FIELD OF THE INVENTION
[0001] This invention relates to use of a cleaning composition in the form of a tablet for
use in fabric washing.
BACKGROUND OF THE INVENTION
[0002] Detergent compositions in tablet form have advantages over powdered products in that
they do not require measuring and are thus easier to handle and dispense into the
washload.
[0003] Single phase tablets of a cleaning composition are generally made by compressing
or compacting a quantity of the composition in particulate form.
[0004] Tablets comprising two or more separate regions have also been described. For example
WO-A-01/42416 describes the production of multi-phase moulded bodies comprising a combination of
core moulded bodies and a particulate premix.
WO-A-00/04129 describes a multi-phase detergent tablet comprising a first phase in the form of
a shaped body having at least one mould therein and a second phase in the form of
a particulate solid compressed within said mould.
WO-A-00/61717 describes a detergent tablet which is characterised in that at least part of its
outer surface is semi-solid. The latter disclosure states that the semi-solid layer
can be rubbed onto heavily stained areas of the fabric to pretreat them, thereby assisting
removal of the stains in the wash. This may be regarded as an extension of the concept
of rubbing stains with a pretreatment composition, e.g. in the form of a stick or
bar. There is already a host of references in the art, relating to such pre-treatment
products, for example
US-A-4 396 521 and
EP-A-205 999.
[0005] Whilst in principle, this method of pre-treatment with a two phase tablet appears
to be workable, in practice, it is desirable for the semi-solid phase to contain a
relatively high level of liquid component(s), especially organic solvent. This results
in a problem that liquid can bleed into the compressed particulate solid layer leading
to a degradation in tablet appearance and/or integrity.
[0006] We have now found that the aforementioned problem can be mitigated or overcome by
having an intermediate layer between the semi-solid layer and the compressed particulate
layer. However, since the regions of different material may in the alternative be
arranged in other than layered fashion, the more generic term "phase" is used in many
places throughout this specification.
DEFINITION OF THE INVENTION
[0007] According to a first aspect of the present invention, there is provided use of a
multi-phase laundry cleaning tablet comprising a compressed particulate phase and
a semi-solid phase for pretreating a region of a fabric prior to washing by rubbing
the semi-solid phase on the region, wherein an intermediate phase is at least partly
situated between the semi-solid phase and the compressed particulate phase, and wherein
the intermediate phase comprises at least 10% by weight of soap.
[0008] A second aspect of the present invention provides a method of pretreating a region
of a fabric prior to washing by rubbing the region with a semi-solid phase of a multi-phase
laundry cleaning tablet comprising the semi-solid phase and a compressed particulate
phase, wherein an intermediate phase is at least partially situated between the semi-solid
phase and the compressed particulate phase and wherein the intermediate phase comprises
at least 10% by weight of soap.
[0009] A third aspect of the present invention provides a method of washing a fabric, comprising
washing the fabric in a wash liquor in which a multi-phase laundry cleaning tablet
has been dispersed and/or dissolved, a region of the fabric having first been rubbed
with a semi-solid phase of the tablet, wherein the tablet further comprises a compressed
particulate phase and wherein an intermediate phase is at least partially situated
between the semi-solid phase and the compressed particulate phase and wherein the
intermediate phase comprises at least 10% by weight of soap.
DETAILED DESCRIPTION OF THE INVENTION
[0010] As used herein, the term "phase" refers to a region or a plurality of regions of
a tablet having a particular composition and/or physical form such as solid homogeneous
mass, compressed particulate mass or semi-solid such as gel. These regions may be
arranged as layers or as islands at least partly surrounded by one or more other such
regions.
[0011] The tablets utilised in the present invention may be any suitable shape, e.g. spherical
or polyhedral. However, preferably they are of cylindrical shape wherein the two main
surfaces (upper side and bottom side) are substantially flat. In another preferred
class of embodiments, the surface of the semi-solid layer is dome-shaped to facilitate
pre-treatment application.
[0012] The multi-phase tablets used in the present invention comprise a semi-solid phase,
an intermediate phase and additionally one phase of compacted particulates. Suitably,
there may be further phases.
[0013] The intermediate phase is at least partly situated between the semi-solid phase and
the compressed particulate phase. That is to say, at least part of the area where
the semi-solid phase would be in contact with the compressed particulate phase at
an interface therebetween, an intermediate phase intervenes. However, some semi-solid
phase could still be in direct contact with compressed particulate phase. Most preferably
though, substantially no semi-solid phase is in direct contact with compressed particulate
phase. The intermediate phase itself may actually comprise regions of intermediate
phase of respective composition and/or physical state which are different from each
other. The only requirement is that they each differ from the semi-solid phase and
the compressed particulate phase. In the case where the compressed particulate phase
and/or semi-solid phase are in the form of a plurality of discrete islands, two or
more such islands could be respectively isolated at the interface by a different intermediate
phase.
[0014] One or more other phases than compressed particulate, semi-solid and intermediate
may also be present in contact with any one or more of the latter phases.
[0015] Most advantageous though, is the location of the intermediate phase substantially
complete between the compressed particulate phase and the semi-solid phase in a stackered
layer structure.
