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    chengan.wangC

    @黄昏晓为谁破 在 第三代涡识别方法liutex的Fortran程序运行出错原因,求助 中说:

    @Vortex学习 我没用过Fortran程序计算Rortex,不过我的方法可以借鉴下,就是使用Tecplot打开Fluent结果,并导出基于节点的data文件,里面只包含xyz坐标以及UVW速度,然后我是在matlab中进行处理获得的R值以及矢量值,在替换data文件里的数值,最后再使用Tecplot打开data文件。这样可以处理较大网格量的数据,不过这个网格量得取决于Tecplot软件,我之前有个2000万的网格,Tecplot无法打开,我就很无奈了。

    您好,这么多节点的UVW速度,如何在matlab里面计算速度梯度张量呢?

  • 关于MULES的疑问

    OpenFOAM
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    C

    @yhdthu

    感谢,没想到知乎上也有大神研究这个!

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    Z

    还有就是如果网格节点无法保证周期性一一对应,可以将对应的周期面设置为interface,然后到fluent里通过匹配两个interface面,并选择对话框下方的Periodic boundary conditions设置
    另外一款网格划分软件Gambit的话就可以直接设置多对周期性边界条件

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    C

    Sorry, Chinese input missing....
    0_1476947519913_oie_yyxHcXChIqBJ.png

  • EMMS曳力UDF

    Fluent
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    李东岳

    不懂Fluent,不过EMMS类似这些模型的Cd,其实都大差不差。我只能点评到这了..

  • Vocab day day day :-)

    CFD彩虹条
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    List 13 desolate
    荒凉的 despair n. vi. desperate adj.
    a feeling that you have no hope at all
    drive sb. to despair
    对某人感到绝望 despair of sb.
    My teacher began to despair of me dispatch
    formal 为了特定的目的send某人或某物到某地
    Dispatch several officers to Beijing despise
    蔑视
    I despise all cowards detain
    拘留 deteriorate
    恶化,变坏
    cause the leather to deteriorate deviate
    偏离
    deviate from the truth
    deviate from the original plan dictate dictation
    口述,使听写
    The boss dictate the plan to us
    She is dictating a plan to her secretary diminish
    reduce discern
    to notice or understand something by thinking about it carefully
    Officials were keen to discern how much public support there was
    I would discern what his heart and soul were like discourse
    演讲
    I felt at home in this kind of discourse
    a discourse on art discreet
    小心谨慎的
    I stood back at a discreet distance
    Reporters asked some discreet questions discrepancy
    a difference between two amounts, details, reports etc that should be the same
    Police found discrepancies in the two men's reports
  • 读博是为了什么?

    CFD彩虹条
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    N

    硕士毕业找到了一些研究所的工作,还是拒了选择读博。因为自己总觉得还有很多东西值得深入地学习。读博是个难得的提升自我的机会,比较enjoy独处的时候可以静下心来思考。生活也不算惨淡,有funding可以不愁吃喝。

  • eddy,vortex和whirl的区别

    Algorithm
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    李东岳

    这个放在他们搞涡那面,估计能讨论一上午 :duang:

    我个人也不太熟悉。在我的文章里面,也不太关心涡的情况。

  • 三个高薪职业

    CFD彩虹条
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    C

    链家燕郊在疯狂抛售。燕郊涨到了二三万,已经有足够首付加上资格攻进帝都,符合下面这条路线:
    燕郊—五四环—四三环。

  • 湍流模拟几个图

    CFD彩虹条
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    0_1472638385877_捕获.JPG
    2_1472638455925_捕获4.JPG 1_1472638455924_捕获3.JPG 0_1472638455924_捕获2.JPG

    Turbulence
    CEFRC Combustion Summer School
    Prof. Dr.-Ing. Heinz Pitsch
    2014

  • 汉莎航空登机牌补办?

    CFD彩虹条
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    .J..

    亏!!

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    Z

    好像乱码了。我直接copy上来。
    #include "udf.h"
    #include "metric.h"
    #include "math.h"
    #include "mem.h"
    #include "sg_mem.h"

    /关键参数设定*/

    /模型参数/
    #define TD 2288 /换热管数量/
    #define IDUDF 57 /udf壁面编号/
    #define N 887 /单根换热管轴向面网格单元数,个/
    #define dy_min 0.008 /换热管轴向网格最小间距,m/
    #define f_inc 1.005 /耦合迭代收敛性控制增益因子(备用)/
    #define f_dec 0.995 /耦合迭代收敛性控制衰减因子(备用)/
    #define nb_factor 0.32 /核态沸腾起始因子,用于初始化核态沸腾换热区起点/
    #define fb_factor 0.61 /膜态沸腾起始因子,用于初始化膜态沸腾换热区起点/
    #define spv_factor 0.71 /单相汽起始因子,用于初始化单相汽对流换热区起点/
    #define p_start 0. /换热段起始坐标,用于壁温分段线性初始化,K/
    #define p_end 26. /换热段终点坐标,用于壁温分段线性初始化,K/
    #define Tw_in 533.15 /初始化入口处壁面温度,如比入口流体温度高50K,应同时保证低于饱和温度/
    #define Tw_nb 640.4 /初始化沸腾起始点壁面温度,如比饱和温度高15K/
    #define Tw_fb 665.4 /初始化膜态沸腾起始点壁面温度,如比饱和温度高40K/
    #define Tw_spv 685.4 /初始化单相汽对流起始点壁面温度,如比饱和温度高60K/
    #define Tw_out 725.4 /初始化出口处壁面温度,如比饱和温度高100K,应同时保证低于钠侧入口温度/

    /工况参数/
    #define Tl_in 483.15
    #define dh_na 0.0396
    #define di_water 0.01
    #define Psat 17000000
    #define Tsat 625.44
    #define m_na 1608.24
    #define m_water 0.067872
    #define G_water 864.605
    #define xcrt 0.357431664

