Field of the Invention
[0001] This invention relates to aqueous liquid detergent compositions and particularly
to dishwashing compositions incorporating a mixture of anionic, ethoxylated nonionic
and zwitterionic surfactants.
Background of the Invention
[0002] Liquid detergent compositions intended for use as dishwashing products conventionally
take the form of clear aqueous solutions containing a mixture of one or more sulphate
and sulphonate anionic surfactants together with a suds stabilising agent. Recently
there has been a trend towards the use of magnesium cations for at least part of the
anionic surfactants present, typified by the disclosures of British Patent Specifications
Nos. 1,524,441 and 1,551,074, British published Patent Application No. 2,010,893 A
and European Patent Application Publication No. 0039110. The art teaches that these
formulations have enhanced performance, particularly when used in water of low mineral
hardness. Nevertheless, the pressure to improve the cost-effectiveness of liquid detergent
compositions has meant that the search has continued for compositions having improved
economy, performance and in-use characteristics. In particular, intensive effort has
been expanded in increasing the concentration of dishwashing liquid detergent compositions
and in reducing the level of non- performing ingredients such as solvents and solubilising
hydrotropes without sacrificing the storage stability of the compositions.
[0003] Ethoxylated nonionic surfactants constitute a class of . materials capable of solubilising
other components in aqueous media but this capability is strongly dependent on their
average degree of ethoxylation (E
av). Highly ethoxylated nonionic surfactants, (i.e. E
av >20), are'very hydrophilic in nature and thus tend to reduce the oily soil removal
capability of liquid dishwashing detergent formulations, which is undesirable where
oil and grease removal is an important criterion of consumer acceptance. On the other
hand, nonionic surfactants having low levels of ethoxylation (i.e. E
av ≼2) are relatively hydrophobic and have a limited ability to form homogeneous solutions
with other components in the absence of other surfactant species.
[0004] A feature shared by all ethoxylated nonionic surfactants is the presence of a level
of unethoxylated material, the magnitude of which depends on the degree of ethoxylation,
but which can constitute up to 20% by weight of the nonionic surfactant.
[0005] Unethoxylated C
6-C
13 aliphatic primary alcohols are odorous materials having a low water solubility, and
these characteristics are discernible in the ethoxylated alcohols to an extent which
depends on the level of ethoxylation, the effect diminishing as E
av increases.
[0006] Liquid dishwashing detergent compositions containing alkyl sulphates and/or alkyl
benzene sulphonates have been found to be particularly subject to odour and storage
stability problems when formulated with ethoxylated nonionic surfactants containing
the normal spread of ethoxylated species, and this effect is tore pronounced when
the composition also contains magnesium ions. However, the Applicants have established
that certain alcohol ethoxylates, containing less than a defined amount of unethoxylated
species, and from which preferably at least part of the mono-ethoxylated species has
been removed, can be incorporated in alkyl benzene sulphonate- or alkyl sulphate-containing
liquid dishwashing detergent compositions without adverse effect on the storage stability
of the latter. The Applicants' copending European Application No. 84303044.6 publication
No. 0125854 relates to liquid dishwashing detergent compositions of this type.
[0007] Zwitterionic surfactants are also known components of detergent compositions particularly
in combination with other surfactant species. Disclosures of compositions of this
type are provided by European Patent Application Publication No. 0036625 and UK Patent
Application No. 2103236A, both of which relate to liquid detergent compositions containing
mixtures of alkyl ethoxy sulphates in combination with other anionic surfactants and
a surface active betaine. Another disclosure is provided by Thiele et al USP 3,634,266
which describes an amylase-containing liquid detergent composition in which the surfactant
system comprises a mixture of alkyl ethoxy sulphate, ethoxylated nonionic and sulphobetaine
species.
[0008] Nevertheless, it appears that the efficacy of a zwitterionic detergent in providing
enhanced grease and particulate soil removal performance is a function not only of
the structure of the zwitterionic surfactant itself, but also of the detergent composition
into which it is blended. In particular, it has been found that zwitterionic surfactants
that give a suds mileage benefit and/or acceptable greasy soil redeposition performance
in one detergent matrix do not give a similar benefit over the same range of usage
conditions in other matrices.
