| blob | 3b069bcbbdc7cd81302dcfba865dde4bd40ffe84 |
1 /*---------------------------------------------------------------------------*\
2 | ========= | |
3 | \\ / F ield | OpenFOAM Extend Project: Open source CFD |
4 | \\ / O peration | Version: 1.6-ext |
5 | \\ / A nd | Web: www.extend-project.de |
6 | \\/ M anipulation | |
7 \*---------------------------------------------------------------------------*/
8 Build : 1.6-ext-b004b7565a8e
9 Exec : navalFoam
10 Date : Nov 12 2010
11 Time : 14:52:59
12 Host : bingo
13 PID : 5773
14 Case : /home/hjasak/OpenFOAM/hjasak-1.6-ext/work/NavalHydro/run/navalFoam/twoDBoat6DOFGGI
15 nProcs : 1
16 SigFpe : Enabling floating point exception trapping (FOAM_SIGFPE).
18 // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
19 Create time
21 Create dynamic mesh for time = 0
23 Selecting dynamicFvMesh floatingBodyFvMesh
24 Selecting motion solver: laplaceFaceDecomposition
25 Selecting motion diffusivity: uniform
27 Reading g
28 Reading field pd
30 Reading field alpha1
32 Reading field U
34 Reading/calculating face flux field phi
36 Initializing the GGI interpolator between master/shadow patches: bargeSlider/boxSlider
37 Reading transportProperties
39 Selecting incompressible transport model Newtonian
40 Selecting incompressible transport model Newtonian
41 Calculating field g.h
43 Selecting turbulence model type RASModel
44 Selecting RAS turbulence model laminar
45 Reading field rAU if present
47 time step continuity errors : sum local = 4.32618e-06, global = 9.16105e-23, cumulative = 9.16105e-23
48 CG: Solving for pcorr, Initial residual = 1, Final residual = 9.57667e-08, No Iterations 55
49 time step continuity errors : sum local = 4.14304e-13, global = 7.51768e-14, cumulative = 7.51768e-14
51 Starting time loop
53 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
54 Courant Number mean: 0.00130603 max: 0.0491134 velocity magnitude: 0.433502
55 deltaT = 0.000238095
56 Time = 0.000238095
58 BiCGStab: Solving for Ux, Initial residual = 1, Final residual = 3.41388e-09, No Iterations 2
59 BiCGStab: Solving for Uy, Initial residual = 1, Final residual = 3.90448e-11, No Iterations 3
60 CG: Solving for pd, Initial residual = 1, Final residual = 9.50751e-08, No Iterations 14
61 CG: Solving for pd, Initial residual = 0.199947, Final residual = 4.15959e-08, No Iterations 13
62 CG: Solving for pd, Initial residual = 0.202624, Final residual = 4.50745e-08, No Iterations 13
63 CG: Solving for pd, Initial residual = 0.103672, Final residual = 8.38906e-08, No Iterations 12
64 CG: Solving for pd, Initial residual = 0.0463827, Final residual = 3.9967e-08, No Iterations 12
65 CG: Solving for pd, Initial residual = 0.0262392, Final residual = 8.70152e-08, No Iterations 11
66 mag(U): max: 1.0081 avg: 0.199844
67 time step continuity errors : sum local = 1.54777e-11, global = -3.6004e-13, cumulative = -2.84863e-13
68 BiCGStab: Solving for alpha1, Initial residual = 1.9863e-06, Final residual = 5.80189e-12, No Iterations 1
69 Liquid phase volume fraction = 0.500445 Min(alpha1) = -0.00010067 Max(alpha1) = 1.00001
70 BiCGStab: Solving for Ux, Initial residual = 0.00312994, Final residual = 3.26313e-09, No Iterations 1
71 BiCGStab: Solving for Uy, Initial residual = 0.0211826, Final residual = 7.08846e-13, No Iterations 2
72 CG: Solving for pd, Initial residual = 0.0194159, Final residual = 8.74843e-08, No Iterations 11
73 CG: Solving for pd, Initial residual = 0.0106653, Final residual = 3.438e-08, No Iterations 10
74 CG: Solving for pd, Initial residual = 0.00600484, Final residual = 6.63721e-08, No Iterations 9
75 CG: Solving for pd, Initial residual = 0.00362709, Final residual = 3.61056e-08, No Iterations 9
76 CG: Solving for pd, Initial residual = 0.0027542, Final residual = 2.95387e-08, No Iterations 9
77 CG: Solving for pd, Initial residual = 0.00221583, Final residual = 8.71277e-08, No Iterations 8
78 mag(U): max: 0.949896 avg: 0.199334
79 time step continuity errors : sum local = 2.87196e-11, global = -6.43782e-13, cumulative = -9.28646e-13
80 Calculating static pressure
81 CG: Solving for p, Initial residual = 1, Final residual = 7.93311e-08, No Iterations 20
82 Relaxation: p = 0.1
83 BiCGStab: Solving for alpha1, Initial residual = 7.19215e-07, Final residual = 4.98806e-13, No Iterations 1
84 Liquid phase volume fraction = 0.500445 Min(alpha1) = -9.28937e-05 Max(alpha1) = 1
85 ExecutionTime = 0.4 s ClockTime = 0 s
87 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
88 Courant Number mean: 0.00158194 max: 0.0817758 velocity magnitude: 0.6431
89 deltaT = 0.000282313
90 Time = 0.000520408
92 BiCGStab: Solving for Ux, Initial residual = 0.0143145, Final residual = 4.26697e-13, No Iterations 2
93 BiCGStab: Solving for Uy, Initial residual = 0.0817995, Final residual = 9.04541e-11, No Iterations 2
94 CG: Solving for pd, Initial residual = 0.0360159, Final residual = 4.66864e-08, No Iterations 12
95 CG: Solving for pd, Initial residual = 0.0222373, Final residual = 8.31941e-08, No Iterations 11
96 CG: Solving for pd, Initial residual = 0.017449, Final residual = 5.40324e-08, No Iterations 11
97 CG: Solving for pd, Initial residual = 0.0148454, Final residual = 4.11494e-08, No Iterations 11
98 CG: Solving for pd, Initial residual = 0.0130657, Final residual = 3.30833e-08, No Iterations 11
99 CG: Solving for pd, Initial residual = 0.0115953, Final residual = 9.14e-08, No Iterations 10
100 mag(U): max: 1.35993 avg: 0.199946
101 time step continuity errors : sum local = 2.7394e-11, global = 7.95572e-13, cumulative = -1.33073e-13
102 BiCGStab: Solving for alpha1, Initial residual = 2.28818e-06, Final residual = 8.06616e-12, No Iterations 1
103 Liquid phase volume fraction = 0.500445 Min(alpha1) = -0.000192322 Max(alpha1) = 1
104 BiCGStab: Solving for Ux, Initial residual = 0.00311801, Final residual = 5.85294e-09, No Iterations 1
105 BiCGStab: Solving for Uy, Initial residual = 0.0153169, Final residual = 8.96318e-12, No Iterations 2
106 CG: Solving for pd, Initial residual = 0.0152055, Final residual = 2.97326e-08, No Iterations 12
107 CG: Solving for pd, Initial residual = 0.0163913, Final residual = 9.87205e-08, No Iterations 10
108 CG: Solving for pd, Initial residual = 0.00978235, Final residual = 8.19863e-08, No Iterations 10
109 CG: Solving for pd, Initial residual = 0.00648619, Final residual = 3.41099e-08, No Iterations 10
110 CG: Solving for pd, Initial residual = 0.00465658, Final residual = 8.79984e-08, No Iterations 9
111 CG: Solving for pd, Initial residual = 0.00345713, Final residual = 8.56548e-08, No Iterations 8
112 mag(U): max: 1.16595 avg: 0.199419
113 time step continuity errors : sum local = 1.19846e-11, global = -8.56394e-14, cumulative = -2.18713e-13
114 Calculating static pressure
115 CG: Solving for p, Initial residual = 0.00955883, Final residual = 4.91644e-08, No Iterations 12
116 Relaxation: p = 0.1
117 BiCGStab: Solving for alpha1, Initial residual = 6.26014e-07, Final residual = 9.30429e-13, No Iterations 1
118 Liquid phase volume fraction = 0.500445 Min(alpha1) = -0.000185441 Max(alpha1) = 1
119 ExecutionTime = 0.65 s ClockTime = 0 s
121 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
122 Courant Number mean: 0.00187213 max: 0.103162 velocity magnitude: 0.700158
123 deltaT = 0.000335855
124 Time = 0.000856263
126 BiCGStab: Solving for Ux, Initial residual = 0.00317945, Final residual = 9.85184e-09, No Iterations 1
127 BiCGStab: Solving for Uy, Initial residual = 0.0190151, Final residual = 4.31025e-12, No Iterations 2
128 CG: Solving for pd, Initial residual = 0.0255358, Final residual = 7.63387e-08, No Iterations 11
129 CG: Solving for pd, Initial residual = 0.0190481, Final residual = 5.00117e-08, No Iterations 11
130 CG: Solving for pd, Initial residual = 0.0147305, Final residual = 9.99704e-08, No Iterations 10
131 CG: Solving for pd, Initial residual = 0.0115411, Final residual = 7.04647e-08, No Iterations 10
132 CG: Solving for pd, Initial residual = 0.00901492, Final residual = 5.27538e-08, No Iterations 10
133 CG: Solving for pd, Initial residual = 0.00720057, Final residual = 4.33237e-08, No Iterations 10
134 mag(U): max: 1.38312 avg: 0.199988
135 time step continuity errors : sum local = 5.53888e-12, global = -2.89418e-13, cumulative = -5.0813e-13
136 BiCGStab: Solving for alpha1, Initial residual = 2.69919e-06, Final residual = 1.05251e-11, No Iterations 1
137 Liquid phase volume fraction = 0.500444 Min(alpha1) = -0.000277425 Max(alpha1) = 1
138 BiCGStab: Solving for Ux, Initial residual = 0.00179529, Final residual = 7.47254e-09, No Iterations 1
139 BiCGStab: Solving for Uy, Initial residual = 0.00933128, Final residual = 6.33625e-12, No Iterations 2
140 CG: Solving for pd, Initial residual = 0.0224683, Final residual = 5.73261e-08, No Iterations 12
141 CG: Solving for pd, Initial residual = 0.0221933, Final residual = 6.70758e-08, No Iterations 10
142 CG: Solving for pd, Initial residual = 0.0095928, Final residual = 6.79826e-08, No Iterations 10
143 CG: Solving for pd, Initial residual = 0.00616061, Final residual = 5.43396e-08, No Iterations 9
144 CG: Solving for pd, Initial residual = 0.0043071, Final residual = 4.35462e-08, No Iterations 9
145 CG: Solving for pd, Initial residual = 0.00338904, Final residual = 7.06307e-08, No Iterations 8
146 mag(U): max: 1.29471 avg: 0.199427
147 time step continuity errors : sum local = 7.65171e-12, global = -6.95918e-13, cumulative = -1.20405e-12
148 Calculating static pressure
149 CG: Solving for p, Initial residual = 0.00371481, Final residual = 4.76037e-08, No Iterations 11
150 Relaxation: p = 0.1
151 BiCGStab: Solving for alpha1, Initial residual = 6.05547e-07, Final residual = 1.85904e-12, No Iterations 1
152 Liquid phase volume fraction = 0.500444 Min(alpha1) = -0.000269291 Max(alpha1) = 1
153 ExecutionTime = 0.9 s ClockTime = 1 s
155 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
156 Courant Number mean: 0.00222513 max: 0.128311 velocity magnitude: 0.732154
157 deltaT = 0.000398828
158 Time = 0.00125509
160 BiCGStab: Solving for Ux, Initial residual = 0.00251255, Final residual = 3.61376e-12, No Iterations 2
161 BiCGStab: Solving for Uy, Initial residual = 0.0124545, Final residual = 6.33304e-11, No Iterations 2
162 CG: Solving for pd, Initial residual = 0.0258412, Final residual = 7.41685e-08, No Iterations 12
163 CG: Solving for pd, Initial residual = 0.0192446, Final residual = 5.0147e-08, No Iterations 12
164 CG: Solving for pd, Initial residual = 0.0150246, Final residual = 9.05407e-08, No Iterations 11
165 CG: Solving for pd, Initial residual = 0.0114497, Final residual = 6.67196e-08, No Iterations 11
166 CG: Solving for pd, Initial residual = 0.00859586, Final residual = 9.87818e-08, No Iterations 10
167 CG: Solving for pd, Initial residual = 0.00677413, Final residual = 7.64443e-08, No Iterations 10
168 mag(U): max: 1.46767 avg: 0.200007
169 time step continuity errors : sum local = 1.01464e-11, global = 4.42869e-14, cumulative = -1.15976e-12
170 BiCGStab: Solving for alpha1, Initial residual = 3.21245e-06, Final residual = 1.53101e-11, No Iterations 1
171 Liquid phase volume fraction = 0.500444 Min(alpha1) = -0.000346184 Max(alpha1) = 1
172 BiCGStab: Solving for Ux, Initial residual = 0.00164854, Final residual = 8.15543e-09, No Iterations 1
173 BiCGStab: Solving for Uy, Initial residual = 0.00791453, Final residual = 7.36618e-12, No Iterations 2
174 CG: Solving for pd, Initial residual = 0.0246512, Final residual = 7.08875e-08, No Iterations 12
175 CG: Solving for pd, Initial residual = 0.0224592, Final residual = 9.33026e-08, No Iterations 10
176 CG: Solving for pd, Initial residual = 0.00885825, Final residual = 6.91504e-08, No Iterations 10
177 CG: Solving for pd, Initial residual = 0.00581435, Final residual = 6.39022e-08, No Iterations 9
178 CG: Solving for pd, Initial residual = 0.00375974, Final residual = 5.55543e-08, No Iterations 9
179 CG: Solving for pd, Initial residual = 0.00317208, Final residual = 8.73189e-08, No Iterations 8
180 mag(U): max: 1.39566 avg: 0.199425
181 time step continuity errors : sum local = 1.07204e-11, global = -5.85224e-13, cumulative = -1.74499e-12
182 Calculating static pressure
183 CG: Solving for p, Initial residual = 0.00216091, Final residual = 9.98399e-08, No Iterations 10
184 Relaxation: p = 0.1
185 BiCGStab: Solving for alpha1, Initial residual = 6.4518e-07, Final residual = 3.65144e-12, No Iterations 1
186 Liquid phase volume fraction = 0.500444 Min(alpha1) = -0.000336329 Max(alpha1) = 1
187 ExecutionTime = 1.14 s ClockTime = 1 s
189 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
190 Courant Number mean: 0.00264187 max: 0.157377 velocity magnitude: 0.760637
191 deltaT = 0.000468623
192 Time = 0.00172371
194 BiCGStab: Solving for Ux, Initial residual = 0.00213498, Final residual = 3.16005e-12, No Iterations 2
195 BiCGStab: Solving for Uy, Initial residual = 0.00907827, Final residual = 6.22492e-10, No Iterations 2
196 CG: Solving for pd, Initial residual = 0.024909, Final residual = 8.91906e-08, No Iterations 12
197 CG: Solving for pd, Initial residual = 0.0192812, Final residual = 6.29507e-08, No Iterations 12
198 CG: Solving for pd, Initial residual = 0.0150742, Final residual = 9.23541e-08, No Iterations 11
199 CG: Solving for pd, Initial residual = 0.0112606, Final residual = 7.05951e-08, No Iterations 11
200 CG: Solving for pd, Initial residual = 0.00871448, Final residual = 5.22337e-08, No Iterations 11
201 CG: Solving for pd, Initial residual = 0.00694614, Final residual = 8.45251e-08, No Iterations 10
202 mag(U): max: 1.54311 avg: 0.200017
203 time step continuity errors : sum local = 1.31199e-11, global = 9.48502e-14, cumulative = -1.65014e-12
204 BiCGStab: Solving for alpha1, Initial residual = 3.7953e-06, Final residual = 2.84942e-11, No Iterations 1
205 Liquid phase volume fraction = 0.500443 Min(alpha1) = -0.00039054 Max(alpha1) = 1
206 BiCGStab: Solving for Ux, Initial residual = 0.0015343, Final residual = 9.59237e-09, No Iterations 1
207 BiCGStab: Solving for Uy, Initial residual = 0.00688938, Final residual = 1.4632e-11, No Iterations 2
208 CG: Solving for pd, Initial residual = 0.0248292, Final residual = 8.29392e-08, No Iterations 12
209 CG: Solving for pd, Initial residual = 0.0213721, Final residual = 9.28485e-08, No Iterations 10
210 CG: Solving for pd, Initial residual = 0.00814328, Final residual = 6.36896e-08, No Iterations 10
211 CG: Solving for pd, Initial residual = 0.00522992, Final residual = 7.30123e-08, No Iterations 9
212 CG: Solving for pd, Initial residual = 0.00353736, Final residual = 6.1711e-08, No Iterations 9
213 CG: Solving for pd, Initial residual = 0.00291169, Final residual = 4.52177e-08, No Iterations 9
214 mag(U): max: 1.48018 avg: 0.199411
215 time step continuity errors : sum local = 6.8506e-12, global = -2.42328e-13, cumulative = -1.89246e-12
216 Calculating static pressure
217 CG: Solving for p, Initial residual = 0.00145441, Final residual = 6.88154e-08, No Iterations 10
218 Relaxation: p = 0.1
219 BiCGStab: Solving for alpha1, Initial residual = 6.96177e-07, Final residual = 6.3491e-12, No Iterations 1
220 Liquid phase volume fraction = 0.500443 Min(alpha1) = -0.000379022 Max(alpha1) = 1
221 ExecutionTime = 1.39 s ClockTime = 1 s
223 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
224 Courant Number mean: 0.00310445 max: 0.189979 velocity magnitude: 0.786281
225 deltaT = 0.000553827
226 Time = 0.00227754
228 BiCGStab: Solving for Ux, Initial residual = 0.00194707, Final residual = 3.87897e-12, No Iterations 2
229 BiCGStab: Solving for Uy, Initial residual = 0.00730465, Final residual = 7.42514e-11, No Iterations 2
230 CG: Solving for pd, Initial residual = 0.0241426, Final residual = 4.59101e-08, No Iterations 13
231 CG: Solving for pd, Initial residual = 0.0189561, Final residual = 7.34866e-08, No Iterations 12
232 CG: Solving for pd, Initial residual = 0.014884, Final residual = 6.33811e-08, No Iterations 12
233 CG: Solving for pd, Initial residual = 0.0111971, Final residual = 9.14794e-08, No Iterations 11
234 CG: Solving for pd, Initial residual = 0.00872854, Final residual = 6.77704e-08, No Iterations 11
235 CG: Solving for pd, Initial residual = 0.00694987, Final residual = 5.2056e-08, No Iterations 11
236 mag(U): max: 1.61225 avg: 0.200002
237 time step continuity errors : sum local = 9.80254e-12, global = 7.02476e-13, cumulative = -1.18999e-12
238 BiCGStab: Solving for alpha1, Initial residual = 4.5442e-06, Final residual = 6.08163e-11, No Iterations 1
239 Liquid phase volume fraction = 0.500442 Min(alpha1) = -0.000405431 Max(alpha1) = 1
240 BiCGStab: Solving for Ux, Initial residual = 0.00144808, Final residual = 3.16924e-12, No Iterations 2
241 BiCGStab: Solving for Uy, Initial residual = 0.0060661, Final residual = 3.69772e-11, No Iterations 2
242 CG: Solving for pd, Initial residual = 0.0245367, Final residual = 5.21626e-08, No Iterations 12
243 CG: Solving for pd, Initial residual = 0.0204536, Final residual = 9.08167e-08, No Iterations 10
244 CG: Solving for pd, Initial residual = 0.00780314, Final residual = 6.28268e-08, No Iterations 10
245 CG: Solving for pd, Initial residual = 0.00500318, Final residual = 7.25837e-08, No Iterations 9
246 CG: Solving for pd, Initial residual = 0.00328882, Final residual = 7.09716e-08, No Iterations 9
247 CG: Solving for pd, Initial residual = 0.00263685, Final residual = 4.98397e-08, No Iterations 9
248 mag(U): max: 1.55732 avg: 0.199379
249 time step continuity errors : sum local = 9.46521e-12, global = -4.37339e-13, cumulative = -1.62733e-12
250 Calculating static pressure
251 CG: Solving for p, Initial residual = 0.00105507, Final residual = 5.09256e-08, No Iterations 10
252 Relaxation: p = 0.1
253 BiCGStab: Solving for alpha1, Initial residual = 7.58843e-07, Final residual = 1.27857e-11, No Iterations 1
254 Liquid phase volume fraction = 0.500442 Min(alpha1) = -0.000392756 Max(alpha1) = 1
