## Buildings.Fluid.UsersGuide

The package `Buildings.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.

#### Computation of flow resistance

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 is the mass flow rate and Δp is the pressure drop. For |ṁ| < δ0, where δ is a parameter and 0 is the mass flow rate at the nominal operating point, 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 conjuction with models from the `Buildings` library.

In actuators such as valves and air dampers, k is a function of the control signal.

#### Computation of mass and energy balance

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 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:

1. If a system model sets the pressure, such as if the volume is connected to a model that sets the pressure, e.g., Buildings.Fluid.Sources.FixedBoundary, then due to the connection between the models, the pressure of the volume is the same as the pressure of the model for the boundary condition.
2. If a system model does not set the pressure, then the pressure starts at the value set by `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:

1. If a system model sets the temperature, such as if the heat port of the volume is connected to a fixed temperature, then T(0) of the volume would be equal to the temperature connected to this port.
2. If a system model does not set the temperature, then the temperature starts at the value `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 m0 is the nominal mass flow rate, τ is the time constant, and ρ0 is the mass density at the nominal condition.

Extends from Modelica.Icons.Information (Icon for general information packages).

Automatically generated Thu Dec 8 16:33:40 2011.