Name | Description |
---|---|
ReynoldsNumber | Return Reynolds number from v, rho, mu, D |
ReynoldsNumber_m_flow | Return Reynolds number from m_flow, mu, D, A |
NusseltNumber | Return Nusselt number |
Calculation of Reynolds Number
Re = |v|ρD/μ
a measure of the relationship between inertial forces (vρ) and viscous forces (D/μ).
The following table gives examples for the characteristic dimension D and the velocity v for different fluid flow devices:
Device Type | Characteristic Dimension D | Velocity v |
---|---|---|
Circular Pipe | diameter | m_flow/ρ/crossArea |
Rectangular Duct | 4*crossArea/perimeter | m_flow/ρ/crossArea |
Wide Duct | distance between narrow, parallel walls | m_flow/ρ/crossArea |
Packed Bed | diameterOfSpericalParticles/(1-fluidFractionOfTotalVolume) | m_flow/ρ/crossArea (without particles) |
Device with rotating agitator | diameterOfRotor | RotationalSpeed*diameterOfRotor |
Name | Description |
---|---|
v | Mean velocity of fluid flow [m/s] |
rho | Fluid density [kg/m3] |
mu | Dynamic (absolute) viscosity [Pa.s] |
D | Characteristic dimension (hydraulic diameter of pipes) [m] |
Name | Description |
---|---|
Re | Reynolds number [1] |
m_flow
instead of the velocity v
to express inertial forces.
Re = |m_flow|*diameter/A/μ with m_flow = v*ρ*ASee also Pipes.BaseClasses.CharacteristicNumbers.ReynoldsNumber. Extends from Modelica.Icons.Function (Icon for functions).
Name | Description |
---|---|
m_flow | Mass flow rate [kg/s] |
mu | Dynamic viscosity [Pa.s] |
D | Characteristic dimension (hydraulic diameter of pipes or orifices) [m] |
A | Cross sectional area of fluid flow [m2] |
Name | Description |
---|---|
Re | Reynolds number [1] |
Nusselt number Nu = alpha*D/lambdaExtends from Modelica.Icons.Function (Icon for functions).
Name | Description |
---|---|
alpha | Coefficient of heat transfer [W/(m2.K)] |
D | Characteristic dimension [m] |
lambda | Thermal conductivity [W/(m.K)] |
Name | Description |
---|---|
Nu | Nusselt number [1] |