[0001] The present invention relates to a method for preparing a granular detergent material.
More in particular, it relates to a method for preparing said granules from a dusty
detergent component, such as soap, builders, e.g. sodium tripolyphosphate, surfactants,
e.g. alkyl benzene sulphonate, soda ash, and corrosion inhibitors, such as disilicate.
[0002] Furthermore, it relates to the granular detergent material thereby obtained.
[0003] Soap is a common ingredient of detergent powder compositions. It may be included
as a detergent active, a builder or a foam suppressor. It may be added to a slurry
which is subsequently spray-dried, or dry-mixed with other particulate ingredients,
including composite particles which are themselves the product of a spray-drying
process.
[0004] When supplied as a raw material for incorporating in such compositions, soap is often
in the form of a fine dusty powder. As well as being messy in the handling, such powders
have a tendency to cause respiratory tract irritation in those working with them.
[0005] Other detergent components, such as mentioned above, are also often provided in the
form of fine powders. In the case of alkaline detergent components, such as soda ash,
the dangers of handling these substances are even more pronounced.
[0006] As to soap, it is known to incorporate extruded soap "noodles" in detergent compositions,
which have a "particle" size much greater than found in the aforementioned dusty powders.
However, this is often done purely for visual appeal, e.g. when such noodles are deliberately
coloured, and this is not a very cost-effective means of supplying the soap, especially
when formulating dry mixed powders.
[0007] US Patents 3,761,549 and 3,588,950 describe a process of making non-dusty granulates
by means of gas fluidisation in a rotating drum. Granules which, it is said, can be
made in this way include those with a core of potassium soap coated with sodium soap,
a core of a strong caustic detergent coated with a mild caustic detergent or a core
of potassium soap with a coating of metasilicate. As described, the core is formed
by interactions during the fluidisation process and the coating is applied by spraying-on
the coating as a liquid.
[0008] According to US Patent 2,730,507, non-dusting soap granulates are formed by mixing
soap dust with fatty acid and an alkaline material which saponifies the acid. Thus,
the resultant particles consist of two kinds of soaps.
[0009] We have now found that non-dusting granules of a detergent component may be made
in a simplified process, optionally in mixture with a wide variety of other materials.
[0010] In particular, we have now found that the detergent component can be worked into
a substantially non-dusty form from a pre-mix comprising:
a) from 1-10% by weight of the binder;
b) up to 40% by weight of a dusty detergent component;
c) the balance being the granulising particles.
[0011] This pre-mix is used to prepare a granular detergent material having a core of granulising
particles coated with a detergent component and a binder, comprising up to 40% by
weight of the detergent component and from 1 to 10% by weight of the binder.
[0012] The physical structure of this granular detergent material can vary. However, it
is believed that the granulising particles are coated with the detergent component
and the binder.
[0013] The dusty detergent component and the granulising particles are admixed intimately
and the resultant product is then admixed with the binder to form said pre-mix. Mixing
of the pre-mix then continues until the granular detergent material is formed.
[0014] This granular detergent material is considerably less dusty than, for instance, known
fine soap powders, yet the process defined above for its production is more cost-effective
than extrusion techniques and the like.
[0015] In the context of the specification, "granulating" as an adjective is used to refer
to components which are capable of being processed to form compositions comprising
granules. On the other hand, "granulising" is used to refer to particles which are
capable of acting on other substances, during processing, to form those substances
into granules.
[0016] The granules obtained are, by themselves, suitable for incorporation in complete
detergent powder compositions which also comprise one or more synthetic detergent
actives selected from anionic, nonionic, cationic, zwitterionic or amphoteric surfactants.
These complete compositions preferably also contain other ingredients usual in such
powders, for example detergency builders (i.e. substances which sequester and/or precipitate
calcium ions contributing to water hardness), soil-suspending and anti-redeposition
agents, corrosion inhibitors, buffers, bleaches (including low-temperature systems
comprising a bleach precursor and an activator therefor), enzymes, enzyme stabilisers,
lather boosters or foam depressors, dyes, pigments, fluorescers and perfumes etc.
[0017] Soap-containing complete detergent powder compositions for which soap-containing
granules according to the present invention are well suited to formulating include
those generically and specifically described in patent specification EP-A-117,568.
[0018] As well as the detergent component, the base mixture also contains the granulising
particles. Thus, it is preferred and desirable that these should have a beneficial
effect in the complete composition. Therefore, it is preferred that the granulising
particles should be of one or more substances which are usual ingredients in detergent
powders such as recited in the preceding paragraph.
