Prediction of shear and elongational properties of polymeric fluids using reversible network

with non-interacting dumbbell model

 

Alfeus Sunarso and Takehiro Yamamoto

Department of Mechanical Engineering

Graduate School of Engineering, Osaka University

2-1, Yamadaoka, Suita, Osaka 565-0871, JAPAN

 

Recently, reversible network with non-interacting dumbbell model has been proposed by Cifre et al. (J. Non-Newtonian Fluid Mech. 113 (2003) 73-96) to model the shear viscosity of associative polymer. It has been shown that this model is capable to predict the main features of associative polymer, such as the presence of Newtonian plateau at low shear rates followed by shear thickening at moderate shear rates and shear thinning at high shear rates. Although this model was initially derived for associative polymer, the basic concept of association and disassociation of network junctions can also be applied to model non-associative polymers such polymer solutions and melts in general. To use the model in the simulation of flow of polymeric fluids in complex channel, the prediction capability of the model should be further investigated. In the present work, we perform a Brownian dynamics simulation based on the work of Cifre et al. to investigate the capability of the reversible network with non-interacting dumbbell model in predicting the shear and elogation properties of polymer solutions and melts. In order to obtain more realistic prediction of elongational properties, we use a FENE connector force instead of a Hookean connector force. By adjusting the parameters controlling the association process of the dumbbells to the networks, we obtain the correct trend in prediction of rheological properties. If the association rate is proportional to the dumbbell length, the model predicts the presence of shear thickening which is typical for associative polymer, otherwise, with a constant association rate, the model predicts only shear thinning behavior (without shear thickening), which is typical for polymer solutions and melts. In the elongational flow, the increasing association rate results in elongational viscosity which is characterized by strain thickening at moderate strain rates followed strain thinning and the second strain thickening at high strain rates. For the constant association rate, there is no second strain thickening region, and the maximum extension parameter governs whether the strain thinning region at high strain rates exists or not exist. The trend in elongational viscosity in the case of constant shear rate is in agreement with the available experimental data of elongation viscosity of polymer solutions and melts.