    /饱和参数/
    #define rou_ls 565.18
    #define rou_vs 119.48
    #define mu_l_s 0.00006472
    #define mu_v_s 0.00002418
    #define Cp_l_s 10817.
    #define Cp_v_s 18309.
    #define K_l_s 0.43061
    #define K_v_s 0.14174
    #define h_l_s 1690035.
    #define h_v_s 2547413.
    #define hlin 903356.96
    #define hv65382 2812819.
    #define hv79182 3339351.
    #define hfv 857376.9
    #define sgm 0.00324
    #define n 1.0

    DEFINE_EXECUTE_ON_LOADING(on_loading, libname)
    {
    Set_User_Memory_Name(2,"U-Temperature_Water_Side");
    Set_User_Memory_Name(12,"U-HTC_Water_Side");
    }

    DEFINE_ADJUST(cal_tl_htc, domain)
    {
    /换热管吸热量求解/
    #if !RP_HOST

    face_t f; cell_t c; Thread *t; Thread *ct; real x[ND_ND]; real A[ND_ND]; real brll,brtl,barea,Tall,Tgr,nalht,F,htcfc,htcnb,retp,S,pw,xtd,QTsub,QTsup,QT65382,QT79182,xjdg; real mu_tw; real Y[N] = {0.0100,0.0300,0.0500,0.0700,0.0900,0.1100,0.1300,0.1500,0.1700,0.1900,0.2040,0.2120,0.2200,0.2330,0.2512,0.2693,0.2873,0.3054,0.3236,0.3417,0.3598,0.3778,0.3960,0.4090,0.4170,0.4250,0.4398,0.4613,0.4827,0.5042,0.5257,0.5473,0.5688,0.5903,0.6118,0.6332,0.6547,0.6762,0.6977,0.7193,0.7340,0.7420,0.7500,0.7634,0.7823,0.8011,0.8200,0.8388,0.8577,0.8765,0.8954,0.9142,0.9331,0.9614,0.9991,1.0367,1.0745,1.1121,1.1350,1.1430,1.1510,1.1738,1.2115,1.2492,1.2869,1.3246,1.3623,1.4000,1.4377,1.4754,1.5131,1.5360,1.5440,1.5520,1.5748,1.6126,1.6502,1.6880,1.7256,1.7634,1.8010,1.8388,1.8764,1.9142,1.9370,1.9450,1.9530,1.9758,2.0136,2.0512,2.0890,2.1267,2.1644,2.2020,2.2397,2.2775,2.3152,2.3380,2.3460,2.3540,2.3768,2.4146,2.4523,2.4899,2.5277,2.5654,2.6030,2.6407,2.6785,2.7162,2.7390,2.7470,2.7550,2.7779,2.8156,2.8533,2.8909,2.9287,2.9664,3.0041,3.0417,3.0795,3.1172,3.1400,3.1480,3.1560,3.1788,3.2166,3.2543,3.2919,3.3296,3.3674,3.4051,3.4427,3.4805,3.5182,3.5410,3.5490,3.5570,3.5798,3.6176,3.6553,3.6930,3.7306,3.7684,3.8061,3.8438,3.8814,3.9192,3.9420,3.9500,3.9580,3.9808,4.0185,4.0563,4.0939,4.1316,4.1694,4.2070,4.2448,4.2824,4.3201,4.3430,4.3510,4.3590,4.3818,4.4195,4.4573,4.4949,4.5326,4.5703,4.6080,4.6458,4.6834,4.7211,4.7440,4.7520,4.7600,4.7828,4.8205,4.8583,4.8959,4.9337,4.9713,5.0090,5.0468,5.0844,5.1221,5.1450,5.1530,5.1610,5.1838,5.2215,5.2592,5.2969,5.3347,5.3723,5.4100,5.4478,5.4854,5.5231,5.5460,5.5540,5.5620,5.5848,5.6226,5.6602,5.6979,5.7357,5.7733,5.8110,5.8488,5.8864,5.9241,5.9470,5.9550,5.9630,5.9858,6.0236,6.0612,6.0989,6.1367,6.1743,6.2120,6.2498,6.2874,6.3252,6.3480,6.3560,6.3640,6.3868,6.4246,6.4622,6.4999,6.5377,6.5753,6.6130,6.6507,6.6884,6.7262,6.7490,6.7570,6.7650,6.7878,6.8256,6.8632,6.9009,6.9387,6.9763,7.0141,7.0517,7.0894,7.1272,7.1500,7.1580,7.1660,7.1888,7.2266,7.2642,7.3019,7.3397,7.3773,7.4151,7.4527,7.4904,7.5282,7.5510,7.5590,7.5670,7.5898,7.6276,7.6652,7.7030,7.7406,7.7783,7.8161,7.8537,7.8914,7.9292,7.9520,7.9600,7.9680,7.9908,8.0286,8.0662,8.1040,8.1417,8.1793,8.2171,8.2548,8.2924,8.3302,8.3530,8.3610,8.3690,8.3919,8.4296,8.4672,8.5050,8.5427,8.5803,8.6180,8.6558,8.6934,8.7311,8.7540,8.7620,8.7700,8.7928,8.8306,8.8682,8.9059,8.9437,8.9813,9.0191,9.0568,9.0944,9.1321,9.1550,9.1630,9.1710,9.1939,9.2316,9.2692,9.3070,9.3447,9.3823,9.4200,9.4578,9.4955,9.5331,9.5560,9.5640,9.5720,9.5948,9.6326,9.6702,9.7079,9.7457,9.7833,9.8210,9.8588,9.8965,9.9341,9.9570,9.9650,9.9730,9.9959,10.0336,10.0712,10.1090,10.1467,10.1844,10.2220,10.2598,10.2975,10.3351,10.3580,10.3660,10.3740,10.3969,10.4346,10.4722,10.5100,10.5477,10.5854,10.6230,10.6608,10.6985,10.7361,10.7590,10.7670,10.7750,10.7979,10.8356,10.8733,10.9109,10.9487,10.9864,11.0240,11.0617,11.0995,11.1371,11.1600,11.1680,11.1760,11.1988,11.2366,11.2743,11.3119,11.3497,11.3874,11.4250,11.4628,11.5005,11.5381,11.5610,11.5690,11.5770,11.5998,11.6376,11.6753,11.7129,11.7507,11.7884,11.8260,11.8638,11.9015,11.9391,11.9620,11.9700,11.9780,12.0008,12.0386,12.0