Abstract
In this work a numerical investigation of wall to bed heat transfer, and the related flow characteristics, was conducted along a conical fluidized bed combustor with a height of 0.8 m and a cone angle of 30°. A two-fluid Eulerian-Eulerian model was used while applying Kinetic Theory for Granular Flow (KTGF) to a wall-to-bed FB reactor. The heat transfer coefficient and hydrodynamics are discussed for two different drag models, namely the Gidaspow and Syamlal-O’Brien models. Furthermore, computational calculations were carried out for a variety of inlet velocities(1.4Umf~4 Umf) and different particle sizes. The heat transfer coefficient in the bed region was evaluated and compared with that calculated by penetration theory. The bed expansion for the two models was compared with that calculated using correlations from literature in order to validate the numerical calculations. The heat transfer coefficient was found to be increasing with increasing gas velocity and decreasing with increasing particle diameter.
Similar content being viewed by others
Abbreviations
- CD :
-
Drag coefficient
- CP :
-
Specific heat (J kg−1 K−1)
- ds :
-
Diameter of the particles (m)
- e s :
-
Coefficient of restitution
- H:
-
Enthalpy (J)
- Hgs :
-
Heat transfer from fluid to solid (J)
- h:
-
Heat transfer coefficient (W m−2 K−1)
- hs :
-
Static (minimum) bed height (m)
- I:
-
Identity tensor
- k:
-
Thermal conductivity (W m−1 K−1)
- q:
-
Diffusive flux
- Pr:
-
Prandtl number
- \(\overline{\overline D}\) :
-
Rate of strain tensor
- g:
-
Gravitational acceleration (m s−2)
- go :
-
Radial distribution function
- Nu:
-
Nusselt number
- P:
-
Pressure (Pa)
- R:
-
Bed expansion ratio
- Re:
-
Reynolds number
- r/R:
-
Radial distance
- U:
-
Gas velocity (m s−1)
- Z:
-
Height above air inlet (m)
- ε:
-
Volume fraction
- β:
-
Interphase exchange coefficient
- γ:
-
Coefficient defined by Eq. (26)
- μ:
-
Viscosity (N s m−1)
- Θ:
-
Granular temperature (m2 s−2)
- νr :
-
Terminal velocity of particles (m s−1)
- ρ:
-
Density (kg m−3)
- τ:
-
Stress tensor
- g:
-
Gas
- m:
-
Mixture
- s:
-
Solid
- pen:
-
penetration
References
McKendry, P., “Energy Production from Biomass (Part 2): Conversion Technologies,” Bioresource Technology, vol. 83, no. 1, pp. 47–54, 2002.
Kaewklum, R., Kuprianov, V. I., and Douglas, P. L., “Hydrodynamics of Air–Sand Flow in a Conical Swirling Fluidized Bed: A Comparative Study between Tangential and Axial Air Entries,” Energy Conversion and Management, vol. 50, no. 12, pp. 2999–3006, 2009.
Ninduangdee, P. and Kuprianov, V. I., “Study on Burning Oil Palm Kernel Shell in a Conical Fluidized-Bed Combustor using Alumina as the Bed Material,” Journal of the Taiwan Institute of Chemical Engineers, vol. 44, no. 6, pp. 1045–1053, 2013.
Kuprianov, V. I. and Arromdee, P., “Combustion of Peanut and Tamarind Shells in a Conical Fluidized-Bed Combustor: A Comparative Study,” Bioresource Technology, Vol. 140, pp. 199–210, 2013.
Kouprianov, V. I. and Permchart, W., “Emissions from a Conical FBC Fired with a Biomass Fuel,” Applied Energy, vol. 74, no. 3–4, pp. 383–392, 2003.
Moharana, Y. C. and Malik, M. K., “Fluidization of Conical Bed and Computational Fluid Dynamics (CFD) Modeling of the Bed,” Department of Chemical Engineering, National Institute of Technology, Rourkela-769 008, 2012.
Patil, R., Pandey, M., and Mahanta, P., “Parametric Studies and Effect of Scale-up on Wall-to-Bed Heat Transfer Characteristics of Circulating Fluidized Bed Risers,” Experimental Thermal and Fluid Science, vol. 35, no. 3, pp. 485–494, 2011.
Gupta, A. V. S. S. K. S. and Nag, P. K., “Bed-to-Wall Heat Transfer Behavior in a Pressurized Circulating Fluidized Bed,” International Journal of Heat and Mass Transfer, vol. 45, no. 16, pp. 3429–3436, 2002.
Kalita, P., Mahanta, P., and Saha, U. K., “Some Studies on Wall-to-Bed Heat Transfer in a Pressurized Circulating Fluidized Bed Unit,” Procedia Engineering, vol. 56, pp. 163–172, 2013.
Armstrong, L. M., Gu, S., and Luo, K. H., “Study of Wall-to-Bed Heat Transfer in a Bubbling Fluidised Bed using the Kinetic Theory of Granular Flow,” International Journal of Heat and Mass Transfer, vol. 53, no. 21–22, pp. 4949–4959, 2010.
