Mass and heat transfer to an ellipsoidal particle
โ Scribed by Dana T. Grow
- Publisher
- Elsevier Science
- Year
- 1990
- Tongue
- English
- Weight
- 267 KB
- Volume
- 80
- Category
- Article
- ISSN
- 0010-2180
No coin nor oath required. For personal study only.
โฆ Synopsis
NOMENCLATURE a semimajor axis of particle (m) b, c semiminor axes of particle (m) C concentration of oxygen (mol m -3) Co oxygen concentration in bulk gas stream (kg m -3) C1 constant of integration C2 constant of integration D diffusion coefficient (m 2 s -l) dp particle diameter (m) h heat transfer coefficient (J m -2 s -l K -l) h average heat transfer coefficient (J m -2 s-t K-I) hi --g')]l/2/2R AH enthalpy of combustion reaction (J kg -l) kc chemical rate constant (kg m -2 s -1 pa-0.5) kdif average diffusion mass transfer coefficient (kg m -2 s -1 Pa -l) N mass flux at surface (kg m -2 s -l) NU Nusselt number average mass flux (kg m -2 S -l ) Nrnax maximum mass flux at surface (kg m -2 S -l) Nmin minimum mass flux at surface (kg m -2 S -1 ) Nsp mass flux for spherical particle at surface (kg m -2 s -l) P02
partial pressure of oxygen (Pa) Ps surface pressure of oxygen averaged over the particle surface (Pa) q heat flux (J m 2 s -l) t/ average heat flux (J m 2 s -1)
๐ SIMILAR VOLUMES
Partlcle-to-emulsion and mterpartrcle heat transfer rates were estimated in the range 1 5 G u/u,,,f 6 3 5, 0 69 c $ G 2 15 mm by drymg wet refractory partlcles m fluldlzed beds of smular dry partlcles of the same sues Overall particle-toemulslon heat transfer coefficients decrease roughly as the mve