[0009] The Applicants have now made the discovery that certain narrowly defined classes
of betaines provide an unexpected improvement in the soil handling capability of the
compositions of the general type disclosed in the previously mentioned European Application
No. 0125854.
[0010] Accordingly in the present invention there is provided a physically stable enzyme-free
liquid detergent composition comprising from 22% to 65% by weight of a surfactant
system composed of a mixture of anionic, nonionic & zwitterionic surfactants in an
organic solubiliser/hydrotrope-water medium wherein
i) the anionic surfactant comprises in combination
a) from 4% to 20% by weight of the composition of a primary C10-C16 alkyl sulphate;
b) from 5% to 20% by weight of the composition of a C10-C16 linear alkyl benzene sulphonate;
c) from 5% to 24% by weight of the composition of a C10-C16 alkyl ethoxysulphate containing an average of up to 6 moles of ethylene oxide per
mole of ethoxysulphate;
wherein, in said anionic surfactant combination, the cations include magnesium ion
in a molar amount corresponding to from 35% to 65% of the molar amount of alkyl sulphate
present in the combination;
ii) the nonionic surfactant comprises from 1% to 10% by weight of the composition
of an ethoxylated C6-C13 aliphatic alcohol containing an average of from 1.5 to 25 moles of ethylene oxide
per mole of alcohol, said ethoxylated alcohol containing not more than 1% by weight
of unethoxylated alcohol where the alcohol contains an average of less than 9 moles
of ethylene oxide and not more than 2% by weight of unethoxylated alcohol where the
ethoxylated alcohol containing an average of from 9 to 25 moles of ethylene oxide
per mole of alcohol;
iii) the zwitterionic surfactant comprises from 0.25% to 10% by weight of the composition
of a compound of the general formula

wherein


R3 is a -(CH2)3 group or a

group
Y is

n & m are O or 1
X is CH2COO- or SO3;
provided that where X is CH
2COO
- m is 0 and where X is SO
- 3 m is 1.
[0011] Preferably, in the zwitterionic surfactant, R
1 is C
10-C
16 alkyl, R
2 is methyl and n is 0 and more preferably the zwitterionic surfactant is a C
12-C
14 alkyl betaine, present in an amount of from 0.5% to 5%, most preferably in an amount
of from 1.0% to 2.5% by weight of the composition
[0012] Preferably the ethoxylated aliphatic alcohol has an HLB in the range from 8.0 to
17.0 more preferably from 11.0 to 17.0, and most preferably from 11.0 to 15.0. Preferred
compositions in accordance with the invention contain from 3 to 5% of a C
9-C
11 primary alcohol condensed with an average of from 6 to 10 moles of ethylene 5 oxide
per mole of alcohol. Preferably, the ethoxylated aliphatic alcohol contains less than
0.7%, most preferably less than 0.5% of unethoxylated material, and in highly preferred
compositions the level of mono-ethoxylated C
9-C
11 alcohol is no more than 5% by weight of the nonionic surfactant.
[0013] one useful group of compositions incorporates a three component anionic surfactant
system, comprising 6-12% by weight of the composition of C
10-C
16 primary alkyl sulphate, 6-14% of a C
10-C
16 primary alkyl ethoxysulphate containing an average of from 1.5 to 3 ethoxy groups
per alkyl group, and 5-15% of a C
10-C
16 alkyl benzene sulphonate. The cations in this system are a mixture of ammonium and
magnesium ions, the level of magnesium corresponding to approximately one half of
the molar amount of alkyl sulphate present.
[0014] Highly preferred compositions in accordance with the invention incorporate an anionic
surfactant system containing from 15 to 20% by weight of the composition of a primary
C
12-C
14 alkyl ethox
y sulphate stock containing an average of from 0.8 to 2.0 ethylene oxide groups per
mole of C
12-C
14 alkyl ethoxy sulphate, this alkyl ethoxy sulphate stock also including from 6 to
10%, by weight of the composition, of C
12-C
14 alkyl sulphate, together with from 5 to 10% by weight of the composition of a C
11.
