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Molecular modelling of entangled polymer fluids under flow The ...

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50 CHAPTER 3. THE POM-POM MODEL IN EXPONENTIAL SHEAR.<br />

against experimental data from Zülle et al. (1987), Venerus (2000) and Suneel et al.<br />

(Submitted) using the multimode generalisation [Inkson et al. (1999)] in section 3.3.<br />

3.2 Single mode pom-pom model<br />

Zülle et al. (1987) make a distinction between two types <strong>of</strong> exponential shear: true<br />

exponential shear as defined in equation 3.1 and nearly exponential shear. Nearly<br />

exponential shear has a shear rate that grows as ˙γ(t) = αe αt . It differs from true<br />

exponential shear by a decaying term <strong>of</strong> αe −αt and hence the two <strong>flow</strong>s converge when<br />

αt ≫ 1. Note that nearly exponential shear does not have a purely exponential growth<br />

<strong>of</strong> the extension ratio, except in the limit <strong>of</strong> long times where the behaviour approaches<br />

true exponential shear. Consequentially the two <strong>flow</strong>s are qualitatively similar and the<br />

data converge for large strains [Zülle et al. (1987)]. In this section the solutions to the<br />

pom-pom equations for nearly exponential shear will be analysed. Since most <strong>of</strong> this<br />

analysis will be in the t ≫ 1/α limit the results will also hold for true exponential shear.<br />

<strong>The</strong> solutions to the pom-pom equations for simple shear and planar extension have<br />

been previously studied [see McLeish and Larson (1998), Bishko et al. (1999), Inkson<br />

et al. (1999), Blackwell et al. (2000)]; they will serve as comparisons to the solutions in<br />

exponential shear.<br />

3.2.1 Solutions to the orientation equation<br />

<strong>The</strong> orientation equation in table 2.2 can be solved analytically for simple shear, nearly<br />

and true exponential shear and planar extension. Throughout the chapter I will be<br />

assume that, for shear <strong>flow</strong>s, the <strong>flow</strong> is in the x-direction and that the velocity gradient<br />

is in the y-direction. For planar extension the principle stretch will always occur in the<br />

x direction with the z-direction neutral. Simple shear <strong>flow</strong> is usually described by the<br />

transient stress growth co-efficient, which is defined as η + (t, ˙γ) = σ xy / ˙γ. <strong>The</strong>re is some<br />

ambiguity in the definition <strong>of</strong> an equivalent material function for exponential shear. In<br />

previous studies a variety <strong>of</strong> material functions have been used, including dividing the<br />

shear stress by the instantaneous shear rate, ˙γ(t). In this chapter I will simply divide<br />

by the initial shear rate, ˙γ 0 . Note that for true exponential shear ˙γ 0 = 2α and for<br />

nearly exponential shear ˙γ 0 = α<br />

In shear <strong>flow</strong>s the rate at which the <strong>flow</strong> stretches the backbone segments, κ : S,<br />

≈ ≈<br />

is equal to ˙γS xy . In addition, S xy is also the component <strong>of</strong> the orientation tensor that<br />

appears in the shear stress. Figure 3.1 shows the solution to the orientation equation for<br />

simple shear with a variety <strong>of</strong> backbone orientation times. For shear rates greater than<br />

1/τ b , S xy rises to a maximum before approaching its steady state value. By maximising<br />

lim t→∞ S xy (t) with respect to τ b the value <strong>of</strong> τ b which produces the largest steady state

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