255 ExecutionTime = 1.65 s ClockTime = 2 s
257 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
258 Courant Number mean: 0.00366956 max: 0.230769 velocity magnitude: 0.812291
259 deltaT = 0.000632945
260 Time = 0.00291049
262 BiCGStab: Solving for Ux, Initial residual = 0.00172582, Final residual = 4.68345e-12, No Iterations 2
263 BiCGStab: Solving for Uy, Initial residual = 0.00585623, Final residual = 3.93477e-11, No Iterations 2
264 CG: Solving for pd, Initial residual = 0.0242581, Final residual = 5.68673e-08, No Iterations 13
265 CG: Solving for pd, Initial residual = 0.0188254, Final residual = 7.69239e-08, No Iterations 12
266 CG: Solving for pd, Initial residual = 0.0146111, Final residual = 5.00047e-08, No Iterations 12
267 CG: Solving for pd, Initial residual = 0.0109712, Final residual = 8.56556e-08, No Iterations 11
268 CG: Solving for pd, Initial residual = 0.00854563, Final residual = 6.99562e-08, No Iterations 11
269 CG: Solving for pd, Initial residual = 0.00651948, Final residual = 9.2611e-08, No Iterations 10
270 mag(U): max: 1.67694 avg: 0.19999
271 time step continuity errors : sum local = 2.07052e-11, global = 1.23729e-12, cumulative = -3.90037e-13
272 BiCGStab: Solving for alpha1, Initial residual = 5.23766e-06, Final residual = 1.10568e-10, No Iterations 1
273 Liquid phase volume fraction = 0.500441 Min(alpha1) = -0.000389639 Max(alpha1) = 1
274 BiCGStab: Solving for Ux, Initial residual = 0.00136463, Final residual = 5.86818e-12, No Iterations 2
275 BiCGStab: Solving for Uy, Initial residual = 0.00543922, Final residual = 1.18265e-10, No Iterations 2
276 CG: Solving for pd, Initial residual = 0.0243915, Final residual = 7.2431e-08, No Iterations 12
277 CG: Solving for pd, Initial residual = 0.0184574, Final residual = 9.30869e-08, No Iterations 10
278 CG: Solving for pd, Initial residual = 0.0070749, Final residual = 5.05285e-08, No Iterations 10
279 CG: Solving for pd, Initial residual = 0.00433196, Final residual = 6.98237e-08, No Iterations 9
280 CG: Solving for pd, Initial residual = 0.00289642, Final residual = 7.66513e-08, No Iterations 9
281 CG: Solving for pd, Initial residual = 0.00232482, Final residual = 8.98543e-08, No Iterations 8
282 mag(U): max: 1.63017 avg: 0.199349
283 time step continuity errors : sum local = 2.08006e-11, global = 4.04096e-13, cumulative = 1.40588e-14
284 Calculating static pressure
285 CG: Solving for p, Initial residual = 0.000835082, Final residual = 3.84547e-08, No Iterations 10
286 Relaxation: p = 0.1
287 BiCGStab: Solving for alpha1, Initial residual = 8.1133e-07, Final residual = 2.30045e-11, No Iterations 1
288 Liquid phase volume fraction = 0.500441 Min(alpha1) = -0.000377547 Max(alpha1) = 1
289 ExecutionTime = 1.9 s ClockTime = 2 s
291 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
292 Courant Number mean: 0.00419429 max: 0.271662 velocity magnitude: 0.838697
293 deltaT = 0.000712063
294 Time = 0.00362255
296 BiCGStab: Solving for Ux, Initial residual = 0.00157487, Final residual = 5.68599e-12, No Iterations 2
297 BiCGStab: Solving for Uy, Initial residual = 0.00493667, Final residual = 3.43321e-11, No Iterations 2
298 CG: Solving for pd, Initial residual = 0.0237354, Final residual = 8.52362e-08, No Iterations 12
299 CG: Solving for pd, Initial residual = 0.0183063, Final residual = 6.04884e-08, No Iterations 12
300 CG: Solving for pd, Initial residual = 0.0138892, Final residual = 9.3303e-08, No Iterations 11
301 CG: Solving for pd, Initial residual = 0.0106199, Final residual = 6.94367e-08, No Iterations 11
302 CG: Solving for pd, Initial residual = 0.00801071, Final residual = 9.85731e-08, No Iterations 10
303 CG: Solving for pd, Initial residual = 0.00615938, Final residual = 7.57126e-08, No Iterations 10
304 mag(U): max: 1.74035 avg: 0.199974
305 time step continuity errors : sum local = 1.9919e-11, global = 1.85808e-12, cumulative = 1.87214e-12
306 BiCGStab: Solving for alpha1, Initial residual = 5.95695e-06, Final residual = 1.88421e-10, No Iterations 1
307 Liquid phase volume fraction = 0.50044 Min(alpha1) = -0.000385655 Max(alpha1) = 1
308 BiCGStab: Solving for Ux, Initial residual = 0.00129589, Final residual = 1.13939e-10, No Iterations 2
309 BiCGStab: Solving for Uy, Initial residual = 0.00494241, Final residual = 3.84679e-10, No Iterations 2
310 CG: Solving for pd, Initial residual = 0.0245936, Final residual = 8.47067e-08, No Iterations 12
311 CG: Solving for pd, Initial residual = 0.0174345, Final residual = 5.28933e-08, No Iterations 11
312 CG: Solving for pd, Initial residual = 0.00663945, Final residual = 5.98744e-08, No Iterations 10
313 CG: Solving for pd, Initial residual = 0.00388563, Final residual = 7.43593e-08, No Iterations 9
314 CG: Solving for pd, Initial residual = 0.0027775, Final residual = 7.8737e-08, No Iterations 9
315 CG: Solving for pd, Initial residual = 0.00213791, Final residual = 6.8173e-08, No Iterations 9
316 mag(U): max: 1.70152 avg: 0.199305
317 time step continuity errors : sum local = 1.87392e-11, global = 1.30321e-12, cumulative = 3.17534e-12
318 Calculating static pressure
319 CG: Solving for p, Initial residual = 0.000702631, Final residual = 3.09371e-08, No Iterations 10
320 Relaxation: p = 0.1
321 BiCGStab: Solving for alpha1, Initial residual = 8.79543e-07, Final residual = 4.25832e-11, No Iterations 1
322 Liquid phase volume fraction = 0.50044 Min(alpha1) = -0.00039793 Max(alpha1) = 1
323 ExecutionTime = 2.16 s ClockTime = 2 s
325 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
326 Courant Number mean: 0.004719 max: 0.315773 velocity magnitude: 0.866414
327 deltaT = 0.000779879
328 Time = 0.00440243
330 BiCGStab: Solving for Ux, Initial residual = 0.00144509, Final residual = 7.25371e-12, No Iterations 2
331 BiCGStab: Solving for Uy, Initial residual = 0.00425152, Final residual = 4.15375e-11, No Iterations 2
332 CG: Solving for pd, Initial residual = 0.0239293, Final residual = 6.71319e-08, No Iterations 12
333 CG: Solving for pd, Initial residual = 0.0183036, Final residual = 5.15628e-08, No Iterations 12
334 CG: Solving for pd, Initial residual = 0.0137676, Final residual = 7.85115e-08, No Iterations 11
335 CG: Solving for pd, Initial residual = 0.0104214, Final residual = 5.77272e-08, No Iterations 11
336 CG: Solving for pd, Initial residual = 0.0078954, Final residual = 9.50674e-08, No Iterations 10
337 CG: Solving for pd, Initial residual = 0.00608337, Final residual = 7.48989e-08, No Iterations 10
338 mag(U): max: 1.80884 avg: 0.199961
339 time step continuity errors : sum local = 2.23708e-11, global = 1.2128e-12, cumulative = 4.38815e-12
340 BiCGStab: Solving for alpha1, Initial residual = 6.58795e-06, Final residual = 2.90875e-10, No Iterations 1
341 Liquid phase volume fraction = 0.500439 Min(alpha1) = -0.000437449 Max(alpha1) = 1
342 BiCGStab: Solving for Ux, Initial residual = 0.00123027, Final residual = 5.67914e-12, No Iterations 2
343 BiCGStab: Solving for Uy, Initial residual = 0.00455125, Final residual = 1.04623e-10, No Iterations 2
344 CG: Solving for pd, Initial residual = 0.0248169, Final residual = 7.58731e-08, No Iterations 12
345 CG: Solving for pd, Initial residual = 0.0173662, Final residual = 5.136e-08, No Iterations 11
346 CG: Solving for pd, Initial residual = 0.00632427, Final residual = 7.52891e-08, No Iterations 10
347 CG: Solving for pd, Initial residual = 0.00341881, Final residual = 6.72826e-08, No Iterations 9
348 CG: Solving for pd, Initial residual = 0.0022826, Final residual = 8.02796e-08, No Iterations 9
349 CG: Solving for pd, Initial residual = 0.00167082, Final residual = 6.88558e-08, No Iterations 9
350 mag(U): max: 1.76997 avg: 0.199253
351 time step continuity errors : sum local = 2.15371e-11, global = -1.95903e-12, cumulative = 2.42911e-12
352 Calculating static pressure
353 CG: Solving for p, Initial residual = 0.000613755, Final residual = 9.37543e-08, No Iterations 9
354 Relaxation: p = 0.1
355 BiCGStab: Solving for alpha1, Initial residual = 9.38405e-07, Final residual = 7.93364e-11, No Iterations 1
356 Liquid phase volume fraction = 0.500439 Min(alpha1) = -0.000449155 Max(alpha1) = 1
357 ExecutionTime = 2.43 s ClockTime = 3 s
359 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
360 Courant Number mean: 0.00516867 max: 0.357575 velocity magnitude: 0.895
361 deltaT = 0.000866532
362 Time = 0.00526896
364 BiCGStab: Solving for Ux, Initial residual = 0.00137672, Final residual = 1.45525e-11, No Iterations 2
365 BiCGStab: Solving for Uy, Initial residual = 0.00383757, Final residual = 6.61271e-11, No Iterations 2
366 CG: Solving for pd, Initial residual = 0.0232102, Final residual = 8.41924e-08, No Iterations 12
367 CG: Solving for pd, Initial residual = 0.0175538, Final residual = 6.53282e-08, No Iterations 12
368 CG: Solving for pd, Initial residual = 0.0131802, Final residual = 9.72945e-08, No Iterations 11
369 CG: Solving for pd, Initial residual = 0.00978923, Final residual = 7.34978e-08, No Iterations 11
370 CG: Solving for pd, Initial residual = 0.007421, Final residual = 5.66767e-08, No Iterations 11
371 CG: Solving for pd, Initial residual = 0.00575846, Final residual = 8.60472e-08, No Iterations 10
372 mag(U): max: 1.87608 avg: 0.199881
373 time step continuity errors : sum local = 2.94599e-11, global = 5.28661e-13, cumulative = 2.95778e-12
374 BiCGStab: Solving for alpha1, Initial residual = 7.42251e-06, Final residual = 4.73746e-10, No Iterations 1
375 Liquid phase volume fraction = 0.500438 Min(alpha1) = -0.000491795 Max(alpha1) = 1.00001
376 BiCGStab: Solving for Ux, Initial residual = 0.00118191, Final residual = 4.08581e-12, No Iterations 2
377 BiCGStab: Solving for Uy, Initial residual = 0.0041646, Final residual = 9.02319e-11, No Iterations 2
378 CG: Solving for pd, Initial residual = 0.024086, Final residual = 7.38335e-08, No Iterations 12
379 CG: Solving for pd, Initial residual = 0.0157559, Final residual = 5.74932e-08, No Iterations 11
380 CG: Solving for pd, Initial residual = 0.00550321, Final residual = 6.46352e-08, No Iterations 10
381 CG: Solving for pd, Initial residual = 0.00292543, Final residual = 7.11664e-08, No Iterations 9
382 CG: Solving for pd, Initial residual = 0.00187152, Final residual = 6.19085e-08, No Iterations 9
383 CG: Solving for pd, Initial residual = 0.00142554, Final residual = 8.49507e-08, No Iterations 8
384 mag(U): max: 1.83575 avg: 0.199226
385 time step continuity errors : sum local = 3.12661e-11, global = -1.45026e-12, cumulative = 1.50751e-12
386 Calculating static pressure
387 CG: Solving for p, Initial residual = 0.000544632, Final residual = 7.41142e-08, No Iterations 9
388 Relaxation: p = 0.1
389 BiCGStab: Solving for alpha1, Initial residual = 9.59861e-07, Final residual = 1.17497e-10, No Iterations 1
390 Liquid phase volume fraction = 0.500438 Min(alpha1) = -0.000502428 Max(alpha1) = 1.00001
391 ExecutionTime = 2.67 s ClockTime = 3 s
393 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
394 Courant Number mean: 0.00574178 max: 0.410978 velocity magnitude: 0.923479
395 deltaT = 0.000818391
396 Time = 0.00608735
398 BiCGStab: Solving for Ux, Initial residual = 0.00111843, Final residual = 1.07709e-11, No Iterations 2
399 BiCGStab: Solving for Uy, Initial residual = 0.00303027, Final residual = 4.12769e-11, No Iterations 2
400 CG: Solving for pd, Initial residual = 0.0251386, Final residual = 9.51056e-08, No Iterations 12
401 CG: Solving for pd, Initial residual = 0.0187127, Final residual = 8.24324e-08, No Iterations 12
402 CG: Solving for pd, Initial residual = 0.0137362, Final residual = 5.82301e-08, No Iterations 12
403 CG: Solving for pd, Initial residual = 0.010494, Final residual = 8.06718e-08, No Iterations 11
404 CG: Solving for pd, Initial residual = 0.00823383, Final residual = 6.30825e-08, No Iterations 11
405 CG: Solving for pd, Initial residual = 0.00660421, Final residual = 5.83947e-08, No Iterations 11
406 mag(U): max: 1.93399 avg: 0.200009
407 time step continuity errors : sum local = 1.87458e-11, global = 1.1914e-13, cumulative = 1.62665e-12
408 BiCGStab: Solving for alpha1, Initial residual = 7.00344e-06, Final residual = 4.18705e-10, No Iterations 1
409 Liquid phase volume fraction = 0.500437 Min(alpha1) = -0.000541948 Max(alpha1) = 1.00001
410 BiCGStab: Solving for Ux, Initial residual = 0.00109082, Final residual = 2.59708e-12, No Iterations 2
411 BiCGStab: Solving for Uy, Initial residual = 0.00401325, Final residual = 5.41332e-11, No Iterations 2
412 CG: Solving for pd, Initial residual = 0.023333, Final residual = 6.8761e-08, No Iterations 12
413 CG: Solving for pd, Initial residual = 0.0152723, Final residual = 4.82834e-08, No Iterations 11
414 CG: Solving for pd, Initial residual = 0.00493534, Final residual = 5.96916e-08, No Iterations 10
415 CG: Solving for pd, Initial residual = 0.00278781, Final residual = 7.10927e-08, No Iterations 9
416 CG: Solving for pd, Initial residual = 0.00170977, Final residual = 6.44212e-08, No Iterations 9
417 CG: Solving for pd, Initial residual = 0.00125676, Final residual = 6.15291e-08, No Iterations 9
418 mag(U): max: 1.88954 avg: 0.1994
419 time step continuity errors : sum local = 2.11602e-11, global = -6.52033e-13, cumulative = 9.74622e-13
420 Calculating static pressure
421 CG: Solving for p, Initial residual = 0.000508732, Final residual = 6.76267e-08, No Iterations 9
422 Relaxation: p = 0.1
423 BiCGStab: Solving for alpha1, Initial residual = 8.5527e-07, Final residual = 1.06573e-10, No Iterations 1
424 Liquid phase volume fraction = 0.500437 Min(alpha1) = -0.000548784 Max(alpha1) = 1.00001
425 ExecutionTime = 2.94 s ClockTime = 3 s
427 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
428 Courant Number mean: 0.00541842 max: 0.398425 velocity magnitude: 0.947037
429 deltaT = 0.000818391
430 Time = 0.00690574
432 BiCGStab: Solving for Ux, Initial residual = 0.00107208, Final residual = 1.43252e-12, No Iterations 2
433 BiCGStab: Solving for Uy, Initial residual = 0.00296405, Final residual = 4.14006e-11, No Iterations 2
434 CG: Solving for pd, Initial residual = 0.0229135, Final residual = 7.80762e-08, No Iterations 12
435 CG: Solving for pd, Initial residual = 0.0170583, Final residual = 6.72191e-08, No Iterations 12
436 CG: Solving for pd, Initial residual = 0.0124767, Final residual = 9.03428e-08, No Iterations 11
437 CG: Solving for pd, Initial residual = 0.00935185, Final residual = 6.90227e-08, No Iterations 11
438 CG: Solving for pd, Initial residual = 0.00705366, Final residual = 5.33502e-08, No Iterations 11
439 CG: Solving for pd, Initial residual = 0.00547427, Final residual = 8.99543e-08, No Iterations 10
440 mag(U): max: 1.97893 avg: 0.200143
441 time step continuity errors : sum local = 2.86508e-11, global = -6.50115e-14, cumulative = 9.0961e-13
442 BiCGStab: Solving for alpha1, Initial residual = 7.00607e-06, Final residual = 3.93666e-10, No Iterations 1
443 Liquid phase volume fraction = 0.500436 Min(alpha1) = -0.000588094 Max(alpha1) = 1.00011
444 BiCGStab: Solving for Ux, Initial residual = 0.00102913, Final residual = 2.76592e-12, No Iterations 2
445 BiCGStab: Solving for Uy, Initial residual = 0.00394808, Final residual = 6.1193e-11, No Iterations 2
446 CG: Solving for pd, Initial residual = 0.0222053, Final residual = 6.62132e-08, No Iterations 12
447 CG: Solving for pd, Initial residual = 0.0153896, Final residual = 5.01872e-08, No Iterations 11
448 CG: Solving for pd, Initial residual = 0.00490678, Final residual = 6.71878e-08, No Iterations 10
449 CG: Solving for pd, Initial residual = 0.00296439, Final residual = 9.10568e-08, No Iterations 9
450 CG: Solving for pd, Initial residual = 0.00174696, Final residual = 7.6515e-08, No Iterations 9
451 CG: Solving for pd, Initial residual = 0.00127006, Final residual = 6.51116e-08, No Iterations 9
452 mag(U): max: 1.93696 avg: 0.199561
453 time step continuity errors : sum local = 2.18485e-11, global = -4.23458e-13, cumulative = 4.86153e-13
454 Calculating static pressure
455 CG: Solving for p, Initial residual = 0.000470551, Final residual = 5.4731e-08, No Iterations 9
456 Relaxation: p = 0.1
457 BiCGStab: Solving for alpha1, Initial residual = 8.4436e-07, Final residual = 1.24969e-10, No Iterations 1
458 Liquid phase volume fraction = 0.500436 Min(alpha1) = -0.000593822 Max(alpha1) = 1.00011
459 ExecutionTime = 3.2 s ClockTime = 4 s
461 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
462 Courant Number mean: 0.00541381 max: 0.40773 velocity magnitude: 0.968366
463 deltaT = 0.000770251
464 Time = 0.00767599
466 BiCGStab: Solving for Ux, Initial residual = 0.000938615, Final residual = 1.53607e-12, No Iterations 2
467 BiCGStab: Solving for Uy, Initial residual = 0.00268772, Final residual = 3.11838e-11, No Iterations 2
468 CG: Solving for pd, Initial residual = 0.0242315, Final residual = 7.89252e-08, No Iterations 12
469 CG: Solving for pd, Initial residual = 0.0177422, Final residual = 5.31633e-08, No Iterations 12
470 CG: Solving for pd, Initial residual = 0.0127718, Final residual = 9.5409e-08, No Iterations 11
471 CG: Solving for pd, Initial residual = 0.00951578, Final residual = 6.84276e-08, No Iterations 11
472 CG: Solving for pd, Initial residual = 0.00724459, Final residual = 5.5155e-08, No Iterations 11
473 CG: Solving for pd, Initial residual = 0.00556508, Final residual = 9.80215e-08, No Iterations 10
474 mag(U): max: 2.01749 avg: 0.200273
475 time step continuity errors : sum local = 2.79576e-11, global = -5.44814e-13, cumulative = -5.86616e-14
476 BiCGStab: Solving for alpha1, Initial residual = 6.58875e-06, Final residual = 3.07591e-10, No Iterations 1
477 Liquid phase volume fraction = 0.500435 Min(alpha1) = -0.000629992 Max(alpha1) = 1.0002
478 BiCGStab: Solving for Ux, Initial residual = 0.000959074, Final residual = 1.69453e-12, No Iterations 2
