Applied Scientific Research

, Volume 57, Issue 2, pp 133–149 | Cite as

Effect of yield stress on the flow of a Casson fluid in a homogeneous porous medium bounded by a circular tube

Article

Abstract

The effect of yield stress on the flow characteristics of a Casson fluid in a homogeneous porous medium bounded by a circular tube is investigated by employing the Brinkman model to account for the Darcy resistance offered by the porous medium. The non-linear coupled implicit system of differential equations governing the flow is first transformed into suitable integral equations and are solved numerically. Analytical solution is obtained for a Newtonian fluid in the case of constant permeability, and the numerical solution is verified with that of the analytic solution. The effect of yield stress of the fluid and permeability of the porous medium on shear stress and velocity distributions, plug flow radius and flow rate are examined. The minimum pressure gradient required to start the flow is found to be independent of the permeability of the porous medium and is equal to the yield stress of the fluid.

Key words

yield stress Casson fluid porous medium 

Nomenclature

h

step length in radial direction

I0

modified Bessel function of first kind order zero

Il

modified Bessel function of first kind of order one

k(r)

permeability function =\(\bar k(\bar r)/R^2 = k_0 f(r)\)

k0

permeability factor

f

radial variation of permeability (=1 or (1−r)/r)

N

number of sub-interval in radial direction

p

dimensionless pressure

P0

characteristic pressure gradient

Q

dimensionless flow rate

R

radius of the tube

r

dimensionless radial distance =\(\bar r/R\)

rj

jth radial nodal point

rp

dimensionless plug flow radius

u

dimensionless axial velocity =\(\bar u/u_c \)

uc

characteristic velocity = −R 2 P 0/2μ

up

dimensionless plug flow velocity

Greek symbols

ɛ1

error of tolerance for τ

ɛ2

error of tolerance forr p

μ

Newtonian viscosity (viscosity at high shear rate)

τ

dimensionless shear stress = τ/τɛc

τc

characteristic shear stress = μ u c /R

τy

dimensionless yield stress

Subscripts

+

shear flow region,r p r≤1

plug flow region, 0≤rr p

Overscore

‘overbar’; represents all dimensional quantities

Preview

Unable to display preview. Download preview PDF.

Unable to display preview. Download preview PDF.

References

  1. 1.
    Bird, R.B., Stewart, W.E. and Lightfoot, E.N.,Transport Phenomena. John Wiley and Sons, New York (1960) chapter 2.Google Scholar
  2. 2.
    Fung, Y.C.,Biomechanics, Mechanical Properties of Living Tissues. Springer-Verlag, New York (1981) chapter 3.Google Scholar
  3. 3.
    Casson, N., A flow equation for pigment oil suspensions of printing, ink type. In: Mill, C.C. (ed.),Rheology of Dispersed System. Pergamon Press, Oxford (1959) pp. 84–102.Google Scholar
  4. 4.
    Scott Blair, G.W., An equation for flow of blood serum through glass tubes.Nature, London 183 (1959) 613–614.CrossRefADSGoogle Scholar
  5. 5.
    Charm, S.E. and Kurland, G.S., Viscometry of human blood for shear rates of 0–100,000 sec−1.Nature, London 206 (1965) 617–618.CrossRefADSGoogle Scholar
  6. 6.
    Merrill, E.W., Benis, A.M., Gilliland, E.R., Sherwood, T.K. and Salzman, E.W., Pressure flow relations of human blood in hollow fibre at low shear rates.Jour. Appl. Physiol. 20 (1965) 954–967.Google Scholar
  7. 7.
    MacDonald, D.A.,Blood Flows in Arteries, 2nd edition. Arnold, London (1974) chapter 2.Google Scholar
  8. 8.
    Tammamasi, B., Consideration of certain haemorheological phenomenon from the stand-point of surface chemistry. In Copley, A.L. (ed.),Haemorheology. Pergamon Press, London (1968) p. 89.Google Scholar
  9. 9.
    Walwander, W.P., Chen, T.Y. and Cala, D.F., An approximate Casson fluid model for tube flow of blood.Biorheology 12 (1975) 111–119.Google Scholar
  10. 10.
    Vinogradov, G.V. and Malkin, A.Y.,Rheology of Polymers. Mir Publisher, Moscow (1979).Google Scholar
  11. 11.
    Jayaraman, G., Lautier, A., Jarry, G., Bui-Mong-Huang and Laurent, D., Numerical scheme for modelling oxygen transfer in tubular oxygenators.Med. & Biol. Engng. & Compt. 19 (1981) 524–534.CrossRefGoogle Scholar
  12. 12.
    Dash, R.K., Jayaraman, G. and Mehta, K.N., Estimation of increased flow resistance in a narrow catheterized artery—A theoretical model.Jour. Biomech. 29 (1996) 917–930.CrossRefGoogle Scholar
  13. 13.
    Dash, R.K., Mehta, K.N. and Jayaraman, G., Casson fluid flow in a pipe filled with a homogeneous porous medium.Int. Jour. Engng. Sci. 34 (1996) 1145–1156.CrossRefGoogle Scholar
  14. 14.
    Das, B. and Batra, R.L., Flow of a Casson fluid in the entrance region of a porous tube. In: Nicholas, P. and Cheremisninoff, P. (eds),Encyclopedia of Fluid Mechanics, Supplement 3, Advances in Fluid Dynamics. Gulf Publishing Company, Texas (1994) pp. 123–137.Google Scholar
  15. 15.
    Das, B. and Batra, R.L., Non-Newtonian flow of a blood in an arteriosclerotic blood vessels with rigid permeable walls.Jour. Theor. Biol. 175 (1995) 1–11.CrossRefGoogle Scholar
  16. 16.
    Bear, J.,Dynamics of Fluids in Porous Media. Elsevier Science, New York (1972).Google Scholar
  17. 17.
    Vradis, G.C. and Protopapas, A.L., Macroscopic conductivity for flow of Bingham Plastics in porous media.Jour. Hydraul. Engng. 119 (1993) 95–108.CrossRefGoogle Scholar
  18. 18.
    Brinkman, H.K., A calculation of the viscous force exerted by a flowing fluid on a dense swarm of particles.Appl. Sci. Res. A1 (1947) 27–34.CrossRefGoogle Scholar
  19. 19.
    Merrill, E.W., Rheology of blood.Physiol. Rev. 49 (1969) 863–888.Google Scholar
  20. 20.
    Chow, C.Y.,An Introduction to Computational Fluid Dynamics. John Wiley and Sons, New York (1979) chapter 4.Google Scholar

Copyright information

© Kluwer Academic Publishers 1997

Authors and Affiliations

  1. 1.Department of MathematicsIndian Institute of TechnologyNew DelhiIndia

Personalised recommendations