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

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2.5. BRANCHED POLYMERS 41<br />

density polyethylene (LDPE) using the multimode approach described by Inkson et al.<br />

(1999). Commercial LDPE is a polydisperse blend <strong>of</strong> molecules with multiple irregularly<br />

spaced long chain branches. Each section <strong>of</strong> this complex molecular architecture<br />

has its own time-scales for orientation and stretch relaxation. Under the multimode<br />

method these sections are modelled by a superposition <strong>of</strong> pom-pom molecules <strong>of</strong> differing<br />

relaxation times and arm numbers. <strong>The</strong> stress contribution <strong>of</strong> these pom-pom<br />

molecules is then summed to obtain the total stress,<br />

σ<br />

≈<br />

=<br />

n∑ n∑<br />

σ = 3 g i λ 2<br />

≈<br />

i S (2.43)<br />

i ≈ i.<br />

i=1 i=1<br />

<strong>The</strong> approximation is the decoupling <strong>of</strong> the modes <strong>of</strong> a connected molecule. <strong>The</strong>re<br />

ought to be interactions between the separate sections on the same molecule, however<br />

these are neglected. <strong>The</strong> moduli, g i , and backbone orientation times, τ bi for a particular<br />

melt can be determined from the linear viscoelastic behaviour <strong>of</strong> the material.<br />

However, the values <strong>of</strong> τ s and q must be determined from a non-linear <strong>flow</strong> experiment,<br />

usually uniaxial extension. In the multimode formulation <strong>of</strong> the pom-pom model<br />

the direct computation <strong>of</strong> timescales from molecular structure is replaced by fitting to<br />

experimental rheology. This set <strong>of</strong> variables {τ bi , g i , τ si , q i } can then by used to make<br />

successful predictions for other simple <strong>flow</strong>s, such as shear and planar extension, and for<br />

complex geometries [Lee et al. (2001)]. <strong>The</strong> method is a generalisation <strong>of</strong> the practice<br />

<strong>of</strong> fitting a spectrum <strong>of</strong> Maxwell modes to linear oscillatory shear data. In this case the<br />

spectrum is extended to include non-linear parameters and the pom-pom model is used<br />

as the <strong>under</strong>lying theory. It should be noted that the range <strong>of</strong> phenomena captured by<br />

this approach is significantly larger than that <strong>of</strong> linear response.<br />

2.5.4 Discussion <strong>of</strong> multimode pom-pom model<br />

On first inspection the decoupling <strong>of</strong> different sections <strong>of</strong> a connected molecule appears<br />

to be severe approximation. It is then, perhaps, surprising that the method works<br />

so well. Blackwell et al. (2001) have investigated this decoupling by deriving a more<br />

rigorous tube theory for symmetric molecules containing multiple layers <strong>of</strong> branching<br />

including the appropriate coupling through the branch points. <strong>The</strong>y compared their<br />

predictions to those <strong>of</strong> the multimode pom-pom and managed to identify some discrepancies<br />

which also appear in the comparison <strong>of</strong> the pom-pom model with real data.<br />

Generally, the errors were not serious, though. It is likely that the errors associated<br />

with the decoupling occur a large strains, particularly in steady state. In this case the<br />

errors will be screened out by the viscous contribution from modes which are in linear<br />

response. This mechanism also explains why the multi-mode pom-pom can be used to<br />

model non-linear shear <strong>of</strong> branched <strong>polymer</strong> melts despite the omission <strong>of</strong> CCR (see

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