479 BiCGStab: Solving for Uy, Initial residual = 0.00388112, Final residual = 5.88155e-11, No Iterations 2
480 CG: Solving for pd, Initial residual = 0.0236304, Final residual = 6.62179e-08, No Iterations 12
481 CG: Solving for pd, Initial residual = 0.0160557, Final residual = 5.46524e-08, No Iterations 11
482 CG: Solving for pd, Initial residual = 0.00501766, Final residual = 6.95021e-08, No Iterations 10
483 CG: Solving for pd, Initial residual = 0.00308164, Final residual = 9.18535e-08, No Iterations 9
484 CG: Solving for pd, Initial residual = 0.00193436, Final residual = 7.49062e-08, No Iterations 9
485 CG: Solving for pd, Initial residual = 0.00140056, Final residual = 7.01356e-08, No Iterations 9
486 mag(U): max: 1.97836 avg: 0.199702
487 time step continuity errors : sum local = 2.07891e-11, global = 6.42066e-13, cumulative = 5.83404e-13
488 Calculating static pressure
489 CG: Solving for p, Initial residual = 0.000444568, Final residual = 4.97315e-08, No Iterations 9
490 Relaxation: p = 0.1
491 BiCGStab: Solving for alpha1, Initial residual = 7.6112e-07, Final residual = 1.0636e-10, No Iterations 1
492 Liquid phase volume fraction = 0.500435 Min(alpha1) = -0.000632805 Max(alpha1) = 1.0002
493 ExecutionTime = 3.46 s ClockTime = 4 s
495 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
496 Courant Number mean: 0.00509255 max: 0.391335 velocity magnitude: 0.986518
497 deltaT = 0.000770251
498 Time = 0.00844624
500 BiCGStab: Solving for Ux, Initial residual = 0.000907181, Final residual = 1.61892e-12, No Iterations 2
501 BiCGStab: Solving for Uy, Initial residual = 0.00266417, Final residual = 2.87838e-11, No Iterations 2
502 CG: Solving for pd, Initial residual = 0.0246345, Final residual = 7.91946e-08, No Iterations 12
503 CG: Solving for pd, Initial residual = 0.0171226, Final residual = 6.99734e-08, No Iterations 12
504 CG: Solving for pd, Initial residual = 0.0121853, Final residual = 9.23863e-08, No Iterations 11
505 CG: Solving for pd, Initial residual = 0.00901243, Final residual = 7.30889e-08, No Iterations 11
506 CG: Solving for pd, Initial residual = 0.00685712, Final residual = 6.07547e-08, No Iterations 11
507 CG: Solving for pd, Initial residual = 0.00526596, Final residual = 9.60245e-08, No Iterations 10
508 mag(U): max: 2.05298 avg: 0.200332
509 time step continuity errors : sum local = 2.64214e-11, global = -8.40053e-13, cumulative = -2.56649e-13
510 BiCGStab: Solving for alpha1, Initial residual = 6.61249e-06, Final residual = 3.18849e-10, No Iterations 1
511 Liquid phase volume fraction = 0.500434 Min(alpha1) = -0.000680194 Max(alpha1) = 1.00031
512 BiCGStab: Solving for Ux, Initial residual = 0.000915937, Final residual = 3.53749e-12, No Iterations 2
513 BiCGStab: Solving for Uy, Initial residual = 0.00375414, Final residual = 6.82671e-11, No Iterations 2
514 CG: Solving for pd, Initial residual = 0.024106, Final residual = 6.69656e-08, No Iterations 12
515 CG: Solving for pd, Initial residual = 0.0161468, Final residual = 5.19194e-08, No Iterations 11
516 CG: Solving for pd, Initial residual = 0.00535883, Final residual = 7.61691e-08, No Iterations 10
517 CG: Solving for pd, Initial residual = 0.00299185, Final residual = 9.38122e-08, No Iterations 9
518 CG: Solving for pd, Initial residual = 0.00185824, Final residual = 8.51693e-08, No Iterations 9
519 CG: Solving for pd, Initial residual = 0.00129029, Final residual = 7.20344e-08, No Iterations 9
520 mag(U): max: 2.01617 avg: 0.199758
521 time step continuity errors : sum local = 2.05216e-11, global = 1.18057e-13, cumulative = -1.38592e-13
522 Calculating static pressure
523 CG: Solving for p, Initial residual = 0.000415923, Final residual = 4.42076e-08, No Iterations 9
524 Relaxation: p = 0.1
525 BiCGStab: Solving for alpha1, Initial residual = 7.50045e-07, Final residual = 1.04556e-10, No Iterations 1
526 Liquid phase volume fraction = 0.500434 Min(alpha1) = -0.000700255 Max(alpha1) = 1.00031
527 ExecutionTime = 3.71 s ClockTime = 4 s
529 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
530 Courant Number mean: 0.00509102 max: 0.398493 velocity magnitude: 1.00342
531 deltaT = 0.000770251
532 Time = 0.00921649
534 BiCGStab: Solving for Ux, Initial residual = 0.000848972, Final residual = 2.90219e-12, No Iterations 2
535 BiCGStab: Solving for Uy, Initial residual = 0.00253134, Final residual = 2.90983e-11, No Iterations 2
536 CG: Solving for pd, Initial residual = 0.0269345, Final residual = 7.54893e-08, No Iterations 12
537 CG: Solving for pd, Initial residual = 0.0187661, Final residual = 6.52995e-08, No Iterations 12
538 CG: Solving for pd, Initial residual = 0.0134987, Final residual = 5.43774e-08, No Iterations 12
539 CG: Solving for pd, Initial residual = 0.0100948, Final residual = 7.40309e-08, No Iterations 11
540 CG: Solving for pd, Initial residual = 0.00768843, Final residual = 4.79862e-08, No Iterations 11
541 CG: Solving for pd, Initial residual = 0.00592217, Final residual = 5.88851e-08, No Iterations 11
542 mag(U): max: 2.08545 avg: 0.200379
543 time step continuity errors : sum local = 1.58166e-11, global = -9.3842e-13, cumulative = -1.07701e-12
544 BiCGStab: Solving for alpha1, Initial residual = 6.65017e-06, Final residual = 3.23815e-10, No Iterations 1
545 Liquid phase volume fraction = 0.500433 Min(alpha1) = -0.000992566 Max(alpha1) = 1.00041
546 BiCGStab: Solving for Ux, Initial residual = 0.000876586, Final residual = 6.93289e-12, No Iterations 2
547 BiCGStab: Solving for Uy, Initial residual = 0.00365716, Final residual = 6.2902e-11, No Iterations 2
548 CG: Solving for pd, Initial residual = 0.0253704, Final residual = 6.82782e-08, No Iterations 12
549 CG: Solving for pd, Initial residual = 0.0162506, Final residual = 5.51923e-08, No Iterations 11
550 CG: Solving for pd, Initial residual = 0.00502395, Final residual = 8.06689e-08, No Iterations 10
551 CG: Solving for pd, Initial residual = 0.00275724, Final residual = 9.44729e-08, No Iterations 9
552 CG: Solving for pd, Initial residual = 0.0016817, Final residual = 8.01536e-08, No Iterations 9
553 CG: Solving for pd, Initial residual = 0.00119586, Final residual = 5.74844e-08, No Iterations 9
554 mag(U): max: 2.0503 avg: 0.199814
555 time step continuity errors : sum local = 1.61231e-11, global = 7.06491e-13, cumulative = -3.70521e-13
556 Calculating static pressure
557 CG: Solving for p, Initial residual = 0.000390543, Final residual = 3.90834e-08, No Iterations 9
558 Relaxation: p = 0.1
559 BiCGStab: Solving for alpha1, Initial residual = 8.18269e-07, Final residual = 9.91354e-11, No Iterations 1
560 Liquid phase volume fraction = 0.500433 Min(alpha1) = -0.00101368 Max(alpha1) = 1.00041
561 ExecutionTime = 3.95 s ClockTime = 5 s
563 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
564 Courant Number mean: 0.00509014 max: 0.405104 velocity magnitude: 1.01882
565 deltaT = 0.0007189
566 Time = 0.00993539
568 BiCGStab: Solving for Ux, Initial residual = 0.000750385, Final residual = 8.93246e-09, No Iterations 1
569 BiCGStab: Solving for Uy, Initial residual = 0.00226422, Final residual = 3.07607e-11, No Iterations 2
570 CG: Solving for pd, Initial residual = 0.0305844, Final residual = 8.43758e-08, No Iterations 12
571 CG: Solving for pd, Initial residual = 0.0208075, Final residual = 7.37721e-08, No Iterations 12
572 CG: Solving for pd, Initial residual = 0.0147279, Final residual = 9.9281e-08, No Iterations 11
573 CG: Solving for pd, Initial residual = 0.0107763, Final residual = 7.61402e-08, No Iterations 11
574 CG: Solving for pd, Initial residual = 0.00814368, Final residual = 5.33178e-08, No Iterations 11
575 CG: Solving for pd, Initial residual = 0.00634721, Final residual = 6.61012e-08, No Iterations 11
576 mag(U): max: 2.11385 avg: 0.200445
577 time step continuity errors : sum local = 1.57686e-11, global = -1.23239e-12, cumulative = -1.60291e-12
578 BiCGStab: Solving for alpha1, Initial residual = 6.23731e-06, Final residual = 2.29504e-10, No Iterations 1
579 Liquid phase volume fraction = 0.500432 Min(alpha1) = -0.00128309 Max(alpha1) = 1.00052
580 BiCGStab: Solving for Ux, Initial residual = 0.000827807, Final residual = 2.48951e-12, No Iterations 2
581 BiCGStab: Solving for Uy, Initial residual = 0.00353228, Final residual = 3.68705e-11, No Iterations 2
582 CG: Solving for pd, Initial residual = 0.0268911, Final residual = 7.73951e-08, No Iterations 12
583 CG: Solving for pd, Initial residual = 0.016536, Final residual = 5.49039e-08, No Iterations 11
584 CG: Solving for pd, Initial residual = 0.00505136, Final residual = 8.35327e-08, No Iterations 10
585 CG: Solving for pd, Initial residual = 0.00292925, Final residual = 6.03571e-08, No Iterations 10
586 CG: Solving for pd, Initial residual = 0.0017887, Final residual = 8.14654e-08, No Iterations 9
587 CG: Solving for pd, Initial residual = 0.00129761, Final residual = 5.69818e-08, No Iterations 9
588 mag(U): max: 2.08099 avg: 0.199893
589 time step continuity errors : sum local = 1.40271e-11, global = 5.94406e-14, cumulative = -1.54347e-12
590 Calculating static pressure
591 CG: Solving for p, Initial residual = 0.000386864, Final residual = 3.6933e-08, No Iterations 9
592 Relaxation: p = 0.1
593 BiCGStab: Solving for alpha1, Initial residual = 7.5984e-07, Final residual = 9.4412e-11, No Iterations 1
594 Liquid phase volume fraction = 0.500432 Min(alpha1) = -0.00130295 Max(alpha1) = 1.00052
595 ExecutionTime = 4.21 s ClockTime = 5 s
597 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
598 Courant Number mean: 0.0047493 max: 0.383485 velocity magnitude: 1.03172
599 deltaT = 0.0007189
600 Time = 0.0106543
602 BiCGStab: Solving for Ux, Initial residual = 0.000744496, Final residual = 8.55393e-09, No Iterations 1
603 BiCGStab: Solving for Uy, Initial residual = 0.00225892, Final residual = 3.25978e-11, No Iterations 2
604 CG: Solving for pd, Initial residual = 0.0296879, Final residual = 8.96415e-08, No Iterations 12
605 CG: Solving for pd, Initial residual = 0.0202005, Final residual = 5.93735e-08, No Iterations 12
606 CG: Solving for pd, Initial residual = 0.0141054, Final residual = 5.14315e-08, No Iterations 12
607 CG: Solving for pd, Initial residual = 0.0102919, Final residual = 9.24113e-08, No Iterations 11
608 CG: Solving for pd, Initial residual = 0.0076913, Final residual = 5.75659e-08, No Iterations 11
609 CG: Solving for pd, Initial residual = 0.00589357, Final residual = 7.90749e-08, No Iterations 11
610 mag(U): max: 2.14068 avg: 0.200475
611 time step continuity errors : sum local = 1.84389e-11, global = -1.45592e-12, cumulative = -2.99939e-12
612 BiCGStab: Solving for alpha1, Initial residual = 6.28972e-06, Final residual = 2.45138e-10, No Iterations 1
613 Liquid phase volume fraction = 0.500432 Min(alpha1) = -0.00157494 Max(alpha1) = 1.00063
614 BiCGStab: Solving for Ux, Initial residual = 0.000799874, Final residual = 3.98429e-12, No Iterations 2
615 BiCGStab: Solving for Uy, Initial residual = 0.00341322, Final residual = 4.17557e-11, No Iterations 2
616 CG: Solving for pd, Initial residual = 0.0279671, Final residual = 8.01211e-08, No Iterations 12
617 CG: Solving for pd, Initial residual = 0.0169751, Final residual = 5.74572e-08, No Iterations 11
618 CG: Solving for pd, Initial residual = 0.00536061, Final residual = 8.30908e-08, No Iterations 10
619 CG: Solving for pd, Initial residual = 0.00285577, Final residual = 9.78562e-08, No Iterations 9
620 CG: Solving for pd, Initial residual = 0.00176786, Final residual = 8.30745e-08, No Iterations 9
621 CG: Solving for pd, Initial residual = 0.00128613, Final residual = 7.45713e-08, No Iterations 9
622 mag(U): max: 2.10952 avg: 0.199939
623 time step continuity errors : sum local = 1.79773e-11, global = -2.82044e-13, cumulative = -3.28143e-12
624 Calculating static pressure
625 CG: Solving for p, Initial residual = 0.000370078, Final residual = 3.55008e-08, No Iterations 9
626 Relaxation: p = 0.1
627 BiCGStab: Solving for alpha1, Initial residual = 7.61617e-07, Final residual = 8.68383e-11, No Iterations 1
628 Liquid phase volume fraction = 0.500432 Min(alpha1) = -0.00159373 Max(alpha1) = 1.00063
629 ExecutionTime = 4.47 s ClockTime = 5 s
631 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
632 Courant Number mean: 0.00474752 max: 0.388642 velocity magnitude: 1.04381
633 deltaT = 0.0007189
634 Time = 0.0113732
636 BiCGStab: Solving for Ux, Initial residual = 0.0007145, Final residual = 7.42954e-09, No Iterations 1
637 BiCGStab: Solving for Uy, Initial residual = 0.00217204, Final residual = 2.1873e-11, No Iterations 2
638 CG: Solving for pd, Initial residual = 0.0317619, Final residual = 6.74294e-08, No Iterations 13
639 CG: Solving for pd, Initial residual = 0.0213098, Final residual = 7.15328e-08, No Iterations 12
640 CG: Solving for pd, Initial residual = 0.0148486, Final residual = 7.51866e-08, No Iterations 12
641 CG: Solving for pd, Initial residual = 0.0108226, Final residual = 7.50901e-08, No Iterations 11
642 CG: Solving for pd, Initial residual = 0.00811339, Final residual = 5.75163e-08, No Iterations 11
643 CG: Solving for pd, Initial residual = 0.00625942, Final residual = 5.37262e-08, No Iterations 11
644 mag(U): max: 2.16554 avg: 0.200508
645 time step continuity errors : sum local = 1.22838e-11, global = -1.49746e-12, cumulative = -4.7789e-12
646 BiCGStab: Solving for alpha1, Initial residual = 6.29754e-06, Final residual = 2.4187e-10, No Iterations 1
647 Liquid phase volume fraction = 0.500431 Min(alpha1) = -0.00186804 Max(alpha1) = 1.00074
648 BiCGStab: Solving for Ux, Initial residual = 0.000771233, Final residual = 7.43286e-12, No Iterations 2
649 BiCGStab: Solving for Uy, Initial residual = 0.00333564, Final residual = 4.30457e-11, No Iterations 2
650 CG: Solving for pd, Initial residual = 0.0290202, Final residual = 8.11727e-08, No Iterations 12
651 CG: Solving for pd, Initial residual = 0.0169074, Final residual = 6.78946e-08, No Iterations 11
652 CG: Solving for pd, Initial residual = 0.00528472, Final residual = 7.76054e-08, No Iterations 10
653 CG: Solving for pd, Initial residual = 0.00281832, Final residual = 9.80341e-08, No Iterations 9
654 CG: Solving for pd, Initial residual = 0.00175301, Final residual = 9.06999e-08, No Iterations 9
655 CG: Solving for pd, Initial residual = 0.00126906, Final residual = 6.37933e-08, No Iterations 9
656 mag(U): max: 2.13625 avg: 0.199973
657 time step continuity errors : sum local = 1.51204e-11, global = -1.04698e-12, cumulative = -5.82588e-12
658 Calculating static pressure
659 CG: Solving for p, Initial residual = 0.000351376, Final residual = 9.8846e-08, No Iterations 8
660 Relaxation: p = 0.1
661 BiCGStab: Solving for alpha1, Initial residual = 8.31778e-07, Final residual = 7.42547e-11, No Iterations 1
662 Liquid phase volume fraction = 0.500431 Min(alpha1) = -0.00188551 Max(alpha1) = 1.00074
663 ExecutionTime = 4.72 s ClockTime = 6 s
665 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
666 Courant Number mean: 0.00474705 max: 0.393593 velocity magnitude: 1.05514
667 deltaT = 0.0007189
668 Time = 0.0120921
670 BiCGStab: Solving for Ux, Initial residual = 0.000687151, Final residual = 7.73033e-09, No Iterations 1
671 BiCGStab: Solving for Uy, Initial residual = 0.00210327, Final residual = 3.13972e-11, No Iterations 2
672 CG: Solving for pd, Initial residual = 0.0330451, Final residual = 5.29103e-08, No Iterations 13
673 CG: Solving for pd, Initial residual = 0.0219641, Final residual = 8.32368e-08, No Iterations 12
674 CG: Solving for pd, Initial residual = 0.0153061, Final residual = 6.11598e-08, No Iterations 12
675 CG: Solving for pd, Initial residual = 0.0110913, Final residual = 9.09327e-08, No Iterations 11
676 CG: Solving for pd, Initial residual = 0.00834078, Final residual = 7.06316e-08, No Iterations 11
677 CG: Solving for pd, Initial residual = 0.00645555, Final residual = 5.796e-08, No Iterations 11
678 mag(U): max: 2.18895 avg: 0.200541
679 time step continuity errors : sum local = 1.30069e-11, global = 1.25724e-12, cumulative = -4.56864e-12
680 BiCGStab: Solving for alpha1, Initial residual = 6.39427e-06, Final residual = 2.43217e-10, No Iterations 1
681 Liquid phase volume fraction = 0.50043 Min(alpha1) = -0.00216063 Max(alpha1) = 1.00086
682 BiCGStab: Solving for Ux, Initial residual = 0.000744391, Final residual = 8.35278e-09, No Iterations 1
683 BiCGStab: Solving for Uy, Initial residual = 0.00328199, Final residual = 2.86391e-11, No Iterations 2
684 CG: Solving for pd, Initial residual = 0.0304823, Final residual = 8.8752e-08, No Iterations 12
685 CG: Solving for pd, Initial residual = 0.0175859, Final residual = 7.08214e-08, No Iterations 11
686 CG: Solving for pd, Initial residual = 0.00546064, Final residual = 8.01342e-08, No Iterations 10
687 CG: Solving for pd, Initial residual = 0.0029921, Final residual = 7.0097e-08, No Iterations 10
688 CG: Solving for pd, Initial residual = 0.00182626, Final residual = 5.73632e-08, No Iterations 10
689 CG: Solving for pd, Initial residual = 0.00126454, Final residual = 6.78579e-08, No Iterations 9
690 mag(U): max: 2.16113 avg: 0.20001
691 time step continuity errors : sum local = 1.57282e-11, global = -7.99949e-13, cumulative = -5.36859e-12
692 Calculating static pressure
693 CG: Solving for p, Initial residual = 0.000336889, Final residual = 9.57375e-08, No Iterations 8
694 Relaxation: p = 0.1
695 BiCGStab: Solving for alpha1, Initial residual = 7.59422e-07, Final residual = 1.00312e-10, No Iterations 1
696 Liquid phase volume fraction = 0.50043 Min(alpha1) = -0.00217673 Max(alpha1) = 1.00086
697 ExecutionTime = 4.99 s ClockTime = 6 s
699 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
700 Courant Number mean: 0.00474544 max: 0.398277 velocity magnitude: 1.06569
701 deltaT = 0.0007189
702 Time = 0.012811
704 BiCGStab: Solving for Ux, Initial residual = 0.000658264, Final residual = 8.23342e-09, No Iterations 1
