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What’s New in FLUENT 6.2

 

By Nicole Diana, FLUENT Product Manager

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The fall release of FLUENT 6.2 promises many exciting new features and capabilities. It focuses on areas such as dynamic mesh, multiphase flows, acoustics, reacting flows, rotating equipment, and heat transfer and phase change. Application areas include automotive in-cylinder flows, positive displacement pumps, store separation and missile launch, bubble column reactors, fluidized bed reactors, flow-induced noise prediction, turbomachinery, fuel cells, underhood flows, and automotive climate control.

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Velocity vectors are shown for a 2D rotary engine simulation, solved using the dynamic mesh model

Dynamic mesh

While the dynamic mesh model has served as the foundation for automotive in-cylinder applications, it has been widely used for other industrial applications as well, ranging from chemical process to biomedical. Dynamic hanging node adaption, new in FLUENT 6.2, allows for more accurate solutions with lower overall cell counts. The remeshing and layering capabilities have been expanded, and include the use of symmetry boundary conditions with local re-meshing, and a more flexible “2.5-D” remeshing technique that is particularly useful for simulating certain types of pumps. A new built-in six degrees of freedom solver is also available for applications with unconstrained motion, including store separation, missile launch, and tank sloshing. Parallel scalability has also been improved.

Multiphase flows

A major new improvement for multiphase systems is the ability to include species transport and homogeneous reactions with all multiphase models, including the Eulerian and VOF models. For heterogeneous reactions, the reaction rates must be specified in a user-defined function (UDF); however, the stoichiometry is easily specified in the graphical user interface (GUI). The Reynolds stress turbulence model can now be used in conjunction with the Eulerian model for the prediction of highly swirling multiphase mixtures. Several enhancements have been added to the granular model to produce more realistic results in certain circumstances. The granular model is now available with the mixture model, providing an economical alternative to the full Eulerian model when appropriate.

Several improvements have been made to the VOF model. A new variable time-stepping scheme provides improved robustness and efficiency for cases where the velocity changes significantly with time, as with tank sloshing and filling. An interface-capture scheme provides more efficient convergence for free surface problems in which the final steady state solution is more important than intermediate solutions, as is common in certain ship hydrodynamics applications. An open channel boundary condition and support for inviscid flows further improves FLUENT’s capabilities for marine applications.

A new wall film model has been added to FLUENT’s suite of spray models. It is particularly important for in-cylinder combustion simulations. New tracking schemes, automated tracking scheme selection, and error-controlled time-step adaption result in more accurate and efficient particle tracking with the discrete phase model.

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Fischer-Tropsch synthesis in a bubble column, used to produce liquid hydrocarbons from carbon monoxide and hydrogen, is modeled using the Eulerian multiphase model with chemical reactions; the liquid volume fraction (top) and bubble velocity vector field, colored by the dissolution rate of H2 (bottom) are shown

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Prominent noise sources on a sedan, computed using the acoustics capabilities in FLUENT

Acoustics

FLUENT 6.2 provides an unparalleled suite of acoustics capabilities. The Ffowcs-Williams Hawkings (FW-H) model that was introduced in FLUENT 6.1 has been extended to handle rotating surfaces, so that fan noise can be modeled. When used in conjunction with rotating reference frames, fan noise predictions can be obtained based on a steady-state simulation, providing an efficient and powerful tool. The FW-H model is now also available with the coupled solver. A new set of broadband source models allows acoustic sources based on the results of steady-state simulations to be estimated. These models are practical tools for evaluating design modifications.

Reacting flows

FLUENT 6.2 includes models for diesel autoignition and gasoline spark ignition. (See the article on page 23.) A new stiff chemistry algorithm for the segregated solver is available for laminar flows. When combined with ISAT, laminar finite rate chemistry problems can be solved more quickly and efficiently. Several enhancements have also been added to the NOx model. Surface chemistry mechanisms can be imported in the Surface CHEMKIN format. Another useful new feature is the ability to create custom material databases. This allows material properties and reaction mechanisms that have been specified in one case to be used again in a different case. PrePDF has been completely integrated into FLUENT 6.2. In addition to improved usability, the integration has also resulted in reduced computation times.

