TY - JOUR
TI - HEAT TRANSFER IN THE VERTICAL TWO-PHASE FLOW OF COARSE PARTICLES
AU - Garić-Grulović Radmila V
AU - Grbavcić Željko
AU - Arsenijević Zorana
AU - Jovanović Stevan
JN - Thermal Science
PY - 2000
VL - 4
IS - 2
SP - 55
EP - 68
PT - Article
AB - Wall-to-bed heat transfer in hydraulic transport of spherical glass particles 1.20, 1.94, and 2.98 mm in diameter and in single-phase flow regime was studied. Experiments were performed by transporting spherical glass
particles with water in a 25.4 mm I. D. copper tube equipped with a steam jacket. In the runs with particles not present tube Reynolds number varied between 2280 and 21300, while in hydraulic transport runs tube
Reynolds number varied between 3300 and 20150. The loading ratio (Gp/Gf,) was between 0.07 and 0.328, and the fluid superficial velocity was between 0.29:U, and 2.86·U, where U, represents single particle
terminal velocity. The data for the heat transfer factor (j<sub>H</sub>) in single phase flow are correlated using general form j<sub>H</sub>=f(Re). The data for wall-to-bed heat transfer in the hydraulic transport of particles shows that 
analogy between heat and momentum transfer exists. The data were correlated by treating the flowing fluid-particle mixture as a pseudofluid, by introducing a modified mixture-wall friction coefficient (f<sub>w</sub>) and a modified
mixture Reynolds number (Re<sub>m</sub>).