705 BiCGStab: Solving for Uy, Initial residual = 0.00204341, Final residual = 5.17683e-11, No Iterations 2
706 CG: Solving for pd, Initial residual = 0.0344907, Final residual = 5.45677e-08, No Iterations 13
707 CG: Solving for pd, Initial residual = 0.0228469, Final residual = 8.02614e-08, No Iterations 12
708 CG: Solving for pd, Initial residual = 0.0157446, Final residual = 6.08831e-08, No Iterations 12
709 CG: Solving for pd, Initial residual = 0.011306, Final residual = 9.23483e-08, No Iterations 11
710 CG: Solving for pd, Initial residual = 0.00844506, Final residual = 6.7691e-08, No Iterations 11
711 CG: Solving for pd, Initial residual = 0.00656995, Final residual = 6.12632e-08, No Iterations 11
712 mag(U): max: 2.21098 avg: 0.200574
713 time step continuity errors : sum local = 1.35985e-11, global = 1.07363e-12, cumulative = -4.29496e-12
714 BiCGStab: Solving for alpha1, Initial residual = 6.44265e-06, Final residual = 2.42125e-10, No Iterations 1
715 Liquid phase volume fraction = 0.50043 Min(alpha1) = -0.00245155 Max(alpha1) = 1.00098
716 BiCGStab: Solving for Ux, Initial residual = 0.000720223, Final residual = 7.66569e-09, No Iterations 1
717 BiCGStab: Solving for Uy, Initial residual = 0.00327741, Final residual = 2.54044e-11, No Iterations 2
718 CG: Solving for pd, Initial residual = 0.0315424, Final residual = 8.82999e-08, No Iterations 12
719 CG: Solving for pd, Initial residual = 0.0176043, Final residual = 6.8173e-08, No Iterations 11
720 CG: Solving for pd, Initial residual = 0.00568275, Final residual = 8.09373e-08, No Iterations 10
721 CG: Solving for pd, Initial residual = 0.00315631, Final residual = 6.79003e-08, No Iterations 10
722 CG: Solving for pd, Initial residual = 0.0019146, Final residual = 6.62558e-08, No Iterations 11
723 CG: Solving for pd, Initial residual = 0.00133076, Final residual = 9.38888e-08, No Iterations 9
724 mag(U): max: 2.18473 avg: 0.200046
725 time step continuity errors : sum local = 2.1674e-11, global = -2.08993e-13, cumulative = -4.50395e-12
726 Calculating static pressure
727 CG: Solving for p, Initial residual = 0.000328767, Final residual = 9.08626e-08, No Iterations 8
728 Relaxation: p = 0.1
729 BiCGStab: Solving for alpha1, Initial residual = 7.15587e-07, Final residual = 9.65425e-11, No Iterations 1
730 Liquid phase volume fraction = 0.50043 Min(alpha1) = -0.00246646 Max(alpha1) = 1.00098
731 ExecutionTime = 5.25 s ClockTime = 6 s
733 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
734 Courant Number mean: 0.00474282 max: 0.402793 velocity magnitude: 1.07565
735 deltaT = 0.000653546
736 Time = 0.0134645
738 BiCGStab: Solving for Ux, Initial residual = 0.000585596, Final residual = 5.39693e-09, No Iterations 1
739 BiCGStab: Solving for Uy, Initial residual = 0.00185987, Final residual = 1.84497e-11, No Iterations 2
740 CG: Solving for pd, Initial residual = 0.0386301, Final residual = 5.54058e-08, No Iterations 13
741 CG: Solving for pd, Initial residual = 0.0250353, Final residual = 7.36096e-08, No Iterations 12
742 CG: Solving for pd, Initial residual = 0.0170965, Final residual = 5.78878e-08, No Iterations 12
743 CG: Solving for pd, Initial residual = 0.0121734, Final residual = 8.44437e-08, No Iterations 11
744 CG: Solving for pd, Initial residual = 0.00907647, Final residual = 6.51634e-08, No Iterations 11
745 CG: Solving for pd, Initial residual = 0.00702156, Final residual = 5.8379e-08, No Iterations 11
746 mag(U): max: 2.23143 avg: 0.200628
747 time step continuity errors : sum local = 1.12069e-11, global = 4.22318e-13, cumulative = -4.08163e-12
748 BiCGStab: Solving for alpha1, Initial residual = 5.88473e-06, Final residual = 1.61499e-10, No Iterations 1
749 Liquid phase volume fraction = 0.500429 Min(alpha1) = -0.00270899 Max(alpha1) = 1.00109
750 BiCGStab: Solving for Ux, Initial residual = 0.00068427, Final residual = 6.55838e-09, No Iterations 1
751 BiCGStab: Solving for Uy, Initial residual = 0.00322777, Final residual = 1.78804e-11, No Iterations 2
752 CG: Solving for pd, Initial residual = 0.033031, Final residual = 8.23578e-08, No Iterations 12
753 CG: Solving for pd, Initial residual = 0.0182103, Final residual = 6.91548e-08, No Iterations 11
754 CG: Solving for pd, Initial residual = 0.0057451, Final residual = 7.20969e-08, No Iterations 10
755 CG: Solving for pd, Initial residual = 0.00318629, Final residual = 8.349e-08, No Iterations 10
756 CG: Solving for pd, Initial residual = 0.00191908, Final residual = 7.81573e-08, No Iterations 9
757 CG: Solving for pd, Initial residual = 0.001372, Final residual = 7.13001e-08, No Iterations 9
758 mag(U): max: 2.20686 avg: 0.200118
759 time step continuity errors : sum local = 1.40132e-11, global = -1.20238e-12, cumulative = -5.28401e-12
760 Calculating static pressure
761 CG: Solving for p, Initial residual = 0.000340231, Final residual = 9.23084e-08, No Iterations 8
762 Relaxation: p = 0.1
763 BiCGStab: Solving for alpha1, Initial residual = 6.16322e-07, Final residual = 5.15029e-11, No Iterations 1
764 Liquid phase volume fraction = 0.500429 Min(alpha1) = -0.00272077 Max(alpha1) = 1.00109
765 ExecutionTime = 5.52 s ClockTime = 7 s
767 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
768 Courant Number mean: 0.0043089 max: 0.369709 velocity magnitude: 1.08357
769 deltaT = 0.000653546
770 Time = 0.0141181
772 BiCGStab: Solving for Ux, Initial residual = 0.000599299, Final residual = 4.68721e-09, No Iterations 1
773 BiCGStab: Solving for Uy, Initial residual = 0.00195249, Final residual = 1.28449e-11, No Iterations 2
774 CG: Solving for pd, Initial residual = 0.0359194, Final residual = 9.30463e-08, No Iterations 12
775 CG: Solving for pd, Initial residual = 0.023469, Final residual = 6.30357e-08, No Iterations 12
776 CG: Solving for pd, Initial residual = 0.0159892, Final residual = 4.97084e-08, No Iterations 12
777 CG: Solving for pd, Initial residual = 0.0113541, Final residual = 7.76944e-08, No Iterations 11
778 CG: Solving for pd, Initial residual = 0.00847395, Final residual = 6.74242e-08, No Iterations 11
779 CG: Solving for pd, Initial residual = 0.00637932, Final residual = 9.12499e-08, No Iterations 10
780 mag(U): max: 2.25158 avg: 0.20065
781 time step continuity errors : sum local = 1.72002e-11, global = 6.49569e-13, cumulative = -4.63444e-12
782 BiCGStab: Solving for alpha1, Initial residual = 5.93405e-06, Final residual = 1.47567e-10, No Iterations 1
783 Liquid phase volume fraction = 0.500428 Min(alpha1) = -0.00296325 Max(alpha1) = 1.0012
784 BiCGStab: Solving for Ux, Initial residual = 0.000665142, Final residual = 6.6917e-09, No Iterations 1
785 BiCGStab: Solving for Uy, Initial residual = 0.00320624, Final residual = 1.81073e-11, No Iterations 2
786 CG: Solving for pd, Initial residual = 0.0340547, Final residual = 8.8302e-08, No Iterations 12
787 CG: Solving for pd, Initial residual = 0.0186028, Final residual = 6.69984e-08, No Iterations 11
788 CG: Solving for pd, Initial residual = 0.00584716, Final residual = 8.44704e-08, No Iterations 10
789 CG: Solving for pd, Initial residual = 0.00321549, Final residual = 8.08485e-08, No Iterations 10
790 CG: Solving for pd, Initial residual = 0.00194681, Final residual = 9.87481e-08, No Iterations 10
791 CG: Solving for pd, Initial residual = 0.00141365, Final residual = 8.63351e-08, No Iterations 9
792 mag(U): max: 2.2279 avg: 0.200138
793 time step continuity errors : sum local = 1.65106e-11, global = -9.27575e-13, cumulative = -5.56202e-12
794 Calculating static pressure
795 CG: Solving for p, Initial residual = 0.000324815, Final residual = 6.78621e-08, No Iterations 8
796 Relaxation: p = 0.1
797 BiCGStab: Solving for alpha1, Initial residual = 6.87271e-07, Final residual = 5.15889e-11, No Iterations 1
798 Liquid phase volume fraction = 0.500428 Min(alpha1) = -0.00297401 Max(alpha1) = 1.0012
799 ExecutionTime = 5.76 s ClockTime = 7 s
801 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
802 Courant Number mean: 0.00430737 max: 0.373179 velocity magnitude: 1.09118
803 deltaT = 0.000653546
804 Time = 0.0147716
806 BiCGStab: Solving for Ux, Initial residual = 0.000579868, Final residual = 4.67503e-09, No Iterations 1
807 BiCGStab: Solving for Uy, Initial residual = 0.00193258, Final residual = 1.45539e-11, No Iterations 2
808 CG: Solving for pd, Initial residual = 0.0371834, Final residual = 9.00691e-08, No Iterations 12
809 CG: Solving for pd, Initial residual = 0.0241341, Final residual = 5.92652e-08, No Iterations 12
810 CG: Solving for pd, Initial residual = 0.0166429, Final residual = 9.61386e-08, No Iterations 11
811 CG: Solving for pd, Initial residual = 0.0119361, Final residual = 6.95475e-08, No Iterations 11
812 CG: Solving for pd, Initial residual = 0.00888358, Final residual = 6.81494e-08, No Iterations 11
813 CG: Solving for pd, Initial residual = 0.00684291, Final residual = 6.01758e-08, No Iterations 11
814 mag(U): max: 2.27064 avg: 0.20068
815 time step continuity errors : sum local = 1.11893e-11, global = 6.8218e-13, cumulative = -4.87984e-12
816 BiCGStab: Solving for alpha1, Initial residual = 5.96938e-06, Final residual = 1.33181e-10, No Iterations 1
817 Liquid phase volume fraction = 0.500428 Min(alpha1) = -0.00321548 Max(alpha1) = 1.00132
818 BiCGStab: Solving for Ux, Initial residual = 0.000644444, Final residual = 5.36419e-09, No Iterations 1
819 BiCGStab: Solving for Uy, Initial residual = 0.00320431, Final residual = 1.45418e-11, No Iterations 2
820 CG: Solving for pd, Initial residual = 0.0352765, Final residual = 9.08031e-08, No Iterations 12
821 CG: Solving for pd, Initial residual = 0.0182743, Final residual = 6.55516e-08, No Iterations 11
822 CG: Solving for pd, Initial residual = 0.00566135, Final residual = 7.34561e-08, No Iterations 10
823 CG: Solving for pd, Initial residual = 0.00319262, Final residual = 7.91369e-08, No Iterations 10
824 CG: Solving for pd, Initial residual = 0.0019545, Final residual = 9.64664e-08, No Iterations 9
825 CG: Solving for pd, Initial residual = 0.00136967, Final residual = 6.4698e-08, No Iterations 9
826 mag(U): max: 2.24744 avg: 0.200173
827 time step continuity errors : sum local = 1.23017e-11, global = -5.4933e-13, cumulative = -5.42917e-12
828 Calculating static pressure
829 CG: Solving for p, Initial residual = 0.000304353, Final residual = 7.32362e-08, No Iterations 8
830 Relaxation: p = 0.1
831 BiCGStab: Solving for alpha1, Initial residual = 6.36333e-07, Final residual = 6.34089e-11, No Iterations 1
832 Liquid phase volume fraction = 0.500428 Min(alpha1) = -0.00322482 Max(alpha1) = 1.00132
833 ExecutionTime = 6.02 s ClockTime = 7 s
835 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
836 Courant Number mean: 0.00430534 max: 0.37645 velocity magnitude: 1.09832
837 deltaT = 0.000653546
838 Time = 0.0154252
840 BiCGStab: Solving for Ux, Initial residual = 0.00055597, Final residual = 5.37627e-09, No Iterations 1
841 BiCGStab: Solving for Uy, Initial residual = 0.00191403, Final residual = 3.43605e-11, No Iterations 2
842 CG: Solving for pd, Initial residual = 0.0384692, Final residual = 6.25312e-08, No Iterations 13
843 CG: Solving for pd, Initial residual = 0.0251471, Final residual = 6.86867e-08, No Iterations 12
844 CG: Solving for pd, Initial residual = 0.0171224, Final residual = 9.43071e-08, No Iterations 11
845 CG: Solving for pd, Initial residual = 0.0121659, Final residual = 8.21496e-08, No Iterations 11
846 CG: Solving for pd, Initial residual = 0.00900342, Final residual = 5.50309e-08, No Iterations 11
847 CG: Solving for pd, Initial residual = 0.00682524, Final residual = 9.90991e-08, No Iterations 10
848 mag(U): max: 2.28818 avg: 0.200707
849 time step continuity errors : sum local = 1.8214e-11, global = -5.81167e-13, cumulative = -6.01033e-12
850 BiCGStab: Solving for alpha1, Initial residual = 5.99902e-06, Final residual = 1.35533e-10, No Iterations 1
851 Liquid phase volume fraction = 0.500427 Min(alpha1) = -0.00346493 Max(alpha1) = 1.00143
852 BiCGStab: Solving for Ux, Initial residual = 0.000626922, Final residual = 4.58808e-09, No Iterations 1
853 BiCGStab: Solving for Uy, Initial residual = 0.00323616, Final residual = 1.22881e-11, No Iterations 2
854 CG: Solving for pd, Initial residual = 0.0359994, Final residual = 9.40786e-08, No Iterations 12
855 CG: Solving for pd, Initial residual = 0.0186763, Final residual = 7.02059e-08, No Iterations 11
856 CG: Solving for pd, Initial residual = 0.00590619, Final residual = 8.35648e-08, No Iterations 10
857 CG: Solving for pd, Initial residual = 0.00356178, Final residual = 9.31118e-08, No Iterations 11
858 CG: Solving for pd, Initial residual = 0.00223701, Final residual = 9.91085e-08, No Iterations 9
859 CG: Solving for pd, Initial residual = 0.00161907, Final residual = 7.36364e-08, No Iterations 9
860 mag(U): max: 2.26554 avg: 0.200204
861 time step continuity errors : sum local = 1.37605e-11, global = -8.38194e-15, cumulative = -6.01872e-12
862 Calculating static pressure
863 CG: Solving for p, Initial residual = 0.00029515, Final residual = 7.1162e-08, No Iterations 8
864 Relaxation: p = 0.1
865 BiCGStab: Solving for alpha1, Initial residual = 5.92547e-07, Final residual = 6.34507e-11, No Iterations 1
866 Liquid phase volume fraction = 0.500427 Min(alpha1) = -0.00347394 Max(alpha1) = 1.00143
867 ExecutionTime = 6.28 s ClockTime = 8 s
869 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
870 Courant Number mean: 0.00430339 max: 0.379523 velocity magnitude: 1.10492
871 deltaT = 0.000653546
872 Time = 0.0160787
874 BiCGStab: Solving for Ux, Initial residual = 0.000543926, Final residual = 5.32056e-09, No Iterations 1
875 BiCGStab: Solving for Uy, Initial residual = 0.00192245, Final residual = 3.32161e-11, No Iterations 2
876 CG: Solving for pd, Initial residual = 0.0393179, Final residual = 6.23978e-08, No Iterations 13
877 CG: Solving for pd, Initial residual = 0.0254777, Final residual = 6.43341e-08, No Iterations 12
878 CG: Solving for pd, Initial residual = 0.0173619, Final residual = 9.11671e-08, No Iterations 11
879 CG: Solving for pd, Initial residual = 0.0123399, Final residual = 7.17977e-08, No Iterations 11
880 CG: Solving for pd, Initial residual = 0.00912516, Final residual = 6.21459e-08, No Iterations 11
881 CG: Solving for pd, Initial residual = 0.00687743, Final residual = 8.50957e-08, No Iterations 11
882 mag(U): max: 2.30472 avg: 0.200736
883 time step continuity errors : sum local = 1.53403e-11, global = -1.20897e-12, cumulative = -7.22769e-12
884 BiCGStab: Solving for alpha1, Initial residual = 6.05764e-06, Final residual = 1.51738e-10, No Iterations 1
885 Liquid phase volume fraction = 0.500427 Min(alpha1) = -0.00371256 Max(alpha1) = 1.00155
886 BiCGStab: Solving for Ux, Initial residual = 0.000611492, Final residual = 4.56763e-09, No Iterations 1
887 BiCGStab: Solving for Uy, Initial residual = 0.00329607, Final residual = 1.48767e-11, No Iterations 2
888 CG: Solving for pd, Initial residual = 0.0368463, Final residual = 9.37956e-08, No Iterations 12
889 CG: Solving for pd, Initial residual = 0.0187378, Final residual = 7.1375e-08, No Iterations 11
890 CG: Solving for pd, Initial residual = 0.00609476, Final residual = 8.77488e-08, No Iterations 10
891 CG: Solving for pd, Initial residual = 0.00353534, Final residual = 8.52693e-08, No Iterations 11
892 CG: Solving for pd, Initial residual = 0.0021986, Final residual = 8.00546e-08, No Iterations 10
893 CG: Solving for pd, Initial residual = 0.00164795, Final residual = 9.13088e-08, No Iterations 9
894 mag(U): max: 2.28228 avg: 0.200238
895 time step continuity errors : sum local = 1.66595e-11, global = -9.00826e-13, cumulative = -8.12852e-12
896 Calculating static pressure
897 CG: Solving for p, Initial residual = 0.00029032, Final residual = 4.53211e-08, No Iterations 8
898 Relaxation: p = 0.1
899 BiCGStab: Solving for alpha1, Initial residual = 5.69453e-07, Final residual = 5.22057e-11, No Iterations 1
900 Liquid phase volume fraction = 0.500427 Min(alpha1) = -0.00372123 Max(alpha1) = 1.00155
901 ExecutionTime = 6.53 s ClockTime = 8 s
903 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
904 Courant Number mean: 0.00430073 max: 0.382396 velocity magnitude: 1.11102
905 deltaT = 0.000653546
906 Time = 0.0167323
908 BiCGStab: Solving for Ux, Initial residual = 0.000534089, Final residual = 4.16679e-09, No Iterations 1
909 BiCGStab: Solving for Uy, Initial residual = 0.00195212, Final residual = 1.35243e-11, No Iterations 2
910 CG: Solving for pd, Initial residual = 0.0392223, Final residual = 5.87947e-08, No Iterations 13
911 CG: Solving for pd, Initial residual = 0.025332, Final residual = 8.32566e-08, No Iterations 12
912 CG: Solving for pd, Initial residual = 0.0173857, Final residual = 7.11374e-08, No Iterations 12
913 CG: Solving for pd, Initial residual = 0.0123026, Final residual = 6.60835e-08, No Iterations 11
914 CG: Solving for pd, Initial residual = 0.00898939, Final residual = 5.42159e-08, No Iterations 11
915 CG: Solving for pd, Initial residual = 0.00685918, Final residual = 9.52967e-08, No Iterations 10
916 mag(U): max: 2.31975 avg: 0.200765
917 time step continuity errors : sum local = 1.71187e-11, global = -1.05043e-12, cumulative = -9.17894e-12
918 BiCGStab: Solving for alpha1, Initial residual = 6.11967e-06, Final residual = 1.48316e-10, No Iterations 1
919 Liquid phase volume fraction = 0.500426 Min(alpha1) = -0.0039584 Max(alpha1) = 1.00167
920 BiCGStab: Solving for Ux, Initial residual = 0.00059678, Final residual = 4.90212e-09, No Iterations 1
921 BiCGStab: Solving for Uy, Initial residual = 0.00334426, Final residual = 1.66216e-11, No Iterations 2
922 CG: Solving for pd, Initial residual = 0.0374628, Final residual = 9.39055e-08, No Iterations 12
923 CG: Solving for pd, Initial residual = 0.0186284, Final residual = 7.07795e-08, No Iterations 11
924 CG: Solving for pd, Initial residual = 0.0060224, Final residual = 9.11048e-08, No Iterations 10