[0019] One preferred class of granulising particles comprises neutral and alkaline salts
of alkali metal cations and organic or inorganic anions, into which class fall many
of the aforementioned "usual ingredients" (which will be mentioned in more detail
hereinbelow). For example, especially preferred salts are the alkali metal metasilicates
(preferably hydrated), for example sodium metasilicate 5 aq. which is a corrosion
inhibitor/alkaline buffer. Examples of other suitable salts are alkali metal orthophosphates,
pyrophosphates and tripolyphosphates, such as potassium pyrophosphate 3 aq. and anhydrous
sodium tripolyphosphate.
[0020] Alternatively, it is possible to use granulising particles which will have no particular
benefit when incorporated in a complete detergent composition; so in that case, one
would either have to accept their presence in the composition and accept the ensuing
increase in costs.
[0021] For all granulising particles, whether salts or otherwise, as a general rule it is
preferred that they should not be too pervious to water, which is why the salts should
be hydrated. The granulising particles should also be capable of surviving without
fragmentation in the mixing apparatus used (
vide infra).
[0022] The dusty detergent component may, in principle, be any usual detergent component.
However, it was found that the process of the invention is particularly suited for
soap; builders like sodium tripolyphosphate, zeolite or polyacrylates; surfactants,
such as alkyl benzene sulphonate; soda ash; and corrosion inhibitors, such as disilicate.
Especially good results are obtained for dusty soap powders.
[0023] In general, the detergent component may be of any kind, provided it is compatible
with the binder, the granulising particles and the mixing apparatus. On the latter
point, it is believed to be important that it should not soften too much or melt with
the heat of mixing, although some softening may aid the granulation process. Generally
it will be added to the mixer in the form of the known fine dusty powders, in order
to convert it to a more acceptable form. However, in some circumstances it may be
possible to add them as larger particles or even lumps, depending on the type of mixer,
the kind of detergent component and the working temperature. Amongst soaps which are
capable of producing extremely good quality granules by this invention are tallow
and hardened fish/rape soaps. In the case of softer soaps, better results may be obtained
if the mixture is cooled during processing.
[0024] The binder is any substance capable of bonding the fine detergent component particles
to form and maintain granules thereof and to enable them to coat the granulising particles.
Thus, it should be compatible with the detergent component and with the granulising
particles. It should also possess a "setting property", either alone or by interaction
with the detergent component. Especially useful are aqueous-based binders, in which
the detergent component is at least partly soluble, for example aqueous solutions
of sugars, polyacrylate polymers or neutral waterglass, the latter being most preferred,
or water. Generally, these substances will be used at aqueous concentrations at which
the liquid is viscous and 'sticky'. Thus, for example, waterglasses may be in solutions
from about 25% to about 50% by weight, typically around 34% by weight. It is also
possible to utilise gums and the like. The binder may also contain other ingredients
such as dyes, optical brighteners and the like.
[0025] Amongst the ingredients mentioned above in respect of complete detergent powder compositions
are the synthetic anionic, nonionic, cationic, zwitterionic and amphoteric surfactants.
These will be well known to those skilled in the art and, for example, may be selected
from the classes, sub-classes and individual agents described in "Surface Active Agents",
Vol. I by Schwartz & Perry (Interscience 1949) and "Surface Active Agents", Vol. II
by Schwartz, Perry and Berch (Interscience 1958).
[0026] The preferred but optional other ingredients of the complete composition are the
"usual ingredients". Most important of these are the detergency builders. Those which
are crystalline, and in some cases amorphous, inorganic or non-polymeric organic salts
may either be added to the complete detergent powder composition and/or constitute
the granulising particles. This class includes water-soluble alkali metal phosphates,
triphosphates, polyphosphates, silicates, borates, and also carbonates. Specific examples
of such salts are sodium and potassium triphosphates, pyrophosphates, orthophosphates,
hexametaphosphates, tetraborates, neutral silicates and carbonates.
[0027] Also in this class are the crystalline and amorphous zeolites and aluminosilicates.
One such aluminosilicate is an amorphous water-insoluble hydrated compound of the
formula Na
x(AlO₂.SiO₂)y, wherein x is a number from 1.0 to 1.2 and y is 1, said amorphous material
being further characterised by an Mg⁺⁺ exchange capacity of from 50 mg eq. CaCO₃/g
to about 150 mq eg. CaCO₃/g and a particle diameter of from about 0.01 micron to about
5 microns. This ion exchange builder is more fully described in British Patent Specification
No. 1 470 250.