763,12.1139,12.1517,12.1894,12.2270,12.2648,12.3025,12.3401,12.3630,12.3710,12.3790,12.4018,12.4396,12.4773,12.5149,12.5527,12.5904,12.6280,12.6658,12.7035,12.7411,12.7640,12.7720,12.7800,12.8028,12.8406,12.8783,12.9159,12.9537,12.9914,13.0290,13.0668,13.1045,13.1421,13.1650,13.1730,13.1810,13.2038,13.2416,13.2793,13.3169,13.3547,13.3924,13.4300,13.4678,13.5055,13.5431,13.5660,13.5740,13.5820,13.6048,13.6426,13.6803,13.7179,13.7557,13.7934,13.8310,13.8688,13.9065,13.9441,13.9670,13.9750,13.9830,14.0058,14.0436,14.0813,14.1189,14.1567,14.1944,14.2320,14.2698,14.3075,14.3451,14.3680,14.3760,14.3840,14.4068,14.4446,14.4823,14.5199,14.5577,14.5954,14.6330,14.6708,14.7085,14.7462,14.7690,14.7770,14.7850,14.8078,14.8456,14.8833,14.9209,14.9587,14.9964,15.0340,15.0717,15.1094,15.1472,15.1700,15.1780,15.1860,15.2088,15.2465,15.2843,15.3219,15.3596,15.3974,15.4351,15.4727,15.5105,15.5482,15.5710,15.5790,15.5870,15.6098,15.6476,15.6853,15.7229,15.7607,15.7984,15.8361,15.8737,15.9115,15.9492,15.9720,15.9800,15.9880,16.0108,16.0485,16.0863,16.1240,16.1616,16.1994,16.2371,16.2747,16.3125,16.3502,16.3730,16.3810,16.3890,16.4118,16.4496,16.4873,16.5250,16.5627,16.6003,16.6381,16.6758,16.7134,16.7512,16.7740,16.7820,16.7900,16.8128,16.8505,16.8883,16.9260,16.9636,17.0014,17.0391,17.0767,17.1145,17.1522,17.1750,17.1830,17.1910,17.2139,17.2516,17.2892,17.3270,17.3647,17.4023,17.4401,17.4778,17.5154,17.5532,17.5760,17.5840,17.5920,17.6149,17.6525,17.6903,17.7280,17.7656,17.8034,17.8411,17.8787,17.9165,17.9542,17.9770,17.9850,17.9930,18.0159,18.0536,18.0912,18.1290,18.1667,18.2043,18.2421,18.2798,18.3174,18.3552,18.3780,18.3860,18.3940,18.4168,18.4545,18.4923,18.5299,18.5676,18.6054,18.6431,18.6807,18.7185,18.7562,18.7790,18.7870,18.7950,18.8179,18.8556,18.8932,18.9310,18.9687,19.0063,19.0441,19.0818,19.1194,19.1572,19.1800,19.1880,19.1960,19.2189,19.2565,19.2943,19.3320,19.3696,19.4074,19.4451,19.4827,19.5205,19.5582,19.5810,19.5890,19.5970,19.6199,19.6576,19.6952,19.7330,19.7707,19.8083,19.8461,19.8837,19.9214,19.9592,19.9820,19.9900,19.9980,20.0208,20.0585,20.0963,20.1339,20.1716,20.2094,20.2471,20.2847,20.3225,20.3601,20.3830,20.3910,20.3990,20.4219,20.4596,20.4972,20.5350,20.5727,20.6103,20.6481,20.6858,20.7234,20.7612,20.7840,20.7920,20.8000,20.8229,20.8605,20.8983,20.9360,20.9736,21.0114,21.0490,21.0868,21.1245,21.1621,21.1850,21.1930,21.2010,21.2239,21.2616,21.2992,21.3370,21.3747,21.4123,21.4501,21.4878,21.5254,21.5632,21.5860,21.5940,21.6020,21.6249,21.6625,21.7003,21.7380,21.7757,21.8134,21.8510,21.8888,21.9265,21.9641,21.9870,21.9950,22.0030,22.0259,22.0636,22.1012,22.1390,22.1767,22.2143,22.2521,22.2898,22.3274,22.3652,22.3880,22.3960,22.4040,22.4269,22.4646,22.5023,22.5399,22.5777,22.6154,22.6530,22.6908,22.7285,22.7661,22.7890,22.7970,22.8050,22.8279,22.8656,22.9032,22.9410,22.9787,23.0163,23.0541,23.0917,23.1294,23.1672,23.1900,23.1980,23.2060,23.2288,23.2666,23.3043,23.3419,23.3797,23.4174,23.4550,23.4928,23.5305,23.5681,23.5910,23.5990,23.6070,23.6299,23.6676,23.7052,23.7430,23.7807,23.8183,23.8561,23.8938,23.9314,23.9692,23.9920,24.0000,24.0080,24.0308,24.0686,24.1063,24.1439,24.1817,24.2194,24.2570,24.2948,24.3325,24.3701,24.3930,24.4010,24.4090,24.4319,24.4696,24.5072,24.5450,24.5827,24.6203,24.6581,24.6958,24.7334,24.7712,24.7940,24.8020,24.8100,24.8328,24.8706,24.9083,24.9459,24.9837,25.0214,25.0590,25.0968,25.1345,25.1721,25.1950,25.2030,25.2110,25.2239,25.2417,25.2595,25.2773,25.2951,25.3129,25.3307,25.3485,25.3663,25.3841,25.4019,25.4197,25.4375,25.4553,25.4731,25.4909,25.5087,25.5265,25.5443,25.5621,25.5750,25.5830,25.5910,25.6040,25.6222,25.6403,25.6583,25.6765,25.6945,25.7127,25.7308,25.7488,25.7670,25.7800,25.7880,25.7960,25.8100,25.8300,25.8500,25.8700,25.8900,25.9100,25.9300,25.9500,25.9700,25.9900}; real QTF[N]; int count = 0; int i=0; int j=0; int k=0; int ii=0;

