Basset force

In a body submerged in a fluid, unsteady forces due to acceleration of that body with respect to the fluid, can be divided into two parts: the virtual mass effect and the Basset force.

The Basset force term describes the force due to the lagging boundary layer development with changing relative velocity (acceleration) of bodies moving through a fluid.^[1] The Basset term accounts for viscous effects and addresses the temporal delay in boundary layer development as the relative velocity changes with time. It is also known as the "history" term. The Basset force is difficult to implement and is commonly neglected for practical reasons; however, it can be substantially large when the body is accelerated at a high rate.^[2]

This force in an accelerating Stokes flow has been proposed by Joseph Valentin Boussinesq in 1885 and Alfred Barnard Basset in 1888. Consequently, it is also referred to as the Boussinesq–Basset force.^[3][4]

Acceleration of a flat plate

Consider an infinitely large plate started impulsively with a step change in velocity—from 0 to u₀—in the direction of the plate–fluid interface plane.

The equation of motion for the fluid—Stokes flow at low Reynolds number—is

${\frac {\partial u}{\partial t}}=\nu _{c}\,{\frac {\partial ^{2}u}{\partial y^{2}}},$

where u(y,t) is the velocity of the fluid, at some time t, parallel to the plate, at a distance y from the plate, and ν_c is the kinematic viscosity of the fluid (c~continuous phase). The solution to this equation is,^[5]

$u=u_{0}-u_{0}\,\operatorname {erf}\left({\frac {y}{2{\sqrt {\nu _{c}t}}}}\right)=u_{0}\operatorname {erfc}\left({\frac {y}{2{\sqrt {\nu _{c}t}}}}\right),$

where erf and erfc denote the error function and the complementary error function, respectively.

Assuming that an acceleration of the plate can be broken up into a series of such step changes in the velocity, it can be shown that the cumulative effect on the shear stress on the plate is

$\tau ={\sqrt {{\frac {\rho _{c}\mu _{c}}{\pi }}}}\int \limits _{0}^{t}{\frac {{\frac {\partial u_{p}}{\partial t'}}}{{\sqrt {t-t'}}}}\,dt',$

where u_p(t) is the velocity of the plate, ρ_c is the mass density of the fluid, and μ_c is the viscosity of the fluid.

Acceleration of a spherical particle

Boussinesq (1885) and Basset (1888) found that the force F on an accelerating spherical particle in a viscous fluid is^[3][4][6][7]

${\mathbf {F}}={\frac {3}{2}}D^{2}{\sqrt {\pi \rho _{c}\mu _{c}}}\int \limits _{0}^{t}{\frac {{\frac {D{\mathbf {u}}}{Dt'}}-{\frac {\partial {\mathbf {v}}}{\partial t'}}}{{\sqrt {t-t'}}}}dt',$

where D is the particle diameter,  ^D⁄_Dt' is the material derivative, and u and v are the fluid and particle velocity vectors, respectively.

See also

• Basset–Boussinesq–Oseen equation
• Stokes boundary layer

References

1. C. Crowe et al., Multiphase flows with droplets and particles, CRC Press, 1998, ISBN 0-8493-9469-4, p. 81
2. R.W. Johnson, The handbook of fluid dynamics, CRC Press, 1998, ISBN 0-8493-2509-9, pp. 18–3
3. F. Candelier; J. R. Angilella; M. Souhar (2004), "On the effect of the Boussinesq–Basset force on the radial migration of a Stokes particle in a vortex", Physics of Fluids, 16 (5): 1765–1776, Bibcode:2004PhFl...16.1765C, doi:10.1063/1.1689970
4. E. E. Michaelides (2003), "Hydrodynamic force and heat/mass transfer from particles, bubbles, and drops—The Freeman Scholar Lecture", Journal of Fluids Engineering, 125 (2): 209–238, doi:10.1115/1.1537258
5. F. M. White (2006) [2006], Viscous fluid flow, New York: McGraw Hill, Chapter 3
6. J. V. Boussinesq (1885), "Sur la résistance qu'oppose un fluide indéfini au repos, sans pesanteur, au mouvement varié d'une sphère solide qu'il mouille sur toute sa surface, quand les vitesses restent bien continues et assez faibles pour que leurs carrés et produits soient négligeables", Comptes Rendus de l'Académie des Sciences, 100: 935–937
7. A. B. Basset (1961) [1888], Treatise on hydrodynamics, 2, Cambridge: Deighton, Bell and Co., Chapter 22