Home » Colouration Methods
When selecting a method of colouration the processor should assess the alternatives available and decide which is the most suitable for his particular circumstances. No single method of colouration is ideal for all applications.
To assist comparison all of the colouring methods in the section are evaluated under the following headings:
If very large runs are involved, colour can be added at the primary extrusion stage when the reactor powder is being converted to granules. It is far more common to re-extrude natural granules together with colourants. Thus compound usually commands a significant surcharge over uncoloured resin, so it is mostly used where other colouring methods are not suitable e.g. rotational moulding. Where the natural polymer needs to be compounded anyway e.g. talc-filled PP, the compound is generally coloured at the same time.
In-plant colouring, where the plastics processor adds the colourant to natural polymer, is on the whole the most economical and versatile method of colouring thermoplastics. Money and space are not tied up in keeping large stocks of various coloured compounds – only natural polymer needs to be stocked.
Suitably colour matched preparations may be supplied in the form of dry colour, masterbatch or liquid colour. Dry colour is almost never used in Australia any more – it is only included here for the sake of completion. Whichever type of preparation is chosen, the processor may blend the colourant with natural polymer and transport the mix to the machine, or add colourant at the machine using an automatic dispenser.
Colourants pre-blended to a specific shade, usually incorporating extenders and dispersion aids. Dry colour is usually mixed with plastic granules in a slow speed blender e.g. tumble mixer, and the mixture transported to the moulding machine. Using disposable plastic drum liners will reduce clean down times. Adding a small amount of a wetting agent such as paraffin oil, epoxidized soya bean oil, etc. when tumble mixing, will eliminate dusting and improve dispersion.
These materials contain high pigment loadings, typically 20% to 80%, pre-dispersed in specific thermoplastic resins.
Normal usage rates are 1% to 5% by weight of natural resin. Masterbatches are usually supplied as granules. For critical applications it is usual to use a masterbatches based on a similar resin to the one being processed. “Universal” or “multipurpose” masterbatches compatible with a number of thermoplastics are available. They have the advantage of reducing the quantity of colourant stocks.
Here the colourants are dispersed in a liquid vehicle. Non-reactive, high boiling point liquids are used, which form an integral part of the polymer matrix when processed. Pigment loadings are usually between 20% and 65% and typical usage is 0.1% to 2% by weight of natural polymer. Pigment loadings are restricted by the need to retain a pumpable viscosity. Liquid colour is usually metered directly onto the screw, using an automatic metering pump activated by the screw back cycle. Diaphragm, piston and peristaltic pumps are available. The peristaltic pump has proven to be the most popular – least clean-up required during colour changes.
The method involves using pigments and dyes as supplied by their manufacturers. It is sometimes used when processing PVC powder e.g. pipe and profile extrusion. This colouring method is the cheapest and most versatile type of in-plant colouring, but is not practical for most plastic converters.
In general best dispersion and also the most uniform melt quality is obtained when a large percentage of the energy input is supplied mechanically. When injection moulding this can be done by lowering barrel temperatures and increasing the back-pressure and screw speed to generate extra heat mechanically. Special compounding screws that help to homogenize the melt are available for most machines.
Problems encountered with mixing the colour uniformly throughout the plastics e.g. with masterbatch used at very low addition rates, can be solved by fitting a mixing nozzle to an injection moulding machine or a melt blender to an extruder.
I have discussed the colorants which possess a balance of properties that makes them suitable for plastics. The choice in any individual situation is made from the total range available, both organic and inorganic, usually combining the two types.
Having settled on a particular matching, there are then several different colouring methods available and no single one is ideal for all applications.
When planning to manufacture a coloured article, the plastics processor would normally consult his suppliers and consider the available alternatives. The colouring method which achieves the required quality standard most efficiently and at the lowest overall cost is then selected.
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