8 linear alkyl benzene sulphonate component.
[0015] Preferably compositions in accordance with the invention also contain 2%-8%, most
preferably 3%-4% by weight of a suds booster selected from C10-C16 alkyl mono or di-C
2-C
3 alkanolamide.
Description of the Invention
[0016] Detergent compositions in accordance with the present invention comprise a mixture
of anionic surfactants of defined constitution, in an amount of from 22% to 65% by
weight of the composition, together with from 1% to 10% by weight of an ethoxylated
nonionic surfactant having a low content of unethoxylated material and from 0.25%
to 10% by weight of a zwitterionic surfactant of defined structure.
[0017] All compositions in accordance with the invention incorporate an alkyl sulphate and
an alkyl benzene sulphonate component in combination with an alkyl ethoxy sulphate.
[0018] The alkyl sulphate component is a primary alkyl sulphate in which the alkyl group
contains 10-16 carbon atoms, more preferably an average of 12-14 carbon atoms preferably
in a linear chain. C
10-C
16 alcohols, derived from natural fats or
Ziegler olefin build-up or OXO synthesis, form suitable sources for the alkyl group.
Examples of synthetically derived materials include
Dobanol 23 (RT
M) sold by Shell Chemicals (UK) Ltd, Ethyl 24 sold by the Ethyl Corporation, a blend
of C
13-C
15 alcohols in the ratio 67% C
13' 33% C
15 sold under the trade name Lutensol by BASF GmbH and Synperonic (RTM) by ICI Ltd,
and Lial 125 sold by Liquichimica Italiana. Examples of naturally occurring materials
from which the alcohols can be derived are coconut oil and palm kernel oil and the
corresponding fatty acids.
[0019] When present in compositions in accordance with the invention, the level of the alkyl
sulphate component lies in the range of from 4% to 20% by weight of the composition,
more generally from 4% to 16% by weight. Preferably the usage level lies in the range
from 6% to 12% by weight, most preferably in the range from 6% to 10% by weight.
[0020] For the purposes of the present invention, the alkyl sulphate is associated with
a source of magnesium ions which, as will be described hereinafter, can either be
introduced as the oxide or hydroxide to neutralise the acid or can be added to the
composition as a water soluble salt. However the addition of appreciable levels of
magnesium salts to the dishwashing compositions of the invention raises the temperature
at which inorganic salt crystals form in the compositions on cooling and is therefore
less preferable.
[0021] The molar amount of magnesium ion in the compositions is controlled to correspond
to 0.35-0.65X, preferably 0.45-0.55X where X is the number of moles of C
10-C
16 alkyl sulphate present. Most preferably the magnesium ion content is adjusted to
provide the stoichiometric equivalent i.e. half the molar amount of the alkyl sulphate
present. In practice the magnesium ion will be present at a level of fran about 0.15%
to about 0.70% by weight, preferably from 0.25% to 0.45% by weight of the composition.
[0022] Alkyl benzene sulphonates useful in compositions of the present invention are those
in which the alkyl group, which is substantially linear, contains 10-16 carbon atoms,
preferably 11-13 carbon atoms, a material with an average carbon chain length of 11.8
being most preferred. The phenyl isomer distribution, i.e. the point of attachment
of the alkyl chain to the benzene nucleus, is not critical, but alkyl benzenes having
a high 2-phenyl isomer content are preferred. When employed in compositions in accordance
with the present invention, an alkylbenzene sulphonate content of from 5% to 20% by
weight of the composition is required generally from 5% to 15% by weight. In a preferred
aspect of the invention an alkylbenzene sulphonate content of from 5% to 10% by weight
is used and highly preferred compositions in accordance with this aspect of the invention
have from 6% to 8% of C11.8 alkyl benzene sulphonate.
[0023] The alkyl ethoxy sulphate surfactant component comprises a primary alkyl ethoxy sulphate
derived from the condensation product of a C
10-C
16 alcohol with an average of up to 6 ethylene oxide groups. The C
10-C
16 alcohol itself can be obtained from any of the sources previously described for the
alkyl sulphate component. It has, however, been found preferable to use alkyl sulphates
and alkyl ether sulphates in which the carbon chain length distributions are the same.
