TECHNICAL FIELD
[0001] The present invention relates to a solid detergent block for obtaining an aqueous
chemical solution having a substantially constant concentration. Such blocks of chemical
are used in industrial cleaning processes such as mechanical warewashing or fabric
washing, and generally comprise alkaline ingredients, detergents, builders, etc.
BACKGROUND OF THE INVENTION
[0002] Industrial warewashing machines generally comprise a wash tank which contains the
cleaning solution for the wash process. In this process, the soiled wash load is doused
with the cleaning solution and subsequently with rinse water which falls into the
wash tank. Each cycle, the cleaning power of the cleaning liquid is reduced, first
because some is exhausted by the soil-removing process and, second, because it is
diluted with rinse water. The cleaning solution is therefore recharged from time to
time by adding fresh cleaning liquid from a dispenser system, which usually provides
a concentrated aqueous solution of the alkaline- and/or surfactant-based chemical
composition.
[0003] A number of techniques are known for converting solid chemicals into a concentrated
solution, dependent on the nature of the solid. For example, according to US patent
2,371,720 a solid powdered chemical can be dissolved by placing it on a sieve and
spraying water on to said sieve from below.
[0004] Alternatively, the powdered material can be dissolved in a dispenser of the "water-in-reservoir"
type. In this type of dispenser, the powdered material is submerged under water, which
therefore becomes loaded or even saturated with the powder. When more water is added,
the excess solution flows into an overflow pipe leading to the washing machine.
[0005] It is also possible to use solid detergent materials in the form of briquettes such
as, for instance, described in US patents 2,382,163, 2,382,164 and 2,382,165. Briquettes
can be used with a "water-in-reservoir" type of dispenser.
[0006] A more recent type of solid detergent is the cast or block form, whereby a solid
detergent block having a weight of several kilograms is formed by pouring a concentrated
aqueous slurry into a container, in which it solidifies upon cooling as a result of
the hydration of the salts in the composition, especially the sodium tripolyphosphate.
Such cast solid blocks are, for example, described in European patent 3,769.
[0007] These solid blocks cast in containers require dispensing systems whereby solvent
is sprayed on to the block while it is inside the container, thereby gradually dissolving
the exposed surface to form a concentrated solution. Such a dispenser system is, for
instance, described in European patent application 244,153.
[0008] Solid detergent blocks have won a certain degree of popularity in the area of industrial
warewashing because they constitute a non-dusty and therefore relatively safe product
form for the often aggressive chemicals used. Furthermore, hydrated solid blocks are
economical in use because they can be manufactured and transported as very concentrated
products.
[0009] A disadvantage of the above-mentioned solid detergent blocks is the difficulty of
incorporating bleach in them, owing to the incompatibility of bleach systems with
the caustic components of the block and the elevated temperatures used in the manufacturing
process of the block. This is true for the hypochlorite-type of bleach, usually sodium
hypochlorite, as well as for organic chlorine-type of bleach.
[0010] Furthermore, the elevated processing temperatures required to prepare the concentrated
slurries adversely affect the stability of heat-labile components. For example, sodium
tripolyphosphate degrades to form ortho-and pyrophosphates, which have poor builder
properties.
[0011] We have now found that solid detergent blocks may be provided which constitute an
even more concentrated product than the solid blocks obtained by hydration, and which
enable the incorporation of stable bleach in the block. Equally surprising was the
constant delivery of the chemicals of the block when the water is sprayed on to the
block.
DEFINITION OF THE INVENTION
[0012] According to the invention there is provided a solid detergent composition in the
form of a block of a compressed granular material, said block having a weight of 0.2-10
kg, preferably 1-5 kg.
[0013] Another aspect of the present invention is a process for the manufacture of these
blocks, whereby a powder is compressed in a mould under a pressure of 3 to 30 kilo
Newton per square cm (KN/cm²) bar to form a solid block.
[0014] Yet another aspect of the present invention is the use of a solid detergent block
according to the invention in an industrial warewashing or fabric washing process.