The Intermediate Phase
[0016] The intermediate phase is intended to reduce bleeding of liquid from the semi-solid
phase into the compressed particulate phase. Preferably, it is sufficient to inhibit
liquid transfer to the extent that after 8 weeks storage immediately after manufacture,
at 37°C and at 70% relative humidity at 1 atmosphere pressure, less than 10% by weight,
more preferably less than 5% by weight of the material in the compressed solid layer
consists of liquid from the semi-solid phase. Thus, after storage at such conditions,
the weight of the compressed particulate phase should preferably increase by less
than 10%, more preferably by less than 5%.
[0017] The intermediate phase comprises at least 10% b weight of soap preferably at least
15%, more preferably at least 20% and even as high as at least 50% by weight of soap.
Typical soap levels in the intermediate phase are from 15% to 50%, preferably from
20% to 40%, more preferably from 25% to 40% by weight. By "soap" is meant one or more
inorganic or organic salts of one or more fatty acids, which independently may be
saturated or unsaturated and optionally may be branched. Suitable soaps preferably
have from 12 to 22 carbon atoms, more preferably from 12 to 18 carbon atoms.
[0018] It is also useful if the intermediate phase is harder than the semi-solid phase and
less hard than the compressed particulate phase.
[0019] Preferably the intermediate phase has a weight of from 0.5 to 40 grammes, more preferred
from 1 to 20 grammes, most preferred from 2 to 10 grammes. Preferably the other phases
each have a weight of 2 to 40 grammes. Preferably the total weight of the cleaning
tablet according to the invention is from 10 to 70 grammes.
[0020] The intermediate phase is preferably applied by compaction in a tabletting machine
and therefore, soap levels substantially higher than 50% by weight (say up to 60%
or up to 55% by weight) are less preferred.
[0021] Other ingredients may alternatively or additionally be present in the intermediate
phase, although preferably, it is substantially free of non-soap surfactants, bleach
ingredients and builder materials. Sometimes it may be advantageous however to incorporate
into the soap rich layer a highly soluble material such as sugars, urea, alkali metal
salts such as sodium chloride. Typically such highly soluble materials will have a
solubility of at least 100 grammes per litre water of 20° C, more preferred at least
250 grammes.
[0022] The intermediate phase, embodied in the form of a soap containing region of the tablet,
may be prepared by any suitable method for example the spraying, applying or brushing
of a soap containing formulation, if appropriate followed by hardening e.g. by cooling.
In a preferred method, the soap-containing layer is obtainable from the compression
of a particulate mixture comprising at least 50% by weight of soap containing particles
together with solid particles of any other optional ingredient. The soap containing
particles preferably comprise at least 10% by weight, preferably at least 25% wt,
more preferably at least 50% wt (based on the particles) of soap surfactants. Suitable
detergent particles may for example be granules or other particles having high soap
levels, for example soap noodles, marumes or granulates with high soap levels.
[0023] Preferably the level of soap surfactants in the soap rich particles is more than
50 wt%, more preferred more than 70 wt%, especially preferred from 75 wt% to 100 wt%.
Preferably the level of soap rich particles in the soap rich phase is at least 60%
wt, more preferred at least 80 % by weight.
[0024] Further surfactants, for example anionic, nonionic or cationic surfactants may equally
be present in the intermediate phase for example at a level of 0.1 to 10 wt% based
on the weight of any soap containing part. However, normally, a soap containing phase
will be substantially free from non-soap surfactants.
[0025] In addition to the soap surfactants, the intermediate soap rich phase may comprise
other materials, for example soluble materials such as electrolyte materials, meltable
organic materials and sugars, at a level of 2 to 70 %wt, more preferably from 3 to
50 wt%, most preferably 5 to 40 % by weight, based on the weight of the smooth part.
Examples of preferred materials are water-soluble materials such as the sodium and
potassium citrates, sodium chloride, sodium sulphate, acetates and carbonates, urea
and sugar. The water solubility at 20° C of these materials is preferably at least
10 grammes per 100 ml of water, more preferred more than 15 grammes, most preferably
more than 20 grammes.
[0026] If these soluble materials are present, their particle size could be chosen such
that the intermediate phase may form as a continuous matrix having dispersed therein
particles of the water soluble material.
[0027] It has been found that these materials provide good dissolution properties to the
soap rich phase. Furthermore these materials do not negatively affect the desired
firm consistency of the soap rich phase.
The Semi-Solid Phase
[0028] The semi-solid phase is one which has a consistency which enables some of it to be
applied to a fabric by rubbing. Phases with a waxy or soapy or gel-like consistency
are especially suitable.
[0029] A preferred semi-solid phase is one which is termed herein, a "smooth phase". Other
suitable semi-solid phases are any described in
WO-A-00/61717.
[0030] Recently it has been suggested, for example in
EP 1,371,719,
EP 1,405,900,
EP 1,382,668,
EP 1,375,636,
EP 1,405,901,
EP 1,405,902,
EP 1,418,224 and
WO 03/104380 to prepare tablets comprising a smooth or semi-solid phase.
