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generally, the default setting is choosing for solver£º

FLUENT provides three di erent solver formulations: segregated coupled implicit

coupled explicit(ÏÔʽ¸ñʽÖ÷ÒªÓÃÓÚ¼¤²¨µÈ²¨¶¯½âµÄ²¶×½ÎÊÌâ)

The segregated solver traditionally has been used for incompressible and mildly compressible flows. The coupled approach, on the other hand, was originally designed for high-speed compressible flows.

By default, FLUENT uses the segregated solver, for high-speed compressible flows (as discussed above), highly coupled flows with strong body forces (e.g., buoyancy or rotational forces), or flows being solved on very fine meshes, you may want to consider the coupled implicit solver instead.

For cases where the use of the coupled implicit solver is desirable, but your machine does not have sufficient memory, you can use the segregated solver or the coupled explicit solver instead.(explicit save memory use,but need more iterations for converged solution. Choosing the Discretization Scheme

1)first-order upwind vs second-order upwind

When the flow is aligned with the grid the first-order upwind discretization may be acceptable. For triangular and tetrahedral grids, since the flow is never aligned with the grid, you will generally obtain more accurate results by using the second-order discretization. For quad/hex grids, you will also obtain better results using the second-order discretization, especially for complex flows. For most cases, you will be able to use the second-order scheme from the start of the calculation. In some cases, however, you may need to start with the first-order scheme and then switch to the second-order scheme after a few iterations. For example, if you are running a high-Mach-number flow calculation that has an initial solution much different than the expected final solution, Finally, if you run into convergence diffculties with the second-order scheme, you should try the first-order scheme instead.

2)Quick vs upwind(QuickÊÊÓÃÓÚ½á¹¹Íø¸ñ£¬Á÷¶¯·½ÏòÓëÍø¸ñÒ»Ö£¬¶ÔÓÚ·Ç½á¹¹Íø¸ñÍÆ¼öÓÃ2½×Ó­·ç)

The QUICK discretization scheme may provide better accuracy than the second-order scheme for rotating or swirling flows solved on quadrilateral or hexahedral meshes. For compressible flows with shocks, using the QUICK scheme for all variables, including density, is highly recommended for quadrilateral, hexahedral, or hybrid meshes. 3)central-differencing scheme vs upwind

The central-differencing scheme is available only when you are using the LES turbulence model, and it should be used only when the mesh spacing(Íø¸ñ¼ä¾à£©is fine enough so that the magnitude of the local Peclet number (Equation 26.2-5) is less than 1. 4)power law vs upwind

A power law scheme is also available, but it will generally yield the same accuracy as the first-order scheme.

Choosing the Pressure Interpolation Scheme(ѹÁ¦ÀëÉ¢¸ñʽ£©

a number of pressure interpolation schemes are available when the segregated solver is used in

FLUENT. For most cases the standard(default) scheme is acceptable, but some types of models may benenit from one of the other schemes:

For problems involving large body forces, the body-force-weighted scheme is recommended. For flows with high swirl numbers, high-Rayleigh-number natural convection, highspeed rotating flows, flows involving porous media, and flows in strongly curved domains, use the PRESTO! scheme.

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Use the second-order scheme for improved accuracy when one of the other schemes is not applicable.

Choosing the Density Interpolation Scheme which is available at solve a single-phase compressible flow.

If you are calculating a compressible flow with shocks, the first-order upwind scheme may tend to smooth the shocks; you should use the second-order-upwind or QUICK scheme for such flows.

Choosing the Pressure-Velocity Coupling Method(ѹÁ¦£­ËÙ¶È·½³ÌñîºÏ·½·¨£© SIMPLE vs. SIMPLEC

SIMPLE is the default, but many problems will benenit from the use of SIMPLEC, For relatively uncomplicated problems (laminar

ows with no additional models activated) in which convergence is limited by the pressure-velocity coupling, you can often obtain a converged solution more quickly using SIMPLEC. With SIMPLEC, the pressurecorrection under-relaxation factor is generally set to 1.0, which aids in convergence speedup. In some problems, however, increasing the pressure-correction under-relaxation to 1.0 can lead to instability due to high grid skewness. For such cases, you will need to use one or more skewness correction schemes, use a slightly more conservative under-relaxation value (up to 0.7), or use the SIMPLE algorithm. The SIMPLEC skewness correction allows FLUENT to obtain a solution on a highly skewed mesh in approximately the same number of iterations as required for a more orthogonal mesh.

Pressure-Implicit with Splitting of Operators (PISO)

The PISO algorithm with neighbor correction is highly recommended for all transient flow calculations, especially when you want to use a large time step. (For problems that use the LES turbulence model, which usually requires small time steps, using PISO may result in increased computational expense, so SIMPLE or SIMPLEC should be considered instead.) PISO can maintain a stable calculation with a larger time step and an under-relaxation factor of 1.0 for both momentum and pressure.

For steady-state problems, PISO with neighbor correction does not provide any noticeable advantage over SIMPLE or SIMPLEC with optimal under-relaxation factors.

When you use PISO neighbor correction, under-relaxation factors of 1.0 or near 1.0 are recommended for all equations.If you use just the PISO skewness correction for highly-distorted meshes (without neighbor correction), set the under-relaxation factors for momentum and pressure so that they sum to 1 (e.g., 0.3 for pressure and 0.7 for momentum). If you use both PISO methods, follow the under-relaxation recommendations for PISO neighbor correction, above.

Fractional Step Method

The Fractional Step method (FSM) is available when you choose to use the NITA scheme, the FSM

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