C12-C13 alkyl ether sulphates are preferred and the level of alkyl ethoxy sulphate
in the composition lies between 5% and 24% by weight of the compositions, generally
in the range from 6% to 14% by weight. In the preferred compositions, the level lies
in the range from 6% to 12% by weight, most preferably in the range from 8% to 12%
by weight.
[0024] Conventional base-catalysed ethoxylation processes to produce an average degree of
ethoxylation of 6 result in a distribution of individual ethoxylates ranging from
1 to 15 ethoxy groups per mole of alcohol, so that the desired average can be obtained
in a variety of ways. Blends can be made of material having different degrees of ethoxylatior.
and/or different ethoxylate distributions arising from the specific ethoxylation techniques
employed and subsequent processifg steps such as distillation. For example, it has
been found that equivalent sudsing and grease removal performance to that given by
a blend of alkyl sulphate and alkyl triethoxy ether sulphate can be obtained by reducing
the level of alkyl sulphate and using an alkyl ether sulphate with an average of approximately
two ethoxy groups per mole of alcohol. In preferred compositions in accordance with
the present invention the average degree of ethoxylation is from 0.5 to 4, more preferably
from 0.8 to 2.0. When an alkyl ether sulphate stock of low ethoxylation level is employed
as a means of incorporating both the alkyl sulphate and alkyl ether sulphate components,
the level of its usage in the composition is from 10% to 25% by weight, more preferably
from 15% to 20% by weight.
[0025] The counter ion for the alkyl ethoxy sulphate component can be any one of sodium,
potassium, ammonium or alkanol-ammonium or a mixture thereof. However, where it is
desirable to achieve a low chill point temperature, (the temperature at which inorganic
salt crystals separate), a significant proportion (e.g. 30%) of the counter ions for
the alkyl ethoxy sulphate component should be ammonium and in order to achieve the
lowest possible chill point temperatures the alkyl ethoxy sulphate should be completely
neutralized by ammonium ions.
[0026] The counter ions in association with the alkyl benzene sulphonate are independently
selected in the same manner as those for the alkyl ethoxy sulphate. In order for compositions
in accordance with the invention to have a chill point of 4 0°C, at least 70% of the
neutralising cations for the anionic surfactants should be ammonium ions.
[0027] The ethoxylated nonionic surfactant component of the invention is a C6-C13 aliphatic
alcohol ethoxylate containing an average of from 1.5 to 25, more preferably from 2
to 15 and most preferably from 6 to 10 moles of ethylene oxide per mole of alcohol.
The aliphatic alcohol ethoxylate contains not more than 1% by weight of unethoxylated
alcohol where the ethoxylated alcohol contains an average of less than 9 moles of
ethylene oxide and not more than 2% by weight of unethoxylated alcohol where the ethoxylated
alcohol contains an average of from 9 to 25 moles of ethylene oxide per mole of alcohol.
[0028] The starting alcohol may be a primary alcohol or secondary but is preferably a primary
alcohol which may be derived from natural or synthetic sources. Thus natural fats
or oils, or products of Ziegler olefin build up reactions or OXO synthesis may all
be used as the source of the hydrocarbon chain, the structure of which may be linear
or branched in type.
[0029] The preferred alcohol chain length range is from C
9 to c
11 as it has been found that the sudsing volume and mileage performance of compositions
in accordance with the invention is optimum when incorporating ethoxylates made from
such alcohols. It is also desirable for performance reasons that the hydrophilic-lipophilic
balance (H
LB) of the ethoxylated alcohol is in the range from 8.0 to 17.0, more preferably from
11.0 to 17.0 and most preferably from 11.0 to 15.0.
[0030] As discussed with respect to the alkyl ethoxy sulfate component, the normal (base
catalysed) ethoxylation process to produce an average degree of ethoxylation of 6
results in a distribution of ethoxylate species which ranges from 1 to 15 moles of
ethylene oxide per mole of alcohol. An increase in E
av causes some change in this distribution, principally a reduction in the level of
unethoxylated material, but an increase in E
av from 3 to 5 will still leave approximately 5-10% of such material in the ethoxylated
product.
