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R

Rui

@Rui
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最新

  • 求助:孔隙介质中流体被加热上浮过程的压力方程求解问题
    R Rui

    @李东岳 , 李老师您好,我已经在chtMultiRegionFoam中植入了第一张图所示的拉普拉斯及泊松方程,

    QQ截图20210619102650.jpg

    QQ截图20210619102636.jpg

    实现了对电势在流固区域的耦合求解,但电荷的求解似乎不对,然后电场力的求解结果也和参考文章里面差的太多,但我边界设置理论上是符合文章要求的,第二张图和第三张图是我和参考文章计算结果的对比。参考文章及我的算例和编译的求解器链接放在这里:https://pan.baidu.com/s/1U8NBBon8CFVvDoF9Fsi9UA 提取码:mppz
    麻烦李老师能抽空看一下,检查一下问题,不胜感激。一个头俩大:136: :136:

    QQ截图20210619095212.jpg QQ截图20210619095249.jpg


  • 求助:孔隙介质中流体被加热上浮过程的压力方程求解问题
    R Rui

    @李东岳 李老师您好,按照您的提示我把div(grad())项改成了laplacian操作符,但是在单独求解图1所示的方程时迭代了几步之后它就挂了,图2 是我的代码,其中epsilonr、ka均是常数,rhoel定义的场是volScalarField,不知是不是自己代码编写的问题,还望李老师指点迷津:chouchou: :chouchou: 提交三.jpg 提交2.jpg 提交1.jpg


  • 求助:孔隙介质中流体被加热上浮过程的压力方程求解问题
    R Rui

    @李东岳 好的,感谢李老师:huahua: :huahua:


  • 求助:孔隙介质中流体被加热上浮过程的压力方程求解问题
    R Rui

    @李东岳 感谢李老师回复:146: ,问题解决,OF小白一只,多多包涵:huahua:


  • 求助:孔隙介质中流体被加热上浮过程的压力方程求解问题
    R Rui

    提交3.jpg 提交二.jpg 提交一.jpg
    @东岳,李老师您好,目前自己在做气动热这块,就想求解第一张图上放的这个方程,自己编译的代码如第二张图所示,epsilonr和rhoel定义的场都是volScalarField,但编译的时候报这种错:134: :141:


  • 关于cht的网格划分问题
    R Rui

    @李东岳 在 关于cht的网格划分问题 中说:

    writeZones

    万分感谢李老师的解答,转化格式(写入命令语句)为
    fluentMeshToFoam xxx.msh -writeZones,
    本人OpenFoam小白,望老师多多包涵:chouchou:


  • 关于cht的网格划分问题
    R Rui

    @李东岳 1.png 李老师您好,我的网格是ICEM画的,然后再导入OpenFoam的,网格分了两个区,为什么导入之后PolyMesh里面看不到任何关于网格区域的信息,如果我想在其中一个区域添加源项该如何调用这个区域呢:134:


  • 指定cellzone区域添加动量源项的问题
    R Rui

    @我是河滩 在 指定cellzone区域添加动量源项的问题 中说:

    遍历了整个网格区域进行搜索

    前辈您好,您是如何遍历整个网格区域并获取网格坐标的呢,是利用mesh.C().component()语句吗:141:


