The Single-Phase Flow Interface Options
Several of the physics interfaces vary only by one or two default settings (see Table 4-1) in the Physical Model and Turbulence sections, which are selected either from a check box or drop-down list. For the Single-Phase Flow branch, all except the Rotating Machinery interfaces have the same Name (spf). The differences are based on the default settings required to model that type of flow as described in Table 4-1. Figure 4-1 shows the Settings window for Laminar Flow where you choose the type of compressibility (incompressible, weakly compressible or compressible at Mach numbers below 0.3) and the turbulence type and model (or none for laminar flow), and a check box to model Stokes flow by neglecting the inertial term.
k-ε
k-ω
k-ε
Creeping Flow
The Creeping Flow Interface () models the Navier-Stokes equations without the contribution of the inertia term. This is often referred to as Stokes flow and is appropriate for flow at small Reynolds numbers, such as in very small channels or in microfluidic applications.
The Creeping Flow interface can also be activated by selecting a check box in the Laminar Flow interface. This physics interface can also model non-Newtonian fluids, using the predefined non-Newtonian models, but not turbulence.
Laminar Flow
The Laminar Flow Interface () is used primarily to model flow at small to intermediate Reynolds numbers. The physics interface solves the Navier-Stokes equations, and by default assumes the flow to be incompressible; that is, the density is assumed to be constant.
Compressible flow is possible to model in this physics interface but you have to maintain control of the density and any of the mass balances that are deployed to accomplish this.
The Laminar Flow Interface allows you to model porous media flow or even mixed free- and porous media flow. A volume force due to gravity can optionally be included.
This physics interface also allows you to simulate flows of the inelastic non-Newtonian fluids. You can model the fluid using the Power law, Carreau, Bingham-Papanastasiou, Herschel-Bukley-Papanastasiou, and Casson-Papanastasiou models.
You can also describe other material properties such as density by entering equations for its dependence on fluid composition and pressure (for compressible flow), or temperature. Many materials in the material libraries use temperature- and pressure-dependent property values. If the density is affected by temperature, a nonisothermal flow interface may be applicable (see The Nonisothermal Flow and Conjugate Heat Transfer, Laminar Flow, Turbulent Flow and LES Interfaces).
Figure 4-1: The Settings window for the Laminar Flow interface. Model incompressible or compressible flow, laminar or turbulent flow, Stokes flow and/or porous media flow. Combinations are also possible.
Turbulent Flow
The various forms of the Single-Phase Flow, Turbulent Flow interfaces () model flow of large Reynolds numbers. The interfaces solve the Reynolds-averaged Navier-Stokes (RANS) equations for the filtered velocity field and filtered pressure as well as models for the turbulent viscosity. See The Creeping Flow, Laminar Flow, Turbulent Flow, and Large Eddy Simulation Interfaces for links to the physics interface information.
There are several turbulence models available: two algebraic turbulence models, the Algebraic yPlus and L-VEL models, and six transport-equation models, including a standard k-ε model, the Realizable k-ε model, a k-ω model, an SST model, a Low Reynolds number k-ε model, the Spalart-Allmaras model, and the v2-f model. Each model has its merits and weaknesses. See the Theory for the Turbulent Flow Interfaces for more details.
Similarly to the Laminar Flow interface, incompressible flow is selected by default. If required, this can be changed to compressible flow. Non-Newtonian fluid models are not available for the Turbulent Flow interfaces
Large eddy simulation
The Single-Phase Flow, Large Eddy Simulation (LES) interfaces () also model flow at large Reynolds numbers. The LES interfaces are designed for resolving the larger three-dimensional unsteady eddies whereas the effect of the smaller eddies are modeled. Hence, simulations with these interfaces must be three-dimensional and time-dependent.
There are three LES models: the Residual-Based Variational Multiscale (RBVM) model, the Residual-Based Variational Multiscale with Viscosity (RBVMWV) model, and the Smagorinsky model. Of these three, the first two use consistent modeling for the unresolved scales. This means that the modeled stresses in the momentum equation vanish in the limit when all scales are resolved. They can therefore also be used to study laminar or transitional flow.
The current formulations are only applicable to incompressible flow of Newtonian fluids.
Rotating Machinery
The Rotating Machinery, Laminar and Turbulent Flow Interfaces () model fluid flow in geometries with rotating parts. For example, stirred tanks, mixers, propellers and pumps.
When the Rotating Machinery, Fluid Flow interfaces are added using the Model Wizard, a Rotating Domain is added under the Definitions node. These interfaces support compressible, weakly compressible and incompressible flow, the flow of non-Newtonian fluids, as well as turbulence. They also support creeping flow.
The Viscoelastic Flow Interface
The Viscoelastic Flow (vef) interface () is used for simulating single-phase flows of viscoelastic fluids. The physics interface is only suitable for incompressible flows.