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External heat transfer in polydispersed fluidized beds at elevated temperatures

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Abstract

The authors present results of a theoretical and experimental study of heat transfer in polydispersed fluidized beds of coarse particles at temperatures up to 1273 K.

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Abbreviations

a :

tube radius

Cf :

specific heat of the gas

di :

mean diameter of the i-th fraction

g:

acceleration due to gravity

H:

height of the fluidized bed

J=ρfu:

mass flow rate of gas

0 :

thickness of the gas film on the heat transfer surface

m0 :

porosity at the onset of fluidization

m:

porosity

r:

radius

R:

radius of the equipment

tf, °C, Tf, °K:

gas temperature

T0 :

initial gas temperature

Tt8, Tw :

temperature of the fluidized bed and of the heat transfer surface, u, u0, speed of filtration and speed at the start of fluidization

a:

heat-transfer coefficient

εw, εb :

emissivities of the heat transfer surface, and the fluidized bed

εS :

emissivity of the particles

ɛe :

effective (apparent) emissivity of the fluidized bed

ηf :

viscosity of the gas

λf :

thermal conductivity of the gas

λf 0f0 c+ncfJd2/m:

thermal conductivity of the gas at tf=0°C

λf c :

molecular thermal conductivity of the gas

〈λf c〉:

at temperature (Tw+Tt8)/2

λf0 c :

molecular thermal conductivity of the gas at tf=0°C, Λ=glf/glf0 c

ρS, ρf :

density of particles in the gas

σ:

Stefan-Boltzmann constant

Ar=gd1ρfρSf)/ηf 2 :

Archimedes Number

Pe=cfJℓ0 2/Hmλf0 c :

Peclet number

Re=ud1ρff :

Reynolds Number

Literature cited

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Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 56, No. 5, pp. 767–773, May, 1989.

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Borodulya, V.A., Teplitskii, Y.S., Sorokin, A.P. et al. External heat transfer in polydispersed fluidized beds at elevated temperatures. Journal of Engineering Physics 56, 541–546 (1989). https://doi.org/10.1007/BF01297603

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  • DOI: https://doi.org/10.1007/BF01297603

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