[0031] In the liquid dishwashing detergent compositions of the invention, this level of
unethoxylated material will give rise to phase stability/chill point problems and/or
will result in a product having a fatty alcohol odour which is unacceptable to consumers
and cannot be masked by conventional deterqent perfumes. It has been found that the
maximum level of unethoxylated alcohol that can be tolerated in the ethoxylated alcohol
component is 1% by weight. More preferably the unethoxylated alcohol level is not
more than 0.7% and most preferably is less than 0.5% by weight of the ethoxylated
alcohol component. Distillation under vacuum is employed to remove the undesired material
and this also removes a portion of the monoethoxylate fraction, thereby increasing
the E
av of the remaining material. In preferred embodiments of the invention the level of
monoethoxylate is not more than 5% by weight of the ethoxylated alcohol.
[0032] The level of usage of the ethoxylated alcohol conponent in compositions of the invention
is from 1% to 10% by weight more preferably from 2 to 6% by weight and most preferably
from 3% to 5% by weight. Liquid dishwashing detergent compositions in accordance with
the invention and incorporating from 3% to 5% by weight of a primary alcohol containing
from 9 to 11 carbon atoms condensed with an average of from 5 to 10 moles ethylene
oxide per mole of alcohol to give an HLB value in the range of from 12 to 15,the alcohol
ethoxylate containing <0.5% by weight of unethoxylated alcohol, display chill points
< 0°
C together with enhanced sudsing and mileage performance relative to compositions not
in accordance with the invention.
[0033] The third component of the compositions of the invention is a zwitterionic surfactant,
present in an amount of from 0.25% to 10%, more preferably from 0.5% to 5% and most
preferably from 1% to 2.5% by weight of the compositions.
[0034] The zwitterionic surfactant has the general formula:

wherein R
1 is C
10-C
16 alkyl
R2 is Ci-C3 alkyl
R3 is a -(CE2)3 group or a

group
Y is

n & m are 0 or 1
X- is CH2COO- or SO- 3;
provided that where X is CH
2OOO
- m is 0 and where X" is SO
- 3 m is
1.
[0035] More preferably R
1 has an average carbon chain length of from 12 to 14 carbon atoms and may be derived
from synthetic sources, in which case the chain may incorporate some branching, or
from natural fats and oils, in which case the chains are linear and may include minor
amounts of C
8-C
10 and C
14-C
18 moieties. Synthetic sources for the R
1 group may be the same as those mentioned previously for the alkyl group in the alkyl
sulphate component.
[0036] Whilst compositions incorporating the C
12-C
14 amido betaine and C
12-C
14 sulpho betaine display the benefits of the invention, the most preferred compositions
utilise a C
12-C
14 alkyl betaine as the zwitterionic surfactant component, the C
12-C
14 alkyl group being derived from a coconut or palm kernel oil feedstock.
[0037] A highly preferred optional ingredient of the composition according to the invention
is a suds-promoting agent present at a level of from 2% to 8% by weight of the composition,
preferably from 3% to 6% and most preferably 3%-4%.
[0038] The suds-promoting agent is normally a C
10-C
16 alkyl mono- or di-C
2-C
3 alkanolamide, examples including coconut alkyl monoethanolamide, coconut alkyl diethanolamide
and palm kernel and coconut alkyl mono-and di-isopropanol amides. The palm kernel
or coconut alkyl residue may either be 'whole cut', including the C
IO and C
16 fractions or may be the so-called 'narrow-cut' C
12-C
14 fraction. Synthetic sources of the C
10-C
16 alkyl group can also be used.
[0039] The balance of the formula comprises a hydrotrope-water system in which the hydrotrope
may be urea, a C
I-C
3 aliphatic alcohol, a lower alkyl or dialkyl benzene sulphonate salt such as toluene
sulphonate, xylene sulphonate, or cumene sulphonate, or mixtures of any of these.