[0031] The semi-solid phase preferably contains one or more ingredients which prior to incorporation
are liquid at 25°C and 1 atmosphere pressure. This may be selected from one or more
aliphatic or aromatic, polar or non-polar organic liquids (particularly organic solvents)
such as liquid alkanols, diols and polyols.
[0032] Some particular suitable organic solvents are polyethyleneglycol, dipropyleneglycol,
isopropanol or (mono-)propyleneglycol.
[0033] Another preferred class of organic liquids comprises liquid non-soap surfactants
such as liquid nonionic surfactants, eg liquid (poly)alkoxylated aliphatic alcohols.
[0034] Preferably, the level of such organic liquids is from 0 to 40 wt%, more preferred
1 to 20, most preferred from 4 to 15 wt% based on the weight of the semi-solid phase.
[0035] The semi-solid phase preferably, however, comprises no or only low levels of water.
Preferably the level of water is less than 20 wt % based on the weight of the smooth
phase, more preferred less than 15 wt%, most preferred from 5 to 12 wt%. Most preferably
the smooth phases are substantially free from water, which means that apart from low
levels of moisture (e.g. for neutralisation or as crystal water) no additional added
water is present.
[0036] For the purpose of this invention the term "smooth phase" refers to compositions
which are on the one hand solid enough to retain their shape at ambient temperature
and on the other hand smooth in appearance. Smooth textures are generally of low or
no porosity and have -at normal viewing distance- the appearance of a continuous phase
for example as opposed to porous and particulate appearance of a compacted particulate
material.
[0037] Preferably the semi-solid is transparent or translucent. Preferably, this means that
the composition has an optical transmissivity of at least 10%, most preferably 20%,
still more preferably 30%, through a path length of 0.5 cm at 25° C. These measurements
may be obtained using a Perkin Elmer UV/VIS Spectrometer Lambda 12 or a Brinkman PC801
Colorimeter at a wavelength of 520nm, using water as the 100% standard.
[0038] The transparency or translucency of a semi-solid phase does not preclude the composition
being coloured, e.g. by addition of a dye, provided that it does not detract substantially
from clarity.
[0039] In an advantageous embodiment of the invention, the semi-solid phase comprises from
30-100 wt% of non-soap surfactants, more preferred 40 to 90 wt% (based on the total
weight of said smooth phase), more preferred from 50 to 80 wt%.
[0040] Preferably the total weight of surfactants in the semi-solid phase, especially when
it is a smooth phase is from 2 to 20 grammes, more preferred from 3 to 10 grammes.
[0041] In a first preferred embodiment of the invention the tablet may be a multi-phase
tablet wherein the phases other than the semi-solid phase as described above comprise
no or only low levels of non-soap surfactants. Especially the level of non-soap surfactants
in the compressed particulate phase is less than 10 wt%(based on the total weight
of said phases), more preferred from 0 to 9 wt%, most preferred from 1 to 8 wt%.
The Compressed Particulate Phase
[0042] A compressed particulate phase is a matrix of compacted particles.
[0043] The compressed particulate phase is essentially a tablet portion comprising granular
and/or simple powder material compressed into a solid mass. Typically, it will comprise
surfactant, preferably also detergency builder and more preferably one or more other
ingredients selected from the classes of ingredients used in solid cleaning compositions,
especially laundry wash compositions (although other cleaning composition types such
as mechanical wavewashing compositions are also possible). Such other optional classes
of ingredients may for example be selected from enzymes, bleaches and bleach systems,
fluorescers, antifoams, anti-dye transfer agents, anti-redeposition agents, disintegrants
and coloured speckles.
[0044] Although the compressed particulate phase may comprise surfactant materials, this
phase preferably comprises ingredients of the tablet other than surfactants. Examples
of these ingredients are for example builders, bleach system, enzymes etc. Preferably
the builders in the tablet are predominantly present in this first compressed particulate
phase.
[0045] Preferably the first compressed particulate phase is from 5 to 50 grams, for example
10 to 40 grams. Especially preferably the regions are present as layers in the cleaning
tablet.
[0046] Preferably the particulate composition has an average particle size in the range
from 200 to 2000 µm, more preferably from 250 to 1400 µm. Fine particles, smaller
than 180 µm or 200 µm may be eliminated by sieving before tableting, if desired, although
we have observed that this is not always essential.
[0047] Tableting to make a compressed particulate phase entails compaction of a particulate
composition.
Processing
[0048] Ways of making individual phases have already been described. However, the phases
have to be bonded together and/or formed as a unitary mass.
[0049] For making phases or combinations of phases comprising particulate matter, a variety
of tableting machinery is known, and can be used. Generally it will function by stamping
a quantity of the particulate composition which is confined in a die.
[0050] Manufacture of a tablet with two layers of differing composition may be carried out
by placing a predetermined quantity of one composition in a mould, then adding a second
composition on top, and next driving a die into the mould to cause compression.
[0051] Alternatively, a predetermined quantity of a first composition may be placed in a
mould and compacted by driving a die into the mould, followed by removing the die,
adding a second composition and compacting again.
