Abstract
In this paper, three-dimensional viscoelastic Taylor-Couette instability between concentric rotating cylinders is studied numerically. The aim is to investigate and provide additional insight about the formation of time-dependent secondary flows in viscoelastic fluids between rotating cylinders. Here, the Giesekus model is used as the constitutive equation. The governing equations are solved using the finite volume method (FVM) and the PISO algorithm is employed for pressure correction. The effects of elasticity number, viscosity ratio, and mobility factor on various instability modes (especially high order ones) are investigated numerically and the origin of Taylor-Couette instability in Giesekus fluids is studied using the order of magnitude technique. The created instability is simulated for large values of fluid elasticity and high orders of nonlinearity. Also, the effect of elastic properties of fluid on the time-dependent secondary flows such as wave family and traveling wave and also on the critical conditions are studied in detail.
Similar content being viewed by others
References
Andereck CD, Hayot F (Eds.). (2012). Ordered and turbulent patterns in Taylor-Couette flow (Vol. 297). Springer Science & Business Media.
Andereck CD, Liu SS, Swinney HL (1986) Flow regimes in a circular Couette system with independently rotating cylinders. J Fluid Mech 164(1):155–183. https://doi.org/10.1017/S0022112086002513
Ashrafi N (2011) Stability analysis of shear-thinning flow between rotating cylinders. Appl Math Model 35(9):4407–4423. https://doi.org/10.1016/j.apm.2011.03.010
Avgousti M, Beris AN (1993a) Viscoelastic Taylor-Couette flow: bifurcation analysis in the presence of symmetries. Proc R Soc Lond A 443(1917):17–37. https://doi.org/10.1098/rspa.1993.0129
Avgousti M, Beris AN (1993b) Non-axisymmetric modes in viscoelastic Taylor-Couette flow. J Non-Newtonian Fluid Mech 50(2-3):225–251. https://doi.org/10.1016/0377-0257(93)80033-8
Baumert BM, Muller SJ (1995) Flow visualization of the elastic Taylor-Couette instability in Boger fluids. Rehologica Acta 34(2):147–159. https://doi.org/10.1007/BF00398434
Beard D, Davies M, Walters K (1966) The stability of elastico-viscous flow between rotating cylinders part 3. Overstability in viscous and Maxwell fluids. J Fluid Mech 24(02):321–334. https://doi.org/10.1017/S0022112066000673
Benjamin T, Mullin T (1981) Anomalous modes in the Taylor experiment. Proc R Soc Lond A 377(1770):221–249. https://doi.org/10.1098/rspa.1981.0122
Carvalho M (2004) Instability of inelastic shear-thinning liquids in a Couette flow between concentric cylinders. J Fluids Eng 126:385–390
Coronado-Matutti O, Souza Mendes PR, Carvalho MS (2004) Instability of inelastic shear-thinning liquids in a Couette flow between concentric cylinders. J Fluids Eng 126(3):385–390. https://doi.org/10.1115/1.1760537
Couette MFA (1890) Etudes sur le frottement des liquides. Ann Chim 21:433–510
Denn M, Roisman J (1969) Rotational stability and measurement of normal stress functions in dilute polymer solutions. AICHE J 15(3):454–459. https://doi.org/10.1002/aic.690150328
Giesekus H (1966) Zur stabilität von Strömungen viskoelastischer Flüssigkeiten: 1. Ebene und kreisförmige Couette-Strömung. Rheol Acta 5(3):239–252. https://doi.org/10.1007/BF01982435
Giesekus H (1982) A unified approach to a variety of constitutive models for polymer fluids based on the concept of configuration-dependent molecular mobility. Rheol Acta 21(4-5):366–375. https://doi.org/10.1007/BF01534296
Jeng J, Zhu K-Q (2010) Numerical simulation of Taylor Couette flow of Bingham fluids. J Non-Newtonian Fluid Mech 165(19-20):1161–1170. https://doi.org/10.1016/j.jnnfm.2010.05.013
Khayat RE (1995) Onset of Taylor vortices and chaos in viscoelastic fluids. Phys Fluids 7(9):2191–2219. https://doi.org/10.1063/1.868469
Kupferman R (1998) A numerical study of the axisymmetric Couette-Taylor problem using a fast high-resolution second-order central scheme. SIAM J Sci Comput 20(3):858–877. https://doi.org/10.1137/S1064827597318009
Larson RG (1992) Instabilities in viscoelastic flows. Rheol Acta 31(3):213–263. https://doi.org/10.1007/BF00366504
Larson RG, Shaqfeh ES, Muller SJ (1990) A purely elastic instability in Taylor–Couette flow. J Fluid Mech 218(1):573–600. https://doi.org/10.1017/S0022112090001124
