[0001] The present invention relates to the field of coated particulate detergent components
or compositions.
[0002] It is known that the flow properties of granular detergents can be improved by "dusting"
them with finely divided particulates, such as zeolite. US-A-3 868 336 discloses detergent
compositions dusted with from 0.5% to 15% by weight of water-insoluble flow-promoting
agents. However, dusting with finely divided particulates does not provide any benefit
for detergent dispensing, it can also make the final detergent product dusty, and
it does not always provide adequate improvements in the flow properties.
[0003] Other coating agents, applied as liquids, melts or solutions are also known in the
field of detergents. GB-A-1 395 006, published on 21st May 1975, discloses cellulosic
polymers as coating agents for detergent components. Sucrose and glucose are also
disclosed therein, as plasticizers with dextrin. However cellulosic polymers and sugars
are nowhere disclosed in combination as coating agents for detergent components.
[0004] The disadvantage of coating a detergent with cellulosic polymer on its own is that
the film formed is slow to dry, and can form a coating that is sticky.
[0005] Mixtures of cellulosic polymers and sugars are known coating agents in the pharmaceutical
field.
JP-51 123 815, published 29th October 1976, and EP-A-0 551 700, published on 21st
July 1993 both disclose combinations of cellulosic polymer and sugars as coating agents
for pharmaceutical products, but there is no suggestion that these coatings are suitable
for use with detergents.
[0006] The object of the present invention relates the application of certain coatings to
particulate detergent components or compositions to improve free-flow properties,
improve dispensing, avoid dust formation and improve stability of storage sensitive
materials.
[0007] A further object of the present invention is to provide a fast-drying coating which
forms a continuous film around the particles of the detergent component or composition.
Summary of the Invention
[0008] The object of the invention is achieved by a two-step coating process, wherein the
first coating step comprises the process of mixing the detergent composition or component
with a finely divided particulate material which is preferably aluminosilicate, and
the second coating step comprises the process of applying a coating agent. Suitable
coating agents comprise from 5% to 95%, preferably from 10% to 60% by weight of cellulosic
polymer; from 5% to 95%, preferably from 60% to 90% by weight of sugar; and optionally,
from 0% to 30% by weight of plasticizer.
[0009] Preferred detergent components include nonionic surfactant, in particular polyhydroxy
fatty acid amide; and bleach activators.
Detailed Description of the Invention
[0010] The term "cellulosic polymer" as used herein means polymers that are built up from
derivatives of cellulose. Cellulose is a polysaccharide made from β-D-glucose units
linked together. In the derivatives one or more of the hydroxyl groups are replaced
by other groups e.g. methyl, ethyl, propyl.
Preferred cellulosic polymers include methyl cellulose, ethyl cellulose, hydroxymethyl
cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, methylhydroxymethyl cellulose,
methylhydroxyethyl cellulose, methylhydroxypropyl cellulose and ethyl hydroxyethyl
cellulose.
[0011] The term "sugar" as used herein is a generic term for a class of carbohydrates which
are usually crystalline and sweet by nature, and which are water soluble. Sugars are
formed form glucose and fructose units which are sugars in their own right. Preferred
sugars include glucose, fructose, galactose, sucrose, maltose, lactose, sorbitol,
manitol, rafinose, trehalose.
[0012] The term "plasticizer" as used herein is a material that is added to the original
material for the purpose of softening the original material, and make it more flexible.
Preferred plastisizers include polyethylene glycol having a molecular weight of between
200 and 20000, polypropylene glycol, glycerol, triacetin
[0013] The second coating agent may be applied in any conventional coating apparatus. Suitable
apparatus include pan coater; rotating drum continuous coater; spray fluidised granular,
or spray fluidised continuous belt. In a particular embodiment of the present invention
the components of the second coating agent are dissolved or dispersed in a suitable
solvent or carrier medium. A preferred solvent is water, and an aqueous solution may
be prepared which is typically 5% to 40% solids.
[0014] The solution or dispersion may then be sprayed on to the detergent component or composition.
The proportion of the second coating agent needed to provide a suitable coating layer
depends on various parameters, such as the surface characteristics of the detergent
component or composition, and will be easily determined by experiment. Preferably
the second coating agent is from 0.1% to 30% of the finished product, more preferably,
from 1% to 5%, and most preferably about 2%.
[0015] In the present invention, the detergent component or composition is coated with a
finely divided particulate material prior to coating with the second coating agent.