[0052] Tableting machinery able to carry out such operations is known. For example, suitable
tablet presses are available from Fette and from Korsch.
[0053] Thus, a two phase tablet comprising the compressed particulate phase and the intermediate
phase may be formed such as described above and then the semi-solid phase applied
over the intermediate phase, eg by melt adhesion or by bonding with a separate adhesive
such as a hot-melt adhesive.
[0054] Tableting may be carried out at ambient temperature or at a temperature above ambient
which may allow adequate strength to be achieved with less applied pressure during
compaction. In order to carry out the tableting at a temperature which is above ambient,
the particulate composition is preferably supplied to the tableting machinery at an
elevated temperature. This will of course supply heat to the tableting machinery,
but the machinery may be heated in some other way also.
[0055] It is known to make tablets using microwave radiation.
WO-A-96/06156 mentions that hydrated materials are useful in this special circumstance to cause
sintering.
[0056] For the present invention, if any heat is supplied, it is envisaged that this will
be supplied conventionally, such as by passing the particulate composition through
an oven, rather than by any application of microwave energy.
[0057] The size of a tablet will suitably range from 10 to 160 grams (gm), preferably from
15 to 60 gm, depending on the conditions of intended use, and whether the tablet represents
a dose for an average load in a fabric washing or a fractional part of such a dose.
The tablets may be of any shape. However, for ease of packaging they are preferably
blocks of substantially uniform cross-section, such as cylinders or cuboids. The overall
density of a tablet is preferably 1040 or 1050 gm/litre, better 1100 gm/litre, up
to 1300 or 1350 gm/litre or even more. The tablet density may well lie in a range
up to no more than 1250 or even 1200 gm/litre.
[0058] While the starting particulate composition may in principle have any bulk density,
the present invention is especially relevant to tablets made by compacting powders
of relatively high bulk density, because of their greater tendency to exhibit disintegration
and dispersion problems. Such tablets have the advantage that, as compared with a
tablet derived from a low bulk density powder, a given dose of composition can be
presented as a smaller tablet.
[0059] Thus the starting particulate composition may suitably have a bulk density of at
least 400 g/litre, preferably at least 500 g/litre, and advantageously at least 700
g/litre. Granular detergent compositions of high bulk density prepared by granulation
and densification in a high-speed mixer/granulator, as described and claimed in
EP-A-340 013,
EP-A-352 135, and
EP-A-425 277, or by the continuous granulation/densification processes described and claimed in
EP-A-367 339 and
EP-A-390 251are inherently suitable for use in the present invention.
Preferred embodiments of the invention will now be described by way of example only.
Further modification within the scope of the present invention will be apparent to
the person skilled in the art.
[0060] Tablets for use according to the invention are preferably manufactured by a process
involving the application of pressure to a particulate mixture. Advantageously the
preparation of the soap containing phase may involve the dosing of a particulate mixture
comprising ingredients of the intermediate phase, i.e. soap rich particles, preferably
in combination with other materials as described above, followed by the exertion of
pressure, preferably above the yield stress of the intermediate phase components.
It has been found that the exertion of pressure to a particulate mixture comprising
significant levels of soap rich particles leads to a certain flow behaviour of the
mixture leading to the formation of an intermediate phase. The semi-solid phase can
then be applied by melt-bonding or by use of a suitable adhesive.
[0061] In a preferred embodiment of the invention the first particulate composition is pre-compressed
at a force of 0.1 to 20 kN/cm
2 between steps (a) and (b) In another preferred embodiment the particulate composition
is flattened between steps (a) and (b).
[0062] Preferably the (co-)compression of the combination of the intermediate and the particulate
region(s) takes place at a force of from 0.05 to 20 kN/cm
2. Especially if the solid region has been pre-compressed the co-compression in step
(c) can advantageously be at a force of 0.1- 10 kN/cm
2, more preferred 0.5 to 5 kN/cm
2. If the solid region has not been pre-compressed, the co-compression preferably takes
place at a force of 1- 100 kN/cm
2., more preferred 2-50 kN/cm
2., most preferred 2-10 kN/cm
2.
[0063] The intermediate phase may also be manufactured separately by compression of a suitable
composition such as a particulate soap rich material e.g. at the compation forces
as indicated above.
[0064] Alternatively the intermediate phase may be prepared by other methods for example
the spraying of a suitable composition such as a soap rich composition, for example
onto the (pre) compressed compacted tablet phase on which the intermediate phase layer
is formed or adhered. Another suitable method for the preparation of an intermediate
phase may involve casting or extrusion of a suitable composition such as a soap containing
composition.
[0065] Optionally the semi-solid phase may also be prepared e.g. by extrusion, casting or
other shaping methods.
[0066] Separately prepared intermediate phase and semi-solid phase can then be adhered to
other part(s) of the tablet for example by gentle pressing or by usage of an adhesive
material.
[0067] Similarly a separately prepared solid phase of compressed particulate materials can
be combined with one ore more pre-prepared intermediate phases e.g. by gentle co-compression,
followed by body of the semi-solid phase.
