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  3. 这网格会有什么问题

这网格会有什么问题

已定时 已固定 已锁定 已移动 Meshy
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  • S 离线
    S 离线
    shrine
    在 中回复了 李东岳 最后由 编辑
    #3

    @李东岳 interFoam

    李东岳李 1 条回复 最后回复
  • 李东岳李 离线
    李东岳李 离线
    李东岳 管理员
    在 中回复了 shrine 最后由 编辑
    #4

    @shrine 把你log贴全看一下

    http://dyfluid.com/index.html
    需要帮助debug算例的看这个 https://cfd-china.com/topic/8018

    S 1 条回复 最后回复
  • S 离线
    S 离线
    shrine
    在 中回复了 李东岳 最后由 编辑
    #5

    @李东岳 Screenshot from 2022-02-24 09-40-19.png

    李东岳李 1 条回复 最后回复
  • 李东岳李 离线
    李东岳李 离线
    李东岳 管理员
    在 中回复了 shrine 最后由 编辑
    #6

    @shrine 用代码高亮的方式把log贴全。你这个目前判断不出来。用下面这种方式,不要截图

    ```加一行空格 asdfasdf
    asdfasdf
    asdfasdf
    asdfasdf
    asdfasdf 加一行空格 ```
    

    http://dyfluid.com/index.html
    需要帮助debug算例的看这个 https://cfd-china.com/topic/8018

    S 1 条回复 最后回复
  • S 离线
    S 离线
    shrine
    在 中回复了 李东岳 最后由 shrine 编辑
    #7

    @李东岳 这是最后发散的

    
                                    
    
    Courant Number mean: 0.00552061 max: 83.2287
    Interface Courant Number mean: 0.000324483 max: 81.0174
    deltaT = 1.18982e-53
    Time = 3.9265
    
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.0137961  Min(alpha.water) = -5.68761e-22  Max(alpha.water) = 1
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.0137961  Min(alpha.water) = -5.6877e-22  Max(alpha.water) = 1
    DICPCG:  Solving for p_rgh, Initial residual = 0.939399, Final residual = 0.0886856, No Iterations 34
    time step continuity errors : sum local = 4.07115e-07, global = -7.89166e-08, cumulative = 8.14176e+13
    DICPCG:  Solving for p_rgh, Initial residual = 0.176142, Final residual = 0.0126346, No Iterations 5
    time step continuity errors : sum local = 7.05788e-07, global = -7.10764e-08, cumulative = 8.14176e+13
    DICPCG:  Solving for p_rgh, Initial residual = 0.0465706, Final residual = 8.69174e-07, No Iterations 141
    time step continuity errors : sum local = 5.76874e-11, global = -1.50599e-12, cumulative = 8.14176e+13
    smoothSolver:  Solving for epsilon, Initial residual = 4.50714e-08, Final residual = 4.50714e-08, No Iterations 0
    smoothSolver:  Solving for k, Initial residual = 0.999977, Final residual = 2.51429e-12, No Iterations 1
    bounding k, min: 1.72065e-45 max: 1.33449e+84 average: 4.66546e+79
    ExecutionTime = 108.46 s  ClockTime = 109 s
    
    Courant Number mean: 1.25464e-05 max: 0.294671
    Interface Courant Number mean: 5.47167e-07 max: 0.098979
    deltaT = 1.39171e-53
    Time = 3.9265
    
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.0137961  Min(alpha.water) = -1.12909e-21  Max(alpha.water) = 1
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.0137961  Min(alpha.water) = -1.41136e-22  Max(alpha.water) = 1
    DICPCG:  Solving for p_rgh, Initial residual = 0.185686, Final residual = 0.0180753, No Iterations 7
    time step continuity errors : sum local = 2.01538e-06, global = 8.36086e-09, cumulative = 8.14176e+13
    DICPCG:  Solving for p_rgh, Initial residual = 1.72997e-14, Final residual = 1.72997e-14, No Iterations 0
    time step continuity errors : sum local = 2.60495e+41, global = 1.67368e+25, cumulative = 1.67368e+25
    DICPCG:  Solving for p_rgh, Initial residual = 1.73034e-14, Final residual = 1.73034e-14, No Iterations 0
    time step continuity errors : sum local = 2.60551e+41, global = 5.1378e+24, cumulative = 2.18746e+25
    
    S 1 条回复 最后回复
  • S 离线
    S 离线
    shrine
    在 中回复了 shrine 最后由 编辑
    #8

    @shrine 最开始,中间太多,贴不全

    /*---------------------------------------------------------------------------*\
      =========                 |
      \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox
       \\    /   O peration     | Website:  https://openfoam.org
        \\  /    A nd           | Version:  8
         \\/     M anipulation  |
    \*---------------------------------------------------------------------------*/
    Build  : 8
    Exec   : interFoam
    Date   : Feb 24 2022
    Time   : 10:28:19
    Host   : "dyfluid"
    PID    : 3889
    I/O    : uncollated
    Case   : /home/dyfluid/OpenFOAM/wjx/simashan10/simashan10-10
    nProcs : 1
    sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE).
    fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 10)
    allowSystemOperations : Allowing user-supplied system call operations
    
    // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
    Create time
    
    Create mesh for time = 3
    
    
    PIMPLE: No convergence criteria found
    
    
    PIMPLE: Operating solver in transient mode with 1 outer corrector
    PIMPLE: Operating solver in PISO mode
    
