillation, sublimation, filtration, chromatography
including column, flash, and high performance liquid chromatography, liquid-liquid
extraction and solid-liquid-extraction. Preferable separation techniques are crystallisation,
winterisation and/or distillation.
[0039] The molar ratio of rice bran fatty acids to alkanolamine in the esterification step
(i) is typically from 1 :2 to 3:1 , preferably 1 :1 to 3:1 , more preferably from
1 :1 to 2:1. If the ratio is too low, the resultant ester amines are formed in an
undesirably low concentration. However, if it is too high, the resultant product exceeds
the desired acidity. Accordingly, depending on the ratio and the employed alkanolamine,
the resultant ester amine or mixture of ester amines may contain monoesters, diesters,
triesters or mixtures thereof.
[0040] The quaternisation step (ii) is typically carried out at temperatures from 0 to 180
°C, preferably from 20 to 120 °C, more preferably from 50 to 100 °C. If the temperature
is too low, the reaction is significantly slowed down and thus is not applicable on
an industrial scale. However, if the temperature is too high, decomposition products
occur at a higher rate and undesired methylation of the other functional groups may
take place.
[0041] The quaternising agent in the quaternization step (ii) is not particularly limited
and may be selected, e.g. from trialkyl oxonium salts, alkyl halides, dialkyl phosphates,
dialkyl carbonates, alkyl sulphonates and dialkyl sulphates, however dialkyl sulphates
are preferred, especially dimethyl sulphate.
[0042] In the quaternization step (ii) the molar ratio between the ester amine and the quaternising
agent is typically from 2:1 to 1 :3, preferably from 1.5:1 to 1 :2, most preferably
from 1.1 :1 to 1:1.1. If the ratio is too low, the quaternisation of the ester amine
or the mixture of ester amines is not complete after the reaction is finished. If
the ratio is too high, there is a risk that other functional groups of the product
are alkylated.
[0043] Preferably, at least a part of the quaternisation step (ii), more preferably the
full quaternization step (ii) is carried out in the absence of a solvent, because
solvents may be alkylated by the quaternizing agent, which may result in increased
odour of the final product. However, one or more solvents may be added to the resultant
mixture after the quaternization is at least partially completed, preferably fully
completed. The solvent is not particularly limited, and can be selected from, e.g.
lower alcohols having from 1 to 6 carbon atoms such as ethyl alcohol, propyl alcohol,
isopropyl alcohol, etc; polyols, such as ethylene glycol, diethylene glycol, propylene
glycol, polyethylene glycol and glycerin, and they can be used alone or in a combination
thereof. Preferably the solvent added after the at least partial completion of the
quaternization step is an alcohol. Most preferably, the alcohol is ethanol or isopropanol.
[0044] The solvent may comprise further solvent components, such as aromatic hydrocarbons,
aliphatic hydrocarbons, ethers, esters, lactones, lactams, amides, amines, furans
and others. Preferably the solvent does not contain any of these further solvent components.
[0045] An example lab scale preparation of a suitable esterquat is as follows: 100 g (0.35
moles) of rice bran fatty acid obtained as a by-product from rice bran oil processing,
may be reacted with triethanolamine (34.8 g, 0.234 moles) using the catalyst hypophosphoric
acid (25 ppm) at 180°C for 6 hours under atmospheric pressure while water was continuously
removed by distillation. An intermediate (i.e. ester amine) may be cooled to room
temperature, 110 g (0.2 moles) of the ester amine may be heated to 80°C and 24.1 g
(0.191 moles) of DMS may be added over the period of 105 minutes, and the reaction
continued for an additional 10 minutes to allow DMS to react. Thereafter, 14.9 g of
ethanol may be added continuously over the period of 80 minutes and the reaction continued
for two hours at 80°C.
[0046] Preferably the fabric conditioners of the present invention comprise more than 1
wt. %, more preferably more than 2 wt. %, most preferably more than 3 wt. % ester
linked quaternary ammonium compounds as described herein by weight of the composition.