[0016] The detergent component or composition is coated with a first coating agent comprising
up to 35%, preferably from 1% to 20% by weight of finely divided particulate material
prior to the application of the second coating agent. The first coating agent has
two purposes. Firstly it allows the detergent particles to be separated (if they are
sticky) so that each one can be fully coated. Secondly it gets combined into the second
coating agent and adds additional structure to the coating.
[0017] Finely divided particulate materials useful herein include aluminosilicates having
the empirical formula:
M
z (zAlO
2)
y ] · x H
2O
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.
Useful aluminosilicate ion exchange materials are commercially available. These aluminosilicates
can be crystalline or amorphous in structure and can be naturally-occurring aluminosilicates
or synthetically derived. A method for producing aluminosilicate ion exchange materials
is disclosed in US-A-3 985 669, Krummel et al, issued October 12, 1976. Preferred
synthetic crystalline aluminosilicate ion exchange materials useful herein are available
under the designations zeolite A, zeolite P(B), zeolite MAP, zeolite X and zeolite
Y. In an especially preferred embodiment, the crystalline aluminosilicate ion exchange
material has the formula :
Na
12 [(AlO
2)
12 (SiO2)
12 ] · x H
2O
wherein x is from about 20 to about 30, especially about 27. This material is known
as zeolite A. Dehydrated zeolites (x=0-10), and "overdried" zeolites (x=10-20) may
also be used herein. The "overdried" zeolites are particularly useful when a low moisture
environment is required, for example to improve stability of detergent bleaches such
as perborate and percarbonate. Preferably, the aluminosilicate has a particle size
of about 0.1-10 micrometers in diameter. Preferred ion exchange materials have a particle
size diameter of from about 0.2 micrometers to about 4 micrometers. The term "particle
size diameter" herein represents the average particle size diameter by weight of a
given ion exchange material as determined by conventional analytical techniques such
as, for example, microscopic determination utilizing a scanning electron microscope.
The crystalline zeolite A materials herein are usually further characterized by their
calcium ion exchange capacity, which is at least about 200 mg equivalent of CaCO
3 water hardness/g of aluminosilicate, calculated on an anhydrous basis, and which
generally is in the range of from about 300 mg eq./g to about 352 mg eq./g. The zeolite
A materials herein are still further characterized by their calcium ion exchange rate
which is at least about 2 grains Ca
++/gallon/minute/gram/gallon (0.13g Ca
++/litre/minute/gram/litre) of aluminosilicate (anhydrous basis), and generally lies
within the range of from about 2 grains/gallon/minute/gram/gallon(0.13g Ca
++/litre/minute/gram/litre) to about 6 grains/gallon/minute/gram/gallon (0.39g Ca
++/litre/minute/gram/litre), based on calcium ion hardness. Optimum aluminosilicate
for builder purposes exhibit a calcium ion exchange rate of at least about 4 grains/gallon/minute/gram/gallon
(0.26g Ca
++/litre/minute/gram/litre).
Other finely divided particulate materials include talc, silica and bentonite, as
well as other clays.
Particulate Detergent Components or Compositions
[0018] Detergent components or compositions are conventionally processed into particulate
form in one of a number of ways. Spray-drying is one such process which has been widely
practised for may decades. More recently dry neutralisation, agglomeration, extrusion,
granulation in fluidised beds, flaking, encapsulation, prilling, pastillation and
other processes have also been used.
[0019] Detergent compositions and components typically comprise surfactants, builders, chelants,
bleach, bleach activators, enzymes, enzyme stabilisers, soil release agents, brightener,
suds suppressor, fabric softener, antiredeposition agents and mixtures of these. The
present invention is particularly suitable for use with nonionic or cationic surfactants,
or with bleach activators.
[0020] Preferred nonionic surfactants for use in the present invention include two families
of nonionics which have been found to be particularly useful. These are nonionic surfactants
based on alkoxylated (especially ethoxylated) alcohols, and those nonionic surfactants
based on amidation products of fatty acid esters and N-alkyl polyhydroxy amine. The
amidation products of the esters and the amines are generally referred to herein as
polyhydroxy fatty acid amides. Particularly useful in the present invention are mixtures
comprising two or more nonionic surfactants wherein at least one nonionic surfactant
is selected from each of the groups of alkoxylated alcohols and the polyhydroxy fatty
acid amides.
[0021] Suitable nonionic surfactants include compounds produced by the condensation of alkylene
oxide groups (hydrophilic in nature) with an organic hydrophobic compound, which may
be aliphatic or alkyl aromatic in nature. The length of the polyoxyalkylene group
which is condensed with any particular hydrophobic group can be readily adjusted to
yield a water-soluble compound having the desired degree of balance between hydrophilic
and hydrophobic elements.
