Abstract
Mass transfer between a slender bubble and a viscous Newtonian liquid in axisymmetric extensional and creeping flow has been studied. The exact steady state solution, at large Peclet numbers, has been obtained using the method presented by Levich for uniform flow around a spherical drop and also by the useful equation derived by Lochiel and Calderbank for axisymmetric bodies of revolution.
Full Text 
Sign-in/Register to access full text options
Sign-in/Register to access full text options 
Published version (
Free)
Free) 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a call
