Characterization and Development of Geldart’s Fluidizing Velocity Profile of Sand Particles for the Application in Fluidized Bed Combustor (FBC)

The objective of this study is to fully utilize the local sand retrieved from Pahang river as a bed material in FBC. The proposed work will study through experiments to deduce a new classification of local river sand in a fluidized bed based on the minimum fluidization velocity of inert particles according Geldart’s classification operated at five different temperatures: 55, 82, 108, 124 and 148 °C respectively. River sand was chosen as a fluidizing medium due to its characteristics that can withstand high operating temperature of more than 1000 °C. Apart from that, its cheap cost and availability make it preferred choice for the operation. The results show that the minimum fluidizing velocity of the sand, \( U_{\text{mf}} \) was found increasing as the temperature increased for the sands operated at low temperature, but maintaining almost at the same value, for the sands operated higher operating temperature respectively. The findings agree well with the reported trend by previous authors, in which their results based on the bed operated at combustion temperature which is above 800 °C. Thus, it can be conclude that the local sands, will exhibits the same trend for the application of fluidized bed combustor.

[1]  Derek Geldart,et al.  The effect of particle size and size distribution on the behaviour of gas-fluidised beds , 1972 .

[2]  J. Chaouki,et al.  Distribution of large biomass particles in a sand‐biomass fluidized bed: Experiments and modeling , 2014 .

[3]  M. Wey,et al.  The effect of particle size distribution on minimum fluidization velocity at high temperature , 2002 .

[4]  V. I. Kuprianov,et al.  Combustion of palm kernel shell in a fluidized bed: Optimization of biomass particle size and operating conditions , 2014 .

[5]  Z. Feng,et al.  Prediction of minimum fluidization velocity for binary mixtures of biomass and inert particles , 2013 .

[6]  Jan Baeyens,et al.  Effect of operating temperature on minimum fluidization velocity , 1991 .

[7]  John R. Grace,et al.  Evaluation of flow regimes in a semi-cylindrical spouted bed through statistical, mutual information, spectral and Hurst's analysis , 2008 .

[8]  Jesse Zhu,et al.  Identification of the flow structures and regime transition in gas–solid fluidized beds through moment analysis , 2013 .

[9]  B. Paudel Experimental Study on Fluidization of Biomass, Inert Particles, and Biomass/Sand Mixtures , 2011 .

[10]  Pichet Ninduangdee,et al.  Combustion of Oil Palm Shells in a Fluidized-bed Combustor Using Dolomite as the Bed Material to Prevent Bed Agglomeration , 2014 .

[11]  Vladimir I. Kuprianov,et al.  Combustion of peanut shells in a cone-shaped bubbling fluidized-bed combustor using alumina as the bed material , 2012 .

[12]  Jennifer S. Curtis,et al.  Classifying the fluidization and segregation behavior of binary mixtures using particle size and density ratios , 2011 .

[13]  Pichet Ninduangdee,et al.  Study on burning oil palm kernel shell in a conical fluidized-bed combustor using alumina as the bed material , 2013 .

[14]  V. Vivacqua,et al.  Fluidization of mixtures of two solids: A unified model of the transition to the fluidized state , 2013 .

[15]  J. Chaouki,et al.  Hydrodynamic characteristics of gas–solid fluidization at high temperature , 2010 .

[16]  S. D. Kim,et al.  Effects of Temperature and Particle Size on Minimum Fluidization and Transport Velocities in a Dual Fluidized Bed , 2009 .

[17]  C. Xiaoping,et al.  Minimum fluidization velocity of particles with wide size distribution at high temperatures , 2013 .

[18]  Tadaaki Shimizu,et al.  The effect of the particle size of alumina sand on the combustion and emission behavior of cedar pellets in a fluidized bed combustor. , 2008, Bioresource technology.