Kuipers, J. A. M., Prins, W., and Van Swaaij, W. P. M., “Numerical Calculation of Wall-to-Bed Heat-Transfer Coefficients in Gas-Fluidized Beds,” AIChE Journal, vol. 38, no. 7, pp. 1079–1091, 1992.
Yusuf, R., Melaaen, M. C., and Mathiesen, V., “Convective Heat and Mass Transfer Modeling in Gas-Fluidized Beds,” Chemical Engineering & Technology, vol. 28, no. 1, pp. 13–24, 2005.
Yusuf, R., Halvorsen, B., and Melaaen, M. C., “An Experimental and Computational Study of Wall to Bed Heat Transfer in a Bubbling Gas–Solid Fluidized Bed,” International Journal of Multiphase Flow, vol. 42, pp. 9–23, 2012.
Hou, Q., Zhou, Z., and Yu, A., “Computational Study of Heat Transfer in Bubbling Fluidized Beds with Geldart a Powder,” Proc. of 7th International Conference on CFD in the Minerals and Process Industries, 2009.
Almuttahar, A. and Taghipour, F., “Computational Fluid Dynamics of a Circulating Fluidized Bed under Various Fluidization Conditions,” Chemical Engineering Science, vol. 63, no. 6, pp. 1696–1709, 2008.
Kaewklum, R. and Kuprianov, V. I., “Theoretical and Experimental Study on Hydrodynamic Characteristics of Fluidization in Air–Sand Conical Beds,” Chemical Engineering Science, vol. 63, no. 6, pp. 1471–1479, 2008.
Sirisomboon, K., Kuprianov, V. I., and Arromdee, P., “Effects of Design Features on Combustion Efficiency and Emission Performance of a Biomass-Fuelled Fluidized-Bed Combustor,” Chemical Engineering and Processing: Process Intensification, vol. 49, no. 3, pp. 270–277, 2010.
Wiens, J. and Pugsley, T., “Tomographic Imaging of a Conical Fluidized Bed of Dry Pharmaceutical Granule,” Powder Technology, vol. 169, no. 1, pp. 49–59, 2006.
Permchart, W., Kuprianov, V. I., and Janvijitsakula, K., “Co-firing of Sugar Cane Bagasse with Rice Husk in a Conical Fuidized-bed Combustor,” Fuel, vol. 85, pp. 434–442, 2006.
Patankar, S., “Numerical Heat Transfer and Fluid Flow,” CRC Press, pp. 126–131, 1980.
Fluent is a Product Name by Ansys, Ansys Inc., Southpointe 275 Technology Drive, Canonsburg, PA 15317, USA.
Syamlal, M. and Gidaspow, D., “Hydrodynamics of Fluidization: Prediction of Wall to Bed Heat Transfer Coefficients,” AIChE Journal, vol. 31, no. 1, pp. 127–135, 1985.
Lun, C. K. K., Savage, S. B., Jeffrey, D. J., and Chepurniy, N., “Kinetic Theories for Granular Flow: Inelastic Particles in Couette Flow and Slightly Inelastic Particles in a General Flowfield,” Journal of Fluid Mechanics, vol. 140, pp. 223–256, 1984.
Schaeffer, D. G., “Instability in the Evolution Equations Describing Incompressible Granular Flow,” Journal of Differential Equations, vol. 66, no. 1, pp. 19–50, 1987.
Chapman, S. and Cowling, T. G. “The Mathematical Theory of Nonuniform Gases,” Cambridge University Press, 3rd Ed., pp. 273–240, 1991.
Gunn, D. J., “Transfer of Heat or Mass to Particles in Fixed and Fluidised Beds,” International Journal of Heat and Mass Transfer, vol. 21, no. 4, pp. 467–476, 1978.
Zehner, P. and Schlünder, E. U., “Wärmeleitfähigkeit von Schüttungen bei mäßigen Temperaturen,” Chemie Ingenieur Technik Vol. 42, no. 14, pp. 933–941, 1970.
Singh, R. K., Suryanarayana, A., and Roy, G. K., “Prediction of Bed Expansion Ratio for Gas-Solid Fluidization in Cylindrical and Non-Cylindrical Beds,” Vol. 79, 1999.
Patil, D. J., Smit, J., van Sint-Annaland, M., and Kuipers, J. A. M., “Wall-to-Bed Heat Transfer in Gas-Solid Bubbling Fluidized Beds,” AIChE Journal, vol. 52, no. 1, pp. 58–74, 2006.
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Abdelmotalib, H.M., Youssef, M.A., Hassan, A.A. et al. Numerical study on the wall to bed heat transfer in a conical fluidized bed combustor. Int. J. Precis. Eng. Manuf. 16, 1551–1559 (2015). https://doi.org/10.1007/s12541-015-0205-z
Received:
Revised:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s12541-015-0205-z