Abstract
This chapter reviews the use of the EMMS drag and paradigm to solve industrial problems including the design, optimization and scale-up of the fluid catalytic cracking (FCC) process, and optimization of fluidized bed combustion and Fischer-Tropsch (FT) synthesis. Application of the EMMS drag to these problems in turn aids its development.
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Abbreviations
- C d :
-
Effective drag coefficient for a particle
- d b :
-
Bubble diameter, m
- d p :
-
Particle diameter, m
- G s :
-
Solids flux, kg/m2 s
- H d :
-
Heterogeneity index
- K*:
-
Saturation carrying capacity, kg/m2 s
- p :
-
Pressure, Pa
- Q :
-
Gas volumetric flow rate, m3/s
- U :
-
Superficial velocity (= uε g), m/s
- U ck :
-
Choking gas velocity, m/s
- U s :
-
Superficial slip velocity, m/s
- W :
-
Solids flow rate (kg/s)
- x :
-
Mass fraction of particles
- Y :
-
Mass fraction of gas species
- z :
-
Axial height, m
- Rep :
-
Local superficial Reynolds number (ρ g d p U s/μ g)
- α :
-
Volume fraction
- Θ :
-
Granular temperature, m2/s2
- μ :
-
Viscosity, Pa s
- ρ :
-
Density, kg/m3
- b:
-
Bubble
- g:
-
Gas phase
- l:
-
Liquid phase
- p:
-
Particle
- s:
-
Solid phase
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Li, J. et al. (2013). Applications of EMMS Drag in Industry. In: From Multiscale Modeling to Meso-Science. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-35189-1_8
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DOI: https://doi.org/10.1007/978-3-642-35189-1_8
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