Larson R, Muller S, Shaqfeh E (1994) The effect of fluid rheology on the elastic Taylor-Couette instability. J Non-Newtonian Fluid Mech 51(2):195–225. https://doi.org/10.1016/0377-0257(94)85012-7
Lockett T, Richardson S, Worraker W (1992) The stability of inelastic non-Newtonian fluids in Couette flow between concentric cylinders: a finite-element study. J Non-Newtonian Fluid Mech 43(2-3):165–177. https://doi.org/10.1016/0377-0257(92)80023-Q
Lueptow RM, Docter A, Min K (1992) Stability of axial flow in an annulus with a rotating inner cylinder. Phys Fluids A 4:2446–2455
Ma T, Wang S (2010) Dynamic transition and pattern formation in Taylor problem. Chin Ann Math Ser B 31(6):953–974. https://doi.org/10.1007/s11401-010-0610-7
Mallock A (1888) Determination of the viscosity of water. Proc R Soc Lond 45(273-279):126–132. https://doi.org/10.1098/rspl.1888.0081
Muller SJ, Larson RG, Shaqfeh ES (1989) A purely elastic transition in Taylor-Couette flow. Rheol Acta 28(6):499–503. https://doi.org/10.1007/BF01332920
Nemri M, Climent E, Charton S, Lanoe J-Y, Ode D (2013) Experimental and numerical investigation on mixing and axial dispersion in Taylor–Couette flow patterns. Chem Eng Res Des 91(12):2346–2354. https://doi.org/10.1016/j.cherd.2012.11.010
Niu X, Shu C, Chew Y (2003) An axisymmetric lattice Boltzmann model for simulation of Taylor–Couette flows between two concentric cylinders. Int J Mod Phys C 14(06):785–796. https://doi.org/10.1142/S0129183103004929
Norouzi M, Varedi S, Maghrebi MJ, Shahmardan M (2013) Numerical investigation of viscoelastic shedding flow behind a circular cylinder. J Non-Newtonian Fluid Mech 197:31–40. https://doi.org/10.1016/j.jnnfm.2013.01.009
Oberkampf WL (2002) Discussion: “comprehensive approach to verification and validation of CFD simulations—part 1: methodology and procedures” (Stern, F., Wilson, R. V., Coleman, H. W., and Paterson, E. G., 2001, ASME J. Fluids Eng., 123, pp. 793–802). J Fluids Eng 124(3):809–810. https://doi.org/10.1115/1.1492826
Philip Z, Mukul M, Martin E (1998) The role of Taylor vortices in the transport of drill cutting, SPE India Oil and Gas Conference and Exhibition. Society of Petroleum Engineers
Pourjafar M, Sadeghy K (2012) Taylor-Couette instability of Giesekus fluids. Annu Trans Nordic Rheol Soc 20:97–97
Qi H, Jin H (2006) Unsteady rotating flows of a viscoelastic fluid with the fractional Maxwell model between coaxial cylinders. Acta Mech Sinica 22(4):301–305. https://doi.org/10.1007/s10409-006-0013-x
Quinzani LM, Armstrong RC, Brown RA (1994) Birefringence and laser-Doppler velocimetry (LDV) studies of viscoelastic flow through a planar contraction. J Non-Newtonian Fluid Mech 52(1):1–36. https://doi.org/10.1016/0377-0257(94)85056-9
Ravanchi MT, Mirzazadeh M, Rashidi F (2007) Flow of Giesekus viscoelastic fluid in a concentric annulus with inner cylinder rotation. Int J Heat Fluid Flow 28(4):838–845. https://doi.org/10.1016/j.ijheatfluidflow.2006.08.003
Ravelet F, Delfos R, Westerweel J (2010) Influence of global rotation and Reynolds number on the large-scale features of a turbulent Taylor–Couette flow. Phys Fluids 22(5):055103. https://doi.org/10.1063/1.3392773
Rayleigh L (1917) On the dynamics of revolving fluids. Proc R Soc Lond Ser A Contain Pap Math Phys Character 93:148–154
Recktenwald A, Lücke M, Müller H (1993) Taylor vortex formation in axial through-flow: linear and weakly nonlinear analysis. Phys Rev E 48(6):4444–4454. https://doi.org/10.1103/PhysRevE.48.4444
Renardy M, Renardy Y, Sureshkumar R, Beris A (1996) Hopf-Hopf and steady-Hopf mode interactions in Taylor-Couette flow of an upper convected Maxwell liquid. J Non-Newtonian Fluid Mech 63(1):1–31. https://doi.org/10.1016/0377-0257(95)01415-2
Rubin H, Elata C (1966) Stability of Couette flow of dilute polymer solutions. Phys Fluids 9(10):1929–1933. https://doi.org/10.1063/1.1761545
Stern F, Wilson RV, Coleman HW, Paterson EG (2001) Comprehensive approach to verification and validation of CFD simulations-part 1: methodology and procedures. Trans Am Soc Mech Eng J Fluids Eng 123(4):793–802. https://doi.org/10.1115/1.1412235
Taylor GI (1923) Stability of a viscous liquid contained between two rotating cylinders. Philos Trans R Soc Lond Ser A Contain Pap Math Phys Character 223:289–343
