| Nomenclature |
|
A
|
[m2] |
Heat transfer surface area |
|
As
|
[m2] |
Heat exchanger surface area |
|
B
|
[K/W] |
|
|
Cp
|
[J/(kg·K)] |
Specific heat |
|
C
|
[W/K] |
heat capacity |
|
D
|
[m] |
Equivalent diameter |
|
f
|
[-] |
Friction factor |
|
h
|
[J/kg] |
Specific enthalpy |
|
L
|
[m] |
Length of the plate |
|
m
|
[kg/s] |
Mass flow rate |
| Nu |
[-] |
Nusselt number |
|
P
|
[kPa] |
Pressure |
| Pr |
[-] |
Prandtl number |
|
Q
|
[W] |
Heat transfer rate |
| Re |
[-] |
Reynolds number |
|
Rf
|
[m2·K/W] |
Resistance due to fouling |
|
S
|
[m2] |
Total cross-sectional surface area |
|
s
|
[J/(kg·K)] |
Specific entropy |
|
T
|
[K] |
Temperature |
|
U
|
[W/(m2·K)] |
Overall heat transfer coefficient |
|
v
|
[m/s] |
Mean velocity |
|
Wi
|
[m] |
Width of the plate |
|
W
|
[W] |
Power output |
|
w
|
[W/m2] |
Power output per unit of surface area |
|
x
|
[-] |
Vapor quality |
|
α
|
[W/(m2·K)] |
Heat transfer coefficient |
| ΔT
|
[K] |
Temperature difference |
|
λ
|
[W/(m·K)] |
Thermal conductivity |
|
Λ
|
[-] |
Lagrange multiplier |
|
μ
|
[Pa·s] |
Dynamic viscosity |
|
ρ
|
[kg/m3] |
Density |
|
τ
|
[Pa] |
heat exchanger wall shear stress |