925 CG: Solving for pd, Initial residual = 0.00362265, Final residual = 8.55934e-08, No Iterations 11
926 CG: Solving for pd, Initial residual = 0.00235509, Final residual = 7.75887e-08, No Iterations 10
927 CG: Solving for pd, Initial residual = 0.00170943, Final residual = 8.80172e-08, No Iterations 9
928 mag(U): max: 2.29785 avg: 0.200274
929 time step continuity errors : sum local = 1.60572e-11, global = -1.02041e-12, cumulative = -1.01994e-11
930 Calculating static pressure
931 CG: Solving for p, Initial residual = 0.00028418, Final residual = 4.33236e-08, No Iterations 8
932 Relaxation: p = 0.1
933 BiCGStab: Solving for alpha1, Initial residual = 5.74128e-07, Final residual = 4.03158e-11, No Iterations 1
934 Liquid phase volume fraction = 0.500426 Min(alpha1) = -0.0039659 Max(alpha1) = 1.00167
935 ExecutionTime = 6.79 s ClockTime = 8 s
937 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
938 Courant Number mean: 0.00429896 max: 0.385094 velocity magnitude: 1.11672
939 deltaT = 0.000653546
940 Time = 0.0173858
942 BiCGStab: Solving for Ux, Initial residual = 0.000526778, Final residual = 3.64169e-09, No Iterations 1
943 BiCGStab: Solving for Uy, Initial residual = 0.00197741, Final residual = 1.00857e-11, No Iterations 2
944 CG: Solving for pd, Initial residual = 0.0394642, Final residual = 5.14873e-08, No Iterations 13
945 CG: Solving for pd, Initial residual = 0.0256222, Final residual = 7.9322e-08, No Iterations 12
946 CG: Solving for pd, Initial residual = 0.0173762, Final residual = 6.27702e-08, No Iterations 12
947 CG: Solving for pd, Initial residual = 0.0122916, Final residual = 8.67199e-08, No Iterations 11
948 CG: Solving for pd, Initial residual = 0.00902512, Final residual = 7.7778e-08, No Iterations 11
949 CG: Solving for pd, Initial residual = 0.00677985, Final residual = 9.398e-08, No Iterations 10
950 mag(U): max: 2.33355 avg: 0.200796
951 time step continuity errors : sum local = 1.68398e-11, global = -2.46725e-13, cumulative = -1.04461e-11
952 BiCGStab: Solving for alpha1, Initial residual = 6.1332e-06, Final residual = 1.30507e-10, No Iterations 1
953 Liquid phase volume fraction = 0.500426 Min(alpha1) = -0.00420137 Max(alpha1) = 1.00179
954 BiCGStab: Solving for Ux, Initial residual = 0.000581663, Final residual = 4.88693e-09, No Iterations 1
955 BiCGStab: Solving for Uy, Initial residual = 0.00337381, Final residual = 1.52064e-11, No Iterations 2
956 CG: Solving for pd, Initial residual = 0.0375215, Final residual = 9.10065e-08, No Iterations 12
957 CG: Solving for pd, Initial residual = 0.0186549, Final residual = 6.99533e-08, No Iterations 11
958 CG: Solving for pd, Initial residual = 0.0062553, Final residual = 9.17732e-08, No Iterations 10
959 CG: Solving for pd, Initial residual = 0.00380365, Final residual = 8.60106e-08, No Iterations 11
960 CG: Solving for pd, Initial residual = 0.00245073, Final residual = 8.05482e-08, No Iterations 10
961 CG: Solving for pd, Initial residual = 0.00178403, Final residual = 8.07993e-08, No Iterations 9
962 mag(U): max: 2.31167 avg: 0.20031
963 time step continuity errors : sum local = 1.47721e-11, global = -4.93314e-14, cumulative = -1.04954e-11
964 Calculating static pressure
965 CG: Solving for p, Initial residual = 0.00027877, Final residual = 3.95028e-08, No Iterations 8
966 Relaxation: p = 0.1
967 BiCGStab: Solving for alpha1, Initial residual = 6.44847e-07, Final residual = 4.56332e-11, No Iterations 1
968 Liquid phase volume fraction = 0.500426 Min(alpha1) = -0.00420731 Max(alpha1) = 1.00179
969 ExecutionTime = 7.04 s ClockTime = 8 s
971 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
972 Courant Number mean: 0.00429818 max: 0.38748 velocity magnitude: 1.12187
973 deltaT = 0.000653546
974 Time = 0.0180394
976 BiCGStab: Solving for Ux, Initial residual = 0.00051893, Final residual = 3.92789e-09, No Iterations 1
977 BiCGStab: Solving for Uy, Initial residual = 0.00199601, Final residual = 5.63345e-11, No Iterations 2
978 CG: Solving for pd, Initial residual = 0.0394578, Final residual = 6.48842e-08, No Iterations 13
979 CG: Solving for pd, Initial residual = 0.025803, Final residual = 8.30373e-08, No Iterations 12
980 CG: Solving for pd, Initial residual = 0.0175161, Final residual = 9.84119e-08, No Iterations 11
981 CG: Solving for pd, Initial residual = 0.0123944, Final residual = 7.96871e-08, No Iterations 11
982 CG: Solving for pd, Initial residual = 0.00914183, Final residual = 6.8447e-08, No Iterations 11
983 CG: Solving for pd, Initial residual = 0.00693529, Final residual = 9.06889e-08, No Iterations 10
984 mag(U): max: 2.34572 avg: 0.200829
985 time step continuity errors : sum local = 1.61436e-11, global = -9.62712e-13, cumulative = -1.14581e-11
986 BiCGStab: Solving for alpha1, Initial residual = 6.08083e-06, Final residual = 1.17438e-10, No Iterations 1
987 Liquid phase volume fraction = 0.500425 Min(alpha1) = -0.00444088 Max(alpha1) = 1.00191
988 BiCGStab: Solving for Ux, Initial residual = 0.000567248, Final residual = 4.00511e-09, No Iterations 1
989 BiCGStab: Solving for Uy, Initial residual = 0.00340091, Final residual = 1.26847e-11, No Iterations 2
990 CG: Solving for pd, Initial residual = 0.0374506, Final residual = 9.12405e-08, No Iterations 12
991 CG: Solving for pd, Initial residual = 0.0186783, Final residual = 7.16306e-08, No Iterations 11
992 CG: Solving for pd, Initial residual = 0.00616819, Final residual = 9.60511e-08, No Iterations 10
993 CG: Solving for pd, Initial residual = 0.00370945, Final residual = 8.17735e-08, No Iterations 11
994 CG: Solving for pd, Initial residual = 0.00239286, Final residual = 8.03894e-08, No Iterations 10
995 CG: Solving for pd, Initial residual = 0.00171377, Final residual = 6.83415e-08, No Iterations 10
996 mag(U): max: 2.32436 avg: 0.200347
997 time step continuity errors : sum local = 1.232e-11, global = 1.01061e-13, cumulative = -1.13571e-11
998 Calculating static pressure
999 CG: Solving for p, Initial residual = 0.000270226, Final residual = 3.82153e-08, No Iterations 8
1000 Relaxation: p = 0.1
1001 BiCGStab: Solving for alpha1, Initial residual = 5.88027e-07, Final residual = 4.9696e-11, No Iterations 1
1002 Liquid phase volume fraction = 0.500425 Min(alpha1) = -0.00444555 Max(alpha1) = 1.00191
1003 ExecutionTime = 7.3 s ClockTime = 9 s
1005 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1006 Courant Number mean: 0.00429682 max: 0.389693 velocity magnitude: 1.12661
1007 deltaT = 0.000653546
1008 Time = 0.0186929
1010 BiCGStab: Solving for Ux, Initial residual = 0.000502069, Final residual = 4.57465e-09, No Iterations 1
1011 BiCGStab: Solving for Uy, Initial residual = 0.00201363, Final residual = 2.99249e-11, No Iterations 2
1012 CG: Solving for pd, Initial residual = 0.0399923, Final residual = 6.53919e-08, No Iterations 13
1013 CG: Solving for pd, Initial residual = 0.0261318, Final residual = 9.89801e-08, No Iterations 12
1014 CG: Solving for pd, Initial residual = 0.017714, Final residual = 6.35931e-08, No Iterations 12
1015 CG: Solving for pd, Initial residual = 0.0125728, Final residual = 8.35971e-08, No Iterations 11
1016 CG: Solving for pd, Initial residual = 0.00936589, Final residual = 7.08237e-08, No Iterations 11
1017 CG: Solving for pd, Initial residual = 0.00712943, Final residual = 6.54285e-08, No Iterations 11
1018 mag(U): max: 2.35718 avg: 0.200859
1019 time step continuity errors : sum local = 1.14738e-11, global = -1.01082e-12, cumulative = -1.23679e-11
1020 BiCGStab: Solving for alpha1, Initial residual = 6.10764e-06, Final residual = 1.11546e-10, No Iterations 1
1021 Liquid phase volume fraction = 0.500425 Min(alpha1) = -0.00467646 Max(alpha1) = 1.00203
1022 BiCGStab: Solving for Ux, Initial residual = 0.000555708, Final residual = 3.84588e-09, No Iterations 1
1023 BiCGStab: Solving for Uy, Initial residual = 0.00348155, Final residual = 1.27558e-11, No Iterations 2
1024 CG: Solving for pd, Initial residual = 0.0382665, Final residual = 9.35937e-08, No Iterations 12
1025 CG: Solving for pd, Initial residual = 0.0193615, Final residual = 8.0537e-08, No Iterations 11
1026 CG: Solving for pd, Initial residual = 0.00669115, Final residual = 9.86157e-08, No Iterations 10
1027 CG: Solving for pd, Initial residual = 0.00412549, Final residual = 7.6434e-08, No Iterations 10
1028 CG: Solving for pd, Initial residual = 0.0026794, Final residual = 8.42723e-08, No Iterations 11
1029 CG: Solving for pd, Initial residual = 0.00193868, Final residual = 8.70687e-08, No Iterations 11
1030 mag(U): max: 2.33669 avg: 0.200382
1031 time step continuity errors : sum local = 1.53123e-11, global = 7.63736e-13, cumulative = -1.16042e-11
1032 Calculating static pressure
1033 CG: Solving for p, Initial residual = 0.000267838, Final residual = 3.65021e-08, No Iterations 8
1034 Relaxation: p = 0.1
1035 BiCGStab: Solving for alpha1, Initial residual = 5.52762e-07, Final residual = 4.99795e-11, No Iterations 1
1036 Liquid phase volume fraction = 0.500424 Min(alpha1) = -0.00468111 Max(alpha1) = 1.00203
1037 ExecutionTime = 7.54 s ClockTime = 9 s
1039 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1040 Courant Number mean: 0.00429608 max: 0.391882 velocity magnitude: 1.13122
1041 deltaT = 0.000653546
1042 Time = 0.0193465
1044 BiCGStab: Solving for Ux, Initial residual = 0.000495751, Final residual = 4.83886e-09, No Iterations 1
1045 BiCGStab: Solving for Uy, Initial residual = 0.00205528, Final residual = 4.94635e-11, No Iterations 2
1046 CG: Solving for pd, Initial residual = 0.0413761, Final residual = 5.49022e-08, No Iterations 13
1047 CG: Solving for pd, Initial residual = 0.0268307, Final residual = 8.48243e-08, No Iterations 12
1048 CG: Solving for pd, Initial residual = 0.0181229, Final residual = 8.57602e-08, No Iterations 11
1049 CG: Solving for pd, Initial residual = 0.0128464, Final residual = 6.4864e-08, No Iterations 11
1050 CG: Solving for pd, Initial residual = 0.00952978, Final residual = 7.04517e-08, No Iterations 11
1051 CG: Solving for pd, Initial residual = 0.00714521, Final residual = 9.73547e-08, No Iterations 10
1052 mag(U): max: 2.36833 avg: 0.200888
1053 time step continuity errors : sum local = 1.67139e-11, global = -1.75458e-12, cumulative = -1.33587e-11
1054 BiCGStab: Solving for alpha1, Initial residual = 6.16376e-06, Final residual = 1.25245e-10, No Iterations 1
1055 Liquid phase volume fraction = 0.500424 Min(alpha1) = -0.00490874 Max(alpha1) = 1.00215
1056 BiCGStab: Solving for Ux, Initial residual = 0.000545228, Final residual = 3.93723e-09, No Iterations 1
1057 BiCGStab: Solving for Uy, Initial residual = 0.00361421, Final residual = 1.51496e-11, No Iterations 2
1058 CG: Solving for pd, Initial residual = 0.0391318, Final residual = 8.3794e-08, No Iterations 12
1059 CG: Solving for pd, Initial residual = 0.0195233, Final residual = 7.94273e-08, No Iterations 11
1060 CG: Solving for pd, Initial residual = 0.00669286, Final residual = 6.63388e-08, No Iterations 11
1061 CG: Solving for pd, Initial residual = 0.00402614, Final residual = 8.71577e-08, No Iterations 10
1062 CG: Solving for pd, Initial residual = 0.00265299, Final residual = 8.83486e-08, No Iterations 11
1063 CG: Solving for pd, Initial residual = 0.00197821, Final residual = 9.01213e-08, No Iterations 10
1064 mag(U): max: 2.34832 avg: 0.200415
1065 time step continuity errors : sum local = 1.54284e-11, global = -2.4611e-13, cumulative = -1.36048e-11
1066 Calculating static pressure
1067 CG: Solving for p, Initial residual = 0.000268027, Final residual = 3.69671e-08, No Iterations 8
1068 Relaxation: p = 0.1
1069 BiCGStab: Solving for alpha1, Initial residual = 5.15445e-07, Final residual = 4.40527e-11, No Iterations 1
1070 Liquid phase volume fraction = 0.500424 Min(alpha1) = -0.00491393 Max(alpha1) = 1.00215
1071 ExecutionTime = 7.8 s ClockTime = 9 s
1073 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1074 Courant Number mean: 0.00429464 max: 0.393953 velocity magnitude: 1.1356
1075 deltaT = 0.000653546
1076 Time = 0.02
1078 BiCGStab: Solving for Ux, Initial residual = 0.000491604, Final residual = 3.97178e-09, No Iterations 1
1079 BiCGStab: Solving for Uy, Initial residual = 0.00214284, Final residual = 2.61719e-11, No Iterations 2
1080 CG: Solving for pd, Initial residual = 0.0410756, Final residual = 8.38909e-08, No Iterations 13
1081 CG: Solving for pd, Initial residual = 0.0265484, Final residual = 6.48975e-08, No Iterations 12
1082 CG: Solving for pd, Initial residual = 0.0178913, Final residual = 5.72056e-08, No Iterations 12
1083 CG: Solving for pd, Initial residual = 0.012549, Final residual = 9.26814e-08, No Iterations 11
1084 CG: Solving for pd, Initial residual = 0.00924231, Final residual = 7.11771e-08, No Iterations 11
1085 CG: Solving for pd, Initial residual = 0.00708242, Final residual = 6.01095e-08, No Iterations 11
1086 mag(U): max: 2.37874 avg: 0.200915
1087 time step continuity errors : sum local = 1.02628e-11, global = -9.23514e-13, cumulative = -1.45284e-11
1088 BiCGStab: Solving for alpha1, Initial residual = 6.21828e-06, Final residual = 1.35648e-10, No Iterations 1
1089 Liquid phase volume fraction = 0.500424 Min(alpha1) = -0.00513797 Max(alpha1) = 1.00227
1090 BiCGStab: Solving for Ux, Initial residual = 0.000534431, Final residual = 4.10371e-09, No Iterations 1
1091 BiCGStab: Solving for Uy, Initial residual = 0.00372268, Final residual = 1.88766e-11, No Iterations 2
1092 CG: Solving for pd, Initial residual = 0.0394419, Final residual = 7.01077e-08, No Iterations 13
1093 CG: Solving for pd, Initial residual = 0.0193143, Final residual = 8.22999e-08, No Iterations 11
1094 CG: Solving for pd, Initial residual = 0.0066515, Final residual = 7.51966e-08, No Iterations 12
1095 CG: Solving for pd, Initial residual = 0.00399226, Final residual = 8.17229e-08, No Iterations 11
1096 CG: Solving for pd, Initial residual = 0.00253245, Final residual = 8.21336e-08, No Iterations 11
1097 CG: Solving for pd, Initial residual = 0.00182055, Final residual = 8.14466e-08, No Iterations 10
1098 mag(U): max: 2.3593 avg: 0.200447
1099 time step continuity errors : sum local = 1.39554e-11, global = 3.46455e-13, cumulative = -1.41819e-11
1100 Calculating static pressure
1101 CG: Solving for p, Initial residual = 0.000264963, Final residual = 7.84389e-08, No Iterations 7
1102 Relaxation: p = 0.1
1103 BiCGStab: Solving for alpha1, Initial residual = 5.13305e-07, Final residual = 3.45875e-11, No Iterations 1
1104 Liquid phase volume fraction = 0.500423 Min(alpha1) = -0.00514289 Max(alpha1) = 1.00227
1105 ExecutionTime = 8.11 s ClockTime = 9 s
1107 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1108 Courant Number mean: 0.00429301 max: 0.395918 velocity magnitude: 1.13977
1109 deltaT = 0.000645161
1110 Time = 0.0206452
1112 BiCGStab: Solving for Ux, Initial residual = 0.00048299, Final residual = 3.03242e-09, No Iterations 1
1113 BiCGStab: Solving for Uy, Initial residual = 0.00218339, Final residual = 2.4456e-12, No Iterations 2
1114 CG: Solving for pd, Initial residual = 0.0421411, Final residual = 7.04303e-08, No Iterations 13
1115 CG: Solving for pd, Initial residual = 0.0269323, Final residual = 8.51494e-08, No Iterations 12
1116 CG: Solving for pd, Initial residual = 0.0180645, Final residual = 9.33586e-08, No Iterations 11
1117 CG: Solving for pd, Initial residual = 0.0126846, Final residual = 7.66989e-08, No Iterations 11
1118 CG: Solving for pd, Initial residual = 0.00924752, Final residual = 8.93789e-08, No Iterations 11
1119 CG: Solving for pd, Initial residual = 0.00701533, Final residual = 7.88984e-08, No Iterations 11
1120 mag(U): max: 2.38855 avg: 0.200942
1121 time step continuity errors : sum local = 1.32456e-11, global = -1.24045e-12, cumulative = -1.54223e-11
1122 BiCGStab: Solving for alpha1, Initial residual = 6.1696e-06, Final residual = 1.27545e-10, No Iterations 1
1123 Liquid phase volume fraction = 0.500423 Min(alpha1) = -0.00535955 Max(alpha1) = 1.00239
1124 BiCGStab: Solving for Ux, Initial residual = 0.00052119, Final residual = 4.03662e-09, No Iterations 1
1125 BiCGStab: Solving for Uy, Initial residual = 0.00377375, Final residual = 1.84644e-11, No Iterations 2
1126 CG: Solving for pd, Initial residual = 0.0397776, Final residual = 9.50293e-08, No Iterations 12
1127 CG: Solving for pd, Initial residual = 0.0189742, Final residual = 7.59476e-08, No Iterations 11
1128 CG: Solving for pd, Initial residual = 0.00644156, Final residual = 9.07715e-08, No Iterations 10
1129 CG: Solving for pd, Initial residual = 0.00393284, Final residual = 8.99299e-08, No Iterations 11
1130 CG: Solving for pd, Initial residual = 0.0024924, Final residual = 7.55302e-08, No Iterations 11
1131 CG: Solving for pd, Initial residual = 0.00179251, Final residual = 8.57518e-08, No Iterations 10
1132 mag(U): max: 2.36963 avg: 0.200479
1133 time step continuity errors : sum local = 1.44922e-11, global = -1.0523e-13, cumulative = -1.55276e-11
1134 Calculating static pressure
1135 CG: Solving for p, Initial residual = 0.000267186, Final residual = 7.21853e-08, No Iterations 7
1136 Relaxation: p = 0.1
1137 BiCGStab: Solving for alpha1, Initial residual = 5.42112e-07, Final residual = 2.9591e-11, No Iterations 1
1138 Liquid phase volume fraction = 0.500423 Min(alpha1) = -0.00536331 Max(alpha1) = 1.00239
1139 ExecutionTime = 8.37 s ClockTime = 10 s
1141 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1142 Courant Number mean: 0.00423741 max: 0.39262 velocity magnitude: 1.14355
1143 deltaT = 0.000645161
1144 Time = 0.0212903
1146 BiCGStab: Solving for Ux, Initial residual = 0.000481185, Final residual = 3.00459e-09, No Iterations 1
1147 BiCGStab: Solving for Uy, Initial residual = 0.00223379, Final residual = 2.55838e-10, No Iterations 2
1148 CG: Solving for pd, Initial residual = 0.0424393, Final residual = 6.99621e-08, No Iterations 13