DETAILED DESCRIPTION OF THE INVENTION
[0015] According to the present invention there is provided a solid detergent composition
in the form of a block of compressed granular material having a weight of 0.2-10 kg,
preferably of 1-5 kg. The blocks are usable for various applications in the area of
industrial cleaning, such as in mechanical warewashing and fabric washing, but other
industrial detergent processes are also envisaged (e.g. bottle washing or conveyor
belt lubricating). Depending on the specific application, the block contains 5-80%
by weight, preferably 5-65% by weight of an alkaline agent, such as sodium- or potassium-hydroxide,
-metasilicate or -carbonate. Fabric washing compositions usually contain mostly metasilicate
and/or carbonate, whereas compositions for mechanical warewashing are the most alkaline
and comprise sodium hydroxide and/or potassium hydroxide.
[0016] Furthermore, the block contains 5-70% by weight, preferably 10-50% of a builder.
This may be a zeolite or a phosphate builder or any other suitable hardness-precipitating
or hardness-sequestering agent.
[0017] The compressed block may contain up to 15% by weight of a bleach component, for example
an active chlorine bleach such as sodium dichloro-isocyanurate. It is a specific advantage
of the compressed blocks according to the invention that high levels of such bleaches
may be incorporated and that the bleach remains stable for several months. In comparable
blocks obtained by hydration, the active chlorine content is known to decrease rapidly
in time.
[0018] The blocks may furthermore comprise 0-10% by weight of a polymer. Suitable polymers
are, for instance, acrylic acid polymers, such as Acrysol LMW 45 ND (ex Rohm & Haas)
or Goodrite K 7058 D (ex BF Goodrich).
[0019] For warewashing purposes, it is common to use an anti-foam agent such as a low-foaming
nonionic surfactant in the wash liquor and such agents may indeed be incorporated
in the solid blocks according to the invention. Amounts of 0-5% by weight proved to
be suitable.
[0020] The blocks according to the invention may further comprise suitable minor ingredients,
such as bleach stabilizers, enzymes, etc. Additional components may be compaction
aids, for instance calcium stearate, hydrophobic silica or talc powder, solubility
aids, such as polyethylene glycol or carbowax.
[0021] The weight, shape and the dimensions of the compressed blocks may vary with the application
envisaged. For mechanical warewashing purposes we found blocks of approximately 1.5
kg to be very suitable.
[0022] According to another aspect of the invention, there is provided a process for manufacturing
a solid detergent block as described above. According to this process, a suitable
granular detergent powder corresponding to the desired chemical composition is compressed
in a mould under a pressure of 3-30 KN/cm².
[0023] This process can be carried out in a suitable press, preferably a hydraulic press,
for instance a LAEIS Hydraulische Doppeldrückpresse, TYP HPF 630 as manufactured by
LAEIS, West-Germany. It proved to be especially advantageous to form the block by
two or more consecutive pressings of increasing pressure. In the first step, a pre-compaction
is achieved at a relatively low pressure, which is then followed by one or more steps
at the maximal pressure. Following this procedure, a higher degree of compaction can
be achieved than by using one single pressing.
[0024] Since the pressing can be carried out at ambient temperature, high levels of heat-labile
components, such as STP or enzymes, may be incorporated in the blocks. This is regarded
as an exceptional advantage of the present invention. After manufacture, the blocks
should be packaged as soon as possible, owing to their hygroscopic nature.
[0025] Another aspect of the invention is the use of the solid blocks according to the invention
in an industrial warewashing or fabric washing process.
[0026] In use, the compressed block is placed inside a suitable dispenser, in which it is
sprayed upon with water in order to obtain an aqueous solution of the solid detergent
material. Depending on the nature of the solid block, the water may also form a slurry
or suspension of the chemical. For the purpose of this invention, all these possibilities
shall be referred to hereafter as aqueous chemical solution.