Thomas D, Al-Mubaiyedh U, Sureshkumar R, Khomami B (2006) Time-dependent simulations of non-axisymmetric patterns in Taylor–Couette flow of dilute polymer solutions. J Non-Newtonian Fluid Mech 138(2-3):111–133. https://doi.org/10.1016/j.jnnfm.2006.04.013
Van Gils DP, Huisman SG, Bruggert G-W, Sun C, Lohse D (2011) Torque scaling in turbulent Taylor-Couette flow with co-and counterrotating cylinders. Phys Rev Lett 106(2):024502. https://doi.org/10.1103/PhysRevLett.106.024502
Versteeg HK, Malalasekera W (2007) An introduction to computational fluid dynamics: the finite volume method. Pearson Education, London
Xue S-C, Phan-Thien N, Tanner R (1998) Three dimensional numerical simulations of viscoelastic flows through planar contractions. J Non-Newtonian Fluid Mech 74(1-3):195–245. https://doi.org/10.1016/S0377-0257(97)00072-4
Author information
Authors and Affiliations
Corresponding author
Electronic supplementary material
(WMV 729 kb)
(WMV 841 kb)
(WMV 1146 kb)
(WMV 2776 kb)
Appendix
Appendix
PISO algorithm
The PISO algorithm is consisted of one predictor step and two corrector steps. This algorithm can be summarized as follows (Versteeg and Malalasekera 2007):
-
i.
Assigning the initial values and boundary conditions for variables;
-
ii.
Solving the discretized equations of momentum and constitutive equation in order to determine the velocity components and the stress tensor;
-
iii.
Calculating the mass fluxes at the cell faces;
-
iv.
Solving the pressure equation;
-
v.
Correcting the mass fluxes at the cell faces;
-
vi.
Correcting the velocity components based on the new pressure;
-
vii.
Updating the boundary conditions and repeat from iii for a certain number of times;
-
viii.
Changing the time step and repeat from ii.
In the finite volume method, vector variables are saved on the control volume faces while scalar variables are stored at the grid points. Thus, for an arbitrary dependent variable, the transport equation can be written as follows (Norouzi et al. 2013):
where (κuξ − D∇ξ) is the flux term in which D represents the diffusivity. f p ξ + f c is the source term for the variable ξ. Furthermore, the mentioned source term in Eq. (A1–1) is a combination of linear and constant terms in an arbitrary choice. Thus, over a control volume, integration of Eq. (A1–1) leads to the following equation:
By using an approximation scheme for Eq. (A1–2) over the control volume, the discretized equation for the dependent variable ξ can be symbolically written as follow:
where
Order of magnitude analysis
Determination of the effect of various parameters on the formation of secondary flow is very crucial in understanding the instability conditions. Here, the order of main flow becomes greater than the order of secondary flow. Thus, the order of velocity components and their derivations can be written as follows:
The order of magnitude for polymeric stress components by assuming negligible value for the mobility factor is presented in Eq. (A2–2). This equation is calculated by simplifying the constitutive equation and neglecting the terms of order ε:
On the other hand, Eq. (A2–3) expresses the momentum equation by considering the order of magnitude analysis. By substituting the stress components into Eq. (A2–3), the resulted equation is valid in the core region (the annulus region between the cylinders and far from the walls) and can be helpful in identifying the effect of various factors on the flow stability:
In the core region, the radial pressure gradient is balanced with the centrifugal and elastic forces. In comparison with Newtonian fluid, the hoop stress leads to different behavior in viscoelastic fluids. In addition, Eq. (A2–4) states the importance of elastic number which expresses the qualitative deviation from Newtonian flow behavior. These equations are used in the paper to discuss the results of CFD simulations.
Rights and permissions
About this article
Cite this article
Norouzi, M., Jafari, A. & Mahmoudi, M. A numerical study on nonlinear dynamics of three-dimensional time-depended viscoelastic Taylor-Couette flow. Rheol Acta 57, 127–140 (2018). https://doi.org/10.1007/s00397-017-1059-3
Received:
Revised:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s00397-017-1059-3