1149 CG: Solving for pd, Initial residual = 0.0276323, Final residual = 8.61998e-08, No Iterations 12
1150 CG: Solving for pd, Initial residual = 0.0184578, Final residual = 9.43946e-08, No Iterations 11
1151 CG: Solving for pd, Initial residual = 0.0128814, Final residual = 7.33465e-08, No Iterations 11
1152 CG: Solving for pd, Initial residual = 0.00931284, Final residual = 7.97512e-08, No Iterations 11
1153 CG: Solving for pd, Initial residual = 0.00697697, Final residual = 7.57918e-08, No Iterations 11
1154 mag(U): max: 2.39771 avg: 0.200965
1155 time step continuity errors : sum local = 1.26831e-11, global = -7.54831e-13, cumulative = -1.62824e-11
1156 BiCGStab: Solving for alpha1, Initial residual = 6.16133e-06, Final residual = 1.21064e-10, No Iterations 1
1157 Liquid phase volume fraction = 0.500423 Min(alpha1) = -0.00557594 Max(alpha1) = 1.00251
1158 BiCGStab: Solving for Ux, Initial residual = 0.000510498, Final residual = 3.8968e-09, No Iterations 1
1159 BiCGStab: Solving for Uy, Initial residual = 0.00380424, Final residual = 1.65205e-11, No Iterations 2
1160 CG: Solving for pd, Initial residual = 0.03945, Final residual = 8.77468e-08, No Iterations 12
1161 CG: Solving for pd, Initial residual = 0.0193634, Final residual = 8.11181e-08, No Iterations 11
1162 CG: Solving for pd, Initial residual = 0.00672379, Final residual = 7.90927e-08, No Iterations 12
1163 CG: Solving for pd, Initial residual = 0.00412169, Final residual = 6.92001e-08, No Iterations 12
1164 CG: Solving for pd, Initial residual = 0.00262003, Final residual = 7.70412e-08, No Iterations 11
1165 CG: Solving for pd, Initial residual = 0.00196282, Final residual = 8.92052e-08, No Iterations 10
1166 mag(U): max: 2.3792 avg: 0.200504
1167 time step continuity errors : sum local = 1.49877e-11, global = 1.70772e-13, cumulative = -1.61116e-11
1168 Calculating static pressure
1169 CG: Solving for p, Initial residual = 0.000266391, Final residual = 6.8358e-08, No Iterations 7
1170 Relaxation: p = 0.1
1171 BiCGStab: Solving for alpha1, Initial residual = 5.81499e-07, Final residual = 3.41668e-11, No Iterations 1
1172 Liquid phase volume fraction = 0.500422 Min(alpha1) = -0.00557858 Max(alpha1) = 1.00251
1173 ExecutionTime = 8.63 s ClockTime = 10 s
1175 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1176 Courant Number mean: 0.004237 max: 0.394282 velocity magnitude: 1.14706
1177 deltaT = 0.000645161
1178 Time = 0.0219355
1180 BiCGStab: Solving for Ux, Initial residual = 0.000472956, Final residual = 3.28121e-09, No Iterations 1
1181 BiCGStab: Solving for Uy, Initial residual = 0.00223942, Final residual = 1.5468e-10, No Iterations 2
1182 CG: Solving for pd, Initial residual = 0.0434477, Final residual = 8.02413e-08, No Iterations 13
1183 CG: Solving for pd, Initial residual = 0.0281961, Final residual = 8.65808e-08, No Iterations 12
1184 CG: Solving for pd, Initial residual = 0.0188728, Final residual = 9.60269e-08, No Iterations 11
1185 CG: Solving for pd, Initial residual = 0.0132079, Final residual = 7.67375e-08, No Iterations 11
1186 CG: Solving for pd, Initial residual = 0.00956425, Final residual = 8.1355e-08, No Iterations 11
1187 CG: Solving for pd, Initial residual = 0.00713433, Final residual = 7.30073e-08, No Iterations 11
1188 mag(U): max: 2.40607 avg: 0.200986
1189 time step continuity errors : sum local = 1.20779e-11, global = -1.00744e-12, cumulative = -1.71191e-11
1190 BiCGStab: Solving for alpha1, Initial residual = 6.09343e-06, Final residual = 1.16654e-10, No Iterations 1
1191 Liquid phase volume fraction = 0.500422 Min(alpha1) = -0.00578708 Max(alpha1) = 1.00263
1192 BiCGStab: Solving for Ux, Initial residual = 0.000500566, Final residual = 3.65931e-09, No Iterations 1
1193 BiCGStab: Solving for Uy, Initial residual = 0.00383824, Final residual = 1.49029e-11, No Iterations 2
1194 CG: Solving for pd, Initial residual = 0.0394607, Final residual = 6.1651e-08, No Iterations 13
1195 CG: Solving for pd, Initial residual = 0.0196066, Final residual = 8.23653e-08, No Iterations 11
1196 CG: Solving for pd, Initial residual = 0.00690487, Final residual = 9.33054e-08, No Iterations 10
1197 CG: Solving for pd, Initial residual = 0.00421198, Final residual = 7.66458e-08, No Iterations 12
1198 CG: Solving for pd, Initial residual = 0.00267096, Final residual = 8.98807e-08, No Iterations 11
1199 CG: Solving for pd, Initial residual = 0.00198101, Final residual = 9.4849e-08, No Iterations 9
1200 mag(U): max: 2.38776 avg: 0.200526
1201 time step continuity errors : sum local = 1.56224e-11, global = -1.36882e-12, cumulative = -1.84879e-11
1202 Calculating static pressure
1203 CG: Solving for p, Initial residual = 0.000259242, Final residual = 9.72878e-08, No Iterations 7
1204 Relaxation: p = 0.1
1205 BiCGStab: Solving for alpha1, Initial residual = 5.26968e-07, Final residual = 3.50486e-11, No Iterations 1
1206 Liquid phase volume fraction = 0.500422 Min(alpha1) = -0.00578936 Max(alpha1) = 1.00263
1207 ExecutionTime = 8.89 s ClockTime = 10 s
1209 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1210 Courant Number mean: 0.00423604 max: 0.395774 velocity magnitude: 1.15024
1211 deltaT = 0.000645161
1212 Time = 0.0225806
1214 BiCGStab: Solving for Ux, Initial residual = 0.000457572, Final residual = 3.82162e-09, No Iterations 1
1215 BiCGStab: Solving for Uy, Initial residual = 0.00226106, Final residual = 2.60747e-11, No Iterations 2
1216 CG: Solving for pd, Initial residual = 0.0450653, Final residual = 5.9931e-08, No Iterations 13
1217 CG: Solving for pd, Initial residual = 0.0291269, Final residual = 7.36125e-08, No Iterations 12
1218 CG: Solving for pd, Initial residual = 0.0193872, Final residual = 7.00119e-08, No Iterations 12
1219 CG: Solving for pd, Initial residual = 0.0136077, Final residual = 9.13763e-08, No Iterations 11
1220 CG: Solving for pd, Initial residual = 0.00975965, Final residual = 7.7187e-08, No Iterations 11
1221 CG: Solving for pd, Initial residual = 0.00734169, Final residual = 7.97805e-08, No Iterations 11
1222 mag(U): max: 2.41359 avg: 0.201003
1223 time step continuity errors : sum local = 1.29271e-11, global = -9.37415e-13, cumulative = -1.94253e-11
1224 BiCGStab: Solving for alpha1, Initial residual = 6.12242e-06, Final residual = 1.0694e-10, No Iterations 1
1225 Liquid phase volume fraction = 0.500422 Min(alpha1) = -0.00599348 Max(alpha1) = 1.00275
1226 BiCGStab: Solving for Ux, Initial residual = 0.000492598, Final residual = 3.62404e-09, No Iterations 1
1227 BiCGStab: Solving for Uy, Initial residual = 0.00397675, Final residual = 1.51063e-11, No Iterations 2
1228 CG: Solving for pd, Initial residual = 0.0406844, Final residual = 9.94306e-08, No Iterations 12
1229 CG: Solving for pd, Initial residual = 0.0198231, Final residual = 8.21491e-08, No Iterations 11
1230 CG: Solving for pd, Initial residual = 0.00714193, Final residual = 9.35902e-08, No Iterations 10
1231 CG: Solving for pd, Initial residual = 0.00433873, Final residual = 8.8693e-08, No Iterations 10
1232 CG: Solving for pd, Initial residual = 0.00278085, Final residual = 8.45056e-08, No Iterations 11
1233 CG: Solving for pd, Initial residual = 0.00201636, Final residual = 8.95305e-08, No Iterations 10
1234 mag(U): max: 2.39531 avg: 0.200544
1235 time step continuity errors : sum local = 1.42401e-11, global = 3.09557e-13, cumulative = -1.91158e-11
1236 Calculating static pressure
1237 CG: Solving for p, Initial residual = 0.000259616, Final residual = 8.35833e-08, No Iterations 7
1238 Relaxation: p = 0.1
1239 BiCGStab: Solving for alpha1, Initial residual = 4.95323e-07, Final residual = 3.42101e-11, No Iterations 1
1240 Liquid phase volume fraction = 0.500421 Min(alpha1) = -0.00599545 Max(alpha1) = 1.00275
1241 ExecutionTime = 9.15 s ClockTime = 11 s
1243 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1244 Courant Number mean: 0.00423517 max: 0.397091 velocity magnitude: 1.15306
1245 deltaT = 0.000645161
1246 Time = 0.0232258
1248 BiCGStab: Solving for Ux, Initial residual = 0.000453151, Final residual = 4.21071e-09, No Iterations 1
1249 BiCGStab: Solving for Uy, Initial residual = 0.00235417, Final residual = 6.19265e-11, No Iterations 2
1250 CG: Solving for pd, Initial residual = 0.0453469, Final residual = 9.0892e-08, No Iterations 13
1251 CG: Solving for pd, Initial residual = 0.0293234, Final residual = 9.29408e-08, No Iterations 12
1252 CG: Solving for pd, Initial residual = 0.019768, Final residual = 6.33695e-08, No Iterations 12
1253 CG: Solving for pd, Initial residual = 0.0139767, Final residual = 9.25809e-08, No Iterations 11
1254 CG: Solving for pd, Initial residual = 0.010191, Final residual = 5.92138e-08, No Iterations 11
1255 CG: Solving for pd, Initial residual = 0.00766007, Final residual = 7.58291e-08, No Iterations 11
1256 mag(U): max: 2.42038 avg: 0.201015
1257 time step continuity errors : sum local = 1.20719e-11, global = -1.17239e-12, cumulative = -2.02881e-11
1258 BiCGStab: Solving for alpha1, Initial residual = 6.16078e-06, Final residual = 1.10063e-10, No Iterations 1
1259 Liquid phase volume fraction = 0.500421 Min(alpha1) = -0.00619513 Max(alpha1) = 1.00287
1260 BiCGStab: Solving for Ux, Initial residual = 0.000485065, Final residual = 3.64525e-09, No Iterations 1
1261 BiCGStab: Solving for Uy, Initial residual = 0.00418733, Final residual = 1.52939e-11, No Iterations 2
1262 CG: Solving for pd, Initial residual = 0.0417622, Final residual = 7.33523e-08, No Iterations 13
1263 CG: Solving for pd, Initial residual = 0.0199746, Final residual = 8.41346e-08, No Iterations 11
1264 CG: Solving for pd, Initial residual = 0.00715169, Final residual = 9.67653e-08, No Iterations 10
1265 CG: Solving for pd, Initial residual = 0.00421467, Final residual = 7.65746e-08, No Iterations 12
1266 CG: Solving for pd, Initial residual = 0.00266828, Final residual = 7.86222e-08, No Iterations 11
1267 CG: Solving for pd, Initial residual = 0.00180329, Final residual = 9.53956e-08, No Iterations 9
1268 mag(U): max: 2.40195 avg: 0.200568
1269 time step continuity errors : sum local = 1.48967e-11, global = -1.02534e-12, cumulative = -2.13135e-11
1270 Calculating static pressure
1271 CG: Solving for p, Initial residual = 0.000257088, Final residual = 7.69928e-08, No Iterations 7
1272 Relaxation: p = 0.1
1273 BiCGStab: Solving for alpha1, Initial residual = 4.80052e-07, Final residual = 3.09286e-11, No Iterations 1
1274 Liquid phase volume fraction = 0.500421 Min(alpha1) = -0.00619483 Max(alpha1) = 1.00287
1275 ExecutionTime = 9.4 s ClockTime = 11 s
1277 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1278 Courant Number mean: 0.00423365 max: 0.398257 velocity magnitude: 1.15555
1279 deltaT = 0.000645161
1280 Time = 0.023871
1282 BiCGStab: Solving for Ux, Initial residual = 0.000452312, Final residual = 3.72907e-09, No Iterations 1
1283 BiCGStab: Solving for Uy, Initial residual = 0.00249304, Final residual = 6.08129e-11, No Iterations 2
1284 CG: Solving for pd, Initial residual = 0.0454881, Final residual = 8.19903e-08, No Iterations 13
1285 CG: Solving for pd, Initial residual = 0.0291858, Final residual = 8.31746e-08, No Iterations 12
1286 CG: Solving for pd, Initial residual = 0.019514, Final residual = 5.62049e-08, No Iterations 12
1287 CG: Solving for pd, Initial residual = 0.0136423, Final residual = 8.90174e-08, No Iterations 11
1288 CG: Solving for pd, Initial residual = 0.00999658, Final residual = 8.24306e-08, No Iterations 11
1289 CG: Solving for pd, Initial residual = 0.00758222, Final residual = 7.83269e-08, No Iterations 11
1290 mag(U): max: 2.42639 avg: 0.201031
1291 time step continuity errors : sum local = 1.24034e-11, global = -9.6959e-13, cumulative = -2.22831e-11
1292 BiCGStab: Solving for alpha1, Initial residual = 6.19507e-06, Final residual = 1.19992e-10, No Iterations 1
1293 Liquid phase volume fraction = 0.500421 Min(alpha1) = -0.00638881 Max(alpha1) = 1.00299
1294 BiCGStab: Solving for Ux, Initial residual = 0.000477103, Final residual = 3.73058e-09, No Iterations 1
1295 BiCGStab: Solving for Uy, Initial residual = 0.0043895, Final residual = 1.88551e-11, No Iterations 2
1296 CG: Solving for pd, Initial residual = 0.042154, Final residual = 6.93861e-08, No Iterations 13
1297 CG: Solving for pd, Initial residual = 0.0199877, Final residual = 8.22649e-08, No Iterations 11
1298 CG: Solving for pd, Initial residual = 0.00697255, Final residual = 8.29154e-08, No Iterations 11
1299 CG: Solving for pd, Initial residual = 0.00415606, Final residual = 8.06178e-08, No Iterations 12
1300 CG: Solving for pd, Initial residual = 0.00259108, Final residual = 7.92183e-08, No Iterations 11
1301 CG: Solving for pd, Initial residual = 0.0017207, Final residual = 9.70587e-08, No Iterations 10
1302 mag(U): max: 2.40797 avg: 0.20059
1303 time step continuity errors : sum local = 1.51245e-11, global = -8.27224e-14, cumulative = -2.23658e-11
1304 Calculating static pressure
1305 CG: Solving for p, Initial residual = 0.00025366, Final residual = 7.39607e-08, No Iterations 7
1306 Relaxation: p = 0.1
1307 BiCGStab: Solving for alpha1, Initial residual = 4.56999e-07, Final residual = 2.80244e-11, No Iterations 1
1308 Liquid phase volume fraction = 0.500421 Min(alpha1) = -0.00638691 Max(alpha1) = 1.00299
1309 ExecutionTime = 9.66 s ClockTime = 11 s
1311 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1312 Courant Number mean: 0.00423166 max: 0.399324 velocity magnitude: 1.15781
1313 deltaT = 0.000645161
1314 Time = 0.0245161
1316 BiCGStab: Solving for Ux, Initial residual = 0.00045361, Final residual = 2.92921e-09, No Iterations 1
1317 BiCGStab: Solving for Uy, Initial residual = 0.00264684, Final residual = 3.74654e-11, No Iterations 2
1318 CG: Solving for pd, Initial residual = 0.0463862, Final residual = 7.37044e-08, No Iterations 13
1319 CG: Solving for pd, Initial residual = 0.0297426, Final residual = 8.94118e-08, No Iterations 12
1320 CG: Solving for pd, Initial residual = 0.0197345, Final residual = 8.50389e-08, No Iterations 12
1321 CG: Solving for pd, Initial residual = 0.0136712, Final residual = 7.58338e-08, No Iterations 11
1322 CG: Solving for pd, Initial residual = 0.00972862, Final residual = 7.00827e-08, No Iterations 11
1323 CG: Solving for pd, Initial residual = 0.00723823, Final residual = 6.67563e-08, No Iterations 12
1324 mag(U): max: 2.43183 avg: 0.201049
1325 time step continuity errors : sum local = 1.05772e-11, global = -8.35513e-13, cumulative = -2.32013e-11
1326 BiCGStab: Solving for alpha1, Initial residual = 6.22597e-06, Final residual = 1.22638e-10, No Iterations 1
1327 Liquid phase volume fraction = 0.50042 Min(alpha1) = -0.00657477 Max(alpha1) = 1.00311
1328 BiCGStab: Solving for Ux, Initial residual = 0.000468341, Final residual = 3.79451e-09, No Iterations 1
1329 BiCGStab: Solving for Uy, Initial residual = 0.00456101, Final residual = 2.37783e-11, No Iterations 2
1330 CG: Solving for pd, Initial residual = 0.042916, Final residual = 6.22177e-08, No Iterations 13
1331 CG: Solving for pd, Initial residual = 0.0192381, Final residual = 9.3792e-08, No Iterations 11
1332 CG: Solving for pd, Initial residual = 0.00658744, Final residual = 7.17549e-08, No Iterations 12
1333 CG: Solving for pd, Initial residual = 0.00385377, Final residual = 9.95553e-08, No Iterations 12
1334 CG: Solving for pd, Initial residual = 0.00235598, Final residual = 7.89043e-08, No Iterations 11
1335 CG: Solving for pd, Initial residual = 0.00153994, Final residual = 6.51678e-08, No Iterations 11
1336 mag(U): max: 2.41345 avg: 0.20061
1337 time step continuity errors : sum local = 1.02792e-11, global = 3.79623e-13, cumulative = -2.28217e-11
1338 Calculating static pressure
1339 CG: Solving for p, Initial residual = 0.000249235, Final residual = 6.27467e-08, No Iterations 7
1340 Relaxation: p = 0.1
1341 BiCGStab: Solving for alpha1, Initial residual = 4.69038e-07, Final residual = 2.26428e-11, No Iterations 1
1342 Liquid phase volume fraction = 0.50042 Min(alpha1) = -0.00657024 Max(alpha1) = 1.00311
1343 ExecutionTime = 9.93 s ClockTime = 11 s
1345 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1346 Courant Number mean: 0.00422979 max: 0.400305 velocity magnitude: 1.15987
1347 deltaT = 0.000619355
1348 Time = 0.0251355
1350 BiCGStab: Solving for Ux, Initial residual = 0.000437665, Final residual = 2.42361e-09, No Iterations 1
1351 BiCGStab: Solving for Uy, Initial residual = 0.00265253, Final residual = 4.75773e-11, No Iterations 2
1352 CG: Solving for pd, Initial residual = 0.047604, Final residual = 6.81827e-08, No Iterations 13
1353 CG: Solving for pd, Initial residual = 0.0303162, Final residual = 8.35602e-08, No Iterations 12
1354 CG: Solving for pd, Initial residual = 0.020151, Final residual = 8.94302e-08, No Iterations 11
1355 CG: Solving for pd, Initial residual = 0.013854, Final residual = 7.37692e-08, No Iterations 11
1356 CG: Solving for pd, Initial residual = 0.0097549, Final residual = 6.33803e-08, No Iterations 11
1357 CG: Solving for pd, Initial residual = 0.00726158, Final residual = 5.81791e-08, No Iterations 11
1358 mag(U): max: 2.43727 avg: 0.201069
1359 time step continuity errors : sum local = 8.72997e-12, global = -1.68323e-12, cumulative = -2.45049e-11
1360 BiCGStab: Solving for alpha1, Initial residual = 5.9953e-06, Final residual = 1.01222e-10, No Iterations 1
1361 Liquid phase volume fraction = 0.50042 Min(alpha1) = -0.00674344 Max(alpha1) = 1.00322
1362 BiCGStab: Solving for Ux, Initial residual = 0.000453465, Final residual = 3.43719e-09, No Iterations 1
1363 BiCGStab: Solving for Uy, Initial residual = 0.00459209, Final residual = 2.06463e-11, No Iterations 2
1364 CG: Solving for pd, Initial residual = 0.0434076, Final residual = 6.16353e-08, No Iterations 13
1365 CG: Solving for pd, Initial residual = 0.0198352, Final residual = 9.58796e-08, No Iterations 11
1366 CG: Solving for pd, Initial residual = 0.00681803, Final residual = 9.61917e-08, No Iterations 11
