Hostname: page-component-cd9895bd7-7cvxr Total loading time: 0 Render date: 2024-12-18T21:03:06.342Z Has data issue: false hasContentIssue false

Pressure drop due to the motion of neutrally buoyant particles in duct flows

Published online by Cambridge University Press:  29 March 2006

Howard Brenner
Affiliation:
Department of Chemical Engineering, Carnegie–Mellon University, Pittsburgh, Pennsylvania

Abstract

The additional pressure drop arising from the presence of a neutrally-buoyant, eccentrically positioned, spherical particle in a Poiseuille flow is calculated to O(a/Ro)5 (a = sphere radius; Ro = tube radius). Similar calculations (of a lesser order of accuracy) are given for non-circular conduits and for ellipsoidal particles. Due to changes in particle orientation resulting from rotation, the instantaneous pressure drop for an ellipsoid of revolution varies periodically with time. This pressure diminution is averaged over one period to obtain the time-average pressure drop.

Type
Research Article
Copyright
© 1970 Cambridge University Press

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

Brenner, H. 1959 Dissipation of energy due to solid particles suspended in a viscous liquid. Phys. Fluids, 1, 338346.Google Scholar
Brenner, H. 1962 Dynamics of a particle in a viscous fluid. Chem. Engng Sci. 17, 435446.Google Scholar
Brenner, H. 1963 The Stokes resistance of an arbitrary particle. Chem. Engng Sci. 18, 125.Google Scholar
Brenner, H. 1964a The Stokes resistance of a slightly deformed sphere. Chem. Engng Sci. 19, 519539.Google Scholar
Brenner, H. 1964b The Stokes resistance of an arbitrary particle: IV. Arbitrary fields of flow. Chem. Engng Sci. 19, 703727.Google Scholar
Brenner, H. 1966a Hydrodynamic resistance of particles at small Reynolds numbers. In Advances in Chemical Engineering. Vol. 6 (T. B. Drew, J. W. Hoopes, Jr. and T. Vermuelen, eds.), pp. 287438. Academic.
Brenner, H. 1966b The Stokes resistance of an arbitrary particle: V. Symbolic operator representation of intrinsic resistance. Chem. Engng Sci. 21, 97109.Google Scholar
Brenner, H. & Happel, J. 1958 Slow viscous flow past a sphere in a cylindrical tube. J. Fluid Mech. 4, 195213.Google Scholar
Bungay, P. M. & Brenner, H. 1970 Modelling of blood flow in the microcirculation. Tube flow of rigid particle suspensions. (To appear.)
Chen, T. C. & Skalak, R. 1970 Stokes flow in a cylindrical tube containing a line of spheroidal particles. Appl. Sci. Res. (in Press).Google Scholar
Cox, R. G. & Brenner, H. 1967 Effect of finite boundaries on the Stokes resistance of an arbitrary particle. III. Translation and rotation. J. Fluid Mech. 28, 391411.Google Scholar
Einstein, A. 1905 Eine neue Bestimmung der Moleküldimensionen. Ann. Phys. (4) 19, 289306.Google Scholar
Einstein, A. 1911 Berichtigung zu meiner Arbeit: Eine neue Bestimmung der Moleküldimensionen. Ann. Phys. (4) 34, 591592.Google Scholar
Famularo, J. & Happel, J. 1965 Sedimentation of dilute suspensions in creeping motion. Am. Inst. Chem. Engns J. 11, 981988.Google Scholar
Goldsmith, H. L. & Mason, S. G. 1967 The microrheology of dispersions. In Rheology: Theory and Applications, Vol. 4 (F. R. Eirich, ed. ), pp. 85220. Academic.
Greenstein, T. & Happel, J. 1968 Theoretical study of the slow motion of a sphere and a fluid in a cylindrical tube. J. Fluid Mech. 34, 705710.Google Scholar
Haberman, W. L. & Sayre, R. M. 1958 Motion of rigid and fluid spheres in stationary and moving liquids inside cylindrical tubes. David Taylor Model Basin Rep. no. 1143.Google Scholar
Hirschfeld, B. & Brenner, H. 1971 Slow motion of a sphere in a cylindrical tube at an arbitrary angle of incidence. (To appear.)
Hochmuth, R. M. & Sutera, S. P. 1970 Spherical caps in low Reynolds number tube flow. Chem. Engng Sci. 25, 593604.Google Scholar
Jeffery, G. B. 1922 The motion of ellipsoidal particles immersed in a viscous fluid. Proc. Roy. Soc. A 102, 161179.Google Scholar
Lamb, H. 1932 Hydrodynamics, 6th ed. Cambridge University Press.
Ripps, D. L. & Brenner, H. 1967 The Stokes resistance of a slightly deformed sphere: II. Intrinsic resistance operators for an arbitrary initial flow. Chem. Engng Sci. 22, 375387.Google Scholar
Schowalter, W. R., Chaffey, C. E. & Brenner, H. 1968 Rheological behaviour of a dilute emulsion. J. Colloid Interface Sci. 26, 152160.Google Scholar
Sonshine, R. M. & Brenner, H. 1966 The Stokes translation of two or more particles along the axis of an infinitely long circular cylinder. Appl. Sci. Res. 16, 425454.Google Scholar
Wang, H. & Skalak, R. 1969 Viscous flow in a cylindrical tube containing a line of spherical particles. J. Fluid Mech. 38, 7596.Google Scholar