Normally a single hydrotrope will be adequate to provide the required phase stability,
but compositions in accordance with the present invention preferably employ a mixture
such as urea-alcohol-water, alcohol-lower alkyl benzene sulphonate-water or urea-lower
alkyl benzene sulphonate-water in order to achieve the desired viscosity, and to remain
stable and easily pourable. For compositions having an organic active concentration
less than about 40% by weight, the preferred alcoholic hydrotrope is ethanol which
is employed at from 3% to 10% by weight of the composition, preferably at from 4%
to 8%, usually in admixture with urea. For compositions having an organic active concentration
greater than about 40% by weight, mixtures of ethanol with urea and/or lower alkyl
benzene sulphonate are preferred. Mixtures of hydrotropes can, of course, be employed
for cost effectiveness reasons irrespective of any stability/viscosity considerations.
[0040] Optional ingredients of the liquid detergent compositions of the invention include
opacifiers such as ethylene glycol distearate, thickeners such as guar gum, antibacterial
agents such as glutaraldehyde and
Bronopol (
RT
M), antitarnish agents such as benzoxytriazole, heavy metal chelating agents such as
ETDA or ETDMP, perfumes and dyes. The pH of the compositions may be anywhere within
the range 6-7.5 but as manufactured the compositions normally have a pH in the range
6.6-7.3 and are subjected to a final pH trimming operation to obtain the desired finished
product pH. For coloured products the pH preferably lies in the range 6.5-6.9 in order
to maintain colour stability.
[0041] The compositions of the invention can be made in a number of ways but it is preferred
that the zwitterionic surfactant is incorporated towards the end of the making process
if not actually forming the last ingredient to be added. This minimises the risk of
any degradation of the zwitterionic surfactant under the acid conditions existing
at the beginning of the making process and also facilitates the control of the viscosity
of the finished product.
[0042] Thus, individual anionic surfactants can be made as aqueous solutions of alkali metal
or ammonium salts which are then mixed together with the ethoxylated nonionic surfactant,
followed by the suds booster and the hydrotrope, after which any magnesium ion can
be introduced as a water soluble salt such as the chloride or sulphate. The zwitterionic
surfactant and any optional minor ingredients are then added at the same time as the
pH and viscosity are adjusted. This method has the advantage of utilising conventional
techniques and equipment but does result in the introduction of additional chloride
or sulphate ions which can increase the chill point temperature (the temperature at
which inorganic salts precipitate as crystals in the liquid).
[0043] In order to simplify the making process the alcohol and alcohol ethoxylate can be
mixed together and a single sulphation and neutralisation can then be carried out
on these two materials. For this, the alcohol and alcohol ethoxylate should be mixed
in a weight ratio lying in the range 4:3 to 1:6. In the most preferred technique however,
a single alcohol ethoxylate stock is produced in which the levels of alcohol and ethoxylated
alcohol species are controlled to provide the desired ratio of these starting materials.
[0044] Sulf(on)ation of the alcohol, alcohol ethoxylate and alkyl benzene
qpn employ any of the conventional sulph(on)ating agents such as sulphur trioxide or
chlorosulphonic acid. Neutralisation of the alkyl ether sulphuric acid and the alkyl
sulphuric acid is then carried out with the appropriate alkali or with a magnesium
oxide or hydroxide slurry which avoids the addition of chloride or sulphate ions.
[0045] In one variant of this technique the alkyl benzene sulphonic acid is added to a neutralising
medium, comprising ammonium hydroxide in an ethanol-water solution, to which the ethoxylated
nonionic surfactant has also been added. This paste then forms a 'heel' to which the
suds booster and a magnesium hydroxide slurry are added followed by the mixed alkyl
sulphuric and alkyl ether sulphuric acids. The neutralisation of the alkyl sulphate
and alkyl ether sulphate actives is carried out to a pH<4 in order to ensure dissolution
of the magnesium hydroxide, after which the pH is adjusted to the finished product
pH of 6.6-7.3 and the minor ingredients (colour, perfume, bactericides etc.) are added
before the zwitterionic component is blended and final adjustment of the viscosity
is carried out.