    #endif

    #if RP_NODE

    QTsub=(h_l_s-hlin)*m_water; QTsup=(h_v_s-hlin)*m_water; QT65382=(hv65382-hlin)*m_water; QT79182=(hv79182-hlin)*m_water; nalht = 0.; barea= 0.; brll=0.; xtd =0.; F =0.; htcfc =0.; pw =0.; htcnb =0.; S =0.; retp=0.; xjdg=xcrt; //膜态沸腾临界含气率 for(i=0;i<TD;i++) //遍历每根换热管 { count = 0; t=Lookup_Thread(domain,IDUDF); if (!t) { Error("Thread IDUDF=%d not found!", IDUDF); return; } //第一次遍历,计算每个管子中face的数量 begin_f_loop(f,t) { ct = F_C0_THREAD(f,t); c = F_C0(f,t); if(C_UDMI(c,ct,15)-i<=0.001) //如果属于第i根传热管 count++; } end_f_loop(f,t) // 跳过空管(防止 malloc(0)) if(count == 0) continue; // 分配存储空间 face_t *selected_faces; if (count>0){ selected_faces = (face_t *)malloc(count * sizeof(face_t)); } int index = 0; // 第二次遍历:存储目标管上所有face的指针 begin_f_loop(f,t) { ct = F_C0_THREAD(f,t); c = F_C0(f,t); if(C_UDMI(c,ct,15)-i<=0.001) //如果属于第i根传热管 selected_faces[index++] = f; } end_f_loop(f,t) // 重新遍历单根传热管 for(j=0;j<N;j++) //遍历轴向面上每个网格 { for (ii = 0; ii < count; ii++) { face_t f = selected_faces[ii]; F_CENTROID(x,f,t); if(x[2] <= Y[j]-1.1*dy_min) //判断网格节点是否匹配 nalht += -WALL_HEAT_FLUX(f, t); //累加每个网格的换热量 } nalht = PRF_GRSUM1(nalht); QTF[j] = nalht; //if(myid==3) // Message("Y=%f, QTF = %f,nalht = %f \n",Y[j],QTF[j],nalht); nalht=0.; } /**耦合求解***/ for (ii = 0; ii < count; ii++) { face_t f = selected_faces[ii]; F_CENTROID(x,f,t); c = F_C0(f,t); F_AREA(A,f,t); ct = F_C0_THREAD(f,t); barea = NV_MAG(A); brll= -WALL_HEAT_FLUX(f,t); brtl=brll/barea; Tall=F_T(f,t); for(j=0;j<N;j++) { if(fabs(x[2]-Y[j]) < 0.2*dy_min) { C_UDMI(c,ct,0) = QTF[j]/*+(-WALL_HEAT_FLUX(f,t)*24*0.85)*/; //C_UDMI(c,ct,0)=传热量 //if(x[0]<1.423440e-3 && x[0]>0 && x[2]<0) // Message("y=%f,Y=%f,QTF =%f,C_UDMI(c,ct,14)=%f,myid=%d \n",x[1],Y[j],QTF[j],C_UDMI(c,ct,14),myid); } } //if(x[0]<1.423440e-3 && x[0]>0 && x[2]<0) // Message("y=%f,Y=%f,QTF =%f,C_UDMI(c,ct,14)=%f\n",x[1],Y[j],QTF[j],C_UDMI(c,ct,14)); if(C_UDMI(c,ct,2)<=Tl_in) C_UDMI(c,ct,2)=Tl_in; if(C_UDMI(c,ct,2)>=791.82) C_UDMI(c,ct,2) = 791.82; //C_UDMI(c,ct,2)=温度,K if(C_UDMI(c,ct,3)<=0) C_UDMI(c,ct,3)=0.000001;if(C_UDMI(c,ct,3)>=1) C_UDMI(c,ct,3)=1; //C_UDMI(c,ct,3)=含气率 if(C_UDMI(c,ct,0)<=0) //传热量 { C_UDMI(c,ct,1)=0; //负传热区 C_UDMI(c,ct,3)=0; C_UDMI(c,ct,4)=0; C_UDMI(c,ct,0)=0; C_UDMI(c,ct,2)= -59.232*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,3)+157.04*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,2)+82.372*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,1)+324.19; if(C_UDMI(c,ct,2)>=Tsat) C_UDMI(c,ct,2) = Tsat; if(C_UDMI(c,ct,2)<Tl_in) C_UDMI(c,ct,2) = Tl_in; /*if(C_UDMI(c,ct,2)>=Tall) C_UDMI(c,ct,2) = f_dec*Tall;*/ C_UDMI(c,ct,5)=-0.0000731372*pow(C_UDMI(c,t,2),3)+0.11175*pow(C_UDMI(c,t,2),2)-58.15118*C_UDMI(c,t,2)+11121.29394; //C_UDMI(c,ct,5)=密度 C_UDMI(c,ct,6)=-0.0000000000145502*pow(C_UDMI(c,t,2),3)+0.0000000245354*pow(C_UDMI(c,t,2),2)-0.0000141776*C_UDMI(c,t,2)+0.00289; //C_UDMI(c,ct,6)=粘度 C_UDMI(c,ct,7)=-0.0000000278887*pow(C_UDMI(c,t,2),3)+0.0000382479*pow(C_UDMI(c,t,2),2)-0.01819*C_UDMI(c,t,2)+3.67367; //C_UDMI(c,ct,7)=热导率 C_UDMI(c,ct,8)=1.58939572558845E-06*pow(C_UDMI(c,t,2),5)-0.00426225564860069*pow(C_UDMI(c,t,2),4)+4.56374090199481*pow(C_UDMI(c,t,2),3)-2438.73022173804*pow(C_UDMI(c,t,2),2)+650360.432339001*C_UDMI(c,t,2)-69238389.168302; //C_UDMI(c,ct,8)=定压比热容 