[0022] Particularly preferred for use in the present invention are nonionic surfactants
such as the polyethylene oxide condensates of alkyl phenols, e.g., the condensation
products of alkyl phenols having an alkyl group containing from about 6 to 16 carbon
atoms, in either a straight chain or branched chain configuration, with from about
4 to 25 moles of ethylene oxide per mole of alkyl phenol.
[0023] Preferred nonionics are the water-soluble condensation products of aliphatic alcohols
containing from 8 to 22 carbon atoms, in either straight chain or branched configuration,
with an average of up to 25 moles of ethylene oxide per more of alcohol. Particularly
preferred are the condensation products of alcohols having an alkyl group containing
from about 9 to 15 carbon atoms with from about 2 to 10 moles of ethylene oxide per
mole of alcohol; and condensation products of propylene glycol with ethylene oxide.
Most preferred are condensation products of alcohols having an alkyl group containing
from about 12 to 15 carbon atoms with an average of about 3 moles of ethylene oxide
per mole of alcohol.
[0024] It is a particularly preferred embodiment of the present invention that the nonionic
surfactant system also includes a polyhydroxy fatty acid amide component.
[0025] Polyhydroxy fatty acid amides may be produced by reacting a fatty acid ester and
an N-alkyl polyhydroxy amine. The preferred amine for use in the present invention
is N-(R1)-CH2(CH2OH)4-CH2-OH, where R1 is typically a alkyl, e.g. methyl group; and
the preferred ester is a C12-C20 fatty acid methyl ester.
[0026] Methods of manufacturing polyhydroxy fatty acid amides have been described in WO
92 6073, published on 16th April, 1992. This application describes the preparation
of polyhydroxy fatty acid amides in the presence of solvents. In a highly preferred
embodiment of the invention N-methyl glucamine is reacted with a C12-C20 methyl ester.
[0027] Other nonionic surfactants which may be used as components of the surfactant systems
herein include ethoxylated nonionic surfactants, glycerol ethers, glucosamides, glycerol
amides, glycerol esters, fatty acids, fatty acid esters, fatty amides, alkyl polyglucosides,
alkyl polyglycol ethers, polyethylene glycols, ethoxylated alkyl phenols and mixtures
thereof.
[0028] The present invention is particularly useful with bleach activators. For hygiene
reasons, the inhalation of many bleach activators should be avoided, so dusty products
should be avoided. The present invention provides a means for minimising or eliminating
dust formation by providing an effective coating.
Particularly suitable bleach activators are caproyl oxybenzene sulfonate; N,N,N
1N
1 tetra acetylated compounds; benzoyloxybenzene sulphonate; benzoyl caprolactam; and
mixtures thereof. Most suitable bleach activators are (6-octanamido-caproyl)oxybenzenesulfonate,
(6-nonanamido-caproyl)oxy benzene sulfonate, (6-decanamido-caproyl)oxybenzenesulfonate,
and mixtures thereof.
Example 1
[0029]
| |
% by weight |
| Poly hydroxy fatty acid amide |
49 |
| Nonionic surfactant (AE5) |
22 |
| Hydrogenated fatty acid |
17 |
| First coating agent - Zeolite A |
10 |
| Second coating agent |
2 |
[0030] A molten mixture consisting of the nonionic surfactants polyhydroxy fatty acid amide,
ethoxylated alcohol and the hydrogenated fatty acid was prepared. Micropastilles of
the molten mixture were then made by forming drops of the molten material on a cold
steel belt, where they solidify. Apparatus for carrying out micropastillation is commercially
available from Sandvik.
[0031] The micropastilles were then coated first with the zeolite (10% by weight), and subsequently
coated with the coating agent which was an aqueous solution with a solids content
of 15%, the solids content comprising hydroxy propyl methyl cellulose (35 parts),
lactose (45 parts), and triacetin (20 parts).
[0032] The first coating of zeolite was applied in a concrete mixer to ensure good distribution
of the flow aid. The second coating agent was applied by spraying the aqueous coating
in a spray fluid bed granulator. The aqueous coating was sprayed onto the particles,
and warm air was used to dry off the excess water.
Example 2
[0033]
| |
% by weight |
| NACA-OBS |
68 |
| Citric acid |
10 |
| Anionic surfactant (AE3S) |
5 |
| Maleic-acrylic copolymer |
5 |
| Water |
2 |
| First coating agent - Zeolite A |
5 |
| Second coating agent |
5 |
NACA-OBS is nonyl amido caproyl oxy benzene sulphonate which is a bleach activator.