Preferably the fabric conditioners of the present invention comprise less than 40
wt. %, more preferably less than 30 wt. %, most preferably less than 20 wt. % ester
linked quaternary ammonium compounds as described herein by weight of the fabric conditioner
composition. Suitably the fabric conditioners comprise 1 to 40 wt. %, preferably 2
to 30 wt.% and more preferably 3 to 20 wt. % ester linked quaternary ammonium compounds
as described herein by weight of the composition.
[0047] The compositions described herein may include additional softening actives (in addition
to the ester linked quaternary ammonium compounds described here). Additional materials
known to soften fabrics may include; non-ester linked quaternary ammonium compounds,
silicone polymers, polysaccharides, clays, amines, fatty esters, fatty acids, dispersible
polyolefins, polymer latexes and mixtures thereof.
Perfume
[0048] The compositions as described herein comprise 0.1 to 30 wt. % perfume materials i.e.
free perfume and/or perfume microcapsules. As is known in the art, free perfumes and
perfume microcapsules provide the consumer with perfume hits at different points during
the laundry process. It is particularly preferred that the compositions of the present
invention comprise a combination of both free perfume and perfume microcapsules.
[0049] Preferably the compositions of the present invention comprise 0.5 to 30 wt.% perfume
materials, more preferably 1 to 20 wt.% perfume materials, most preferably 1 to 15
wt. % perfume materials.
[0050] Useful perfume components may include materials of both natural and synthetic origin.
They include single compounds and mixtures. Specific examples of such components may
be found in the current literature, e.g., in
Fenaroli's Handbook of Flavor Ingredients, 1975, CRC Press;
Synthetic Food Adjuncts, 1947 by M. B. Jacobs, edited by Van Nostrand; or Perfume and
Flavor Chemicals by S. Arctander 1969, Montclair, N.J. (USA). These substances are well known to the person skilled in the art of perfuming,
flavouring, and/or aromatizing consumer products.
[0051] The compositions of the present invention preferably comprise 0.5 to 20 wt.% free
perfume, more preferably 0.5 to 12 wt. % free perfume.
[0052] Particularly preferred perfume components are blooming perfume components and substantive
perfume components. Blooming perfume components are defined by a boiling point less
than 250°C and a LogP or greater than 2.5. Substantive perfume components are defined
by a boiling point greater than 250°C and a LogP greater than 2.5. Boiling point is
measured at standard pressure (760 mm Hg). Preferably a perfume composition will comprise
a mixture of blooming and substantive perfume components. The perfume composition
may comprise other perfume components.
[0053] It is commonplace for a plurality of perfume components to be present in a free oil
perfume composition. In the compositions for use in the present invention it is envisaged
that there will be three or more, preferably four or more, more preferably five or
more, most preferably six or more different perfume components. An upper limit of
300 perfume components may be applied.
[0054] The compositions of the present invention preferably comprise 0.5 to 20 wt.% perfume
microcapsules, more preferably 0.5 to 12 wt. % perfume microcapsules. The weight of
microcapsules is of the material as supplied.
[0055] When perfume components are encapsulated, suitable encapsulating materials, may comprise,
but are not limited to; aminoplasts, proteins, polyurethanes, polyacrylates, polymethacrylates,
polysaccharides, polyamides, polyolefins, gums, silicones, lipids, modified cellulose,
polyphosphate, polystyrene, polyesters or combinations thereof. Particularly preferred
materials are aminoplast microcapsules, such as melamine formaldehyde or urea formaldehyde
microcapsules.
[0056] Perfume microcapsules of the present invention can be friable microcapsules and/or
moisture activated microcapsules. By friable, it is meant that the perfume microcapsule
will rupture when a force is exerted. By moisture activated, it is meant that the
perfume is released in the presence of water. The compositions of the present invention
preferably comprise friable microcapsules. Moisture activated microcapsules may additionally
be present. Examples of a microcapsules which can be friable include aminoplast microcapsules.
[0057] Perfume components contained in a microcapsule may comprise odiferous materials and/or
pro-fragrance materials.
