A bead-spring-chain model including hydrodynamic-interaction effects is used to calculate the rheological properties of dilute polymer solutions undergoing steady shear flow. The hydrodynamic fluctuations are explicitly taken into account within the context of the recently developed Gaussian approximation for the hydrodynamic interaction. In this Gaussian approach expressions for the non-Newtonian stress tensor at arbitrary shear rate are calculated. For short chains, the shear-rate–dependent predictions for the viscometric functions are presented. Also, the Brownian dynamics simulation technique is applied to determine exact rheological behavior of the model. Comparing the simulation results to the corresponding predictions of the Gaussian, consistent-averaging, and preaveraging approximations the validity and the superiority of the Gaussian method is clearly demonstrated.
The Brownian dynamics simulation technique is used to calculate exact rheological properties of the Hookean-dumbbell model with hydrodynamic interaction. The simulation results for steady shear flow are compared to the corresponding predictions of the preaveraging approximation, the consistent-averaging approximation, and the Gaussian approximation developed in the preceding article. Our calculations of the viscometric functions of the Hookean-dumbbell model are performed for various hydrodynamic-interaction tensors.
A mechanical polymer model including hydrodynamic-interaction and excluded-volume effects is used to predict universal rheological and diffusive properties of dilute polymer solutions. For steady shear flow, explicit expressions for the shear-rate-dependent hydrodynamic-interaction contribution to the stress tensor and polymer diffusion tensors are obtained by employing a perturbation scheme. In the limit of long chains, these contributions are calculated systematically by using renormalization-group methods. The universal shear-rate-dependent predictions for the polymer contribution to the viscosity, the first normalstress coefficient, the ratio of the second to the first normal-stress coefficient, and the polymer diffusion tensor are presented and discussed for good and for solvents.
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