  • 添加湍流模型遇到问题(重发)
    R Rui

    李老师您好,请问这个问题解决了吗?我也遇到类似的问题,就是只改湍流模型的名字,在编译的时候也出现了一些error


  • OpenFoam使用rhoReactingFoam过程中出现的问题
    R Rui

    @Rui 我自己尝试过的办法有检查边界,更改离散格式和时间步长等等,换过求解器为reactingFoam.但都未能解决这个问题,希望大佬们能够指点,谢谢~


  • OpenFoam使用rhoReactingFoam过程中出现的问题
    R Rui
    diagonal:  Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
    smoothSolver:  Solving for Ux, Initial residual = 0.00441557, Final residual = 1.54512e-07, No Iterations 1
    smoothSolver:  Solving for Uy, Initial residual = 0.00624943, Final residual = 1.18395e-07, No Iterations 1
    DILUPBiCG:  Solving for H2, Initial residual = 0.00188285, Final residual = 7.43415e-08, No Iterations 1
    DILUPBiCG:  Solving for O2, Initial residual = 0.00188283, Final residual = 1.01514e-07, No Iterations 1
    DILUPBiCG:  Solving for H, Initial residual = 0, Final residual = 0, No Iterations 0
    DILUPBiCG:  Solving for OH, Initial residual = 0, Final residual = 0, No Iterations 0
    DILUPBiCG:  Solving for H2O, Initial residual = 0.00188283, Final residual = 1.01514e-07, No Iterations 1
    DILUPBiCG:  Solving for O, Initial residual = 0, Final residual = 0, No Iterations 0
    smoothSolver:  Solving for h, Initial residual = 0.00147451, Final residual = 5.51534e-08, No Iterations 1
    --> FOAM Warning : 
        From function Foam::scalar Foam::janafThermo<EquationOfState>::limit(Foam::scalar) const [with EquationOfState = Foam::perfectGas<Foam::specie>; Foam::scalar = double]
        in file /home/ubuntu/OpenFOAM/OpenFOAM-6/src/thermophysicalModels/specie/lnInclude/janafThermoI.H at line 117
        attempt to use janafThermo<EquationOfState> out of temperature range 200 -> 3500;  T = 30.769
    --> FOAM Warning : 
        From function Foam::scalar Foam::janafThermo<EquationOfState>::limit(Foam::scalar) const [with EquationOfState = Foam::perfectGas<Foam::specie>; Foam::scalar = double]
        in file /home/ubuntu/OpenFOAM/OpenFOAM-6/src/thermophysicalModels/specie/lnInclude/janafThermoI.H at line 117
        attempt to use janafThermo<EquationOfState> out of temperature range 200 -> 3500;  T = -214.865
    --> FOAM Warning : 
        From function Foam::scalar Foam::janafThermo<EquationOfState>::limit(Foam::scalar) const [with EquationOfState = Foam::perfectGas<Foam::specie>; Foam::scalar = double]
        in file /home/ubuntu/OpenFOAM/OpenFOAM-6/src/thermophysicalModels/specie/lnInclude/janafThermoI.H at line 117
        attempt to use janafThermo<EquationOfState> out of temperature range 200 -> 3500;  T = 147.685
    --> FOAM Warning : 
        From function Foam::scalar Foam::janafThermo<EquationOfState>::limit(Foam::scalar) const [with EquationOfState = Foam::perfectGas<Foam::specie>; Foam::scalar = double]
        in file /home/ubuntu/OpenFOAM/OpenFOAM-6/src/thermophysicalModels/specie/lnInclude/janafThermoI.H at line 117
        attempt to use janafThermo<EquationOfState> out of temperature range 200 -> 3500;  T = 147.687
    --> FOAM Warning : 
        From function Foam::scalar Foam::janafThermo<EquationOfState>::limit(Foam::scalar) const [with EquationOfState = Foam::perfectGas<Foam::specie>; Foam::scalar = double]
        in file /home/ubuntu/OpenFOAM/OpenFOAM-6/src/thermophysicalModels/specie/lnInclude/janafThermoI.H at line 117
        attempt to use janafThermo<EquationOfState> out of temperature range 200 -> 3500;  T = -215.127
    --> FOAM Warning : 
        From function Foam::scalar Foam::janafThermo<EquationOfState>::limit(Foam::scalar) const [with EquationOfState = Foam::perfectGas<Foam::specie>; Foam::scalar = double]
        in file /home/ubuntu/OpenFOAM/OpenFOAM-6/src/thermophysicalModels/specie/lnInclude/janafThermoI.H at line 117
        attempt to use janafThermo<EquationOfState> out of temperature range 200 -> 3500;  T = 28.5007
    min/max(T) = 200, 534.025
    smoothSolver:  Solving for p, Initial residual = 0.00340835, Final residual = 7.54003e-11, No Iterations 1
    smoothSolver:  Solving for p, Initial residual = 2.66055e-10, Final residual = 2.66055e-10, No Iterations 0
    smoothSolver:  Solving for p, Initial residual = 2.66055e-10, Final residual = 2.66055e-10, No Iterations 0
    diagonal:  Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
    time step continuity errors : sum local = 1.58233e-12, global = 8.75409e-14, cumulative = 6.66904e-12
    smoothSolver:  Solving for p, Initial residual = 2.46585e-05, Final residual = 5.53512e-13, No Iterations 1
    smoothSolver:  Solving for p, Initial residual = 2.76545e-12, Final residual = 2.76545e-12, No Iterations 0
    smoothSolver:  Solving for p, Initial residual = 2.76545e-12, Final residual = 2.76545e-12, No Iterations 0
    diagonal:  Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
    time step continuity errors : sum local = 1.65649e-14, global = 1.10285e-15, cumulative = 6.67015e-12
    #0  Foam::error::printStack(Foam::Ostream&) at ??:?
    #1  Foam::sigFpe::sigHandler(int) at ??:?
    #2  ? in "/lib/x86_64-linux-gnu/libc.so.6"
    #3  log in "/lib/x86_64-linux-gnu/libm.so.6"
    #4  Foam::omegaWallFunctionFvPatchScalarField::calculate(Foam::turbulenceModel const&, Foam::List<double> const&, Foam::fvPatch const&, Foam::Field<double>&, Foam::Field<double>&) at ??:?
    #5  Foam::omegaWallFunctionFvPatchScalarField::calculateTurbulenceFields(Foam::turbulenceModel const&, Foam::Field<double>&, Foam::Field<double>&) at ??:?
    #6  Foam::omegaWallFunctionFvPatchScalarField::updateCoeffs() at ??:?
    #7  Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh>::Boundary::updateCoeffs() at ??:?
    #8  Foam::kOmegaSST<Foam::eddyViscosity<Foam::RASModel<Foam::EddyDiffusivity<Foam::ThermalDiffusivity<Foam::CompressibleTurbulenceModel<Foam::fluidThermo> > > > >, Foam::EddyDiffusivity<Foam::ThermalDiffusivity<Foam::CompressibleTurbulenceModel<Foam::fluidThermo> > > >::correct() at ??:?
    #9  ? at ??:?
    #10  __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6"
    #11  ? at ??:?
    浮点数例外 (核心已转储)
    
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