C_UDMI(c,ct,9)=G_water/C_UDMI(c,ct,5); //C_UDMI(c,ct,9)=流速 C_UDMI(c,ct,10)=C_UDMI(c,ct,5)*C_UDMI(c,ct,9)*di_water/C_UDMI(c,ct,6); //C_UDMI(c,ct,10)=雷诺数 C_UDMI(c,ct,11)=C_UDMI(c,ct,6)*C_UDMI(c,ct,8)/C_UDMI(c,ct,7); //C_UDMI(c,ct,11)=普朗特数 C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.4)*C_UDMI(c,ct,7)/di_water; //C_UDMI(c, ct, 12)=DB公式换热系数 C_UDMI(c,ct,14) = C_UDMI(c,ct,12); //C_UDMI(c,ct,14)=换热系数 } if( C_UDMI(c,ct,0)<=QTsub && C_UDMI(c,ct,0)>0) //单相水 { C_UDMI(c,ct,1)=1;//C_UDMI(c,ct,1)=换热区域编号,1过冷,2泡核,3膜态,4饱和 C_UDMI(c,ct,3)=0; C_UDMI(c,ct,4)=0; //C_UDMI(c,ct,4)=空泡份额 C_UDMI(c,ct,2)=-59.232*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,3)+157.04*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,2)+82.372*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,1)+324.19; if(C_UDMI(c,ct,2)>=Tsat) C_UDMI(c,ct,2) = Tsat; //if(C_UDMI(c,ct,2)>=Tall) // C_UDMI(c,ct,2) = f_dec*Tall; C_UDMI(c,ct,5)=-0.0000731372*pow(C_UDMI(c,t,2),3)+0.11175*pow(C_UDMI(c,t,2),2)-58.15118*C_UDMI(c,t,2)+11121.29394; //C_UDMI(c,ct,5)=密度 C_UDMI(c,ct,6)=-0.0000000000145502*pow(C_UDMI(c,t,2),3)+0.0000000245354*pow(C_UDMI(c,t,2),2)-0.0000141776*C_UDMI(c,t,2)+0.00289; //C_UDMI(c,ct,6)=粘度 C_UDMI(c,ct,7)=-0.0000000278887*pow(C_UDMI(c,t,2),3)+0.0000382479*pow(C_UDMI(c,t,2),2)-0.01819*C_UDMI(c,t,2)+3.67367; //C_UDMI(c,ct,7)=热导率 C_UDMI(c,ct,8)=1.58939572558845E-06*pow(C_UDMI(c,t,2),5)-0.00426225564860069*pow(C_UDMI(c,t,2),4)+4.56374090199481*pow(C_UDMI(c,t,2),3)-2438.73022173804*pow(C_UDMI(c,t,2),2)+650360.432339001*C_UDMI(c,t,2)-69238389.168302; //C_UDMI(c,ct,8)=定压比热容 C_UDMI(c,ct,9)=G_water/C_UDMI(c,ct,5); C_UDMI(c,ct,10)=C_UDMI(c,ct,5)*C_UDMI(c,ct,9)*di_water/C_UDMI(c,ct,6); C_UDMI(c,ct,11)=C_UDMI(c,ct,6)*C_UDMI(c,ct,8)/C_UDMI(c,ct,7); C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.4)*C_UDMI(c,ct,7)/di_water; C_UDMI(c,ct,14) = C_UDMI(c,ct,12); } if( C_UDMI(c,ct,0)>QTsub && C_UDMI(c,ct,0)<QTsup && C_UDMI(c,ct,3)> xjdg) //膜态沸腾 { C_UDMI(c,ct,1)=3; C_UDMI(c,ct,2) = Tsat; C_UDMI(c,ct,3)=(C_UDMI(c,ct,0)/m_water+hlin-h_l_s)/hfv ;//平衡含汽率 if(C_UDMI(c,ct,3)>1) C_UDMI(c,ct,3)=1; if(C_UDMI(c,ct,3)<0) C_UDMI(c,ct,3)=0.00001; C_UDMI(c,ct,4)=1/(1+(1-C_UDMI(c,ct,3))/C_UDMI(c,ct,3)*rou_vs/rou_ls); C_UDMI(c,ct,5)=rou_vs*C_UDMI(c,ct,4)+rou_ls*(1-C_UDMI(c,ct,4)); //均相流 C_UDMI(c,ct,6)=mu_v_s*C_UDMI(c,ct,4)+mu_l_s*(1-C_UDMI(c,ct,4)); C_UDMI(c,ct,7)=K_v_s*C_UDMI(c,ct,4)+K_l_s*(1-C_UDMI(c,ct,4)); C_UDMI(c,ct,8)=Cp_v_s*C_UDMI(c,ct,4)+Cp_l_s*(1-C_UDMI(c,ct,4)); //C_UDMI(c,ct,6)=-4.842954771e-6+4.415494732e-8*Tall; //C_UDMI(c,ct,7)=4.962527816-0.01961204*Tall+0.0000261092*pow(Tall,2)-0.0000000115221*pow(Tall,3); //C_UDMI(c,ct,8)=1158168.03485404-4651.253221*Tall+6.23591198*pow(Tall,2)-0.002783744*pow(Tall,3); C_UDMI(c,ct,9)=G_water/C_UDMI(c,ct,5); C_UDMI(c,ct,10)=C_UDMI(c,ct,5)*C_UDMI(c,ct,9)*di_water/C_UDMI(c,ct,6); C_UDMI(c,ct,11)=C_UDMI(c,ct,6)*C_UDMI(c,ct,8)/C_UDMI(c,ct,7); C_UDMI(c,ct,12)=0.0193*pow(G_water*C_UDMI(c,ct,3)*di_water/mu_v_s,0.8)*pow(mu_v_s*Cp_v_s/K_v_s,1.23)*pow((rou_vs/(rou_vs*C_UDMI(c,ct,4)+rou_ls*(1-C_UDMI(c,ct,4)))),0.68)*pow(rou_vs/rou_ls,0.068)*K_v_s/di_water; C_UDMI(c,ct,14)=0.021*pow(G_water*C_UDMI(c,ct,3)*di_water/mu_v_s,0.8)*pow(C_UDMI(c,ct,11),0.43)*(1-0.1*pow((rou_ls/rou_vs-1)*(1-C_UDMI(c,ct,3)),0.4))*pow(C_UDMI(c,ct,3)+rou_ls/rou_vs*(1-C_UDMI(c,ct,3)),0.8); } if( C_UDMI(c,ct,0)>QTsub && C_UDMI(c,ct,0)<QTsup && C_UDMI(c,ct,3)<=xjdg) //泡核沸腾 { C_UDMI(c,ct,1)=2; C_UDMI(c,ct,2) = Tsat; C_UDMI(c,ct,3)=(C_UDMI(c,ct,0)/m_water+hlin-h_l_s)/hfv ; if(C_UDMI(c,ct,3)>=1) C_UDMI(c,ct,3)=1.0; if(C_UDMI(c,ct,3)<=0) C_UDMI(c,ct,3)=0.00001; C_UDMI(c,ct,4)=1/(1+(1-C_UDMI(c,ct,3))/C_UDMI(c,ct,3)*rou_vs/rou_ls); C_UDMI(c,ct,5)=rou_vs*C_UDMI(c,ct,4)+rou_ls*(1-C_UDMI(c,ct,4)); C_UDMI(c,ct,6)=mu_v_s*C_UDMI(c,ct,4)+mu_l_s*(1-C_UDMI(c,ct,4)); C_UDMI(c,ct,7)=K_v_s*C_UDMI(c,ct,4)+K_l_s*(1-C_UDMI(c,ct,4)); C_UDMI(c,ct,8)=Cp_v_s*C_UDMI(c,ct,4)+Cp_l_s*(1-C_UDMI(c,ct,4)); C_UDMI(c,ct,9)=G_water/C_UDMI(c,ct,5); C_UDMI(c,ct,10)=C_UDMI(c,ct,5)*C_UDMI(c,ct,9)*di_water/C_UDMI(c,ct,6); C_UDMI(c,ct,11)=C_UDMI(c,ct,6)*C_UDMI(c,ct,8)/C_UDMI(c,ct,7); xtd = pow(C_UDMI(c,ct,3)/(1-C_UDMI(c,ct,3)),0.9)*pow(rou_ls/rou_vs,0.5)*pow(mu_v_s/mu_l_s,0.1); if(xtd>0.1) {F=2.35*pow((xtd+0.213),0.736);} else {F=1.;} htcfc=0.023*K_l_s/di_water*pow((G_water*(1-C_UDMI(c,ct,3))*di_water/mu_l_s),0.8)*pow((mu_l_s*Cp_l_s/K_l_s),0.4)*F; retp=G_water*(1-C_UDMI(c,ct,3))*di_water/mu_l_s*pow(F,1.25)/10000; if(retp<32.5) S=1/(1+0.12*pow(retp,1.14)); if(retp>=32.5&&retp<70) S=1/(1+0.42*pow(retp,0.78)); if(retp>=70) S=0.1; if(Tall<646.) { pw = 299581676.5-1112854.9*Tall + 1056.9284*pow(Tall,2); pw = pw>=Psat? pw:Psat; } else pw = 22115000.; Tgr = Tall-Tsat; if(Tgr<=0) Tgr=0.; htcnb=0.00122*S*pow(Tgr,0.24)*pow((pw-Psat),0.75)*pow(Cp_l_s,0.45)*pow(rou_ls,0.49)*pow(K_l_s,0.79)/(pow(sgm,0.5)*pow(hfv,0.24)*pow(mu_l_s,0.29)*pow(rou_vs,0.24)); C_UDMI(c,ct,12) = pow(pow(htcfc,n)+pow(htcnb,n),1/n); C_UDMI(c,ct,14) = htcfc+htcnb; xtd =0.; F =0.; htcfc =0.; pw =0.; htcnb =0.; S =0.; retp=0.; } if(C_UDMI(c,ct,0) >= QTsup && C_UDMI(c,ct,0) <= QT65382) //单相汽 { C_UDMI(c,ct,1)=4; C_UDMI(c,ct,3)=1; C_UDMI(c,ct,4)=1; //C_UDMI(c,ct,2)=(-47513.190209+pow((pow(47513.190209,2)-4*(-32.65115792)*(-14182632.67-hlin-C_UDMI(c,ct,0)/m_water)),0.5))/(-32.65115792*2); //C_UDMI(c,ct,2)=(-80531.30434781+pow(80531.30434781*80531.30434781-4*(-58.7944664 )*(-24601481.9069136-(hlin+C_UDMI(c,ct,0)/m_water)),0.5))/(-58.7944664 *2); C_UDMI(c,ct,2)=15.75*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,3)+74.564*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,2)-632.88*(C_UDMI(c,ct,0)/m_water+hlin)/1e6+1496.8; if(C_UDMI(c,ct,2)<=Tsat) C_UDMI(c,ct,2) = Tsat; if(C_UDMI(c,ct,2)>=653.82) C_UDMI(c,ct,2) = 653.82; C_UDMI(c,ct,5)=-0.0000768859547860944*pow(C_UDMI(c,t,2),3)+0.164068505626203*pow(C_UDMI(c,t,2),2)-116.820593637976*C_UDMI(c,t,2)+27823.3434320337; C_UDMI(c,ct,6)=-1.15138327125887E-12*pow(C_UDMI(c,t,2),3)+2.47167061066652E-09*pow(C_UDMI(c,t,2),2)-1.72523309775328E-06*C_UDMI(c,t,2)+0.000417905039504174; mu_tw=-4.842954771e-6+4.415494732e-8*Tall; C_UDMI(c,ct,7)=1.64756047401987E-09*pow(C_UDMI(c,t,2),4)-4.66295787905828E-06*pow(C_UDMI(c,t,2),3)+0.00494746512861121*pow(C_UDMI(c,t,2),2)-2.33242356172728*C_UDMI(c,t,2)+412.339466304253; C_UDMI(c,ct,8)=0.000827737277387106*pow(C_UDMI(c,t,2),4)-2.31871761943198*pow(C_UDMI(c,t,2),3)+2433.72280465395*pow(C_UDMI(c,t,2),2)-1134380.21513071*C_UDMI(c,t,2)+198127195.165049; C_UDMI(c,ct,9)=G_water/C_UDMI(c,ct,5); C_UDMI(c,ct,10)=C_UDMI(c,ct,5)*C_UDMI(c,ct,9)*di_water/C_UDMI(c,ct,6); C_UDMI(c,ct,11)=C_UDMI(c,ct,6)*C_UDMI(c,ct,8)/C_UDMI(c,ct,7); C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.4)*C_UDMI(c,ct,7)/di_water; //C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.33)*C_UDMI(c,ct,7)*pow(C_UDMI(c,ct,6)/mu_tw,0.14)/di_water; C_UDMI(c,ct,14) = C_UDMI(c,ct,12); } if(C_UDMI(c,ct,0)>QT65382 && C_UDMI(c,ct,0)<= QT79182 ) { C_UDMI(c,ct,1)=4; C_UDMI(c,ct,3)=1; C_UDMI(c,ct,4)=1; C_UDMI(c,ct,2)=-85.051*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,3)+959.84*pow((C_UDMI(c,ct,0)/m_water+hlin)/1e6,2)-3225.4*(C_UDMI(c,ct,0)/m_water+hlin)/1e6+4028.5; if(C_UDMI(c,ct,2)<=653.82) C_UDMI(c,ct,2) = 653.82; if(C_UDMI(c,ct,2)>=791.82) C_UDMI(c,ct,2) = 791.82; //if(C_UDMI(c,ct,2)>=Tall) // C_UDMI(c,ct,2) = f_dec*Tall; C_UDMI(c,ct,5)=-0.0000768859547860944*pow(C_UDMI(c,t,2),3)+0.164068505626203*pow(C_UDMI(c,t,2),2)-116.820593637976*C_UDMI(c,t,2)+27823.3434320337; C_UDMI(c,ct,6)=-1.15138327125887E-12*pow(C_UDMI(c,t,2),3)+2.47167061066652E-09*pow(C_UDMI(c,t,2),2)-1.72523309775328E-06*C_UDMI(c,t,2)+0.000417905039504174; mu_tw=-4.842954771e-6+4.415494732e-8*Tall; C_UDMI(c,ct,7)=1.64756047401987E-09*pow(C_UDMI(c,t,2),4)-4.66295787905828E-06*pow(C_UDMI(c,t,2),3)+0.00494746512861121*pow(C_UDMI(c,t,2),2)-2.33242356172728*C_UDMI(c,t,2)+412.339466304253; C_UDMI(c,ct,8)=0.000827737277387106*pow(C_UDMI(c,t,2),4)-2.31871761943198*pow(C_UDMI(c,t,2),3)+2433.72280465395*pow(C_UDMI(c,t,2),2)-1134380.21513071*C_UDMI(c,t,2)+198127195.165049; C_UDMI(c,ct,9)=G_water/C_UDMI(c,ct,5); C_UDMI(c,ct,10)=C_UDMI(c,ct,5)*C_UDMI(c,ct,9)*di_water/C_UDMI(c,ct,6); C_UDMI(c,ct,11)=C_UDMI(c,ct,6)*C_UDMI(c,ct,8)/C_UDMI(c,ct,7); C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.4)*C_UDMI(c,ct,7)/di_water; //C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.33)*C_UDMI(c,ct,7)*pow(C_UDMI(c,ct,6)/mu_tw,0.14)/di_water; C_UDMI(c,ct,14) = C_UDMI(c,ct,12); } if(C_UDMI(c,ct,0)>QT79182) { C_UDMI(c,ct,1)=4; C_UDMI(c,ct,3)=1; C_UDMI(c,ct,4)=1; C_UDMI(c,ct,2)=791.82; //if(C_UDMI(c,ct,2)>=Tall) // C_UDMI(c,ct,2) = f_dec*Tall; C_UDMI(c,ct,5)=-0.0000768859547860944*pow(C_UDMI(c,t,2),3)+0.164068505626203*pow(C_UDMI(c,t,2),2)-116.820593637976*C_UDMI(c,t,2)+27823.3434320337; C_UDMI(c,ct,6)=-1.15138327125887E-12*pow(C_UDMI(c,t,2),3)+2.47167061066652E-09*pow(C_UDMI(c,t,2),2)-1.72523309775328E-06*C_UDMI(c,t,2)+0.000417905039504174; mu_tw=-4.842954771e-6+4.415494732e-8*Tall; C_UDMI(c,ct,7)=1.64756047401987E-09*pow(C_UDMI(c,t,2),4)-4.66295787905828E-06*pow(C_UDMI(c,t,2),3)+0.00494746512861121*pow(C_UDMI(c,t,2),2)-2.33242356172728*C_UDMI(c,t,2)+412.339466304253; C_UDMI(c,ct,8)=0.000827737277387106*pow(C_UDMI(c,t,2),4)-2.31871761943198*pow(C_UDMI(c,t,2),3)+2433.72280465395*pow(C_UDMI(c,t,2),2)-1134380.21513071*C_UDMI(c,t,2)+198127195.165049; C_UDMI(c,ct,9)=G_water/C_UDMI(c,ct,5); C_UDMI(c,ct,10)=C_UDMI(c,ct,5)*C_UDMI(c,ct,9)*di_water/C_UDMI(c,ct,6); C_UDMI(c,ct,11)=C_UDMI(c,ct,6)*C_UDMI(c,ct,8)/C_UDMI(c,ct,7); C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.4)*C_UDMI(c,ct,7)/di_water; //C_UDMI(c,ct,12)=0.023*pow(C_UDMI(c,ct,10),0.8)*pow(C_UDMI(c,ct,11),0.33)*C_UDMI(c,ct,7)*pow(C_UDMI(c,ct,6)/mu_tw,0.14)/di_water; C_UDMI(c,ct,14) = C_UDMI(c,ct,12); } } free(selected_faces); // 释放内存 selected_faces = NULL; // 防止悬垂指针

