Abstract (EN):
The present work describes the mass transfer
process between a moving fluid and a slightly soluble
cylinder, with the axis perpendicular to flow direction,
buried in a packed bed of small inert particles, with
uniform voidage. Fluid flow in the packed bed around
the cylinder was assumed to follow Darcy¿s law and, at
each point, dispersion of solute was assumed to be
determined by radial and axial dispersion coefficients, in
the cross-stream and streamwise directions, respectively.
Numerical solutions of the differential equation describing
solute mass conservation were undertaken to obtain
the concentration field near the soluble surface and the
mass transfer flux was integrated to give the Sherwood
number as a function of the relevant parameters. Mathematical
expressions are proposed that describes accurately
the dependence found numerically between the
value of the Sherwood number and the values of Peclet
number, Schmidt number and the ratio between the
diameter of cylinder and the diameter of inerts.
Language:
English
Type (Professor's evaluation):
Scientific
No. of pages:
10