1367 CG: Solving for pd, Initial residual = 0.00389595, Final residual = 8.84696e-08, No Iterations 11
1368 CG: Solving for pd, Initial residual = 0.00244236, Final residual = 7.93145e-08, No Iterations 11
1369 CG: Solving for pd, Initial residual = 0.00169897, Final residual = 7.38728e-08, No Iterations 10
1370 mag(U): max: 2.41932 avg: 0.200634
1371 time step continuity errors : sum local = 1.09473e-11, global = -3.46474e-13, cumulative = -2.48514e-11
1372 Calculating static pressure
1373 CG: Solving for p, Initial residual = 0.000260677, Final residual = 6.54236e-08, No Iterations 7
1374 Relaxation: p = 0.1
1375 BiCGStab: Solving for alpha1, Initial residual = 4.69549e-07, Final residual = 1.88596e-11, No Iterations 1
1376 Liquid phase volume fraction = 0.50042 Min(alpha1) = -0.00673599 Max(alpha1) = 1.00322
1377 ExecutionTime = 10.19 s ClockTime = 12 s
1379 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1380 Courant Number mean: 0.00405951 max: 0.385174 velocity magnitude: 1.16153
1381 deltaT = 0.000619355
1382 Time = 0.0257548
1384 BiCGStab: Solving for Ux, Initial residual = 0.000441453, Final residual = 2.52693e-09, No Iterations 1
1385 BiCGStab: Solving for Uy, Initial residual = 0.00273289, Final residual = 1.55747e-10, No Iterations 2
1386 CG: Solving for pd, Initial residual = 0.0475777, Final residual = 9.22961e-08, No Iterations 13
1387 CG: Solving for pd, Initial residual = 0.0304456, Final residual = 9.24929e-08, No Iterations 12
1388 CG: Solving for pd, Initial residual = 0.0201757, Final residual = 7.7393e-08, No Iterations 12
1389 CG: Solving for pd, Initial residual = 0.0138897, Final residual = 7.92295e-08, No Iterations 11
1390 CG: Solving for pd, Initial residual = 0.00987618, Final residual = 6.76746e-08, No Iterations 11
1391 CG: Solving for pd, Initial residual = 0.00733208, Final residual = 6.42776e-08, No Iterations 11
1392 mag(U): max: 2.44251 avg: 0.201086
1393 time step continuity errors : sum local = 9.55543e-12, global = -1.27745e-12, cumulative = -2.61289e-11
1394 BiCGStab: Solving for alpha1, Initial residual = 5.97587e-06, Final residual = 9.7964e-11, No Iterations 1
1395 Liquid phase volume fraction = 0.500419 Min(alpha1) = -0.00690507 Max(alpha1) = 1.00334
1396 BiCGStab: Solving for Ux, Initial residual = 0.000445119, Final residual = 3.35784e-09, No Iterations 1
1397 BiCGStab: Solving for Uy, Initial residual = 0.00464379, Final residual = 1.99281e-11, No Iterations 2
1398 CG: Solving for pd, Initial residual = 0.043528, Final residual = 6.88115e-08, No Iterations 13
1399 CG: Solving for pd, Initial residual = 0.0202883, Final residual = 8.52901e-08, No Iterations 11
1400 CG: Solving for pd, Initial residual = 0.0067498, Final residual = 9.14063e-08, No Iterations 12
1401 CG: Solving for pd, Initial residual = 0.0039444, Final residual = 9.36526e-08, No Iterations 10
1402 CG: Solving for pd, Initial residual = 0.00248412, Final residual = 8.32539e-08, No Iterations 11
1403 CG: Solving for pd, Initial residual = 0.00172169, Final residual = 9.43224e-08, No Iterations 10
1404 mag(U): max: 2.42463 avg: 0.200653
1405 time step continuity errors : sum local = 1.38015e-11, global = 3.73871e-13, cumulative = -2.5755e-11
1406 Calculating static pressure
1407 CG: Solving for p, Initial residual = 0.000257033, Final residual = 7.62007e-08, No Iterations 7
1408 Relaxation: p = 0.1
1409 BiCGStab: Solving for alpha1, Initial residual = 4.99092e-07, Final residual = 2.00604e-11, No Iterations 1
1410 Liquid phase volume fraction = 0.500419 Min(alpha1) = -0.00689484 Max(alpha1) = 1.00334
1411 ExecutionTime = 10.45 s ClockTime = 12 s
1413 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1414 Courant Number mean: 0.00405889 max: 0.385992 velocity magnitude: 1.16308
1415 deltaT = 0.000619355
1416 Time = 0.0263742
1418 BiCGStab: Solving for Ux, Initial residual = 0.000434825, Final residual = 2.75398e-09, No Iterations 1
1419 BiCGStab: Solving for Uy, Initial residual = 0.00273772, Final residual = 1.41651e-10, No Iterations 2
1420 CG: Solving for pd, Initial residual = 0.0490963, Final residual = 9.87763e-08, No Iterations 13
1421 CG: Solving for pd, Initial residual = 0.0313586, Final residual = 7.82797e-08, No Iterations 13
1422 CG: Solving for pd, Initial residual = 0.0206976, Final residual = 8.89064e-08, No Iterations 12
1423 CG: Solving for pd, Initial residual = 0.0142105, Final residual = 7.49883e-08, No Iterations 12
1424 CG: Solving for pd, Initial residual = 0.0100941, Final residual = 7.28328e-08, No Iterations 11
1425 CG: Solving for pd, Initial residual = 0.00747144, Final residual = 7.51958e-08, No Iterations 11
1426 mag(U): max: 2.44716 avg: 0.201102
1427 time step continuity errors : sum local = 1.10047e-11, global = -1.42093e-12, cumulative = -2.71759e-11
1428 BiCGStab: Solving for alpha1, Initial residual = 5.92903e-06, Final residual = 9.70243e-11, No Iterations 1
1429 Liquid phase volume fraction = 0.500419 Min(alpha1) = -0.00705914 Max(alpha1) = 1.00345
1430 BiCGStab: Solving for Ux, Initial residual = 0.000437396, Final residual = 3.28734e-09, No Iterations 1
1431 BiCGStab: Solving for Uy, Initial residual = 0.00471318, Final residual = 1.75483e-11, No Iterations 2
1432 CG: Solving for pd, Initial residual = 0.0437671, Final residual = 7.43185e-08, No Iterations 13
1433 CG: Solving for pd, Initial residual = 0.020567, Final residual = 9.00368e-08, No Iterations 11
1434 CG: Solving for pd, Initial residual = 0.00677145, Final residual = 7.89829e-08, No Iterations 12
1435 CG: Solving for pd, Initial residual = 0.00392063, Final residual = 7.56073e-08, No Iterations 12
1436 CG: Solving for pd, Initial residual = 0.00241101, Final residual = 8.5948e-08, No Iterations 10
1437 CG: Solving for pd, Initial residual = 0.0016763, Final residual = 9.39152e-08, No Iterations 10
1438 mag(U): max: 2.42917 avg: 0.200671
1439 time step continuity errors : sum local = 1.34313e-11, global = -2.50318e-13, cumulative = -2.74262e-11
1440 Calculating static pressure
1441 CG: Solving for p, Initial residual = 0.000251193, Final residual = 6.701e-08, No Iterations 7
1442 Relaxation: p = 0.1
1443 BiCGStab: Solving for alpha1, Initial residual = 4.60582e-07, Final residual = 1.92091e-11, No Iterations 1
1444 Liquid phase volume fraction = 0.500419 Min(alpha1) = -0.00704678 Max(alpha1) = 1.00345
1445 ExecutionTime = 10.72 s ClockTime = 13 s
1447 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1448 Courant Number mean: 0.00405806 max: 0.386698 velocity magnitude: 1.16445
1449 deltaT = 0.000619355
1450 Time = 0.0269935
1452 BiCGStab: Solving for Ux, Initial residual = 0.000421592, Final residual = 3.09984e-09, No Iterations 1
1453 BiCGStab: Solving for Uy, Initial residual = 0.00278424, Final residual = 5.90464e-10, No Iterations 2
1454 CG: Solving for pd, Initial residual = 0.0514346, Final residual = 9.22249e-08, No Iterations 13
1455 CG: Solving for pd, Initial residual = 0.0326493, Final residual = 6.04719e-08, No Iterations 14
1456 CG: Solving for pd, Initial residual = 0.021558, Final residual = 5.90362e-08, No Iterations 12
1457 CG: Solving for pd, Initial residual = 0.0147486, Final residual = 7.52989e-08, No Iterations 12
1458 CG: Solving for pd, Initial residual = 0.0104596, Final residual = 7.19893e-08, No Iterations 11
1459 CG: Solving for pd, Initial residual = 0.00775957, Final residual = 9.74802e-08, No Iterations 10
1460 mag(U): max: 2.45097 avg: 0.201117
1461 time step continuity errors : sum local = 1.38793e-11, global = -1.66115e-12, cumulative = -2.90874e-11
1462 BiCGStab: Solving for alpha1, Initial residual = 5.91412e-06, Final residual = 9.25061e-11, No Iterations 1
1463 Liquid phase volume fraction = 0.500418 Min(alpha1) = -0.00720651 Max(alpha1) = 1.00356
1464 BiCGStab: Solving for Ux, Initial residual = 0.000431587, Final residual = 3.17966e-09, No Iterations 1
1465 BiCGStab: Solving for Uy, Initial residual = 0.0049258, Final residual = 1.55106e-11, No Iterations 2
1466 CG: Solving for pd, Initial residual = 0.0453824, Final residual = 6.68527e-08, No Iterations 13
1467 CG: Solving for pd, Initial residual = 0.0207874, Final residual = 8.816e-08, No Iterations 11
1468 CG: Solving for pd, Initial residual = 0.00680908, Final residual = 9.74968e-08, No Iterations 10
1469 CG: Solving for pd, Initial residual = 0.00382692, Final residual = 8.24142e-08, No Iterations 12
1470 CG: Solving for pd, Initial residual = 0.00235886, Final residual = 7.92738e-08, No Iterations 11
1471 CG: Solving for pd, Initial residual = 0.00163184, Final residual = 6.99833e-08, No Iterations 11
1472 mag(U): max: 2.43224 avg: 0.200687
1473 time step continuity errors : sum local = 9.58635e-12, global = 1.8151e-13, cumulative = -2.89059e-11
1474 Calculating static pressure
1475 CG: Solving for p, Initial residual = 0.000251799, Final residual = 6.16949e-08, No Iterations 7
1476 Relaxation: p = 0.1
1477 BiCGStab: Solving for alpha1, Initial residual = 4.24391e-07, Final residual = 1.75502e-11, No Iterations 1
1478 Liquid phase volume fraction = 0.500418 Min(alpha1) = -0.00719299 Max(alpha1) = 1.00356
1479 ExecutionTime = 10.98 s ClockTime = 13 s
1481 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1482 Courant Number mean: 0.004057 max: 0.387145 velocity magnitude: 1.16543
1483 deltaT = 0.000619355
1484 Time = 0.0276129
1486 BiCGStab: Solving for Ux, Initial residual = 0.000413733, Final residual = 3.52334e-09, No Iterations 1
1487 BiCGStab: Solving for Uy, Initial residual = 0.0029227, Final residual = 7.14222e-11, No Iterations 2
1488 CG: Solving for pd, Initial residual = 0.0526385, Final residual = 8.54259e-08, No Iterations 13
1489 CG: Solving for pd, Initial residual = 0.0334827, Final residual = 8.031e-08, No Iterations 12
1490 CG: Solving for pd, Initial residual = 0.0221091, Final residual = 6.12861e-08, No Iterations 12
1491 CG: Solving for pd, Initial residual = 0.0152279, Final residual = 8.50698e-08, No Iterations 11
1492 CG: Solving for pd, Initial residual = 0.0107708, Final residual = 7.93891e-08, No Iterations 11
1493 CG: Solving for pd, Initial residual = 0.00788461, Final residual = 8.03123e-08, No Iterations 11
1494 mag(U): max: 2.45341 avg: 0.201128
1495 time step continuity errors : sum local = 1.11651e-11, global = -1.68344e-12, cumulative = -3.05893e-11
1496 BiCGStab: Solving for alpha1, Initial residual = 5.94854e-06, Final residual = 8.71302e-11, No Iterations 1
1497 Liquid phase volume fraction = 0.500418 Min(alpha1) = -0.00734808 Max(alpha1) = 1.00367
1498 BiCGStab: Solving for Ux, Initial residual = 0.000426019, Final residual = 3.08483e-09, No Iterations 1
1499 BiCGStab: Solving for Uy, Initial residual = 0.00521105, Final residual = 1.24412e-11, No Iterations 2
1500 CG: Solving for pd, Initial residual = 0.047254, Final residual = 7.43778e-08, No Iterations 13
1501 CG: Solving for pd, Initial residual = 0.0211086, Final residual = 7.18861e-08, No Iterations 12
1502 CG: Solving for pd, Initial residual = 0.006952, Final residual = 8.83469e-08, No Iterations 11
1503 CG: Solving for pd, Initial residual = 0.00382155, Final residual = 8.20583e-08, No Iterations 12
1504 CG: Solving for pd, Initial residual = 0.00235275, Final residual = 9.59886e-08, No Iterations 11
1505 CG: Solving for pd, Initial residual = 0.00159951, Final residual = 8.7646e-08, No Iterations 10
1506 mag(U): max: 2.43468 avg: 0.2007
1507 time step continuity errors : sum local = 1.16304e-11, global = -4.17818e-13, cumulative = -3.10071e-11
1508 Calculating static pressure
1509 CG: Solving for p, Initial residual = 0.00024958, Final residual = 5.6187e-08, No Iterations 7
1510 Relaxation: p = 0.1
1511 BiCGStab: Solving for alpha1, Initial residual = 4.08348e-07, Final residual = 1.61851e-11, No Iterations 1
1512 Liquid phase volume fraction = 0.500418 Min(alpha1) = -0.00733398 Max(alpha1) = 1.00367
1513 ExecutionTime = 11.25 s ClockTime = 13 s
1515 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1516 Courant Number mean: 0.0040554 max: 0.387511 velocity magnitude: 1.1662
1517 deltaT = 0.000619355
1518 Time = 0.0282323
1520 BiCGStab: Solving for Ux, Initial residual = 0.000411187, Final residual = 3.45856e-09, No Iterations 1
1521 BiCGStab: Solving for Uy, Initial residual = 0.00309019, Final residual = 8.83087e-11, No Iterations 2
1522 CG: Solving for pd, Initial residual = 0.0525069, Final residual = 7.30613e-08, No Iterations 13
1523 CG: Solving for pd, Initial residual = 0.033289, Final residual = 9.05536e-08, No Iterations 12
1524 CG: Solving for pd, Initial residual = 0.0217997, Final residual = 6.47794e-08, No Iterations 12
1525 CG: Solving for pd, Initial residual = 0.0150325, Final residual = 9.30722e-08, No Iterations 11
1526 CG: Solving for pd, Initial residual = 0.010788, Final residual = 8.19152e-08, No Iterations 11
1527 CG: Solving for pd, Initial residual = 0.00805728, Final residual = 7.91846e-08, No Iterations 11
1528 mag(U): max: 2.45534 avg: 0.201139
1529 time step continuity errors : sum local = 1.08924e-11, global = -1.65399e-12, cumulative = -3.26611e-11
1530 BiCGStab: Solving for alpha1, Initial residual = 5.96459e-06, Final residual = 9.04222e-11, No Iterations 1
1531 Liquid phase volume fraction = 0.500418 Min(alpha1) = -0.00748437 Max(alpha1) = 1.00378
1532 BiCGStab: Solving for Ux, Initial residual = 0.000419844, Final residual = 3.13763e-09, No Iterations 1
1533 BiCGStab: Solving for Uy, Initial residual = 0.00546966, Final residual = 1.08182e-11, No Iterations 2
1534 CG: Solving for pd, Initial residual = 0.0482198, Final residual = 8.61337e-08, No Iterations 13
1535 CG: Solving for pd, Initial residual = 0.0216726, Final residual = 8.30294e-08, No Iterations 12
1536 CG: Solving for pd, Initial residual = 0.00698677, Final residual = 9.47764e-08, No Iterations 10
1537 CG: Solving for pd, Initial residual = 0.00402991, Final residual = 8.45646e-08, No Iterations 11
1538 CG: Solving for pd, Initial residual = 0.00251127, Final residual = 9.03645e-08, No Iterations 12
1539 CG: Solving for pd, Initial residual = 0.00175278, Final residual = 9.27083e-08, No Iterations 11
1540 mag(U): max: 2.43645 avg: 0.200711
1541 time step continuity errors : sum local = 1.21867e-11, global = -1.17341e-13, cumulative = -3.27785e-11
1542 Calculating static pressure
1543 CG: Solving for p, Initial residual = 0.000244589, Final residual = 5.91681e-08, No Iterations 7
1544 Relaxation: p = 0.1
1545 BiCGStab: Solving for alpha1, Initial residual = 4.24906e-07, Final residual = 1.51723e-11, No Iterations 1
1546 Liquid phase volume fraction = 0.500418 Min(alpha1) = -0.00746913 Max(alpha1) = 1.00378
1547 ExecutionTime = 11.51 s ClockTime = 14 s
1549 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1550 Courant Number mean: 0.00405327 max: 0.387779 velocity magnitude: 1.16676
1551 deltaT = 0.000619355
1552 Time = 0.0288516
1554 BiCGStab: Solving for Ux, Initial residual = 0.000412145, Final residual = 2.95421e-09, No Iterations 1
1555 BiCGStab: Solving for Uy, Initial residual = 0.00330685, Final residual = 6.2814e-11, No Iterations 2
1556 CG: Solving for pd, Initial residual = 0.0525507, Final residual = 8.1081e-08, No Iterations 13
1557 CG: Solving for pd, Initial residual = 0.0330458, Final residual = 9.14351e-08, No Iterations 12
1558 CG: Solving for pd, Initial residual = 0.021552, Final residual = 5.75847e-08, No Iterations 12
1559 CG: Solving for pd, Initial residual = 0.0148733, Final residual = 9.65417e-08, No Iterations 11
1560 CG: Solving for pd, Initial residual = 0.0105658, Final residual = 9.32979e-08, No Iterations 11
1561 CG: Solving for pd, Initial residual = 0.00786092, Final residual = 7.29517e-08, No Iterations 11
1562 mag(U): max: 2.45667 avg: 0.201149
1563 time step continuity errors : sum local = 1.00084e-11, global = -1.75975e-12, cumulative = -3.45382e-11
1564 BiCGStab: Solving for alpha1, Initial residual = 5.98699e-06, Final residual = 9.52431e-11, No Iterations 1
1565 Liquid phase volume fraction = 0.500417 Min(alpha1) = -0.00761462 Max(alpha1) = 1.00389
1566 BiCGStab: Solving for Ux, Initial residual = 0.000413275, Final residual = 3.232e-09, No Iterations 1
1567 BiCGStab: Solving for Uy, Initial residual = 0.0055921, Final residual = 1.39413e-11, No Iterations 2
1568 CG: Solving for pd, Initial residual = 0.0487306, Final residual = 9.45574e-08, No Iterations 12
1569 CG: Solving for pd, Initial residual = 0.021311, Final residual = 9.01583e-08, No Iterations 11
1570 CG: Solving for pd, Initial residual = 0.00718587, Final residual = 7.81509e-08, No Iterations 11
1571 CG: Solving for pd, Initial residual = 0.004086, Final residual = 9.03347e-08, No Iterations 11
1572 CG: Solving for pd, Initial residual = 0.00257316, Final residual = 6.87643e-08, No Iterations 11
1573 CG: Solving for pd, Initial residual = 0.00173234, Final residual = 8.96476e-08, No Iterations 11
1574 mag(U): max: 2.43774 avg: 0.200721
1575 time step continuity errors : sum local = 1.17798e-11, global = -2.18478e-13, cumulative = -3.47567e-11
1576 Calculating static pressure
1577 CG: Solving for p, Initial residual = 0.000235611, Final residual = 6.08209e-08, No Iterations 7
1578 Relaxation: p = 0.1
1579 BiCGStab: Solving for alpha1, Initial residual = 3.97311e-07, Final residual = 1.44652e-11, No Iterations 1
1580 Liquid phase volume fraction = 0.500417 Min(alpha1) = -0.00759712 Max(alpha1) = 1.00389
1581 ExecutionTime = 11.77 s ClockTime = 14 s
1583 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1584 Courant Number mean: 0.00405109 max: 0.38798 velocity magnitude: 1.16716
1585 deltaT = 0.000619355
1586 Time = 0.029471
1588 BiCGStab: Solving for Ux, Initial residual = 0.000414638, Final residual = 2.67823e-09, No Iterations 1
1589 BiCGStab: Solving for Uy, Initial residual = 0.00349513, Final residual = 3.29812e-11, No Iterations 2
1590 CG: Solving for pd, Initial residual = 0.052669, Final residual = 7.32643e-08, No Iterations 13
