[0001] This invention relates to a process for the manufacture of coloured detergent powder.
[0002] Coloured detergent powders are normally made by adding dye or pigment to a crutcher
slurry and converting the slurry to a powder by spray-drying. Alternatively dye solution
can be injected into the main feed to the nozzles of the spray-drying tower with similar
results. The disadvantage of these processes is that they contaminate the whole of
the spray-drying plant with dyestuff so that when a white powder is subsequently to
be made it is necessary to clean down, with consequent loss of production time.
[0003] One of the ways of avoiding this disadvantage is to spray a solution of dyestuff
onto white powder. The main difficulty with this is that of contacting each individual
particle, to an equal extent. It that is not achieved, then a speckled or mottled
powder results.
[0004] United States Patent No 4 162 228 relates to a method of colouring detergent flakes
which contain nonionic surfactant as an essential component. The method involves mixing
a dry colourant into the flakes whereupon the nonionic surfactant dissolves the colourant,
imparting an overall hue to the flakes. Flakes are, of course, easier to colour than
powders since they are translucent, and the whole formulation is contained within
the flake. In contrast, powders normally consist of two components - a spray-dried
portion and a dry-dosed portion which may have different affinities for colourant
resulting in the powder having a mottled appearance.
[0005] We have now discovered contrary to what would have been expected that coloured powder
can be manufactured by simply mixing a particulate colorant with a detergent powder.
[0006] Accordingly, the present invention provides a process for the manufacture of a coloured
detergent powder which comprises admixing a particulate colourant with the powder.
[0007] If desirable or necessary, after the mixing step, the coloured powder may be sprayed
with a small percentage, for example 1-5% by weight, of water or of an ethoxylated
alcohol nonionic surfactant in liquid or molten form. This can help to accentuate
the colouration.
[0008] When choosing the colourant system it is important to select substances which will
colour the powder adequately and yet not produce staining problems in the wash. We
have found a combination of the pigment Ultramarine Blue, the dyestuff Duasyn Acid
Blue and the blue-whitener Polar Brilliant Blue to give excellent results on all types
of detergent powder.
[0009] Other dyestuffs which have been found to be satisfactory are Carbolan Violet, Gulf
Acid Blue 6JSO and Milling Blue 2BR, all of which are available from Imperial Chemical
Industries Limited.
[0010] Preferably the mean particle size of the colourant is 0.5 to 5 microns, most preferably
abut 2 microns.
[0011] The process may be applied to powder which has been prepared by spray-drying, spray-cooling,
granulation or agglomeration or any combination of these techniques. Additionally,
any of the powder so produced may be dosed with conventional detergent powder additives
such as sodium perborate tetrahydrate without altering the effectiveness of the process.
[0012] The apparatus used for mixing the particulate colourant and the powder is not critical
to the process. We have found a rotating drum mixer to be perfectly satistactory and
also, a Patterson-Kelly (Trade Mark) batch blender has performed well.
[0013] The invention will be further described in the following example.
Example
[0014] White, spray-dried detergent powder is first fed down a chute at a flow rate of about
350 Kg/hour controlled by a slide valve into one end of the interior of a rotatable
drum mixer without internal baffles. The axis of the drum mixer is approximately horizontal
but the mean residence time of the powder in the drum which is about 2 minutes can
be adjusted to some extent by moving the axis up or down by a few degrees. The drum
is rotated and a finely powdered mixture of the following colourants is fed into the
drum from a variable speed dosing unit:

[0015] Substantially uniformly blue coloured powder emerges from the discharge end of the
drum mixer.
[0016] If desired the small quantity of water or nonionic surfactant referred to above,
say 1-3% by weight may be sprayed onto the powder in the drum through spray nozzles
located along the axis.
[0017] There are several advantages to the process described above. Most importantly it
avoids colouration of the spray-drying plant, but also it appears to be independent
of formulation, and is suitable for colouring fully-formulated powder and not just
the spray-dried portion.
1. A process for the manufacture of coloured detergent powder characterised by admixing
particulate colourant with the powder.
2. A process according to claim 1 wherein the coloured powder is sprayed with from
1 to 5% by weight of water.
3. A process according to claim 1 or claim 2 wherein the coloured powder is sprayed
with from 1 to 5% by weight of an ethoxylated alcohol nonionic surfactant in liquid
or molten form.
4. A process according to any one of the preceding claims wherein the mean particle
size of the colourant is from 0.5 to 5 microns.
5. A process according to claim 4 wherein the mean particle size ot the colourant
is about 2 microns.