The problem of unsteady mass transfer from a sphere that impulsively moves from rest to a finite velocity in a non-uniform concentration distribution is studied. A range of low Reynolds numbers (Re<1) and moderate Peclet numbers (Pe ranges from 5.6 to 300) is investigated (typical of the parameters encountered in anchorage dependent cell cultures in micro gravity). Using time scales, the effects of flow field development, concentration boundary layer development and free stream concentration variation are investigated. For the range of parameters considered, the development of the flow field has a negligible effect on the time variation of the Sherwood number (Sh). The Sh time dependence is dominated by concentration boundary layer development for early times and free stream concentration variations at later times.
Skip Nav Destination
e-mail: kleis@uh.edu
Article navigation
Technical Papers
Time Scales for Unsteady Mass Transfer From a Sphere at Low-Finite Reynolds Numbers
Stanley J. Kleis,
e-mail: kleis@uh.edu
Stanley J. Kleis
Department of Mechanical Engineering, University of Houston, Houston, TX 77204-4006
Search for other works by this author on:
Ivan Rivera-Solorio
Ivan Rivera-Solorio
Department of Mechanical Engineering, University of Houston, Houston, TX 77204-4006
Search for other works by this author on:
Stanley J. Kleis
Department of Mechanical Engineering, University of Houston, Houston, TX 77204-4006
e-mail: kleis@uh.edu
Ivan Rivera-Solorio
Department of Mechanical Engineering, University of Houston, Houston, TX 77204-4006
Contributed by the Heat Transfer Division for publication in the JOURNAL OF HEAT TRANSFER. Manuscript received by the Heat Transfer Division July 12, 2002; revision received March 10, 2003. Associate Editor: A. F. Emery.
J. Heat Transfer. Aug 2003, 125(4): 716-723 (8 pages)
Published Online: July 17, 2003
Article history
Received:
July 12, 2002
Revised:
March 10, 2003
Online:
July 17, 2003
Citation
Kleis, S. J., and Rivera-Solorio, I. (July 17, 2003). "Time Scales for Unsteady Mass Transfer From a Sphere at Low-Finite Reynolds Numbers ." ASME. J. Heat Transfer. August 2003; 125(4): 716–723. https://doi.org/10.1115/1.1576813
Download citation file:
Get Email Alerts
Cited By
Ducted heat exchanger aerodynamic shape and thermal optimization
J. Heat Mass Transfer
A Simplified Thermal Hydraulic Model for Solid Pin-Fueled Molten Salt Reactors Under Low-Flow Accident Scenarios
J. Heat Mass Transfer (December 2024)
Effect of Forced Convection Heat Transfer on Vapor Quality in Subcooled Flow Boiling
J. Heat Mass Transfer (December 2024)
Related Articles
Effect of Double Stratification on Free Convection in a Darcian Porous Medium
J. Heat Transfer (April,2004)
Magnetohydrodynamic Mixed-Convective Flow and Heat and Mass Transfer Past a Vertical Plate in a Porous Medium With Constant Wall Suction
J. Heat Transfer (November,2008)
Mass Transfer From a Rotating Disk to a Bingham Fluid
J. Appl. Mech (January,2006)
Semi-Analytical Solution for Heat Transfer in a Water Film Flowing Over a Heated Plane
J. Heat Transfer (June,2010)
Related Proceedings Papers
Related Chapters
Aerodynamic Performance Analysis
Axial-Flow Compressors
Cavitating Structures at Inception in Turbulent Shear Flow
Proceedings of the 10th International Symposium on Cavitation (CAV2018)
Extended Surfaces
Thermal Management of Microelectronic Equipment