Abstract
The lateral effective thermal conductivity was measured in a fluidized bed with horizontal multitube internals. The tube diameter and tube pitch used in this work were in the range from 1.0 to 5.0 cm and 2.5 to 10 cm, respectively. The minimum fluidized gas velocity of fluidized particles and the superficial velocity were in the range from 4.0 to 27 cm/sec and 10 to 70 cm/sec, respectively. The lateral effective thermal conductivity in the bed is influenced by the properties of fluidized particles, the hydraulic diameter of the tube internals, the minimum fluidized gas velocity and the intensity of fluidization. An empirical equation for the lateral effective thermal conductivity in a fluidized bed with horizontal multi-tube internals is obtained.
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.
