用fluet做旋流分离的时候，计算出错，大家帮分析一下呀

Justin08

[这个贴子最后由Justin08在 2007/04/13 08:12pm 第 1 次编辑]

自己真的没折了，大虾们指点一条出路，谢了
错误信息如下：（附件中也有）
iter continuity u-water_ph u-oil_phas v-water_ph v-oil_phas w-water_ph w-oil_phas          k    epsilon vf-oil_pha     time/iter
  2762 6.5885e-04 4.0239e-06 3.2855e-05 3.5355e-06 7.1863e-05 6.7930e-07 3.3695e-05 1.0063e-05 1.9737e-05 1.8460e-03 3780:07:57 997238
  2763 6.5922e-04 3.9713e-06 4.0756e-05 3.5790e-06 7.5052e-05 6.8614e-07 3.1885e-05 1.0239e-05 1.7869e-05 1.8336e-03 3799:43:54 997237
  2764 6.4058e-04 3.7438e-06 4.4454e-05 3.5229e-06 6.3140e-05 6.7591e-07 3.2307e-05 1.0083e-05 1.6844e-05 1.8335e-03 3760:00:30 997236
  2765 6.7545e-04 3.6998e-06 4.2628e-05 3.5032e-06 5.5817e-05 6.7755e-07 3.8609e-05 9.9437e-06 1.5547e-05 1.8477e-03 3783:37:51 997235
  2766 6.4165e-04 3.6783e-06 4.4404e-05 3.5101e-06 6.8315e-05 6.6620e-07 4.6080e-05 9.8350e-06 1.4928e-05 1.8489e-03 3747:07:34 997234
  2767 6.2988e-04 3.6307e-06 3.5217e-05 3.4901e-06 6.0222e-05 6.6105e-07 3.7290e-05 9.7524e-06 1.4580e-05 1.8351e-03 3773:19:25 997233
  2768 5.9528e-04 3.6068e-06 3.0770e-05 3.4741e-06 5.7704e-05 6.4698e-07 3.1074e-05 9.6996e-06 1.4549e-05 1.8173e-03 3794:16:51 997232
  2769 5.9953e-04 3.5999e-06 3.0633e-05 3.4786e-06 7.0974e-05 6.4463e-07 3.4170e-05 9.6585e-06 1.4416e-05 1.8251e-03 3755:38:38 997231
  2770 6.1391e-04 3.5904e-06 2.8689e-05 3.4539e-06 6.3889e-05 6.4545e-07 3.2198e-05 9.6243e-06 1.4284e-05 1.8156e-03 3780:08:08 997230
  2771 6.1806e-04 3.5797e-06 3.0343e-05 3.4485e-06 5.8200e-05 6.4074e-07 3.2648e-05 9.5916e-06 1.4183e-05 1.8131e-03 3799:43:40 997229
  2772 6.0912e-04 3.5752e-06 2.9791e-05 3.4316e-06 5.3284e-05 6.3489e-07 2.9906e-05 9.5603e-06 1.4107e-05 1.8008e-03 3759:59:58 997228
  iter continuity u-water_ph u-oil_phas v-water_ph v-oil_phas w-water_ph w-oil_phas          k    epsilon vf-oil_pha     time/iter
  2773 5.7010e-04 3.5440e-06 2.5607e-05 3.4061e-06 4.5220e-05 6.3004e-07 2.6734e-05 9.5290e-06 1.4022e-05 1.7858e-03 3783:37:03 997227
  2774 5.6470e-04 3.5347e-06 2.5242e-05 3.4073e-06 4.6624e-05 6.2665e-07 2.7774e-05 9.5005e-06 1.3949e-05 1.7776e-03 3802:30:41 997226
  2775 5.5550e-04 3.5231e-06 2.5161e-05 3.3986e-06 4.6647e-05 6.1987e-07 2.4838e-05 9.4715e-06 1.3874e-05 1.7682e-03 3762:13:26 997225
  2776 5.6434e-04 3.5458e-06 4.8788e-05 3.4080e-06 6.7366e-05 6.2262e-07 3.0919e-05 9.4540e-06 1.3850e-05 1.7797e-03 3785:23:41 997224
  2777 5.6742e-04 3.5257e-06 4.0486e-05 3.4075e-06 6.2983e-05 6.3484e-07 2.7041e-05 9.4272e-06 1.3781e-05 1.7731e-03 3803:55:51 997223
  2778 5.3327e-04 3.4948e-06 3.2400e-05 3.3827e-06 5.4452e-05 6.2114e-07 2.3218e-05 9.3979e-06 1.3712e-05 1.7631e-03 3763:21:27 997222
  2779 5.9021e-04 3.5185e-06 4.7230e-05 3.4013e-06 7.2545e-05 6.2721e-07 4.2915e-05 9.3976e-06 1.3763e-05 1.8037e-03 3786:17:57 997221
  2780 5.7738e-04 3.5193e-06 4.6045e-05 3.3972e-06 7.5243e-05 6.2256e-07 4.0004e-05 9.3735e-06 1.3681e-05 1.7922e-03 3804:39:07 997220
  2781 5.5604e-04 3.4842e-06 3.4551e-05 3.4063e-06 8.2947e-05 6.0775e-07 3.1834e-05 9.3553e-06 1.3657e-05 1.7797e-03 3763:55:56 997219
  2782 5.6891e-04 3.4748e-06 2.8838e-05 3.3733e-06 6.6194e-05 6.0666e-07 2.9858e-05 9.3360e-06 1.3627e-05 1.7663e-03 3786:45:24 997218
  2783 5.5933e-04 3.4708e-06 2.3619e-05 3.3784e-06 5.1701e-05 6.0953e-07 2.6243e-05 9.3112e-06 1.3574e-05 1.7516e-03 3805:00:56 997217
  iter continuity u-water_ph u-oil_phas v-water_ph v-oil_phas w-water_ph w-oil_phas          k    epsilon vf-oil_pha     time/iter
  2784 5.5072e-04 3.8088e-06 2.1695e-05 3.3669e-06 4.4083e-05 6.0898e-07 2.2370e-05 9.6928e-06 1.8995e-05 1.7404e-03 3764:13:15 997216