[0028] A second such water-insoluble synthetic aluminosilicate ion exchage material is crystalline
and has the formula Na
z [(AlO₂)
y(SiO₂)] xH₂O, wherein z and y are integers of at least 6; the molar ratio of z to
y is in the range from 1.0 to about 0.5, and x is an integer from about 15 to about
264, said aluminosilicate ion exchange material having a particle size diameter from
about 0.1 micron to about 100 microns; a calcium ion exchange capacity on an anhydrous
basis of at least about 200 milligrams equivalent of CaCO₃ hardness per gram; and
a calcium ion exchange rate on an anhydrous basis of at least about 2 gralns/gallon/minute/gram.
These synthetic aluminosilicates are more fully described in British Patent Specification
No. 1 429 143.
[0029] Examples of suitable organic builder salts in this class are:
(1) water-soluble amino polycarboxylates, e.g. sodium and potassium ethylene diamine
tetraacetates, nitrilotriacetates and N-(2-hydroxyethyl)-nitrilodiacetates;
(2) water-soluble salts of phytic acid, e.g. sodium and potassium phytates (see U.S.
Patent Specification No. 2 379 942);
(3) water-soluble polyphosphonates, including specifically sodium, potassium and lithium
salts of ethane-1-hydroxy-1,1-diphosphonic acid; sodium, potassium and lithium salts
of methylene diphosphonic acid; sodium, potassium and lithium salts of ethylene di-phosphonic
acid; and sodium, potassium and lithium salts of ethane-1,1,2-triphosphonic acid.
[0030] Other examples include the alkali metal salts of ethane-2-carboxy-1,1-diphosphonic
acid, hydroxymethane diphosphonic acid, carboxyl diphosphonic acid, ethane-1-hydroxy-1,1,2-triphosphonic
acid, ethane-2-hydroxy-1,1,2-triphosphonic acid, propane-1,1,3,3-tetraphosphonic
acid, propane-1,1,2,3,-tetraphosphonic acid, and propane-1,2,2,3-tetraphosphonic acid.
Further examples are alkylmalonates, alkylsuccinates, alkylsulphocarboxylates and
carboxymethyloxymalonates. These include the salts of the free acids or of esters
thereof. Other polycarboxylate builders which can be used satisfactorily, include
water-soluble salts of mellitic acid, citric acid, and carboxymethyloxy succinic acid
and salts of polymers of itaconic acid and maleic acid.
[0031] Builders which would normally be added only to the complete composition (unless formulated
into a substantially non-water pervious forms) are the polymer builders.
[0032] Amongst these polymer builders are the water-soluble salts of polycarboxylate polymers
and copolymers as described in U.S. Patent Specification No. 3 308 067.
[0033] Other usual ingredients which may be used as the granulising particles (as well as
or alternatively being added in the complete composition are the oxygen bleaches such
as alkali metal peroxygen compounds (perborates, percarbonates, etc.) as well as activators
therefor. A large number of such activators is known, but one preferred agent in the
context of this invention, especially as the granulising particles, is N,N,N′,N′-tetraacetyl
ethylenediamine, otherwise known as TAED.
[0034] The foregoing list of usual ingredients for use as the granulising particles or in
the complete composition is not exhaustive and in the light of the teaching herein,
a wide range of alternatives will now be appreciated by the skilled worker in this
art.
[0035] The pre-mix and granular detergent material described above may be prepared, using
any mixing apparatus according to the scale intended but the Lödige (Trade Mark) batch-type
of mixers, for example the FKM-range, are especially preferred.
[0036] In the Lödige batch-type of mixer, it has been found preferable for the dusty detergent
component and the granulising particles to be admixed for about half to about 5 minutes
(typically about 3); the binder is then added in an amount which by simple trial and
error will be found to yield the best formed particles with minimum lumps present.
A good guide is to add the binder slowly until the mix just takes on a slightly wet
appearance. Below this concentration there is an increasing tendency for the granules
to form imperfectly. Above this level, there is a progressive tendency for the mixture
to stick to the knives of the mixer and eventually form lumps which contaminate the
final product. After addition of the binder, mixing is continued for at least 3 minutes,
most preferably for 5 or even 10 minutes, the best results being obtained after about
15 minutes or more.
[0037] The binder is added in an amount of about 1 to about 10% by weight, but we have found
that in most situations the optimum is in the range from about 5 to about 7%. Generally
speaking, the more dusty detergent component is present, the more binder is needed.
It is possible to granulate up to 40% by weight of detergent component in the total
composition by this method, but normally this will be from about 25 to about 38%.
In most situations, the balance of the pre-mix will consist only of the granulising
particles, but optionally small amounts of other components may also be present.