[0068] In general, a fabric washing tablet as a whole will be likely to contain at least
2 wt%, probably at least 5 wt%, up to 40 or 50 wt% surfactant based on the whole tablet,
and from 5 to 80 wt% detergency builder, based on the whole tablet.
[0069] Materials which may be used in tablets of this invention will now be discussed in
more detail.
Disintegrants
[0070] Preferably, the compressed particulate phase comprises one or more disintegrants.
[0071] Preferred disintegrants are materials which have a solubility in (preferably deionised)
water at 20°C of at least 50 grams per 100 grams of water.
[0072] This disintegrant may be present in an amount which is at least 5wt%, 7 wt% or 12
wt% of the tablet. Some of the disintegrant may be present in the base powder used
to make the complete tablet formulation used for the compressed particulate phase,
whilst the remainder, preferably the majority, is added as a post-dosed ingredient
to the base powder before tableting in the compressed particulate phase. It is preferred
that at least 75wt% or even 85wt% of the material is not in the base powder, but is
added as a post-dosed ingredient.
[0073] A solubility of at least 50 grams per 100 grams of water at 20°C is an exceptionally
high solubility: many materials which are classified as water soluble are less soluble
than this.
[0074] Some highly water-soluble materials which may be used are listed below, with their
solubilities expressed as grams of solid required to form a saturated solution in
100 grams of water at 20°C:
Material |
Water Solubility (g/100g) |
Sodium citrate dihydrate |
72 |
Potassium carbonate |
112 |
Urea |
>100 |
Sodium acetate (anhydrous) |
119 |
Sodium acetate trihydrate |
76 |
5 Magnesium sulphate 7H2O |
71 |
Potassium acetate |
>200 |
[0075] By contrast the solubilities of some other common materials at 20°C are:
Material |
Water Solubility (g/100g) |
Sodium chloride |
36 |
Sodium sulphate decahydrate |
21.5 |
Sodium carbonate anhydrous |
8.0 |
Sodium percarbonate anhydrous |
12 |
Sodium perborate anhydrous |
3.7 |
Sodium tripolyphosphate anhydrous |
15 |
[0076] Preferably this highly water-soluble disintegrant is incorporated as particles of
the material in a substantially pure form (i.e. the majority of such particles contain
over 95% by weight of the material). However, the said particles may contain material
of such solubility in a mixture with other material, provided that material of the
specified solubility provides at least 50% by weight of these particles.
[0077] The preferred disintegrant of high water-solubility are sodium citrate dihydrate,
potassium carbonate, urea, sodium acetate in its anhydrous or trihydrate form, sodium
acetate which is partially hydrated - as can be the case when it is spray dried, magnesium
sulphate 7H
2O and potassium acetate. Mixtures of these can also be used. The most preferred of
the aforementioned materials are sodium citrate dihydrate, sodium acetate in either
its anhydrous, trihydrate or partially hydrated form. Mixtures of these most preferred
materials can also be used.
[0078] Another suitable class of disintegrants comprises cellulose disintegrants.
Surfactant Compounds
[0079] Compositions which are used in tablets of the invention will contain one or more
detergent surfactants. In a fabric washing composition, these preferably provide from
5 to 50% by weight of the overall tablet composition, more preferably from 8 or 9%
by weight of the overall composition up to 40% or 50% by weight. Surfactant may be
anionic (soap or soap), cationic, zwitterionic, amphoteric, nonionic or a combination
of these.
[0080] Anionic surfactant may be present in an amount from 0.5 to 50% by weight, preferably
from 2% or 4% up to 30% or 40% by weight of the tablet composition.
[0081] Synthetic (i.e. non-soap) anionic surfactants are well known to those skilled in
the art. Examples include alkylbenzene sulphonates, particularly sodium linear alkylbenzene
sulphonates having an alkyl chain length of C
8-C
15; olefin sulphonates; alkane sulphonates; dialkyl sulphosuccinates; and fatty acid
ester sulphonates.
[0082] Primary alkyl sulphate having the formula
ROSO
3- M
+
in which R is an alkyl or alkenyl chain of 8 to 18 carbon atoms especially 10 to 14
carbon atoms and M
+ is a solubilising cation, is commercially significant as an anionic surfactant. Linear
alkyl benzene sulphonate of the formula

where R is linear alkyl of 8 to 15 carbon atoms and M
+ is a solubilising cation, especially sodium, is also a commercially significant anionic
surfactant.
[0083] Frequently, such linear alkyl benzene sulphonate or primary alkyl sulphate of the
formula above, or a mixture thereof will be the desired anionic surfactant and may
provide 75 to 100 wt% of any anionic soap surfactant in the composition.
[0084] In some forms of this invention the amount of non-soap anionic surfactant lies in
a range from 5 to 20 wt% of the tablet composition.
[0085] Soaps for use in accordance to the invention are preferably sodium soaps derived
from naturally occurring fatty acids, for example, the fatty acids from coconut oil,
beef tallow, sunflower or hardened rapeseed oil. Especially preferably soaps are selected
from C
12 to C
22 soaps for example from C
12 to C
18 soaps.