[0046] A further and preferred variation involves the neutralisation of the mixed alkyl
sulphuric and alkyl ether sulphuric acids in the alcoholic ammonia solution and the
use of this paste, at a surfactant concentration of from 40 to 60% by weight and a
pH of from 7 to 8, as the 'heel' to which the monoethanolamide suds booster, magnesium
hydroxide slurry and alkyl benzene sulphonic acid are added. The pH of the system
after the sulphonic acid is added must be in the range of from 2 to 4 to ensure complete
dissolution of the magnesium hydroxide. The minor ingredient addition, pH trimming,
zwitterionic surfactant incorporation and viscosity adjustment are as before.
[0047] Preferred compositions in accordance with the invention are dear single phase liquids,
but the invention also embraces opaque products containing dispersed phases provided
that such products are physically stable (i.e., do not separate) on storage.
[0048] The invention is illustrated in the following non-limitative examples in which all
parts and percentages are by weight unless otherwise specified.

[0049] In the preparation of Compositions A-D, a mixture of alcohol and alcohol ethoxylate
was sulphated using so
3-air sulphation, and was then neutralised to a solution pH of 4 in an alcoholic ammonium
hydroxide solution to which magnesium hydroxide had been added in an amount corresponding
to half the molar quantity of alkyl sulphate present. After dissolution of the magnesium
hydroxide, ammonia was added to form a neutralising solution for the alkyl benzene
sulphonic acid. A separate sulphonation of the alkyl benzene was employed to produce
the alkyl benzene sulphonic acid which was added to the alkaline solution of the other
actives and neutralised with the excess ammonia to pH 7. The monoethanolamide and,
where present, the betaine were then added before final pH trimming to pH 6.8. The
chill point of Composition A was -5°C. Compositions incorporating ethoxylated nonionic
surfactant (i.e. E-H) were prepared in a similar manner except that the ethoxylated
nonionic surfactant was added during the final pH trimming operation.
[0050] A comparison of the suds mileage of the compositions under identical test conditions
was made using a prepared particulate soil and a prepared grease soil in the mechanical
sudsing test method described.
Test Conditions
[0051] Product Concentration 0.12% Water Temperature 47°C Water Hardness 2°H and 18°H
Particulate soil
[0052] Soil : Cake Mix / Mixed free fatty acids (MFFA) The Cake Mix is McDougall's Sponge
Mix The free fatty acids comprise 2 parts oleic acid 2 parts linoleic acid 1 part
stearic acid 2.5 parts palmitic acid 367 parts corn oil to give 2% MFFA mixture.
Grease soil
[0053] 6 parts palmitic acid 94 parts corn oil to give 6% FA soil Test Method
[0054] The method uses 4 cylinders of length 30 cm and diameter 10 cm fixed side by side,
and rotatable at a speed of 24 rpm about a central axis. Each cylinder is charged
with 500 mls of product solution at a concentration of 0.12% and a temperature of
47°C. The outer two cylinders are used for one of the products being compared and
the inner two for the other product.
[0055] The cylinders are rotated for 2 minutes, stopped, the initial suds are measured and
a soil load is then added. In the particulate soil test all of the Cake Mix soil (5g)
is added together at this stage with 1 ml of the 2% MFFA. In the grease soil test
1 ml of the 6% FA soil alone is added. After 1 minute the cylinders are restarted
and allowed to rotate for 1 minute. The suds height is noted and 1 ml of the 2% MFFA
or 6% FA (depending on the test) is added to each cylinder. After 1 minute the cylinders
are restarted. This process continues until the suds height in the cylinder is lower
than 0.3 cms.
[0056] One product is designated as the control and suds mileage figures are calculated
for the other product versus the 'control' product on the following basis.

[0057] The results of various mileage comparisons were as follows;
1) Comparison of compositions A-D using composition A as control (i.e. 100%):

2) Comparison of compositions A, C and E-H using composition E as control (i.e. 100%):

[0058] A comparison of the performance of compositions A-D shows that little, if any, benefit
is obtained from increasing zwitterionic level above 1.5% by weight of the composition.