AE3S is alkyl ether sulphate (with 3 EO groups per molecule). |
[0034] A detergent component comprising the bleach activator, citric acid, anionic surfactant,
copolymer and water was prepared by mixing the dry materials and binders and passing
the mixture through an extruder forming noodles of materials. These noodles are allowed
to drop into a spheroniser (a Marumeriser® having a rotating bowl with a friction
plate) which shapes beads of the desired size.
[0035] The beads were then coated first with the zeolite (5% by weight), and subsequently
coated with the second coating agent which was an aqueous solution with a solids content
of 15%, the solids content comprising hydroxy propyl methyl cellulose (35 parts),
lactose (45 parts), and triacetin (20 parts). The coating was applied in a fluid bed
granulator.
Example 3
[0036]
| |
% by weight |
| Poly hydroxy fatty acid amide |
6 |
| Nonionic surfactant (AE5) |
18 |
| Hydrogenated fatty acid |
3 |
| Glycerol Tristearate |
1 |
| Zeolite A |
56 |
| Carbonate |
6 |
| First coating agent - Zeolite A |
5 |
| Second coating agent |
5 |
[0037] A molten mixture consisting of the nonionic surfactants polyhydroxy fatty acid amide,
ethoxylated alcohol, hydrogenated fatty acid and glycerol tristearate was prepared.
This paste was cooled and agglomerated in a CB Loedige® with the zeolite and carbonate.
The finished agglomerates were dusted with additional zeolite in a KM Loedige®.
[0038] The agglomerates were subsequently coated with the second coating agent which was
an aqueous solution with a solids content of 40%, the solids content comprising hydroxy
propyl methyl cellulose (10 parts), lactose (45 parts), and sucrose (45 parts).
[0039] The second coating agent was applied by spraying the aqueous coating in a spray fluid
bed granulator. The aqueous coating was sprayed onto the particles, and warm air was
used to dry off the excess water.
1. A particulate detergent composition or component; the detergent composition or component
being coated by a two-step coating process, wherein the first coating step comprises
the process of mixing the detergent composition or component with a finely divided
particulate material, and characterised in that the second coating step comprises
the process of applying an coating agent, the coating agent comprising:
(i) from 5% to 95% by weight of a cellulosic polymer;
(ii) from 5% to 95% by weight of a sugar.
2. A particulate detergent composition or component according to claim 1 wherein the
coating agent applied in the second coating step comprises:
(i) from 10% to 60% by weight of a cellulosic polymer;
(ii) from 60% to 90% by weight of a sugar; and
(iii) optionally from 0% to 30% by weight of a plasticizer.
3. A particulate detergent composition or component according to claim 1 wherein the
finely divided particulate material is aluminosilicate.
4. A detergent composition or component according to claim 1 wherein the coating agent
comprises cellulosic polymers selected from the group consisting of methyl cellulose,
ethyl cellulose, hydroxymethyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose,
methylhydroxymethyl cellulose, methylhydroxyethyl cellulose, methylhydroxypropyl cellulose,
ethyl hydroxyethyl cellulose or mixtures thereof.
5. A detergent composition or component according to claim 1 wherein the coating agent
comprises sugar selected from the group consisting of sucrose, glucose, lactose, fructose,
dextrin, cellulose, sorbitol, rafinose, trehalose or mixtures thereof.
6. A detergent composition or component according to claim 1 wherein the coating agent
comprises at least 1% by weight of a plasticizer selected from the group consisting
of polyethylene glycol, polypropylene glycol, having a molecular weight of between
200 and 20000; glucose, triacetin or mixtures thereof.
7. A detergent composition or component according to any of claims 1 to 6 wherein the
detergent component or composition comprises nonionic surfactant.
8. A detergent composition or component according to claim 7 wherein the nonionic surfactant
comprises polyhydroxy fatty acid amide.
9. A detergent composition or component according to any of claims 1 to 6 wherein the
detergent component or composition comprises bleach activator selected from the group
consisting of caproyl oxybenzene sulfonate; N,N,N1N1 tetra acetylated compounds; (6-octanamido-caproyl)oxybenzenesulfonate, (6-nonanamidocaproyl)oxy
benzene sulfonate, (6-decanamido-caproyl)oxybenzenesulfonate; benzoyl caprolactam,
and mixtures thereof.