On Laminar Flow of Non-Newtonian Fluids in Porous Media
详细信息    查看全文
  • 作者:Hassan E. Fayed ; Nadeem A. Sheikh ; Oleg Iliev
  • 关键词:Laminar flow ; Non ; Newtonian ; Power law ; Carreau model ; Friction factor
  • 刊名:Transport in Porous Media
  • 出版年:2016
  • 出版时间:January 2016
  • 年:2016
  • 卷:111
  • 期:1
  • 页码:253-264
  • 全文大小:1,347 KB
  • 参考文献:Balhoff, M.T., Thompson, K.E.: Amacroscopic model for shear-thinning flow in packed beds based on network modeling. Chem. Eng. Sci. 61, 698–719 (2006)CrossRef
    Bird, R.B., Stewart, W.E., Lightfoot, W.E.: Transport Phenomena, 2nd edn. Wiley, New York (2002)
    Blunt, M.J.: Flow in porous media—pore-network models and multiphase flow. Colloid Interface Sci. 6, 197–207 (2001)CrossRef
    Chenlo, F., Moreira, R., Silva, C.: Rheological properties od aqueous dispersions of tragacanth and guar gums at different concentration. Texture Stud. 41, 396–415 (2010)CrossRef
    Chhabra, R.P.: Bubbles, Drops, and Particles in Non-Newtonian Fluids. Taylor & Francis Group, New York (2007)
    Dodge, D.W., Metzner, A.B.: Turbulent flow of non-Newtonian systems. A.I.Ch.E. 5(2), 189–204 (1959)CrossRef
    Di Federico, V., Pinelli, M., Ugarelli, R.: Estimates of effective permeability for non-Newtonian fluid flow in randomly heterogeneous porous media. Stoch. Environ. Res. Risk Assess. 24(7), 1067–1076 (2010)CrossRef
    Garcia, E.J., Steffe, J.F.: Comparison of friction factor equations for non-Newtonian fluids in pipe flow. Food Process Eng. 9, 93–120 (1986)CrossRef
    Guzel, B., Frigaarda, I., Martinez, D.M.: Predicting laminar–turbulent transition in poiseuille pipe flow for non-Newtonian fluids. Chem. Eng. Sci. 64, 254–264 (2009)CrossRef
    Liu, S., Masliyah, J.: On non-Newtonian fluid flow in ducts and porous media. Chem. Eng. Sci. 53(6), 1175–1201 (1998)CrossRef
    Liu, S., Masliyah, J.: Non-linear flows in porous media. J. Non-Newton. Fluid Mech. 86, 229–252 (1999)CrossRef
    Lopez, X., Valvatne, P.H., Blunt, M.J.: Predictive network modeling of single-phase non-Newtonian flow in porous media. Colloid Interface Sci. 264, 256–265 (2003)CrossRef
    Metzner, A.B.: Non-Newtonian fluid flow. Ind. Eng. Chem. 49(9), 1429–1432 (1957)CrossRef
    Morais, A.F., Seybold, H., Herrmann, H.J., Andrade, J.: Non-Newtonian fluid flow through three-dimensional disordered porous media. Phys. Rev. Lett. 103(19), 194502 (2009)CrossRef
    Pakdemirli, M., Sari, P., Solmaz, B.: Analytical and numerical solutions of a generalized hyperbolic non-Newtonian fluid flow. Z. Naturforsch 65a, 151–160 (2010)
    Perrin, C.L., Tardy, P., Sorbie, K., Crawshaw, J.: Experimental and modeling study of Newtonian and non-Newtonian fluid flow in pore network micromodels. Colloid Interface Sci. 295(2), 542–550 (2006)CrossRef
    Pinho, F.T., Whitela, J.H.: Flow of non-Newtonian fluids in a pipe. J. Non-Newton. Fluid Mech. 34, 129–144 (1990)CrossRef
    Raoof, A., Majid, H.S., Leijnse, A.: Upscaling transport of adsorbing solutes in porous media: pore-network modeling. Vadose Zone 9, 624–636 (2010)CrossRef
    Sabiri, N., Comiti, J.: Pressure drop in non-Newtonian purely viscous fluid flow through porous media. Chem. Eng. Sci. 50(7), 1193–1201 (1995)CrossRef
    Shames, I.: Mechanics of Fluids. McGraw Hill, New York (1994)
    Sochi, T.: Non-Newtonian flow in porous media. Polymer 51, 5007–5023 (2010)CrossRef
    Sullivan, S.P., Gladden, L.F., Johns, M.L.: Simulation of power-law fluid flow through porous media using lattice Boltzmann techniques. Non-Newton. Fluid Mech. 133(2–3), 91–98 (2006)CrossRef
    Tang, G.H., Lu, Y.B.: A resistance model for Newtonian and power-law non-Newtonian fluid transport in porous media. Transp. Porous Media 104, 435–449 (2014)CrossRef
