1990
DOI: 10.1007/bf01332379
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Rheological properties of dilute polymer solutions: An extended thermodynamic approach

Abstract: It is shown that extended irreversible thermodynamics can be used to account for the shear rate and frequency dependences of several material functions like shear viscosity, first and second normal stress coefficients, dynamic viscosity and storage modulus. Comparison with experimental data on steady shearing and small oscillatory shearing flows is performed. A good agreement between the model and experiment is reached in a wide scale of variation of the shear rate and the frequency of oscillations. The relati… Show more

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Cited by 16 publications
(7 citation statements)
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“…Viscosity is shear-dependent, or stress is not directly proportional to the deformation. Rheological models for both linear viscoelasticity and nonlinear generalized Newtonian fluids can also be derived [5,163,164,200,201,[211][212][213][214][215][216], as we have pointed out in Section 5.1., by specializing the evolution equations of EIT. We proceed to give concrete cases.…”
Section: Special Cases: Theological Modelsmentioning
confidence: 99%
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“…Viscosity is shear-dependent, or stress is not directly proportional to the deformation. Rheological models for both linear viscoelasticity and nonlinear generalized Newtonian fluids can also be derived [5,163,164,200,201,[211][212][213][214][215][216], as we have pointed out in Section 5.1., by specializing the evolution equations of EIT. We proceed to give concrete cases.…”
Section: Special Cases: Theological Modelsmentioning
confidence: 99%
“…The internal energy of a solution of elastic dumbbells is not the same in equilibrium as in shear. The rheological models for polymer solutions [5, 164,200,201,[215][216][217][218][219] assume that the roles of solvent and polymer can be separated. The viscous pressure tensor is decomposed [218,219] into two parts P* = P 0 + P p (143) where subscripts "o" and "p" denote the contribution of the solvent and polymer, respectively.…”
Section: B Polymer Solutionsmentioning
confidence: 99%
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“…In order to fulfil the objectivity requirement, the coefficient C has to be taken constant while E must be zero : otherwise Juk,k and consequently the r.h.s, of (3. has been shown to account in a fairly good way for the steady and oscillatory sheafing flows if it is admitted that x, ~q and a are power-laws of the invariants of Pi~ [14]. Comparison between experimental data and the present model is reported on figures 1 and 2 for a 2.5%…”
Section: Extended Thermodynamics Of Second-order Non-newtonian Fluidsmentioning
confidence: 79%
“…In figure 2, the material functions r I' (dynamic viscosity) and G' (storage modulus) are represented as a function of the oscillations frequency 0~. The solid lines represent the theoretical predictions; results corresponding to other materials can be found in [14]. …”
Section: Extended Thermodynamics Of Second-order Non-newtonian Fluidsmentioning
confidence: 98%