[0027] Suitable dispensers for solid blocks are known in the art. A good constant delivery
was for example obtained when the compressed block according to the invention was
placed in a dispenser as described in our co-pending British application 8830006.6.
[0028] The invention will now be further explained by the following non-limiting Examples.
Examples 1-5
[0029] Batches of 4.3 kg each of the detergent compositions shown in Table I (weight %)
were compressed in a LAEIS hydraulic press, TYP HPF 630, to form solid blocks of 17.5
x 21 cm, having a height of 7.5 cm. The compression was carried out in two steps.
First, a pressure of 5.3 KN/cm² was applied, then a second compression was carried
out at 6.4 KN/cm².
Table I
|
1 |
2 |
3 |
4 |
5 |
Sodium tripolyphosphate.6 aq. |
30.5 |
30.0 |
29.0 |
31.0 |
0 |
Sodium tripolyphosphate.0 aq. |
0 |
0 |
0 |
0 |
30.5 |
NaOH |
59.0 |
51.0 |
49.0 |
62.0 |
59.0 |
Polyacrylate |
5.0 |
5.0 |
5.0 |
5.0 |
5.0 |
Na dichloroisocyanurate |
3.5 |
0 |
0 |
0 |
3.5 |
Triton DF 12 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
Dequest 2041 |
0 |
2.0 |
2.0 |
0 |
0 |
Sodium-metasilicate.5 aq. |
0 |
10.0 |
0 |
0 |
0 |
Sodium perborate monohydrate |
0 |
0 |
10.0 |
0 |
0 |
TAED |
0 |
0 |
3.0 |
0 |
0 |
[0030] The blocks obtained were then stored in a closed container for a period of three
months at 20° or 30°C. Subsequently, they were analyzed for their sodium tripolyphosphate
(STP) and active chlorine content. The results are shown in Table II. The STP content
and the active chlorine content are expressed as a percentage of the values found
for the starting material.
Example 6
[0031] In order to investigate the delivery of the chemicals from a solid detergent block
according to the invention, a block was prepared according to Example 1. Subsequently,
it was sawn into smaller blocks of 7.5 x 7.5 x 16 cm. One of these blocks was placed
in a dispenser as described in our co-pending British application 8830006.6. Subsequently,
it was sprayed upon in portions of 200 ml water, for 10 seconds, with intervals of
60 seconds. The water had a temperature of 20°C and was of 7° German Hardness. The
conductivity of the effluent was measured as a function of the number of sprays. The
results are shown in the accompanying Figure. As can be seen from the Figure, the
concentration in the effluent was found to be essentially constant over a prolonged
period of time of more than 4 hours.
1. Solid detergent composition in the form of a block of a compressed granular material,
said block having a weight of 0.2-10 kg.
2. Solid detergent composition according to Claim 1, having a weight of 1-5 kg.
3. Solid detergent composition according to Claims 1-2, comprising:
5 - 80% by weight of an alkaline agent;
5 - 70% by weight of a builder; and
0 - 15% by weight of an active chlorine bleach;
4. Solid detergent composition according to Claims 1-3, comprising:
10 - 65% by weight of an alkaline agent;
10 - 50% by weight of a builder.
5. Solid detergent composition according to Claims 1-4, wherein the builder is sodium
tripolyphosphate.
6. Solid detergent composition according to Claims 1-5, wherein the active chlorine
bleach is sodium or potassium dichloro isocyanurate.
7. Process for the manufacturing of a solid detergent composition according to any
of Claims 1-6, whereby a powder having a corresponding composition is compressed in
a mould under a pressure of 3-30 KN/cm² to form a solid block.
8. Process according to Claim 7, whereby the block is formed by two or more consecutive
pressings of increasing pressure.
9. Process according to Claim 8, whereby the first compression is carried out at a
pressure of 3-10 KN/cm² and the second compression at a pressure of 10-30 KN/cm².
10. Use of a solid detergent composition according to Claims 1-6 in an industrial
warewashing or fabric washing process.