    }
    #endif

    }

    DEFINE_PROFILE(t_water,t,i)
    {
    face_t f;
    cell_t c;
    Thread *ct;

    begin_f_loop(f,t) { ct = F_C0_THREAD(f,t); c = F_C0(f,t); F_PROFILE(f,t,i) = C_UDMI(c,ct,2); } end_f_loop(f,t)

    }

    DEFINE_PROFILE(hct_water,t,i)
    {
    face_t f;
    cell_t c;
    Thread *ct;

    begin_f_loop(f,t) { ct = F_C0_THREAD(f,t); c = F_C0(f,t); F_PROFILE(f,t,i) = C_UDMI(c,ct,12); } end_f_loop(f,t)

    }

  • 相平均概念求助

    Algorithm
    3
    0 赞同
    3 帖子
    4k 浏览
    P

    @jinlinna 感谢!

  • (principle) Reynolds (shear) stress (tensor)

    Algorithm
    4
    0 赞同
    4 帖子
    6k 浏览
    李东岳

    $\tau$这个雷诺应力,对角线的是normal stress,非对角线的是shear stress。不过你说的更详细,感谢分享!

  • 求一篇openfoam的文章

    OpenFOAM
    1
    0 赞同
    1 帖子
    2k 浏览
    Y

    H. Weller, A New Approach to VOF-based Interface Capturing Methods for Incompressible and Compressible Flow, OpenCFD Ltd., Report TR/HGW/04, (2008).

  • 关于OpenFOAM矩阵求解器

    Algorithm
    9
    0 赞同
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    19k 浏览

    @micro 网格数量越多,网格尺度越小,计算肯定更加不稳定,您可以查一下CFL数

  • 聚并破碎的SQMOM方法

    Algorithm
    1
    0 赞同
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    2k 浏览
    李东岳

    对于给定的NDF,划分为$i$个$N_{pp}$,对每个$i$上定义$k$阶矩$m_k^i$,给定$m_k^i$,可以计算第$i$区间的节点$d^i_0,d^i_1$以及权重$w^i_0,w^i_1$:
    \begin{equation}
    \begin{split}
    w^i_0&=w^i_1=0.5
    \\
    d^i_0&=m_1^i-\frac{1}{\sqrt{3}}\sqrt{\frac{m_3^i}{m_1^i}-{m_1^i}^2}
    \\
    d^i_1&=m_1^i+\frac{1}{\sqrt{3}}\sqrt{\frac{m_3^i}{m_1^i}-{m_1^i}^2}
    \end{split}
    \end{equation}
    对于仅考虑破碎的PBE:
    \begin{equation}\label{pbe}
    \frac{\p n(d)}{\p t}=\int_d^{d_{max}}g(d')\beta(d|d')n(d')\rd d'-g(d)n(d)
    \end{equation}
    对方程\eqref{pbe}在$i$上取$k$阶矩:
    \begin{equation}\label{m}
    \frac{\p m_k^i}{\p t}=\int_{d_{i-1/2}}^{d_{i+1/2}}\int_d^{d_{max}}g(d')d^k\beta(d|d')n(d')\rd d'\rd d-\sum^2_{j=0} g(d_j^i)w_j^i(d_j^i)^k
    \end{equation}
    \begin{equation}
    \begin{split}
    \int_{d_{i-1/2}}^{d_{i+1/2}}\int_d^{d_{max}}g(d')\beta(d|d')n(d')\rd d'\rd d&=
    \int_{d_{i-1/2}}^{d_{max}}g(d')n(d')\left(\int_{d_{i-1/2}}^{d'}\beta(d|d')\rd d\right)\rd d'
    \\&=
    \sum_{m=i}^{N}\sum_{j=0}^2g(d_j^m)w_j^m\left(\int_{d_{i-1/2}}^{d_j^m}d^k\beta(d|d_j^m)\rd d\right)
    \end{split}
    \end{equation}
    Therefore
    \begin{equation}
    \frac{\p m_k^i}{\p t}=\sum_{m=i}^{N}\sum_{j=0}^2g(d_j^m)w_j^m\left(\int_{d_{i-1/2}}^{d_j^m}d^k\beta(d|d_j^m)\rd d\right)-\sum^2_{j=0} g(d_j^i)w_j^i(d_j^i)^k
    \end{equation}

  • 0 赞同
    9 帖子
    15k 浏览
    李东岳

    充值100送100

  • isoAdvection模拟水中上升的气泡边界不稳

    OpenFOAM
    16
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    linhan.geL

    @东岳 嗯嗯,这也是个办法。两种方法速度都比较难调节。

  • 关于fluent多台机器运算的问题

    Fluent
    1
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    1 帖子
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    A

    最近在研究用intelmpi进行两台一样配置的电脑算一个算例的问题,现在两台电脑都在一个局域网内且mpi也都安装上了,按照手册配置机器名称和核心数启动之后,一直卡在生成node上,系统是windows,fluent是2025r1,请问有无成功运行的朋友能教教具体如何设置?