[0058] Particularly preferred perfume components contained in a microcapsule are blooming
perfume components and substantive perfume components. Blooming perfume components
are defined by a boiling point less than 250°C and a LogP greater than 2.5. Preferably
the encapsulated perfume compositions comprises at least 20 wt.% blooming perfume
ingredients, more preferably at least 30 wt.% and most preferably at least 40 wt.%
blooming perfume ingredients. Substantive perfume components are defined by a boiling
point greater than 250°C and a LogP greater than 2.5. Preferably the encapsulated
perfume compositions comprise at least 10 wt.% substantive perfume ingredients, more
preferably at least 20 wt.% and most preferably at least 30 wt.% substantive perfume
ingredients. Boiling point is measured at standard pressure (760 mm Hg). Preferably
a perfume composition will comprise a mixture of blooming and substantive perfume
components. The perfume composition may comprise other perfume components.
[0059] It is commonplace for a plurality of perfume components to be present in a microcapsule.
In the compositions for use in the present invention it is envisaged that there will
be three or more, preferably four or more, more preferably five or more, most preferably
six or more different perfume components in a microcapsule. An upper limit of 300
perfume components may be applied.
[0060] The microcapsules may comprise perfume components and a carrier for the perfume ingredients,
such as zeolites or cyclodextrins.
Polymeric viscosity control agents
[0061] The compositions as described herein may preferably include a polymeric viscosity
control agent. This may be particularly preferred in 'dilute' compositions. Polymeric
viscosity control agents include nonionic and cationic polymers, such as hydrophobically
modified cellulose ethers (e.g. Natrosol Plus, ex Hercules), cationically modified
starches (e.g. Softgel BDA and Softgel BD, both ex Avebe), cationic cross linked polymers.
Preferably the viscosity control agent is selected from cationic cross linked polymers.
Cationic cross-linked polymers are derivable from the polymerization of from 5 to
100 mole percent of cationic vinyl addition monomer, from 0 to 95 mole percent of
acrylamide and from 50 to 1000 ppm of a difunctional vinyl addition monomer cross-linking
agent. Preferred cationic cross-linked polymers are cross-linked copolymers of acrylamide
and methacrylate cross-linked with a difuncitonal vinyl addition monomer, such as
methylene bisacrylamide. Particularly preferred cationic cross-linked polymers are
copolymers of from about 20 percent acrylamide and about 80 percent MADAM methyl chloride
(MADAM is dimethyl amino ethyl methacrylate) cross-linked with from 450 to 600 ppm
of methylene bisacrylamide. Such materials are commercially available from SNF Floerger
under the trade names Flosoft 200 and Flosoft 222 (ex SNF Floerger).
[0062] Polymeric viscosity control agents are preferably used in amounts of from 0.7 to
2.5 wt.%, preferably from 1 to 2 wt.% of the composition.
Preservatives
[0063] The compositions as described herein preferably comprise preservatives, either a
single preservative or a combination of preservatives. The level of preservatives
is important to ensure preservation both before and after dilution of the concentrated
formulations. Two preferred classes of preservatives are organic acid and/or the salts
thereof and isothiazolinones. Examples of organic acid and/or the salts thereof are
potassium sorbate and sodium benzoate. Examples of isothiazolinones are Methylisothiazolinone
(MIT), Chloromethylisothiazolinone (CMIT) and Benzisothiazolinone (BIT). Generally
preservatives are preferably included at an inclusion level of 0.005 to 1 wt.%, more
preferably 0.01 to 0.8 wt. %. Preferred inclusion levels of organic acid and/or the
salts thereof are 0.05 to 0.8 wt.% and preferred inclusion levels of isothiazolinones
is 0.01 to 0.05 wt.%.
Other ingredients
[0064] The concentrated compositions described herein may comprise other ingredients of
fabric conditioner liquids as will be known to the person skilled in the art. Among
such materials there may be mentioned: antifoams, insect repellents, shading or hueing
dyes, anti-bacterial agents, anti-virus agents, pH buffering agents, perfume carriers,
hydrotropes, antiredeposition agents, soil-release agents, polyelectrolytes, anti-shrinking
agents, anti-wrinkle agents, anti-oxidants, dyes, colorants, sunscreens, anti-corrosion
agents, drape imparting agents, anti-static agents, sequestrants and ironing aids.