[0038] Granulising particles may be chosen from amongst a very wide range of particle sizes.
Here, average particle size means the diameter value in which 50% of the particles
are larger and 50% are smaller. Of course, the particles will not be as small as the
fine dusty detergent component referred to previously. In general, the average particle
size will be from about 75 µm to about 4,000 µm, preferably from about 250 µm to about
2,500 µm.
[0039] The invention will now be explained better by way of the following non-limiting Examples.
Examples 1-3
[0040] The following compositions were prepared by mixing of soap and granulising particles
for three minutes in a Lödige M 20 (a batch-type of mixer), followed by addition of
the binder and continued mixing for a further 15 minutes. In all cases the resulting
product was a granular mixture. The products had the consistency shown. All amounts
are percentages by weight.
Particle Size Distribution (%) |
<180 µm |
21.1 |
>500 µm |
16.6 |
>180 µm |
13.3 |
>710 µm |
11.2 |
>250 µm |
28.4 |
>1000 µm |
9.5 |
Examples 4-6
[0041] To compare different granulising particles, the following were prepared. In all cases
the resulting product was good non-dusty, non-sticky granules.
[0042] Amounts are in percentages by weight.
![](https://data.epo.org/publication-server/image?imagePath=1989/28/DOC/EPNWA2/EP88202736NWA2/imgb0002)
Example 7
[0043] Examples 1-3 were repeated, using as the dusty detergent component a mixture of :
Alkyl benzene sulphonate |
18.0 |
Burkeite adjunct |
20.0 |
Soap |
4.0 |
Sodium carboxymethyl cellulose |
0.5 |
Savinase (enzyme) |
0.65 |
Perfume |
0.35 |
Na-metasilicate 5 aq. |
6.0 |
the granulising particles :
binder :
Na-waterglass solution, 34% |
2.0 |
A free-flowing mixture of granular particles was obtained having excellent powder
properties.
Example 8
[0044] Examples 1-3 were repeated, using dusty sodium tripolyphosphate (20.1%), sodium metasilicate.5
aq. (77.9%) as granulising particles and a 34% solution of sodium waterglass (2.0%)
as binder. Granules having good powder properties were obtained.
Example 9
[0045] Examples 1-3 were repeated, using dusty alkylbenzene sulphonate (26.0%), sodium tripolyphosphate
particles (72.5%) as granulising particles and a 34% solution of sodium waterglass
(1.5%) as binder. Granules having good powder properties were obtained.
Example 10
[0046] Examples 1-3 were repeated, using dusty soda ash (15.0%), sodium metasilicate.5 aq.
particles (79.1%) as granulising particles and a 34% solution of waterglass (5-7%)
as binder. The properties of the granules obtained were good.
Example 11
[0047] Examples 1-3 were repeated, using dusty sodium disilicate (20.0%), STP granules (78.0%)
as granulising particles and water (2.0%) as binder. The granules obtained had good
powder properties.
1. Granular detergent material having a core of granulising particles coated with
a detergent component and a binder, comprising up to 40% by weight of the detergent
component and from 1 to 10% by weight of the binder.
2. Granular detergent material according to Claim 1, wherein the detergent component
is selected from soap, anionic surfactants, builders, soda ash or corrosion inhibitors.
3. Granular detergent material according to any one of Claims 1-2, wherein the detergent
component is soap.
4. A composition which is a pre-mix for preparing the granular detergent material
according to any of Claims 1-3, the pre-mix comprising :
a) from 1-10% by weight of the binder,
b) up to 40% by weight of a dusty detergent component,
c) the balance being the granulising particles.
5. A composition according to any one of Claims 1-4, wherein the binder comprises
an aqueous solution of either neutral waterglass and/or a polyacrylate polymer, or
water.
6. A composition according to any one of Claims 1-5, wherein the granulising particles
comprise crystals of a salt of an alkali metal cation and an organic or inorganic
anion.
7. A composition according to Claim 6, wherein said crystals are selected from alkali
metal crystals, metasilicates and alkali metal orthophosphates, pyrophosphates and
tripolyphosphates and mixtures thereof.
8. A composition according to any one of Claims 1-7, wherein the granulising particles
have an average size in the range of from 75 µm to 4,000 µm.
9. A method for preparing a pre-mix composition according to Claim 4 by intimate admixture,
for about 0.5 to 5.0 minutes, of the granulising particles and the dusty detergent
component, followed by admixture therewith of the binder.
10. A method for preparing a granular detergent material according to any one of Claims
1-3, by continued mixing of the pre-mix obtained according to Claim 9 for at least
3 minutes, preferably at least 5 minutes.