[0086] Suitable nonionic surfactant compounds which may be used include in particular the
reaction products of compounds having a hydrophobic group and a reactive hydrogen
atom, for example, aliphatic alcohols, acids, amides or alkyl phenols with alkylene
oxides, especially ethylene oxide.
[0087] Specific nonionic surfactant compounds are alkyl (C
8-22) phenol-ethylene oxide condensates, the condensation products of linear or branched
aliphatic C
8-20 primary or secondary alcohols with ethylene oxide, and products made by condensation
of ethylene oxide with the reaction products of propylene oxide and ethylene-diamine.
[0088] Especially preferred are the primary and secondary alcohol ethoxylates, especially
the C
9-11 and C
12-15 primary and secondary alcohols ethoxylated with an average of from 5 to 20 moles
of ethylene oxide per mole of alcohol.
In some fabric washing tablets of this invention, the amount of nonionic surfactant
lies in a range from 4 to 40%, better 4 or 5 to 30% by weight of the whole tablet.
[0089] Many nonionic surfactants are liquids. These may be absorbed onto particles of the
composition.
[0090] In a machine dishwashing tablet the surfactant may be wholy nonionic, in an amount
below 5 wt% of the whole tablet although it is known to include some anionic surfactant
and to use up to 10 wt% surfactant in total.
Detergency Builder
[0091] A composition which is used in tablets of the invention will usually contain from
5 to 80%, more usually 15 to 60% by weight of detergency builder. This may be provided
wholly by water soluble materials, or may be provided in large part or even entirely
by water-insoluble material with water-softening properties. Water-insoluble detergency
builder may be present as 5 to 80 wt%, better 5 to 60 wt% of the composition.
[0092] Alkali metal aluminosilicates are strongly favoured as environmentally acceptable
water-insoluble builders for fabric washing. Alkali metal (preferably sodium) aluminosilicates
may be either crystalline or amorphous or mixtures thereof, having the general formula:
0.8-1.5 Na
2O.Al
2O
3. 0.8-6 SiO
2. xH
2O
[0093] These materials contain some bound water (indicated as "xH2O") and are required to
have a calcium ion exchange capacity of at least 50 mg CaO/g. The preferred sodium
aluminosilicates contain 1.5-3.5 SiO
2 units (in the formula above). Both the amorphous and the crystalline materials can
be prepared readily by reaction between sodium silicate and sodium aluminate, as amply
described in the literature.
[0094] Suitable crystalline sodium aluminosilicate ion-exchange detergency builders are
described, for example, in
GB 1429143 (Procter & Gamble). The preferred sodium aluminosilicates of this type are the well known commercially
available zeolites A and X, the novel zeolite P described and claimed in
EP 384070 (Unilever) and mixtures thereof.
[0095] Conceivably a water-insoluble detergency builder could be a layered sodium silicate
as described in
US 4664839. NaSKS-6 is the trademark for a crystalline layered silicate marketed by Hoechst
(commonly abbreviated as "SKS-6"). NaSKS-6 has the delta-Na
2SiO
5 morphology form of layered silicate. It can be prepared by methods such as described
in
DE-A-3,417,649 and
DE-A-3,742,043. Other such layered silicates, such as those having the general formula NaMSi
xO
2x+1.yH
2O wherein M is sodium or hydrogen, x is a number from 1.9 to 4, preferably 2, and
y is a number from 0 to 20, preferably 0 can be used.
[0096] Water-soluble phosphorous-containing inorganic detergency builders, include the'alkali-metal
orthophosphates, metaphosphates, pyrophosphates and polyphosphates. Specific examples
of inorganic phosphate builders include sodium and potassium tripolyphosphates, orthophosphates
and hexametaphosphates.
[0097] Non-phosphorous water-soluble builders may be organic or inorganic. Inorganic builders
that may be present include alkali metal (generally sodium) carbonate; while organic
builders include polycarboxylate polymers, such as polyacrylates, acrylic/maleic copolymers,
and acrylic phosphonates, monomeric polycarboxylates such as citrates, gluconates,
oxydisuccinates, glycerol mono- di- and trisuccinates, carboxymethyloxysuccinates,
carboxymethyloxymalonates, dipicolinates and hydroxyethyliminodiacetates.
[0098] At least one region (preferably the second region) of a fabric washing tablet preferably
include polycarboxylate polymers, more especially polyacrylates and acrylic/maleic
copolymers which can function as builders and also inhibit unwanted deposition onto
fabric from the wash liquor.
Bleach System
[0099] Tablets according to the invention may contain a bleach system in at least one region
of a tablet, preferably in the second region. This preferably comprises one or more
peroxy bleach compounds, for example, inorganic persalts or organic peroxyacids, which
may be employed in conjunction with activators to improve bleaching action at low
wash temperatures. If any peroxygen compound is present, the amount is likely to lie
in a range from 10 to 25% by weight of the composition.
