Abstract
The local gas hold-up and average gas bubble velocity in three-phase fluidized beds (TPFBs) were measured by optical fiber probes. A radial gas dispersion model was applied to analyse the gas hold-up distribution in the TPFB. The gas dispersion was found high near the grid and the dispersion decreased sharply to a much lower level and stabilized at higher axial positions.
Sign-in/Register to access full text options 
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 callDisclaimer: 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.
