m |
Mass |
[M] |
z |
Elevation |
[L] |
L |
Length |
[L] |
W |
Width |
[L] |
H |
Height |
[L] |
D |
Diameter |
[L] |
r |
Radius |
[L] |
A |
Area |
[L]2 |
−V |
Volume |
[L]3 |
v |
Velocity |
[L][T] |
Q |
Flow rate |
[L]3[T] |
n |
Number, Amount |
Dimensionless |
C |
Concentration |
[M][L]3 |
p |
Pressure |
[M][L][T]2 |
g |
Acceleration due to Gravity |
[L][T]2 |
ρ |
Density |
[M][L]3 |
μ |
Dynamic viscosity |
[M][T][L] |
ν |
Kinematic viscosity |
[L]2[T] |
h |
Head, Elevation |
[L] |
hL |
Headloss |
[L] |
hf |
Major Loss (friction) |
[L] |
ϵ |
Surface roughness |
[L] |
f |
Darcy-Weisbach friction factor |
Dimensionless |
Re |
Reynolds Number |
Dimensionless |
he |
Minor Loss (expansion) |
[L] |
K |
Minor Loss coefficient |
Dimensionless |
Π |
Dimensionless Proportionality Ratio |
Dimensionless |
Πvc |
Vena Contracta Area Ratio |
Dimensionless |
ΠError |
Linearity Error Ratio |
Dimensionless |
M |
Fluid Momentum |
[M][L][T]2 |
F |
Force |
[M][L][T]2 |
t |
Time |
[T] |
θ |
Residence Time |
[T] |
G |
Velocity Gradient/Fluid Deformation |
1[T] |
ε |
Energy Dissipation Rate |
[L]2[T]3 |
ΠGMaxˉG |
GMaxˉG Ratio in a Reactor |
Dimensionless |
ΠεMaxˉε |
εMaxˉε Ratio in a Reactor |
Dimensionless |
ΠHS |
Height to Baffle Spacing in a Flocculator |
Dimensionless |
He |
Height Between Flow Expansions in a Flocculator |
[L] |
S |
Spacing Between Two Objects |
[L] |
B |
Center-to-Center Spacing Between Two Objects |
[L] |
T |
Object Thickness |
[L] |
P |
Power |
[M][L]2[T]3 |
ηK |
Kolmogorov Length Scale |
[L] |
λν |
Inner Viscous Length Scale |
[L] |
ΠKν |
Ratio of Inner Viscous Length Scale to Kolmogorov Length Scale |
Dimensionless |
Λ |
Distance Between Particles |
[L] |