Article information

2019 , Volume 24, ¹ 5, p.75-89

Ryltseva K.E., Shrager G.R.

Numerical simulation of a non-isothermal power-law fluid flow in a channel with abrupt contraction

Viscous fluid flow through a sudden contraction is frequently encountered in a number of industrial equipment dealing with processing and transporting of liquid materials. Generally, the fluid exhibits non-Newtonian behavior and flows under non-isothermal conditions. Such flow is characterized by specific structure, viscous dissipation, and local pressure losses.

In this work, a numerical solution to the problem of a non-isothermal power-law fluid flow through a two-to-one axisymmetric abrupt contraction is presented. Mathematical model includes the momentum, continuity and energy equations written in terms of stream function, vorticity and temperature variables. The rheological behavior of the fluid is specified by the Ostwald-de Waele power law. The proposed flow model accounts for viscous dissipation and temperature-dependent rheological properties. To solve the problem, the relaxation method is used, followed by the implementation of the finitedifference method based on the scheme of alternative directions. The equations in a discrete form are solved using the tridiagonal matrix algorithm.

It is found that the flow includes both one-dimensional and two-dimensional flow regions. The lengths of these regions are studied versus the Reynolds number, the Peclet numder, and power-law index. Comparing isothermal and non-isothermal cases, it is revealed that an increase in the power-law index leads to a decrease in the downstream two-dimensional zone in the first case, and, in contrast, it provides a significant increase in the second case. The viscosity and temperature distributions are presented to show the effect of the Peclet number for pseudoplastic, Newtonian, and dilatant fluids. The parametric investigation of the local pressure losses is implemented in a wide range of the main parameters.

[full text]
Keywords: non-isothermal flow, viscous dissipation, abrupt contraction, non-Newtonian fluid, the Ostwald de Waele model, flow structure, local pressure losses

doi: 10.25743/ICT.2019.24.5.007.

Author(s):
Ryltseva Kira Evgenevna
Position: engineer
Office: National Research Tomsk State University
Address: 634050, Russia, Tomsk, 36 Lenin Ave.
E-mail: kiraworkst@gmail.com
SPIN-code: 5202-8909

Shrager Gennadiy Rafailovich
Dr. , Professor
Position: Professor
Office: National Research Tomsk State University
Address: 634050, Russia, Tomsk, 36 Lenin Ave.
E-mail: shg@ftf.tsu.ru
SPIN-code: 3407-2109

References:
[1] Astarita, G., Greco, G. Excess pressure drop in laminar flow through sudden contraction. Non-Newtonian liquids with droplets. Industrial & Engineering Chemistry Fundamentals. 1968; 7(4):595–598.

[2] Rama Murthy, A.V., Boger, D.V. Developing velocity profiles on the downstream side of a contraction for inelastic polymer solutions. Transactions of the Society of Rheology. 1971; 15(4):709–730.

[3] Christiansen, E.B., Kelsey, S.J., Carter, T.R. Laminar tube flow through an abrupt contraction. American Institute Of Chemical Engineers Journal. 1972; 18(2):372–380.

[4] Oliveira, M.S.N., Oliveira, P.J., Pinho, F.T., Alves, M.A. Effect of contraction ratio upon viscoelastic flow in contractions: The axisymmetric case. Journal of Non-Newtonian Fluid Mechanics. 2007; (147):92–108.

[5] Kfuri, S.L.D., Silva, J.Q., Soares, E.J., Thompson, R.L. Friction losses for power-law and viscoplastic materials in an entrance of a tube and an abrupt contraction. Journal of Petroleum Science and Engineering. 2011; 76(3–4):224–235.

[6] Pitz, D.B., Franco, A.T. Negrao, C.O.R. Effect of the Reynolds number on viscoelastic fluid flows through axisymmetric sudden contraction. Journal of the Brazilian Society of Mechanical Sciences and Engineering. 2017; 39(5):1709–1720.

[7] Regirer, S.A. Some thermohydrodynamic problems of steady one-dimensional flow of a viscous liquid. Journal of Applied Mathematics and Mechanics. 1957; 21(3):424–430. (In Russ.)

[8] Kearsley, E.A. The viscous heating correction for viscometer flows. Transactions of the Society of Rheology. 1962; (6):253–261.

[9] Kaganov, S.A. On a steady laminar flow of incompressible fluid in plane channel and round cylindrical tube with allowance for heat of friction and temperature dependence of viscosity. Journal of Applied Mechanics and Technical Physics. 1962; (3):96–99. (In Russ.)

[10] Martin, B. Some analytical solutions for viscometric flows of power-law fluids with heat generation and temperature dependent viscosity. International Journal of Non-Linear Mechanics. 1967; 2(4):285–301.

[11] Bostandzhiyan, S.A., Merzhanov, A.G., Khudyaev, S.I. On the hydrodynamic thermal explosion. Doklady Akademii Nauk SSSR. 1965; 163(1):133–136. (In Russ.)

[12] Bostandzhiyan, S.A., Chernyaeva, S.M. On the hydrodynamic thermal explosion in a non-Newtonian fluid flow. Doklady Akademii Nauk SSSR. 1966; 170(2):301–304. (In Russ.)

