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The effects of fluid viscoelasticity on the expansion of gas bubbles in
polymer foams for both non-reactive and reactive polymers are investigated.
Polymer foams are used extensively in consumer products, from car parts
to upholstery. They are produced either by injection moulding (of non-reactive
polymeric fluids) or reaction injection moulding.
We use standard rheological models (Oldroyd B and Pompom) to investigate
bubble growth driven by gas diffusion as a model for injection moulding. To
model reaction injection moulding, we develop a new fluid model based on
existing linear theory for a gelling liquid. In this case gas is produced as
a by-product of the polymer reaction.
At small bubble volume fractions gas bubbles remain spherical and isolated
from neighbouring bubbles during expansion. In this regime we demonstrate the
effects of rheology and gelation on the bubble growth.
At high bubble volume fractions neighbouring bubbles compete for the available
gas and become distorted in shape. The effects of viscoelasticity on the
expansion of gas bubbles arranged in a two-dimensional hexagonal array in a
non-reacting polymeric fluid are investigated. In addition to a full finite
element calculation of the two-dimensional flow, two one-dimensional
approximations valid in the limits of small and large gas area fractions are
presented. We show that these approximations give accurate predictions of the
evolution of the bubble area, but give less accurate predictions of the bubble
shape.
Finally we consider how bubbles of different sizes evolve in an expanding foam.
We illustrate how the surface tension driven phenomenon known as Ostwald
Ripening causes large bubbles to grow at the expense of smaller ones. For the
case of bubbles of two different sizes we examine the effects of
viscoelasticity on the shapes of the bubbles within the structure and show
that viscoelasticity has a different effect on the bubble size distribution
depending upon the initial geometry.
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