[0100] Preferred inorganic persalts are sodium perborate monohydrate and tetrahydrate, and
sodium percarbonate, advantageously employed together with an activator. Bleach activators,
also referred to as bleach precursors, have been widely disclosed in the art. Preferred
examples include peracetic acid precursors, for example, tetraacetylethylene diamine
(TAED), now in widespread commercial use in conjunction with sodium perborate; and
perbenzoic acid precursors. The quaternary ammonium and phosphonium bleach activators
disclosed in
US 4751015 and
US 4818426 (Lever Brothers Company) are also of interest. Another type of bleach activator which
may be used, but which is not a bleach precursor, is a transition metal catalyst as
disclosed in
EP-A-458397,
EP-A-458398 and
EP-A-549272. A bleach system may also include a bleach stabiliser (heavy metal sequestrant) such
as ethylenediamine tetramethylene phosphonate and diethylenetriamine pentamethylene
phosphonate.
[0101] As indicated above, if a bleach is present and is a water-soluble inorganic peroxygen
bleach, the amount may well be from 10% to 25% by weight of the composition.
Other Detergent Ingredients
[0102] The detergent tablets of the invention may also contain (preferably in the second
region) one of the detergency enzymes well known in the art for their ability to degrade
and aid in the removal of various soils and stains. Suitable enzymes include the various
proteases, cellulases, lipases, amylases, and mixtures thereof, which are designed
to remove a variety of soils and stains from fabrics. Examples of suitable proteases
are Alcalase (Trade Mark), and Savinase (Trade Mark), as supplied by Novo Industri
Als, Copenhagen, Denmark. Detergency enzymes are commonly employed in the form of
granules or marumes, optionally with a protective coating, in amount of from about
0.1% to about 3.0% by weight of the composition; and these granules or marumes present
no problems with respect to compaction to form a tablet.
[0103] The detergent tablets of the invention may also contain (preferably in the second
region) a fluorescer (optical brightener), for example, Tinopal (Trade Mark) DMS or
Tinopal CBS available from Ciba Ceigy AC, Basel, Switzerland. Tinopal DMS is disodium
4,4'bis-(2-morpholino-4-anilino-s-triazin-6-ylamino) stilbene disulphonate; and Tinopal
CBS is disodium 2,2'-bis-(phenyl-styryl) disulphonate.
[0104] An antifoam material is advantageously included (preferably in the second region),
especially if a detergent tablet is primarily intended for use in front-loading drum-type
automatic washing machines. Suitable antifoam materials are usually in granular form,
such as those described in
EP 266863A (Unilever). Such antifoam granules typically comprise a mixture of silicone oil,
petroleum jelly, hydrophobic silica and alkyl phosphate as antifoam active material,
absorbed onto a porous absorbed water-soluble carbonate-based inorganic carrier material.
Antifoam granules may be present in an amount up to 5% by weight of the composition.
[0105] It may also be desirable that a detergent tablet of the invention includes an amount
of an alkali metal silicate, particularly sodium ortho-, meta- or disilicate. The
presence of such alkali metal silicates at levels, for example, of 0.1 to 10 wt%,
may be advantageous in providing protection against the corrosion of metal parts in
washing machines, besides providing some measure of building and giving processing
benefits in manufacture of the particulate material which is compacted into tablets.
[0106] A tablet for fabric washing will generally not contain more than 15 wt% silicate.
A tablet for machine dishwashing will often contain more than 20 wt% silicate. Preferably
the silicate is present in the second region of the tablet.
[0107] Further ingredients which can optionally be employed in a region of a fabric washing
detergent of the invention tablet (preferably the second region) include anti-redeposition
agents such as sodium carboxymethylcellulose, straight-chain polyvinyl pyrrolidone
and the cellulose ethers such as methyl cellulose and ethyl hydroxyethyl cellulose,
fabric-softening agents; heavy metal sequestrants such as EDTA; perfumes; and colorants
or coloured speckles.
[0108] Further ingredients which can optionally be used in tablets of the invention, preferably
in the second region are dispersing aids. Examples of suitable dispersing aids are
water-swellable polymers (e.g. SCMC) highly soluble materials (e.g. sodium citrate,
potassium carbonate or sodium acetate) or sodium tripolyphospate with preferably at
least 40% of the anhydrous phase I form.
Particle Size and Distribution
[0109] When the intermediate phase is embodied as a soap rich region of the tablet, it may
advantageously be prepared by compacting particles with a high soap content as described
above. Preferably these particles have a mean particle size of from 100 to 1000 µm.
[0110] The intermediate phase is of course a separate phase from the compressed particulate
phase which is preferably a matrix of compacted particles.
[0111] Preferably any particulate composition has a mean particle size in the range from
200 to 2000 µm, more preferably from 250 to 1400 µm. Fine particles, smaller than
180 µm or 200 µm may be eliminated by sieving before tableting, if desired, although
we have observed that this is not always essential.
[0112] While the starting particulate composition may in principle have any bulk density,
the present invention is especially relevant to tablets made by compacting powders
of relatively high bulk density, because of their greater tendency to exhibit disintegration
and dispersion problems. Such tablets have the advantage that, as compared with a
tablet derived from a low bulk density powder, a given dose of composition can be
presented as a smaller tablet.
