.TRANSFORM.Fluid.Pipes.GenericPipe_MultiTransferSurface .TRANSFORM.Fluid.Pipes.GenericPipe_MultiTransferSurfaceBase model for distributed flow models. The total volume is split into nV segments along the flow path. The default value is nV=2.
The following boundary flow and source terms are part of the mass, energy, species, and trace balances and must be specified in an extending class:
Wall temperature is passed to the flow model as it is needed for some cases. When use_HeatTransfer = false, the wall temperature is assumed to be equal to the medium temperature.
It provides the complete balance equations for one-dimensional fluid flow as formulated in UsersGuide.ComponentDefinition.BalanceEquations.
This generic model offers a large number of combinations of possible parameter settings. In order to reduce model complexity, consider defining and/or using a tailored model for the application at hand, such as HeatExchanger.
In reality this model is not a partial model BUT it is listed as such so different applications of this model will be generated with proper applications of the parameters, icons, etc.
The mass and energy balances are inherited from Interfaces.PartialDistributedVolume. One total mass and one energy balance is formed across each segment according to the finite volume approach. Substance mass balances are added if the medium contains more than one component.
An extending model needs to define the geometry and the difference in heights between the flow segments (static head).
The momentum balance is determined by the
FlowModel component, which can be replaced with
any model extended from
BaseClasses.FlowModels.PartialStaggeredFlowModel. The default
setting is
DetailedPipeFlow.
This considers
flowModel.use_Ib_flows is true.The momentum balances are formulated across the segment
boundaries along the flow path according to the staggered grid
approach. The configurable modelStructure
determines the formulation of the boundary conditions at
port_a and port_b. The options include
(default: av_vb):
av_vb: Symmetric setting with nV-1 momentum
balances between nV flow segments. The ports port_a
and port_b expose the first and the last thermodynamic
state, respectively. Connecting two or more flow devices therefore
may result in high-index DAEs for the pressures of connected flow
segments.a_v_b: Alternative symmetric setting with nV+1
momentum balances across nV flow segments. Half momentum balances
are placed between port_a and the first flow segment
as well as between the last flow segment and port_b.
Connecting two or more flow devices therefore results in algebraic
pressures at the ports. The specification of good start values for
the port pressures is essential for the solution of large nonlinear
equation systems.av_b: Asymmetric setting with nV momentum
balances, one between nth volume and port_b, potential
pressure state at port_aa_vb: Asymmetric setting with nV momentum balance,
one between first volume and port_a, potential
pressure state at port_bWhen connecting two components, e.g., two pipes, the momentum balance across the connection point reduces to
pipe1.port_b.p = pipe2.port_a.p
This is only true if the flow velocity remains the same on each side of the connection. Consider using a fitting for any significant change in diameter or fluid density, if the resulting effects, such as change in kinetic energy, cannot be neglected. This also allows for taking into account friction losses with respect to the actual geometry of the connection point.
The model treats the partial differential equations with the finite volume method and a staggered grid scheme for momentum balances. The default value is nV=2. This results in two lumped mass and energy balances and one lumped momentum balance across the model.
Note that this
generally leads to high-index DAEs for pressure states if this
model are directly connected to each other, or generally to models
with storage exposing a thermodynamic state through the port. This
may not be valid if the model is connected to a model with
non-differentiable pressure, like a Sources.Boundary_pT with
prescribed jumping pressure. The modelStructure
can be configured as
appropriate in such situations, in order to place a momentum
balance between a pressure state of the pipe and a
non-differentiable boundary condition.
The default
modelStructure is av_vb
(see Advanced tab). The
simplest possible alternative symmetric configuration, avoiding
potential high-index DAEs at the cost of the potential introduction
of nonlinear equation systems, is obtained with the setting
nV=1, modelStructure=a_v_b. Depending on the configured model
structure, the first and the last segment, or the flow path length
of the first and the last momentum balance, are of half
size.
The
HeatTransfer component specifies the source
term Qb_flows of the energy balance. The default
component uses a constant coefficient for the heat transfer between
the bulk flow and the segment boundaries exposed through the
heatPorts.
The HeatTransfer model is replaceable and can be
exchanged with any model extended from
TRANSFORM.Fluid.Pipes.BaseClasses.HeatTransfer.PartialFlowHeatTransfer.
The intended use is for complex networks of pipes and other flow devices, like valves. See, e.g.,
| Name | Description |
|---|---|
 Geometry |
Geometry |
 FlowModel |
Flow models (i.e., momentum, pressure loss, wall friction) |
 HeatTransfer |
Coefficient of heat transfer |
 InternalHeatGen |
Internal heat generation |
 TraceMassTransfer |
Trace Substance mass transfer |
 InternalTraceGen |
Internal trace mass generation |
mC are stored
in the same way as the species mXi.