.AixLib.Fluid.UsersGuide .AixLib.Fluid.UsersGuide
The package AixLib.Fluid consists of models for pressure
driven mass flow rate and for heat and moisture exchange in fluid
flow networks.
The models have the same interface as models of the package Modelica.Fluid, but have in general a simpler set of parameters that may be better suited if the models are used in early design of building systems. For example, in addition to the detailed pipe model from Modelica.Fluid, this package also contains models for which a user has to specify the mass flow and pressure drop at a nominal flow rate, which is typically more readily available prior to the detailed HVAC system design.
Component models of this package have fluid ports, which are a subclass of Modelica.Fluid.Interfaces.FluidPort. Fluid ports declare the variables listed in the table below.
| Variable | Description |
|---|---|
m_flow
|
Mass flow rate ṁ. The convention is that m_flow ≥ 0 if at this port,
mass flows into the component.
|
p
|
Absolute total pressure p. The absolute total pressure is the sum of the static pressure and the dynamic pressure. As the total pressure is used in the connector, components do not need to specify the area of the port or the velocity at the port. This convention is consistent with the Modelica Standard Library. Note that component models typically simplify the pressure balance by not taking into account the static pressure that is caused by the height of the medium column, i.e., the term Δp = Δh ρ g, where Δh is the height of the medium column, ρ is the mass density and g = 9.81 m/s2 is the gravity acceleration, is ignored. |
h_outflow
|
Specific enthalpy h of the outflowing fluid, i.e.,
assuming ṁ < 0. The specific enthalpy in the fluid port always carries the value of the enthalpy that the medium would have if it was leaving the component. Users who need to access the actual enthalpy for the given flow direction can do so using the sensor AixLib.Fluid.Sensors.SpecificEnthalpyTwoPort. |
Xi_outflow[Medium.nXi]
|
Independent mixture mass fractions mi/m close
to the connection point, i.e., assuming ṁ < 0. The independent mixture mass fraction in the fluid port always carries the value that the medium would have if it was leaving the component. Users who need to access the actual value for the given flow direction can do so using the sensor AixLib.Fluid.Sensors.MassFractionTwoPort. Note that this variable is only present for fluids that are a mixture of different substances such as moist air. For water, this variable is automatically removed when a model is translated. |
C_outflow[Medium.nC]
|
Trace substances ci/m close to the connection
point, i.e., assuming ṁ < 0. The trace substances in the fluid port always carries the value that the medium would have if it was leaving the component. Users who need to access the actual value for the given flow direction can do so using the sensor AixLib.Fluid.Sensors.TraceSubstancesTwoPort. Note that this variable is only present for fluids that declare a trace substance such as CO2. See for example AixLib.Fluid.Sensors.Examples.TraceSubstances. |
Most component models compute pressure drop as a function of flow
rate. If their pressure drop at the nominal conditions is set to
zero, for example by setting the parameter value
dp_nominal=0, then the equation for the pressure drop is
removed from the model. This allows, for example, to model a heating
and a cooling coil in series, and lump their pressure drops into a
single element, thereby reducing the dimension of the nonlinear
system of equations.
The flow resistance is computed as
k = ṁ ⁄ √ Δp
where ṁ is the mass flow rate and Δp is the pressure
drop. For |ṁ| < δṁ ṁ0, where
δṁ is equal to the parameter deltaM
and ṁ0 is the mass flow rate at the nominal
operating point, as set by the parameter m_flow_nominal,
the equation is linearized. The pressure drop is computed as a
function of mass flow rate instead of volume flow rate as this often
leads to fewer equations. Otherwise, the pressure drop would depend
on the density and hence on temperature.
The flow coefficient k is typically computed based on nominal
values for the mass flow rate and the pressure drop, i.e., k =
ṁ0 ⁄ √ Δp0 . This functional
form has been used as in building HVAC systems, a more exact
computation of the pressure drop would require detailed knowledge of
the duct or pipe dimensions and the flow bends and junctions. This
information is often not available during early design. However, if a
more detailed pressure drop calculation is required, then models from
Modelica.Fluid can be used in
conjunction with models from the Buildings library.
In actuators such as valves and air dampers, k is a function of the control signal.