[13] Petukhov, B.S. Teploobmen i soprotivlenie pri laminarnom techenii zhidkosti v trubah [Heat transfer and drag in laminar fluid flow through the pipes]. Moscow: Energiya; 1967: 409. (In Russ.)

[14] Froyshteter, G.B., Danilevich, S.Yu., Radionova, N.V. Techenie i teploobmen nen'jutonovskih zhidkostej v trubah [Flow and heat transfer of nonNewtonian fluids through the pipes]. Kiev: Naukova dumka; 1990: 216. (In Russ.)

[15] Mitsoulis, E., Vlachopoulos, J. Non-isothermal creeping flow through parallel plates and a sudden planar contraction. The Canadian Journal of Chemical Engineering. 1984; (62):837–844.

[16] Bell, B.C., Surana, K.S. p-Version least squares finite element formulation for two-dimensional incompressible Newtonian and non-Newtonian non-isothermal fluid flow. Computers & Structures. 1995; 54(1):83–96.

[17] Habla, F., Woitalka, A., Neuner, S., Hinrichsen, O. Development of a methodology for numerical simulation of non-isothermal viscoelastic fluid flows with application to axisymmetric 4:1 contraction flows. Chemical Engineering Journal. 2012; (207–208):772–784.

[18] Sylvester, N.D., Rosen, S.L. Laminar flow in the entrance region of a cylindrical tube. American Institute Of Chemical Engineers Journal. 1970; 16(6):964–966.

[19] Pienaar, V.G. Viscous flow through sudden contractions: Dis. Doctoral degree. Cape Town: Cape Peninsula University of Technology; 2004:198.

[20] Jay, P., Magnin, A., Piau, J.M. Numerical simulation of viscoplastic fluid flows through an axisymmetric contraction. Journal of Fluids Engineering. 2002; (124):700–705.

[21] Fester, V., Mbiya, B., Slatter, P. Energy losses of non-Newtonian fluids in sudden pipe contractions. Chemical Engineering Journal. 2008; (145):57–63.

[22] Liu, M., Chen, M., Duan, Yu. Local resistance characteristics of highly concentrated coalwater slurry flow through fittings. Korean Journal of Chemical Engineering. 2009; 26(2):569–575.

[23] Kfuri, S.L.D., Soares, E.J., Thompson, R.L., Siqueira, R.N. Friction coefficients for Bingham and power-law fluids in abrupt contractions and expansions. Journal of Fluids Engineering. 2016; 139(2):021203.

[24] Christiansen, E.B., Kelsey, S.J. Nonisothermal laminar contracted flow. American Institute Of Chemical Engineers Journal. 1972; 18(4):713–720.

[25] Yesilata, B., Oztekin, A., Neti, S. Non-isothermal viscoelastic flow through an axisymmetric sudden contraction. Journal of Non-Newtonian Fluid Mechanics. 2000; (89):133–164.

[26] Yankov, V.I., Glot, I.O., Trufanova, N.M, Shakirov, N.V. Techenie polimerov v otverstiyakh fil'er. Teoriya, raschet, praktika [Flow of the polymers through the spinneret holes. Theory, computation, and practice]. Moscow - Izhevsk: Regulyarnaya i khaoticheskaya dinamika; 2010: 368. (In Russ.)

[27] Ostwald, W. Ueber die rechnerische Darstellung des Strukturgebietes der Viskositat. Kolloid Zeitschrift. 1929; 47(2):176–187.

[28] Borzenko, E.I., Shrager, G.R. Non-isothermal steady flow of power-law fluid in a planar/axismetric channel // Tomsk State University Journal of Mathematics and Mechanics. 2018. No. 52. P. 41–52. (In Russ.)

[29] Godunov, S.K., Ryabenkiy, V.S. Difference Schemes. North-Holland: Elsevier Science Ltd; 1987: 440.

[30] Samarskiy, À.À. Vvedenie v teoriyu raznostnykh skhem [Introduction to the theory of difference schemes]. Moscow: Nauka; 1971: 553. (In Russ.)

[31] Roache, P.J. Computational fluid dynamics. Albuquerque: Hermosa Publs; 1976: 446.

[32] Yankov, V.I., Boyarchenko, V.I., Pervadchyuk, V.P., Glot, I.O., Shakirov, N.V. Processing of fiber-forming polymers. Fundamentals of the rheology of polymers, and the flow of polymers in channels. Moscow - Izhevsk: Regulyarnaya i khaoticheskaya dinamika; 2008: 264. (In Russ.)

[33] Idel’chik, I.E. Handbook of Hydraulic Resistance. Jerusalem: Israel Program for Scientific Translations; 1966: 517.

[34] Tiu, C., Boger, D.V., Halmos, A.L. Generalized method for predicting loss coefficients in entrance region flows for inelastic fluids. The Chemical Engineering Journal. 1972; 4(2):113–117.


Bibliography link:
Ryltseva K.E., Shrager G.R. Numerical simulation of a non-isothermal power-law fluid flow in a channel with abrupt contraction // Computational technologies. 2019. V. 24. ¹ 5. P. 75-89
Home| Scope| Editorial Board| Content| Search| Subscription| Rules| Contacts
ISSN 1560-7534
© 2024 FRC ICT