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Symbol Alternative<br />

Units<br />

Quantity or parameter<br />

Symbol<br />

A surface area m 2<br />

a w water activity -<br />

B nucleation rate kg -1 m -1 s -1<br />

b breakage function m -3<br />

C constant or coefficient -<br />

c specific heat capacity J/kgK<br />

D equipment diameter m<br />

D Γ, δ diffusion coefficient m²/s<br />

D transport tensor m²/s<br />

d diameter or size <strong>of</strong> solids m<br />

E energy J<br />

F mass flux function -<br />

f relative (normalized) drying rate -<br />

f multi-dimensional number density -<br />

G shear function or modulus Pa<br />

G growth rate kg/s<br />

g acceleration due to gravity m/s 2<br />

H height m<br />

H enthalpy J<br />

H Heaviside step function -<br />

h specific enthalpy (dry basis) J/kg<br />

~<br />

h h N molar enthalpy J/mol<br />

∆ h v<br />

specific enthalpy <strong>of</strong> evaporation J/kg<br />

I total number <strong>of</strong> intervals -<br />

J numerical flux function -<br />

K constant -<br />

K<br />

dilatation function or bulk modulus<br />

L length m<br />

M m mass kg<br />

M ~ M, M N molecular mass kg/kmol<br />

M & W mass flow rate kg/s<br />

m& J mass flux, drying rate kg/m²s<br />

N number -<br />

N molar amount mol<br />

N & W N molar flow rate mol/s<br />

n molar density, molar concentration mol/m³<br />

n number density m -3<br />

n<br />

outward normal unit vector<br />

n& J N molar flux mol/m²s<br />

P power W<br />

P total pressure kg m/s 2<br />

p partial pressure / vapour pressure <strong>of</strong> component kg m/s 2<br />

Q & Q heat flow rate W<br />

q& q heat flux W/m 2<br />

R equipment radius m<br />

R individual gas constant J/kgK<br />

R ~ R N universal gas constant J/kmolK<br />

r radial coordinate m


pore (throat) radius m<br />

S saturation -<br />

S selection function 1/s<br />

s boundary layer thickness m<br />

T temperature K, °C<br />

t time s<br />

u velocity in z-direction m/s<br />

u displacement m<br />

V volume m 3<br />

V & F volumetric flow rate m³/s<br />

v specific volume m 3 /kg<br />

v velocity in x-direction m/s<br />

v general velocity vector ms -1<br />

W weight force N<br />

w velocity in y-direction m/s<br />

X solids moisture content (dry basis) -<br />

x mass fraction in liquid phase -<br />

x particle volume in population balances m³<br />

x lateral coordinate m<br />

x general eulerian coordinate m<br />

x 0 general lagrangian coordinate m<br />

x~ x N molar fraction in liquid phase -<br />

Y gas moisture content (dry basis) -<br />

y lateral coordinate m<br />

y mass fraction in gas phase -<br />

y~ y N molar fraction in gas phase -<br />

z axial coordinate m<br />

Special <strong>symbols</strong><br />

∇<br />

gradient operator<br />

∇⋅<br />

divergence operator<br />

∆ difference operator -<br />

Greek letters<br />

α h heat transfer coefficient W/m²K<br />

β k mass transfer coefficient m/s<br />

β aggregation kernel 1/s<br />

δ<br />

Dirac-delta distribution<br />

ε voidage -<br />

ε emissivity -<br />

ε<br />

strain<br />

η efficiency -<br />

θ angle, angular coordinate rad<br />

κ thermal diffusivity m²/s<br />

λ thermal conductivity W/mK<br />

µ dynamic viscosity kg/ms<br />

µ moment <strong>of</strong> the particle size distribution<br />

ν kinematic viscosity m 2 /s<br />

π circular constant -


ρ density, mass concentration kg/m 3<br />

Σ summation operator -<br />

σ surface tension N/m<br />

σ Stefan-Boltzmann constant for radiative heat transfer W/m 2 K 4<br />

σ standard deviation (<strong>of</strong> pore size distribution) m<br />

σ stress Pa<br />

τ dimensionless time -<br />

Φ characteristic moisture content -<br />

ϕ relative humidity -<br />

ω angular velocity rad<br />

Subscripts<br />

a<br />

at ambient conditions<br />

as<br />

at adiabatic saturation conditions<br />

bed<br />

bed<br />

c<br />

cross section<br />

c<br />

capillary<br />

cr<br />

at critical moisture content<br />

D<br />

drag<br />

dry<br />

dry<br />

dp<br />

at dewpoint<br />

eff<br />

effective<br />

eq<br />

equilibrium (moisture content)<br />

f<br />

friction<br />

g<br />

gas (dry)<br />

H<br />

wet (humid) gas<br />

i<br />

inner<br />

i,1,2,…<br />

component index, particle index<br />

i,j,k coordinate index, i,j,k = 1 to 3<br />

in<br />

inlet value<br />

l<br />

liquid (alternative: as a superscript)<br />

m<br />

mean value<br />

max<br />

maximum<br />

mf<br />

at minimum fluidisation<br />

min<br />

minimum<br />

N<br />

molar quantity<br />

o<br />

outer<br />

out<br />

outlet value<br />

P<br />

at constant pressure<br />

p<br />

particle<br />

pbe<br />

population balance equation<br />

ph<br />

at the interface<br />

r<br />

radiation<br />

rel<br />

relative velocity<br />

s<br />

solid (compact solid phase), alternative: as a superscript<br />

S<br />

at saturation conditions<br />

surf<br />

surface<br />

V<br />

based on volume<br />

v<br />

vapour, evaporation<br />

w<br />

water<br />

w<br />

wall


wb<br />

wet<br />

∞<br />

at wet bulb conditions<br />

wet<br />

at large distance from interface<br />

Superscripts<br />

average, phase average<br />

α<br />

intrinsic phase average<br />

v<br />

volumetric strain<br />

* rheological strain<br />

* at saturation conditions<br />

Multiple subscripts should be separated by a colon, e.g.:<br />

Bold <strong>symbols</strong> denote vector or tensor quantities<br />

ρ<br />

p, dry<br />

: density <strong>of</strong> dry particle.

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