    Toms, B.A.: Detection of a wall effect in laminar flow of solutions of a linear polymer. Colloid Sci. 4, 511–521 (1949)CrossRef
    Tosco, T., Marchisio, D.L., Lince, F., Sethi, R.: Extension of the Darcy–Forchheimer law for shear-thinning fluids and validation via pore-scale flow simulations. Transp. Porous Media 96, 1–20 (2013)CrossRef
    Tsakiroglou, C.D.: A methodology for the derivation of non-Darcian models for the flow of generalized Newtonian fluids in porous media. Non-Newton. Fluid Mech. 105(2–3), 79–110 (2002)CrossRef
    Woudberg, S., Du Plessis, J.P., Smit, G.J.F.: Non-Newtonian purely viscous flow through isotropic granular porous media. Chem. Eng. Sci. 61(13), 4299–4308 (2006)CrossRef
    Yao, L.S., Molla, MdM, Moulic, S.G.: Fully-developed circular pipe flow of a non-Newtonian pseudoplastic fluid. Univers. J. Mech. Eng. 1(2), 23–31 (2013)
    Yun, M.: Seepage characteristics study on power-law fluid in fractal porous media. Math. Probl. Eng. 2014, 813561 (2014)
  • 作者单位:Hassan E. Fayed (1)
    Nadeem A. Sheikh (1)
    Oleg Iliev (1) (2)

    1. Numerical Porous Media SRI Center, King Abdullah University of Science and Technology, Thuwal, 23955-6900, Saudi Arabia
    2. Department of Flows and Materials Simulation, Fraunhofer Institute for Industrial Mathematics (ITWM), Kaiserslautern, Germany
  • 刊物类别:Earth and Environmental Science
  • 刊物主题:Earth sciences
    Geotechnical Engineering
    Industrial Chemistry and Chemical Engineering
    Civil Engineering
    Hydrogeology
    Mechanics, Fluids and Thermodynamics
  • 出版者:Springer Netherlands
  • ISSN:1573-1634
文摘
Flow of generalized Newtonian fluids in porous media can be modeled as a bundle of capillary tubes or a pore-scale network. In general, both approaches rely on the solution of Hagen–Poiseuille equation using power law to estimate the variations in the fluid viscosity due to the applied shear rate. Despite the effectiveness and simplicity, power law tends to provide unrealistic values for the effective viscosity especially in the limits of zero and infinite shear rates. Here, instead of using power law, Carreau model (bubbles, drops, and particles in non-Newtonian fluids. Taylor & Francis Group, New York, 2007) is used to determine the effective viscosity as a function of the shear strain rate. Carreau model can predict accurately the variation in the viscosity at all shear rates and provide more accurate solution for the flow physics in a single pore. Using the results for a single pore, normalized Fanning friction coefficient has been calculated and plotted as a function of the newly defined Reynolds number based on pressure gradient. For laminar flow, the variation in the friction coefficient with Reynolds number has been plotted and scaled. It is observed that generalized Newtonian fluid flows show Newtonian nature up to a certain Reynolds number. At high Reynolds number, deviation from the Newtonian behavior is observed. The main contribution of this paper is to present a closed-form solution for the flow in a single pore using Carreau model, which allows for fast evaluation of the relationship between flux and pressure gradient in an arbitrary pore diameter. In this way, we believe that our development will open the perspectives for using Carreau models in pore-network simulations at low computational costs to obtain more accurate prediction for generalized Newtonian fluid flows in porous media.
NGLC 2004-2010.National Geological Library of China All Rights Reserved.
Add:29 Xueyuan Rd,Haidian District,Beijing,PRC. Mail Add: 8324 mailbox 100083
For exchange or info please contact us via email.