Abstract

The aim of this work was to predict energy equilibrium values in a bench-scale fluidized bed (FB: 105 × 200 mm), using a thermal breakthrough analysis (TBA). For this purpose, a simple “unsteady state” energy balance was proposed by harnessing dynamic model approach on the basis of heat exchange between the bed and the gas. To investigate thermal behavior of the bed, low temperature runs at different flow rates (5.2 ≤ Q 0, m 3 h − 1 ≤ 7.4) and heating rates (97 ≤ q, kJ h − 1 ≤ 765) were carried out. FB was heated by means of an electrical heater (10 × 50 mm) horizontally immersed into the bed particles for heating period and then the power input was terminated for cooling period. The bed temperatures ( T B) were continuously measured for obtaining thermal breakthrough curves for all periods. Temperature–time data were used for extracting bed-to-gas heat transfer film coefficients ( h BG) from linear forms of proposed model. The model was also employed for calculating amounts of shared energies by fluidized bed phases ( q y − q x ). A good agreement between experimental values and model values of T B was found. The results were thus confirmed by proposed model. The latter may be successfully used to predict energy equilibrium data for e.g. drying or combustion.

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.