Most models have parameters massDynamics and
energyDynamics that allow using a dynamic or a
steady-state equation for the mass and energy balance. The table
below shows the different settings and how they affect the mass and
energy balance equations. For the mass balance, the following
configurations can be selected:
| Parameter |
Initialization problem If density depends on pressure |
Initialization problem If density is independent of pressure |
Equation used during time integration |
|---|---|---|---|
| DynamicsFreeInitial | Unspecified | Unspecified | dm(t)/dt = ∑ ṁ(t) |
| FixedInitial | p(0)=p0 | Unspecified | dm(t)/dt = ∑ ṁ(t) |
| SteadyStateInitial | dp(0)/dt=0 | Unspecified | dm(t)/dt = ∑ ṁ(t) |
| SteadyState | Unspecified | Unspecified | 0 = ∑ ṁ(t) |
where m(t) is the mass of the control volume, ṁ(t) is the mass flow rate, p is the pressure and p0 is the initial pressure, which is a parameter. Unspecified means that no equation is declared for p(0). In this situation, there can be two cases:
p(start=Medium.p_default),
where Medium is the medium model.
Similarly, for the energy balance, the following configurations can be selected:
| Parameter | Initialization problem | Equation used during time integration |
|---|---|---|
| DynamicsFreeInitial | Unspecified | dU(t)/dt = ∑ ṁ(t) h(t) + Q̇(t) |
| FixedInitial | T(0)=T0 | dU(t)/dt = ∑ ṁ(t) h(t) + Q̇(t) |
| SteadyStateInitial | dT(0)/dt=0 | dU(t)/dt = ∑ ṁ(t) h(t) + Q̇(t) |
| SteadyState | Unspecified | 0 = ∑ ṁ(t) h(t) + Q̇(t) |
where U(t) is the internal energy of the control volume, h(t) is the enthalpy carried by the medium and Q̇(t) is the heat flow rate that is added to the medium through the heat port. Unspecified means that no equation is declared for T(0). In this situation, there can be two cases:
T(start=Medium.T_default), where Medium is
the medium model
In most models, the size of volume is configured using the parameter
tau. This parameter is equal to the time constant that
the volume has if the mass flow rate is at its nominal value, as set
by the parameter m_flow_nominal. Using the time
constant, as opposed to the actual fluid volume, allows in many cases
an easier parametrization, since the volume is automatically enlarged
if the nominal mass flow rate is increased. This allows an easy
adjustment of the component size. The actual size of the control
volume is then set as
V = ṁ0 τ/ρ0
where ṁ0 is the nominal mass flow rate, τ is the time constant, and ρ0 is the mass density at the nominal condition.
Most components have a parameters for the nominal operating
conditions. These parameters have names that end in
_nominal and they should be set to the values that the
component typically have if they are run at full load or design
conditions. Depending on the model, these parameters are used
differently, and the respective model documentation or code should be
consulted for details. However, the table below shows typical use of
parameters in various model to help the user understand how they are
used.
| Parameter | Model | Functionality |
|---|---|---|
|
m_flow_nominal dp_nominal |
Flow resistance models | These parameter may be used to define a point on the flow rate versus pressure drop curve. For other mass flow rates, the pressure drop is typically adjusted using similarity laws. See AixLib.Fluid.FixedResistances.PressureDrop. |
|
m_flow_nominal m_flow_small |
Sensors Volumes Heat exchangers Chillers |
Some of these models set
m_flow_small=1E-4*abs(m_flow_nominal) as the default
value. Then, m_flow_small is used to regularize, or
replace, equations when the mass flow rate is smaller than
m_flow_small in magnitude. This is needed to improve
the numerical properties of the model. The error in the results
is for typical applications negligible, because at flow rates
below 0.01% from the design flow rate, most model
assumptions are not applicable anyways, and the HVAC system is
not operated in this region. However, because Modelica simulates
in the continuous-time domain, such small flow rates can occur,
and therefore models are implemented in such a way that they are
numerically well-behaved for zero or near-zero flow rates.
|
|
tau m_flow_nominal |
Sensors Volumes Heat exchangers Chillers |
Because Modelica simulates in the continuous-time domain, dynamic
models are in general numerically more efficient than
steady-state models. However, dynamic models require product data
that are generally not published by manufacturers. Examples
include the volume of fluid that is contained in a device, and
the weight of heat exchangers. In addition, other effects such as
transport delays in pipes and heat exchangers of a chiller are
generally unknown and require detailed geometry that is typically
not available during the design stage. To circumvent this problem, many models take as a parameter the time constant tau and lump all its thermal mass into
a fluid volume. The time constant tau can be
understood as the time constant that one would observe if the
input to the component has a step change, and the mass flow rate
of the component is equal to m_flow_nominal. Using
these two values and the fluid density rho,
components adjust their fluid volume V=m_flow_nominal
tau/rho because having such a volume gives the specified
time response. For most components, engineering experience can be
used to estimate a reasonable value for tau, and
where generally applicable values can be used, components already
set a default value for tau.
|
The models are implemented using base classes from AixLib.Fluid.Interfaces and from Modelica.Fluid.Interfaces. This allows models to be fully compatible with Modelica.Fluid, and it allows the implementation of component models that reuse base classes for heat transfer, mass transfer and flow resistance.