The products of the invention may contain pearlisers and/or opacifiers. A preferred
sequestrant is HEDP, an abbreviation for Etidronic acid or 1-hydroxyethane 1,1-diphosphonic
acid.
Form of the invention
[0065] The concentrated compositions described herein are aqueous compositions. The compositions
preferably comprise more than 50 wt.% water, more preferably more than 60 wt.% water.
Method and use
[0066] The fabric conditioner compositions described herein are used in the laundry process.
In ester linked quaternary ammonium compounds, wherein the ester linked quaternary
ammonium compounds comprise carbon chains derived from fatty acids; the fatty acids
have an iodine value of 0 to 75; and the fatty acids comprise non-edible rice bran
fatty acids and; wherein the ester linked quaternary ammonium compounds comprise of
35 to 65 % C16 fatty acid chains and 35 to 65 % C18 fatty acid chains, by weight of
total fatty acid chains, can be used in a method of improving the water absorbency
of fabric and/or the perfume performance of fabric.
[0067] Preferably the compositions are used to treat towels or sportswear, particularly
sportswear made from synthetic fabrics. Examples of synthetic fibres are polyester,
nylon, polyvinyl chloride (PVC), spandex/lycra/elastane and acrylic fibres. A fabric
comprising synthetic fibres preferably comprises 20 wt.% to 100 wt.% synthetic fibres,
more preferably 40 wt.% to 100 wt.% synthetic fibres, more preferably 60 wt.% to 100
wt.% synthetic fibres and most preferably 80 wt.% to 100 wt.% synthetic fibres by
weight of the fabric.
[0068] Preferably the synthetic fabric comprises 20 wt.% to 100 wt.% polyester, more preferably
40 wt.% to 100 wt.% polyester, more preferably 60 wt.% to 100 wt.% polyester and most
preferably 80 wt.% to 100 wt.% polyester by weight of the fabric.
[0069] Preferably the sportswear comprises only synthetic fibres (i.e. 100% synthetic fibres),
most preferably the fabric comprises 100 % polyester.
[0070] In one aspect of the present invention, clothes are treated with the fabric conditioner
composition. The treatment is preferably during the washing process. This may be hand
washing or machine washing. Preferable the fabric conditioner is used in the rinse
stage of the washing process.
[0071] Preferably the clothes are treated with a 10 to 100 ml dose of fabric conditioner
for a 4 to 7 kg load of clothes. More preferably, 10 to 80 ml for a a 4 to 7 kg load
of clothes.
Use
[0072] The fabric conditioner compositions described herein may be used to improve the water
absorbency of fabric and/or the perfume performance of fabric. In particular the fabric
conditioners may be used to treat towels or synthetic fabrics as described above.
Examples:
[0073]
Table 1: Example composition
Ingredient |
wt. % Composition |
Concentrate |
Regular |
Dilute |
Fabric Softening active1 |
20 |
9 |
4 |
Fatty alcohol |
- |
- |
0.5 |
Nonionic surfactant |
- |
1.5 |
0.01 |
Cationic polymer2 |
0.2 |
0.2 |
0.2 |
Perfume |
2.0 |
0.8 |
0.3 |
Microcapsule |
2.5 |
0.5 |
- |
Silicone Antifoam |
0.05 |
0.05 |
0.1 |
Preservative |
0.7 |
0.7 |
0.7 |
Mirrors, dyes, pH regulators, etc. |
< 1 wt.% |
< 1 wt.% |
< 1 wt.% |
Water |
To 100 |
To 100 |
To 100 |
Fabric Softening active1 - Comprising rice bran fatty acids as prepared according to WO 2020/011876 and additional C16 fatty acids from rice bran oil.
Cationic polymer2 - Flosoft 270LS ex. SNF |
[0074] The example compositions may be produced using the following method: Pre-melt the
fabric softening active at a temperature of ∼65°C. Separately heat the water to ∼45°C
and add antifoam, preservative and some minors. Slowly add the pre-melt with stirring.
Add any remaining ingredients and slowly cool.