  2785 5.4777e-04 3.7340e-06 2.1425e-05 3.3692e-06 4.2722e-05 6.0664e-07 2.2298e-05 9.8729e-06 1.7133e-05 1.7375e-03 3786:59:08 997215
  2786 5.5536e-04 3.5368e-06 2.2941e-05 3.3476e-06 4.3083e-05 6.0893e-07 2.2709e-05 9.7146e-06 1.6129e-05 1.7329e-03 3805:11:46 997214
  2787 5.3208e-04 3.5013e-06 3.3353e-05 3.3377e-06 5.1465e-05 6.0046e-07 2.4019e-05 9.5640e-06 1.4760e-05 1.7285e-03 3764:21:48 997213
  2788 5.4534e-04 3.4717e-06 3.0669e-05 3.3319e-06 4.9292e-05 5.9608e-07 2.3138e-05 9.4687e-06 1.4183e-05 1.7362e-03 3787:05:49 997212
  2789 5.4335e-04 3.4578e-06 2.8931e-05 3.3461e-06 5.6929e-05 5.9355e-07 2.8496e-05 9.3937e-06 1.3836e-05 1.7346e-03 3805:16:59 997211
  2790 6.1525e-04 3.4623e-06 3.4000e-05 3.3744e-06 8.0532e-05 6.0703e-07 3.9711e-05 9.3633e-06 1.3904e-05 1.7892e-03 3764:25:50 997210
  2791 6.3308e-04 3.8474e-06 3.9207e-05 3.3992e-06 9.6898e-05 6.1997e-07 4.9290e-05 9.7449e-06 1.8724e-05 1.7910e-03 3787:08:55 997209
  2792 7.6192e-04 3.7643e-06 3.1496e-05 3.3691e-06 7.8983e-05 6.0441e-07 4.0645e-05 9.8181e-06 1.6783e-05 1.8922e-03 3805:19:19 997208
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 30 cells
  2793 2.8016e+00 3.6069e-06 5.8080e-05 3.4197e-06 3.8731e-05 6.4540e-07 3.1312e-05 1.2126e+00 2.2055e+04 2.3666e-01 4484:39:53 997207
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 1257 cells
  2794 1.9176e+01 8.9295e+01 6.6481e-01 3.7569e+00 1.6606e-01 1.2926e+01 5.9672e-01 4.7387e+01 1.9448e+02 1.2426e-01 4363:19:58 997206
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 7752 cells
  iter continuity u-water_ph u-oil_phas v-water_ph v-oil_phas w-water_ph w-oil_phas          k    epsilon vf-oil_pha     time/iter
  2795 7.0581e+03 1.4244e+00 5.9368e-01 1.2407e-03 3.0667e-03 3.7830e-03 1.0976e-02 7.3626e+02 2.2223e+06 2.8434e-02 4321:40:01 997205
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 66296 cells
  2796 6.8618e+04 2.2082e-01 1.0292e-01 9.3029e-02 3.5072e-03 6.4311e-02 1.3482e-02 1.4895e+00 4.2158e+01 6.2544e-03 4343:44:01 997204
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 129257 cells
  2797 1.0478e+05 2.9167e+00 4.8853e-01 2.6572e-01 1.0902e-01 5.8425e-01 5.1694e-01 5.5637e-01 1.5280e+00 2.3174e-02 4416:47:10 997203
reversed flow in 836 faces on outflow 8.
reversed flow in 900 faces on outflow 8.
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 160221 cells
  2798 2.3379e+05 3.2294e-01 4.5507e-01 3.7764e-01 3.3509e-01 1.1980e-01 1.8961e-01 2.2967e-01 3.4536e-01 6.6223e-02 4419:49:38 997202
reversed flow in 1130 faces on outflow 8.
reversed flow in 2 faces on outflow 9.
reversed flow in 1154 faces on outflow 8.
reversed flow in 1 faces on outflow 9.
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 133580 cells
  2799 3.2248e+05 2.7840e-01 3.7183e-01 2.4157e-01 5.5119e-01 7.6130e-02 1.3649e-01 2.2735e-01 3.9948e-01 1.1163e-01 4366:51:33 997201
reversed flow in 1168 faces on outflow 8.
reversed flow in 3 faces on outflow 9.
reversed flow in 1192 faces on outflow 8.
reversed flow in 2 faces on outflow 9.
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 110478 cells
  2800 3.4329e+05 2.6828e-01 3.3465e-01 2.0371e-01 3.8124e-01 5.6177e-02 1.3132e-01 1.7320e-01 3.8647e-01 3.8685e-01 4324:29:01 997200
reversed flow in 1019 faces on outflow 8.
reversed flow in 3 faces on outflow 9.
reversed flow in 1074 faces on outflow 8.
reversed flow in 3 faces on outflow 9.
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 329111 cells
Error: Floating point error: invalid number
Error Object: ()

hongfw2

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