[0113] Thus the starting particulate composition may suitably have a bulk density of at
least 400 g/litre, preferably at least 500 g/litre, and perhaps at least 600 g/litre.
[0114] Tableting machinery able to carry out the manufacture of tablets of the invention
is known, for example suitable tablet presses are available from Fette and from Korch.
[0115] Tableting may be carried out at ambient temperature or at a temperature above ambient
which may allow adequate strength to be achieved with less applied pressure during
compaction. In order to carry out the tableting at a temperature which is above ambient,
the particulate composition is preferably supplied to the tableting machinery at an
elevated temperature. This will of course supply heat to the tableting machinery,
but the machinery may be heated in some other way also.
[0116] The size of a tablet will suitably range from 10 to 160 grams, preferably from 10
to 70g, depending on the conditions of intended use, and whether it represents a dose
for an average load in a fabric washing or dishwashing machine or a fractional part
of such a dose. The tablets may be of any shape. However, for ease of packaging they
are preferably blocks of substantially uniform cross-section, such as cylinders or
cuboids. The overall density of a tablet preferably lies in a range from 1040 or 1050gm/litre
up to 1600gm/litre.
[0117] The present invention will now be explained in more detail by way of the following
non-limiting examples.
EXAMPLES
[0118] The compressed particulate phase had the following composition:
Composition (%wt) |
P1 |
Na-LAS |
4.15 |
Nonionic 7EO |
1.82 |
Soap |
0.33 |
zeolite A24 (anhydrous) |
9.30 |
Na Acetate.3aq |
1.18 |
Na Carbonate |
1.38 |
SCMC (68%) |
0.18 |
Moisture, salts, NDOM |
1.67 |
Antifoam granule |
1.01 |
Fluorescer granule (15 % active) |
2.31 |
STP HPA |
48.1 |
Nabion/Disilicate co granule. |
2.50 |
TAED (as granule 83%) |
4.52 |
Coated Percarbonate |
17.2 |
Dequest 2047 (43%) |
2.70 |
Enzymes |
0.94 |
Perfume |
0.71 |
TOTAL |
100.0 |
[0119] The following compositions were used for the intermediate phase
Composition wt% |
I1 |
I2 |
Soap granules (Prisavon 1878 ex Uniqema) |
25 |
50 |
Granular sodium sulphate |
75 |
50 |
[0120] The semi-solid phase had the following composition:
Composition wt% |
S1 |
Na-LAS |
32.90 |
Nonionic 5EO |
27.35 |
Na soap (C16/C18) |
2.96 |
Tween 40 |
12.05 |
DiPropyleneGlyc ol |
17.77 |
Dye |
0.011 |
Water |
6.96 |
Total |
100 |
Example 1
[0121] A tablet consisting of a compressed particulate phase, an intermediate phase and
a semi-solid phase was produced by first compressing 25 gr of composition P1 in a
Fette tabletting machine. An intermediate phase was then formed on top of this particulate
phase, by compressing 2 gr of composition I1 in the same Fette tabletting machine.
The semi-solid phase was produced by casting 5 gr of liquid composition S1 at 90°C
into a mould, after which the phase was let to solidify. The semi-solid phase was
then glued onto the intermediate phase with 0.3 gr of a hot melt water soluble glue,
to form the complete tablet.
[0122] With the semi-solid phase a cross was drawn onto the following stains and testcloths:
- WFK10LS (lipstick on cotton)
- WFK10M (motor oil on cotton)
- Ballpoint ink on cotton
[0123] Per stain, roughly 0.3 gr of the semi-solid phase was applied.
The pre-treated stains were subsequently washed with the remaining tablet + one extra
tablet with the same composition in a Miele washing machine at 40°C.
In a comparative experiment the test cloths and stains were washed with the same tablets,
without using the semi-solid phase to pre-treat the stains.
After the wash the pre-treated areas on the stains were visibly much better cleaned
than the untreated areas.
Example 2, comparative Example A
[0124] To demonstrate the necessity of the intermediate phase, tablets were made in the
same manner as in Example 1, but now using composition I2 for the intermediate layer
(Example 2) and a tablet which did not contain an intermediate layer (comparative
Example A).
[0125] The full tablets thus made were flow wrapped and packed in carton boxes and stored
for 7 weeks at 37°C and 70% relative humidity.
[0126] After the storage period, the semi-solid phases were removed carefully and re-weighed.
The loss in weight (in % of the original gel weight) is a measure of the amount leaked
into the compacted particulate phase. The compacted particulate phase was examined
visually for changes in colour.
[0127] The table below shows the results:
Example |
1 |
2 |
A |
Weight loss of gel (wt%) |
4 |
6 |
28 |
Colour of compacted particulate phase |
white |
white |
Yellow spots |
[0128] This result clearly shows the necessity of the intermediate layer to provide stability
upon storage, which is an essential feature for these tablets. It also shows that
even at fairly low levels of soap (Example 1) surprisingly good barrier properties
can be obtained.