modelHANaturalCylinder
Extends from Modelica.Blocks.Icons.Block (Basic graphical layout of input/output block).
Information
This model calculates the convection coefficient h for natural convection from a cylinder submerged in fluid. h is calcualted using Eq 9.34 from Incropera and DeWitt (1996). Output of the block is the hA value.
The Nusselt number is computed as
NuD = (0.6 + (0.387 RaD(1/6))/(1+(0.559 Pr) (9/16))(8/27))2);
where NuD is the Nusselt number, RaD is the
Rayleigh number and
Pr is the Prandtl number.
This correclation is accurate for RaD less than 1012.
h is then calculated from the Nusselt number. The equation is
h = NuD k/D
where k is the thermal conductivity of the fluid and D is the diameter of the submerged cylinder.
References
Fundamentals of Heat and Mass Transfer (Fourth Edition), Frank Incropera and David DeWitt, John Wiley and Sons, 1996
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Modelica.Units.SI.Diameter | ChaLen | Characteristic length of the cylinder | |
| General › Nominal condition | |||
| Modelica.Units.SI.ThermalConductance | hA_nominal | Convective heat transfer coefficient | |
| Modelica.Units.SI.Temperature | TFlu_nominal | Fluid temperature at hA_nominal | |
| Modelica.Units.SI.Temperature | TSur_nominal | Surface temperature at hA_nominal | |
Connectors
| Type | Name | Default | Description |
|---|---|---|---|
| Modelica.Blocks.Interfaces.RealInput | TSur | Temperature of the external surface of the heat exchanger | |
| Modelica.Blocks.Interfaces.RealInput | TFlu | Temperature of the fluid in the heat exchanger | |
| Modelica.Blocks.Interfaces.RealOutput | hA | hA-value of the heat exchanger |
Components
| Type | Name | Default | Description |
|---|---|---|---|
| Real | h | Convection coefficient |
Contents
| Name | Description |
|---|---|
| Medium inside the tank | |
| nusseltprotected |
Revisions
-
August 29, 2014 by Michael Wetter:
Refactored function calls for medium properties. -
May 10, 2013 by Michael Wetter:
Revised implementation to usehA_nominalas a parameter, and compute the associated surface areaA. This revision was required to have a consistent computation of thehAvalues inside and outside of the coil in the heat exchanger model of the water tank. -
February 26, 2013 by Peter Grant:
First implementation.