[0059] It can be seen that in a comparison of the mileage performance of compositions A,
C, E and F, the addition of 1.5% betaine to composition A to form composition C does
not produce as great an overall mileage benefit as does the addition of 4.7% alcohol
to composition A to form composition E. Addition of betaine to composition E to form
composition F provides, overall, a greater benefit than that arising from adding betaine
to composition A to form composition C. Comparison of the mileage performance of compositions
E-H show that whilst both the amido betaine-containing composition F and the sulphobetaine
containing composition G both show significant advantages over the base composition
E, the alkyl betaine-containing composition H is much superior to the other two.
EXAMPLE 2
[0060] Products were made using the process of Example 1 having the following compositions:-
1 Associated with a mixture of Magnesium and Ammonium ions, the amount of magnesium
corresponding to half the molar level of alkyl sulphate present
2 A predominantly linear C9-C11 alcohol blend containing an average of 10 ethylene oxide units per mole of alcohol,
and containing less than 2% by weight of unethoxylated alcohol.
3 A Coconut alkyl betaine in which 95% by weight of alkyl groups comprise C12 or C14 radicals.
4 5% Ethanol 4% urea.
[0061] The performance of the above products was then assessed using the test methods identified
below:-
1. Grease Cutting 8.5 cm dia metal dishes each containing 5 ml of solidified household
fat (Mpt 45°C), as a uniform thickness layer, were suspended in a 0.12% solution of
each product at 45°C for 30 minutes. The fat released by each product solution was
collected via an inverted funnel immersed in the solution and overlying the dish.
The weight of the fat released and collected was measured. Tests were carried out
in both 2°H and 18°H water and the average of the measured fat weight in the two water
hardnesses calculated for each product. This was then compared to that released by
the standard product I and expressed as an Index Value relative to product I at 100.
2. Grease redeposition Clean ceramic slides were dipped into product solutions comprising
500 mls of 0.12% wt concentration in 2°H and 18°H water containing 5 mls household
fat soil which had been mixed at 45°C for 2 minutes. The slides were withdrawn and
compared and graded visually by an expert panel. The results were recorded in terms
of panel score units of a Scheffe scale and the average of the results for each product
in the two water hardnesses were expressed as better than, or poorer than, the standard
product I.
3. Initial Suds A model test was employed in which product solutions of 0.12% concentration
at 45°C with no soil present were subjected to impact by pouring 4.5 litres of water
at 45°C on to the solution from a height of 20 cm in a.9 litre graduated bowl. The
height of the suds generated by this technique was found to be correlatable to the
initial suds experienced by consumers in use. The performance of each product was
expressed as better than, or poorer than, that of the standard product I.
4. Suds Mileage This was carried out as described in Example 1 except that the grease
soil comprised 5% of a mixture of fatty acids and 95% corn oil by weight, the mixture
of fatty acids comprising 2 parts oleic acid, 2 parts linoleic acid, 1 part stearic
acid and 2.5 parts palmtic acid. Product I was used as the standard.
[0062] The results were as follows:

[0063] It can be seen that Products J, K and L in accordance with the invention, although
providing the suds mileage benefits of the invention do not all perform equally well
in other areas. Product J, which comprises the addition of 1.5% alkyl betaine to Product
I, improves suds mileage and grease cutting but shows technical deficiencies in initial
suds level and grease redeposition. A more preferred embodiment Product K, in which
the anionic surfactant level has been slightly increased, eliminates the initial suds
performance deficiency of Product J. A highly preferred embodiment of the invention
is constituted by Product L in which the ratio of alkyl benzene sulphonate to alkyl
sulphate/alkyl ether sulphate has been significantly reduced. This formulation demonstrates
improved grease redeposition performance relative to the other products, whilst employing
a lower total level of anionic surfactant. However, elimination of the alkyl benzene
sulphonate component and an increase in the level of the alkyl sulphate/alkyl ether
sulphate component to give a formulation of equal cost (Product M) shows a marked
decline in suds mileage performance, particularly on greasy soils, where the performance
is worse than that of the reference product I.