Rotating equipment

A new sliding mesh model is available in FLUENT 6.2 that addresses the robustness issues associated with earlier versions of the model. The improvements also apply to non-conformal interfaces in general. Of particular interest to turbomachinery users is automated full multigrid initialization. This feature allows an initial solution field to be computed so that a higher Courant number can be used with the coupled implicit solver, resulting in faster overall convergence. Non-reflecting boundary conditions are now supported for unsteady flows.

Heat transfer and phase change

A new solar load model has been implemented in FLUENT 6.2. The solar load model allows the radiant energy transport between the sun and a wall surface to be solved, based on the intensity and position of the sun. This model is important for automotive and building climate control applications.

For the discrete ordinates (DO) model, a second order discretization option is now available for obtaining more accurate results, particularly for cases with high optical thickness. A UDF can be used to customize the absorption coefficient for each band with the gray-banded DO model. Several improvements have also been made to the surface-to-surface radiation model, including the ability to specify the number of faces per surface cluster for different boundaries, allowing fine clustering to be used only where it is needed. The result is a more accurate solution without the memory penalty associated with using fine clustering everywhere.

A wet steam model has been implemented in FLUENT 6.2. Two-phase flow in steam turbine applications is one area that will benefit. Cases with shell conduction no longer require encapsulation in parallel; this significantly improves calculation efficiency. Several enhancements have also been made to both the cavitation and heat exchanger models.

Solver improvements

Several enhancements to the numerics in FLUENT 6.2 result in improved solver accuracy and efficiency. For the segregated solver, an improved Rhie-Chow interpolation technique has been implemented that can significantly improve accuracy on tetrahedral meshes. In addition, a new, locally 3rd order discretization scheme has been implemented for both the segregated and coupled solvers.

Time-dependent flows

FLUENT 6.2 contains some significant improvements in non-iterative transient solution methods. A non-iterative PISO solution scheme is now available, and an implicit fractional step method has been implemented for incompressible and mildly compressible flows. Both methods result in significant speed-ups compared with the iterative transient solution method. Neither, however, can be used with dynamic mesh, sliding mesh, reacting, or Eulerian multiphase flows.

Some improvements have also been made to the coupled solver that result in better accuracy along with a speed-up in the time required per iteration. Additional modifications were made for unsteady cases that result in improved accuracy and convergence for the coupled solver when implicit time-stepping is used. In particular, the coupled implicit solver now captures pressure wave propagation with accuracy similar to the coupled explicit solver. Further, the number of iterations required for these problems is significantly reduced.

Turbulence

In the area of turbulence modeling, there is an effort underway to improve the large eddy simulation (LES) capability. FLUENT 6.2 includes several new sub-grid scale viscosity models, including two dynamic models that improve the quality of LES predictions. To help accelerate convergence, an LES simulation can be launched from a steady-state RANS solution using turbulence synthesization. Two new methods for specifying the stochastic velocity boundary condition at inlets, more rigorous than previous offerings, are now available. The usability of the detached eddy simulation (DES) model has also been enhanced.

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Solids distribution in an unbaffled stirred tank containing four LIGHTNIN A310 impellers, solved using the Eulerian granular multiphase and Reynolds stress models

And more…

FLUENT 6.2 also includes add-on modules for proton-exchange membrane (PEM) fuel cells and solid oxide fuel cells (SOFC). The modules will be included on the FLUENT 6.2 CD, but a special license will be required to activate them. There are several other enhancements in FLUENT 6.2, including substantial improvements to the speed of reading cases files into the parallel version of FLUENT, new particle animation capabilities, the ability to display multiple monitors in a single graphics window, and more.


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