Flow models for generic resistances
The geometry parameters of energy devices necessary for the pressure loss calculations are often not exactly known. Therefore the modelling of the detailed pressure loss calculation has to be simplified. In this package components are present that provide different forms of such approximations.
Extends from Modelica.Icons.VariantsPackage (Icon for package containing variants).
Name | Description |
---|---|
VolumeFlowRate | Flow model for generic resistance parameterized with the volume flow rate |
Flow model for generic resistance parameterized with the volume flow rate
This component models a generic resistance parameterized with the volume flow rate:
dp = a*V_flow^2 + b*V_flow m_flow = rho*V_flow
with
a | as quadratic coefficient [Pa*s^2/m^6], |
b | as linear coefficient [Pa*s/m3], |
dp | as pressure loss [Pa], |
m_flow | as mass flow rate [kg/s], |
rho | as density of fluid [kg/m3], |
V_flow | as volume flow rate [m3/s]. |
The geometry parameters of energy devices necessary for the pressure loss calculations are often not exactly known. Therefore the modelling of the detailed pressure loss calculation has to be simplified. This components use a linear and a quadratic dependence of the pressure loss on the volume flow rate. It is assumed that neither mass nor energy is stored in this component. In the model basically a function is called to compute the mass flow rate as a function of pressure loss. Also the inverse of this function is defined, and a tool might use this inverse function instead, in order to avoid the solution of a nonlinear equation.
The details of the model are described in the documentation of the underlying function.
Extends from Modelica.Fluid.Dissipation.Utilities.Icons.PressureLoss.General_i (Icon for general pressure drop), Modelica.Fluid.Interfaces.PartialTwoPortTransport (Partial element transporting fluid between two ports without storage of mass or energy).
Name | Description |
---|---|
replaceable package Medium | Medium in the component |
dp = a*V_flow^2 + b*V_flow | |
a | Coefficient for quadratic term [(Pa.s2)/m6] |
b | Coefficient for linear term [(Pa.s)/m3] |
Assumptions | |
allowFlowReversal | = true to allow flow reversal, false restricts to design direction (port_a -> port_b) |
Advanced | |
dp_start | Guess value of dp = port_a.p - port_b.p [Pa] |
m_flow_start | Guess value of m_flow = port_a.m_flow [kg/s] |
m_flow_small | Small mass flow rate for regularization of zero flow [kg/s] |
Diagnostics | |
show_T | = true, if temperatures at port_a and port_b are computed |
show_V_flow | = true, if volume flow rate at inflowing port is computed |
Name | Description |
---|---|
port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |