Citation: Bodnár, T.; Sequeira, A.
Analysis of the Shear-Thinning
Viscosity Behavior of the
Johnson–Segalman Viscoelastic
Fluids. Fluids 2022, 7, 36. https://
doi.org/10.3390/fluids7010036
Academic Editors: Kannan N.
Premnath and Ramesh Agarwal
Received: 30 November 2021
Accepted: 12 January 2022
Published: 14 January 2022
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fluids
Article
Analysis of the Shear-Thinning Viscosity Behavior of the
Johnson–Segalman Viscoelastic Fluids
Tomáš Bodnár
1,2,∗
and Adélia Sequeira
3
1
Department of Technical Mathematics, Faculty of Mechanical Engineering, Czech Technical University in
Prague, Karlovo námˇ estí 13, 121 35 Prague 2, Czech Republic
2
Institute of Mathematics, Czech Academy of Sciences, Žitná 25, 115 67 Prague 1, Czech Republic
3
Department of Mathematics and CEMAT, Instituto Superior Técnico, University of Lisbon, Av. Rovisco Pais,
1049-001 Lisbon, Portugal; adelia.sequeira@tecnico.ulisboa.pt
* Correspondence: Tomas.Bodnar@fs.cvut.cz; Tel.: +420-2-2435-7548
Abstract: This paper presents a numerical comparison of viscoelastic shear-thinning fluid flow
using a generalized Oldroyd-B model and Johnson–Segalman model under various settings. Results
for the standard shear-thinning generalization of Oldroyd-B model are used as a reference for
comparison with those obtained for the same flow cases using Johnson–Segalman model that has
specific adjustment of convected derivative to assure shear-thinning behavior. The modeling strategy
is first briefly described, pointing out the main differences between the generalized Oldroyd-B model
(using the Cross model for shear-thinning viscosity) and the Johnson–Segalman model operating in
shear-thinning regime. Then, both models are used for blood flow simulation in an idealized stenosed
axisymmetric vessel under different flow rates for various model parameters. The simulations are
performed using an in-house numerical code based on finite-volume discretization. The obtained
results are mutually compared and discussed in detail, focusing on the qualitative assessment of the
most distinct flow field differences. It is shown that despite all models sharing the same asymptotic
viscosities, the behavior of the Johnson–Segalman model can be (depending on flow regime) quite
different from the predictions of the generalized Oldroyd-B model.
Keywords: viscoelastic fluid; shear-thinning viscosity; Johnson–Segalman model; generalized Oldroyd-B
model
1. Introduction
Many fluids of practical interest exhibit a complex behavior that cannot be predicted
using mathematical models employing the classical Newtonian rheological laws. Phe-
nomena such as shear-thinning/thickening, yield stress, stress relaxation or viscoelastic
behavior are quite commonly observed in real fluids, but fail to be properly represented
using classical Newtonian fluids models. A wide class of so-called non-Newtonain models
was developed and used to capture specific fluid properties and flow behavior. A compre-
hensive overview and discussion of complex fluid rheology and corresponding models
can be found for example in classical books [1–3] or in papers [4,5]. From the plethora of
non-Newtonian fluids properties we will only remind and discuss two, the shear-thinning
and viscoelasticity, that are relevant within the scope of this paper.
The shear-thinning behavior is typically captured by a specific sub-class of the so
called generalized Newtonian models. In classical Newtonian models the stress tensor
is directly proportional (by a constant coefficient named viscosity) to the fluid rate of
strain tensor (which is nothing but symmetric part of velocity gradient). The generalized
Newtonian models follow this concept, but allow the proportionality coefficient (viscosity)
to be variable, typically depending on some relevant physical quantities, most importantly
the invariants of the rate of strain tensor. Classical representative of this class of generalized
Newtonian models is the well known power law viscosity model. The shear-thinning
Fluids 2022, 7, 36. https://doi.org/10.3390/fluids7010036 https://www.mdpi.com/journal/fluids