    
    Reading field p_rgh
    
    Reading field U
    
    Reading/calculating face flux field phi
    
    Reading transportProperties
    
    Selecting incompressible transport model Newtonian
    Selecting incompressible transport model Newtonian
    Selecting turbulence model type RAS
    Selecting RAS turbulence model kEpsilon
    RAS
    {
        RASModel        kEpsilon;
        turbulence      on;
        printCoeffs     on;
        Cmu             0.09;
        C1              1.44;
        C2              1.92;
        C3              0;
        sigmak          1;
        sigmaEps        1.3;
    }
    
    
    Reading g
    
    Reading hRef
    Calculating field g.h
    
    No MRF models present
    
    No finite volume options present
    Restarting alpha
    DICPCG:  Solving for pcorr, Initial residual = 1, Final residual = 9.43948e-11, No Iterations 234
    time step continuity errors : sum local = 4.25911e-18, global = -6.53738e-21, cumulative = -6.53738e-21
    Courant Number mean: 0.00577809 max: 0.443976
    
    Starting time loop
    
    Courant Number mean: 0.00577809 max: 0.443976
    Interface Courant Number mean: 0.00156001 max: 0.443976
    deltaT = 0.00487805
    Time = 3.00488
    
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.0116292  Min(alpha.water) = -5.92388e-18  Max(alpha.water) = 1
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.011635  Min(alpha.water) = -1.68355e-18  Max(alpha.water) = 1
    DICPCG:  Solving for p_rgh, Initial residual = 0.0133921, Final residual = 0.000600949, No Iterations 2
    time step continuity errors : sum local = 3.14837e-05, global = -1.42553e-09, cumulative = -1.42553e-09
    DICPCG:  Solving for p_rgh, Initial residual = 0.0042361, Final residual = 0.000293054, No Iterations 2
    time step continuity errors : sum local = 1.5383e-05, global = -1.52887e-09, cumulative = -2.95441e-09
    DICPCG:  Solving for p_rgh, Initial residual = 0.00109826, Final residual = 9.11591e-07, No Iterations 46
    time step continuity errors : sum local = 4.78222e-08, global = 2.49579e-09, cumulative = -4.58612e-10
    smoothSolver:  Solving for epsilon, Initial residual = 0.00269233, Final residual = 1.17508e-07, No Iterations 2
    smoothSolver:  Solving for k, Initial residual = 0.00185872, Final residual = 1.4954e-07, No Iterations 2
    ExecutionTime = 0.68 s  ClockTime = 1 s
    
    Courant Number mean: 0.00641595 max: 0.484557
    Interface Courant Number mean: 0.00171789 max: 0.484557
    deltaT = 0.00502587
    Time = 3.0099
    
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.0116409  Min(alpha.water) = -4.24191e-18  Max(alpha.water) = 1
    MULES: Solving for alpha.water
    Phase-1 volume fraction = 0.0116468  Min(alpha.water) = -2.19039e-18  Max(alpha.water) = 1
    DICPCG:  Solving for p_rgh, Initial residual = 0.0141558, Final residual = 0.000625894, No Iterations 2
    time step continuity errors : sum local = 3.48527e-05, global = 4.988e-09, cumulative = 4.52939e-09
    DICPCG:  Solving for p_rgh, Initial residual = 0.00456781, Final residual = 0.000295155, No Iterations 2
    time step continuity errors : sum local = 1.64706e-05, global = 5.11498e-09, cumulative = 9.64437e-09
    DICPCG:  Solving for p_rgh, Initial residual = 0.00118887, Final residual = 9.82617e-07, No Iterations 86
    time step continuity errors : sum local = 5.47957e-08, global = 5.40295e-11, cumulative = 9.6984e-09
    smoothSolver:  Solving for epsilon, Initial residual = 0.00272111, Final residual = 1.30398e-07, No Iterations 2
    smoothSolver:  Solving for k, Initial residual = 0.0018956, Final residual = 1.65103e-07, No Iterations 2
    ExecutionTime = 0.89 s  ClockTime = 1 s
    
    Courant Number mean: 0.00661659 max: 0.49063
    Interface Courant Number mean: 0.0017706 max: 0.49063
    deltaT = 0.00510359
    Time = 3.01501
               
    
    1 条回复 最后回复
  • 李东岳李 离线
    李东岳李 离线
    李东岳 管理员
    写于 最后由 编辑
    #9

    目前只能看出发散了。库朗数太大。直接发散了。你可以换结构网格试一下。应该会好很多。

    http://dyfluid.com/index.html
    需要帮助debug算例的看这个 https://cfd-china.com/topic/8018

    S 1 条回复 最后回复
  • S 离线
    S 离线
    shrine
    在 中回复了 李东岳 最后由 编辑
    #10

    @李东岳

    背面有圆弧,很难全部用结构网格
    QQ图片20220226141414.jpg

    1 条回复 最后回复
  • 李东岳李 离线
    李东岳李 离线
    李东岳 管理员
    写于 最后由 编辑
    #11

    你目前画的圆弧的地方就是结构网格啊 :135:
    目前只能看出发散了

    http://dyfluid.com/index.html
    需要帮助debug算例的看这个 https://cfd-china.com/topic/8018

    S 1 条回复 最后回复
  • S 离线
    S 离线
    shrine
    在 中回复了 李东岳 最后由 shrine 编辑
    #12

    @李东岳 把圆弧去掉,全部改成六面体网格,还是发散。
    从细管流入水池就发散了。
    附了log文件
    Screenshot from 2022-03-01 09-14-34.png

    Screenshot from 2022-03-01 09-12-07.png

    Screenshot from 2022-03-01 09-12-19.png

    log

    1 条回复 最后回复
  • 黒 离线
    黒 离线
    黒洛克
    写于 最后由 编辑
    #13

    你是不是算的倒虹吸啊

    1 条回复 最后回复

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