Abstract

The studies [1-6] examined the settling of gas suspensions in an enclosed volume, a process which is of interest in a wide range of production operations. The authors of [i-3] studied hindered steady-state settling in a unidimensional approximation in order to establish the dependence of the settling rate on particle concentration. A two-velocity model was used in [4], again in the unidimensional case, for highlyconcentrated suspensions in order to find the nonsteady rate of particle deposition. Analysis of the settling of a suspension in a two-dimensional formulation within the framework of the two-velocity model [5, 6] showed that the non-unidimensional flows of liquid which develop significantly alter the characteristics of unidimensional settling.

Full Text
Paper version not known

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

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.