1591 CG: Solving for pd, Initial residual = 0.0332159, Final residual = 7.14989e-08, No Iterations 12
1592 CG: Solving for pd, Initial residual = 0.0216589, Final residual = 6.25816e-08, No Iterations 12
1593 CG: Solving for pd, Initial residual = 0.0147278, Final residual = 8.7168e-08, No Iterations 11
1594 CG: Solving for pd, Initial residual = 0.0104724, Final residual = 7.15863e-08, No Iterations 11
1595 CG: Solving for pd, Initial residual = 0.00779744, Final residual = 6.91091e-08, No Iterations 11
1596 mag(U): max: 2.45754 avg: 0.201158
1597 time step continuity errors : sum local = 9.47522e-12, global = 3.13302e-13, cumulative = -3.44434e-11
1598 BiCGStab: Solving for alpha1, Initial residual = 6.00783e-06, Final residual = 9.66033e-11, No Iterations 1
1599 Liquid phase volume fraction = 0.500417 Min(alpha1) = -0.00773733 Max(alpha1) = 1.004
1600 BiCGStab: Solving for Ux, Initial residual = 0.000406446, Final residual = 3.3013e-09, No Iterations 1
1601 BiCGStab: Solving for Uy, Initial residual = 0.00553855, Final residual = 1.76194e-11, No Iterations 2
1602 CG: Solving for pd, Initial residual = 0.0491059, Final residual = 8.75335e-08, No Iterations 12
1603 CG: Solving for pd, Initial residual = 0.0210519, Final residual = 9.02764e-08, No Iterations 11
1604 CG: Solving for pd, Initial residual = 0.00698996, Final residual = 7.93068e-08, No Iterations 11
1605 CG: Solving for pd, Initial residual = 0.00395641, Final residual = 8.31173e-08, No Iterations 11
1606 CG: Solving for pd, Initial residual = 0.00246398, Final residual = 9.19342e-08, No Iterations 10
1607 CG: Solving for pd, Initial residual = 0.00169325, Final residual = 7.89268e-08, No Iterations 11
1608 mag(U): max: 2.43842 avg: 0.200731
1609 time step continuity errors : sum local = 1.04759e-11, global = -1.62063e-14, cumulative = -3.44596e-11
1610 Calculating static pressure
1611 CG: Solving for p, Initial residual = 0.000230953, Final residual = 5.6264e-08, No Iterations 7
1612 Relaxation: p = 0.1
1613 BiCGStab: Solving for alpha1, Initial residual = 4.18647e-07, Final residual = 1.53942e-11, No Iterations 1
1614 Liquid phase volume fraction = 0.500417 Min(alpha1) = -0.00771623 Max(alpha1) = 1.004
1615 ExecutionTime = 12.03 s ClockTime = 14 s
1617 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1618 Courant Number mean: 0.00404916 max: 0.388087 velocity magnitude: 1.16736
1619 deltaT = 0.000619355
1620 Time = 0.0300903
1622 BiCGStab: Solving for Ux, Initial residual = 0.000417802, Final residual = 2.58872e-09, No Iterations 1
1623 BiCGStab: Solving for Uy, Initial residual = 0.00363197, Final residual = 9.12879e-11, No Iterations 2
1624 CG: Solving for pd, Initial residual = 0.0527331, Final residual = 8.78186e-08, No Iterations 13
1625 CG: Solving for pd, Initial residual = 0.033399, Final residual = 6.93353e-08, No Iterations 12
1626 CG: Solving for pd, Initial residual = 0.0217616, Final residual = 7.0624e-08, No Iterations 12
1627 CG: Solving for pd, Initial residual = 0.0148102, Final residual = 8.91531e-08, No Iterations 11
1628 CG: Solving for pd, Initial residual = 0.0105033, Final residual = 8.32543e-08, No Iterations 11
1629 CG: Solving for pd, Initial residual = 0.0078081, Final residual = 6.95887e-08, No Iterations 11
1630 mag(U): max: 2.45795 avg: 0.201168
1631 time step continuity errors : sum local = 9.56192e-12, global = 3.91378e-13, cumulative = -3.40682e-11
1632 BiCGStab: Solving for alpha1, Initial residual = 6.01529e-06, Final residual = 9.35867e-11, No Iterations 1
1633 Liquid phase volume fraction = 0.500416 Min(alpha1) = -0.00784719 Max(alpha1) = 1.00411
1634 BiCGStab: Solving for Ux, Initial residual = 0.00039939, Final residual = 3.29511e-09, No Iterations 1
1635 BiCGStab: Solving for Uy, Initial residual = 0.00543736, Final residual = 1.91187e-11, No Iterations 2
1636 CG: Solving for pd, Initial residual = 0.0490371, Final residual = 8.57504e-08, No Iterations 12
1637 CG: Solving for pd, Initial residual = 0.0212468, Final residual = 9.69032e-08, No Iterations 11
1638 CG: Solving for pd, Initial residual = 0.00716238, Final residual = 9.31646e-08, No Iterations 11
1639 CG: Solving for pd, Initial residual = 0.00403849, Final residual = 7.41349e-08, No Iterations 12
1640 CG: Solving for pd, Initial residual = 0.00253756, Final residual = 9.25409e-08, No Iterations 11
1641 CG: Solving for pd, Initial residual = 0.00173455, Final residual = 7.73894e-08, No Iterations 11
1642 mag(U): max: 2.43894 avg: 0.200741
1643 time step continuity errors : sum local = 1.03426e-11, global = 2.12244e-13, cumulative = -3.3856e-11
1644 Calculating static pressure
1645 CG: Solving for p, Initial residual = 0.000231935, Final residual = 5.46048e-08, No Iterations 7
1646 Relaxation: p = 0.1
1647 BiCGStab: Solving for alpha1, Initial residual = 4.33253e-07, Final residual = 1.66955e-11, No Iterations 1
1648 Liquid phase volume fraction = 0.500416 Min(alpha1) = -0.00782563 Max(alpha1) = 1.00411
1649 ExecutionTime = 12.29 s ClockTime = 15 s
1651 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1652 Courant Number mean: 0.00404752 max: 0.388183 velocity magnitude: 1.16749
1653 deltaT = 0.000619355
1654 Time = 0.0307097
1656 BiCGStab: Solving for Ux, Initial residual = 0.000418415, Final residual = 2.64092e-09, No Iterations 1
1657 BiCGStab: Solving for Uy, Initial residual = 0.00372115, Final residual = 2.03607e-10, No Iterations 2
1658 CG: Solving for pd, Initial residual = 0.054003, Final residual = 8.35776e-08, No Iterations 13
1659 CG: Solving for pd, Initial residual = 0.0340503, Final residual = 7.87266e-08, No Iterations 12
1660 CG: Solving for pd, Initial residual = 0.0222498, Final residual = 6.28695e-08, No Iterations 12
1661 CG: Solving for pd, Initial residual = 0.0150741, Final residual = 9.54384e-08, No Iterations 11
1662 CG: Solving for pd, Initial residual = 0.0107009, Final residual = 8.92316e-08, No Iterations 11
1663 CG: Solving for pd, Initial residual = 0.00791406, Final residual = 8.50964e-08, No Iterations 11
1664 mag(U): max: 2.45815 avg: 0.201176
1665 time step continuity errors : sum local = 1.16445e-11, global = 1.15091e-12, cumulative = -3.27051e-11
1666 BiCGStab: Solving for alpha1, Initial residual = 5.99298e-06, Final residual = 8.97425e-11, No Iterations 1
1667 Liquid phase volume fraction = 0.500416 Min(alpha1) = -0.00794744 Max(alpha1) = 1.00422
1668 BiCGStab: Solving for Ux, Initial residual = 0.000393044, Final residual = 3.25836e-09, No Iterations 1
1669 BiCGStab: Solving for Uy, Initial residual = 0.00530297, Final residual = 1.78973e-11, No Iterations 2
1670 CG: Solving for pd, Initial residual = 0.0487642, Final residual = 8.34483e-08, No Iterations 12
1671 CG: Solving for pd, Initial residual = 0.0216453, Final residual = 6.36436e-08, No Iterations 13
1672 CG: Solving for pd, Initial residual = 0.00733896, Final residual = 8.74051e-08, No Iterations 12
1673 CG: Solving for pd, Initial residual = 0.0041547, Final residual = 8.47693e-08, No Iterations 11
1674 CG: Solving for pd, Initial residual = 0.00264157, Final residual = 8.72789e-08, No Iterations 11
1675 CG: Solving for pd, Initial residual = 0.00182004, Final residual = 9.09006e-08, No Iterations 10
1676 mag(U): max: 2.43927 avg: 0.20075
1677 time step continuity errors : sum local = 1.20883e-11, global = -9.10085e-14, cumulative = -3.27961e-11
1678 Calculating static pressure
1679 CG: Solving for p, Initial residual = 0.000231198, Final residual = 5.81154e-08, No Iterations 7
1680 Relaxation: p = 0.1
1681 BiCGStab: Solving for alpha1, Initial residual = 4.59504e-07, Final residual = 1.61747e-11, No Iterations 1
1682 Liquid phase volume fraction = 0.500416 Min(alpha1) = -0.00792536 Max(alpha1) = 1.00422
1683 ExecutionTime = 12.55 s ClockTime = 15 s
1685 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1686 Courant Number mean: 0.00404666 max: 0.388256 velocity magnitude: 1.16755
1687 deltaT = 0.000619355
1688 Time = 0.031329
1690 BiCGStab: Solving for Ux, Initial residual = 0.000413921, Final residual = 2.80489e-09, No Iterations 1
1691 BiCGStab: Solving for Uy, Initial residual = 0.00373976, Final residual = 1.63864e-10, No Iterations 2
1692 CG: Solving for pd, Initial residual = 0.0550008, Final residual = 8.89843e-08, No Iterations 13
1693 CG: Solving for pd, Initial residual = 0.0343782, Final residual = 7.73091e-08, No Iterations 12
1694 CG: Solving for pd, Initial residual = 0.0224711, Final residual = 6.75471e-08, No Iterations 12
1695 CG: Solving for pd, Initial residual = 0.0151435, Final residual = 9.28473e-08, No Iterations 11
1696 CG: Solving for pd, Initial residual = 0.0107235, Final residual = 9.3814e-08, No Iterations 11
1697 CG: Solving for pd, Initial residual = 0.00787911, Final residual = 5.78599e-08, No Iterations 12
1698 mag(U): max: 2.45824 avg: 0.201163
1699 time step continuity errors : sum local = 7.79652e-12, global = 1.21039e-12, cumulative = -3.15857e-11
1700 BiCGStab: Solving for alpha1, Initial residual = 5.94345e-06, Final residual = 8.8802e-11, No Iterations 1
1701 Liquid phase volume fraction = 0.500416 Min(alpha1) = -0.00803874 Max(alpha1) = 1.00433
1702 BiCGStab: Solving for Ux, Initial residual = 0.000387029, Final residual = 3.15722e-09, No Iterations 1
1703 BiCGStab: Solving for Uy, Initial residual = 0.00516289, Final residual = 1.53433e-11, No Iterations 2
1704 CG: Solving for pd, Initial residual = 0.0490393, Final residual = 8.63794e-08, No Iterations 12
1705 CG: Solving for pd, Initial residual = 0.0222618, Final residual = 4.74361e-08, No Iterations 13
1706 CG: Solving for pd, Initial residual = 0.0079147, Final residual = 8.6764e-08, No Iterations 12
1707 CG: Solving for pd, Initial residual = 0.004417, Final residual = 8.44318e-08, No Iterations 11
1708 CG: Solving for pd, Initial residual = 0.00273913, Final residual = 8.5388e-08, No Iterations 11
1709 CG: Solving for pd, Initial residual = 0.00168679, Final residual = 9.34702e-08, No Iterations 9
1710 mag(U): max: 2.43939 avg: 0.200731
1711 time step continuity errors : sum local = 1.20748e-11, global = -4.20967e-13, cumulative = -3.20066e-11
1712 Calculating static pressure
1713 CG: Solving for p, Initial residual = 0.000232032, Final residual = 6.13834e-08, No Iterations 7
1714 Relaxation: p = 0.1
1715 BiCGStab: Solving for alpha1, Initial residual = 4.39323e-07, Final residual = 1.52407e-11, No Iterations 1
1716 Liquid phase volume fraction = 0.500416 Min(alpha1) = -0.00801658 Max(alpha1) = 1.00433
1717 ExecutionTime = 12.82 s ClockTime = 16 s
1719 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1720 Courant Number mean: 0.00404646 max: 0.388299 velocity magnitude: 1.16754
1721 deltaT = 0.000619355
1722 Time = 0.0319484
1724 BiCGStab: Solving for Ux, Initial residual = 0.000403136, Final residual = 3.11756e-09, No Iterations 1
1725 BiCGStab: Solving for Uy, Initial residual = 0.00374579, Final residual = 2.41711e-10, No Iterations 2
1726 CG: Solving for pd, Initial residual = 0.059016, Final residual = 9.21866e-08, No Iterations 13
1727 CG: Solving for pd, Initial residual = 0.0366197, Final residual = 7.31618e-08, No Iterations 12
1728 CG: Solving for pd, Initial residual = 0.0240421, Final residual = 6.18715e-08, No Iterations 12
1729 CG: Solving for pd, Initial residual = 0.016083, Final residual = 9.32299e-08, No Iterations 11
1730 CG: Solving for pd, Initial residual = 0.0114765, Final residual = 8.03222e-08, No Iterations 11
1731 CG: Solving for pd, Initial residual = 0.00852835, Final residual = 7.5606e-08, No Iterations 11
1732 mag(U): max: 2.45801 avg: 0.201173
1733 time step continuity errors : sum local = 1.01081e-11, global = 5.80488e-13, cumulative = -3.14262e-11
1734 BiCGStab: Solving for alpha1, Initial residual = 5.88917e-06, Final residual = 8.79014e-11, No Iterations 1
1735 Liquid phase volume fraction = 0.500415 Min(alpha1) = -0.00812191 Max(alpha1) = 1.00443
1736 BiCGStab: Solving for Ux, Initial residual = 0.000382592, Final residual = 3.00484e-09, No Iterations 1
1737 BiCGStab: Solving for Uy, Initial residual = 0.0049071, Final residual = 1.17438e-11, No Iterations 2
1738 CG: Solving for pd, Initial residual = 0.0499942, Final residual = 8.53713e-08, No Iterations 12
1739 CG: Solving for pd, Initial residual = 0.0218776, Final residual = 4.94703e-08, No Iterations 13
1740 CG: Solving for pd, Initial residual = 0.00755865, Final residual = 8.7729e-08, No Iterations 11
1741 CG: Solving for pd, Initial residual = 0.00421265, Final residual = 9.97083e-08, No Iterations 11
1742 CG: Solving for pd, Initial residual = 0.00268846, Final residual = 7.17793e-08, No Iterations 13
1743 CG: Solving for pd, Initial residual = 0.00183957, Final residual = 7.36315e-08, No Iterations 11
1744 mag(U): max: 2.43893 avg: 0.200739
1745 time step continuity errors : sum local = 9.36844e-12, global = -4.16399e-13, cumulative = -3.18426e-11
1746 Calculating static pressure
1747 CG: Solving for p, Initial residual = 0.000235344, Final residual = 5.79329e-08, No Iterations 7
1748 Relaxation: p = 0.1
1749 BiCGStab: Solving for alpha1, Initial residual = 4.06239e-07, Final residual = 1.49764e-11, No Iterations 1
1750 Liquid phase volume fraction = 0.500415 Min(alpha1) = -0.00809957 Max(alpha1) = 1.00443
1751 ExecutionTime = 13.09 s ClockTime = 16 s
1753 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1754 Courant Number mean: 0.00404539 max: 0.388241 velocity magnitude: 1.16732
1755 deltaT = 0.000619355
1756 Time = 0.0325677
1758 BiCGStab: Solving for Ux, Initial residual = 0.00039107, Final residual = 3.53831e-09, No Iterations 1
1759 BiCGStab: Solving for Uy, Initial residual = 0.00395675, Final residual = 5.73739e-11, No Iterations 2
1760 CG: Solving for pd, Initial residual = 0.0593015, Final residual = 8.96204e-08, No Iterations 13
1761 CG: Solving for pd, Initial residual = 0.0371951, Final residual = 7.8757e-08, No Iterations 12
1762 CG: Solving for pd, Initial residual = 0.0243473, Final residual = 6.03256e-08, No Iterations 12
1763 CG: Solving for pd, Initial residual = 0.0162824, Final residual = 7.33534e-08, No Iterations 12
1764 CG: Solving for pd, Initial residual = 0.0115349, Final residual = 9.60065e-08, No Iterations 11
1765 CG: Solving for pd, Initial residual = 0.00848888, Final residual = 8.41892e-08, No Iterations 11
1766 mag(U): max: 2.45733 avg: 0.201185
1767 time step continuity errors : sum local = 1.10338e-11, global = 6.65733e-13, cumulative = -3.11768e-11
1768 BiCGStab: Solving for alpha1, Initial residual = 5.91656e-06, Final residual = 8.31329e-11, No Iterations 1
1769 Liquid phase volume fraction = 0.500415 Min(alpha1) = -0.00819812 Max(alpha1) = 1.00454
1770 BiCGStab: Solving for Ux, Initial residual = 0.000378974, Final residual = 2.87117e-09, No Iterations 1
1771 BiCGStab: Solving for Uy, Initial residual = 0.00457412, Final residual = 8.3501e-12, No Iterations 2
1772 CG: Solving for pd, Initial residual = 0.0518989, Final residual = 8.4093e-08, No Iterations 12
1773 CG: Solving for pd, Initial residual = 0.0221352, Final residual = 6.80997e-08, No Iterations 13
1774 CG: Solving for pd, Initial residual = 0.00754727, Final residual = 9.16801e-08, No Iterations 12
1775 CG: Solving for pd, Initial residual = 0.00417616, Final residual = 9.18395e-08, No Iterations 12
1776 CG: Solving for pd, Initial residual = 0.00267845, Final residual = 8.68066e-08, No Iterations 11
1777 CG: Solving for pd, Initial residual = 0.00184633, Final residual = 9.09878e-08, No Iterations 10
1778 mag(U): max: 2.43808 avg: 0.200751
1779 time step continuity errors : sum local = 1.11847e-11, global = -2.42198e-13, cumulative = -3.1419e-11
1780 Calculating static pressure
1781 CG: Solving for p, Initial residual = 0.000236912, Final residual = 5.20837e-08, No Iterations 7
1782 Relaxation: p = 0.1
1783 BiCGStab: Solving for alpha1, Initial residual = 3.83812e-07, Final residual = 1.43344e-11, No Iterations 1
1784 Liquid phase volume fraction = 0.500415 Min(alpha1) = -0.00817529 Max(alpha1) = 1.00454
1785 ExecutionTime = 13.35 s ClockTime = 16 s
1787 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1788 Courant Number mean: 0.00404441 max: 0.388119 velocity magnitude: 1.16696
1789 deltaT = 0.000619355
1790 Time = 0.0331871
1792 BiCGStab: Solving for Ux, Initial residual = 0.000389609, Final residual = 3.80741e-09, No Iterations 1
1793 BiCGStab: Solving for Uy, Initial residual = 0.00421642, Final residual = 8.73882e-11, No Iterations 2
1794 CG: Solving for pd, Initial residual = 0.0593433, Final residual = 8.22043e-08, No Iterations 13
1795 CG: Solving for pd, Initial residual = 0.0371304, Final residual = 6.99189e-08, No Iterations 12
1796 CG: Solving for pd, Initial residual = 0.0242444, Final residual = 7.0346e-08, No Iterations 12
1797 CG: Solving for pd, Initial residual = 0.0166363, Final residual = 9.72896e-08, No Iterations 11
1798 CG: Solving for pd, Initial residual = 0.0116861, Final residual = 8.31848e-08, No Iterations 11
1799 CG: Solving for pd, Initial residual = 0.00852553, Final residual = 8.14413e-08, No Iterations 11
1800 mag(U): max: 2.45628 avg: 0.201197
1801 time step continuity errors : sum local = 1.05273e-11, global = 6.53121e-13, cumulative = -3.07659e-11
1802 BiCGStab: Solving for alpha1, Initial residual = 5.93179e-06, Final residual = 7.88992e-11, No Iterations 1
1803 Liquid phase volume fraction = 0.500415 Min(alpha1) = -0.00826709 Max(alpha1) = 1.00464
1804 BiCGStab: Solving for Ux, Initial residual = 0.000374687, Final residual = 2.85281e-09, No Iterations 1
1805 BiCGStab: Solving for Uy, Initial residual = 0.00420594, Final residual = 5.61593e-12, No Iterations 2
1806 CG: Solving for pd, Initial residual = 0.0531274, Final residual = 8.75126e-08, No Iterations 12
1807 CG: Solving for pd, Initial residual = 0.0224453, Final residual = 7.69167e-08, No Iterations 12
1808 CG: Solving for pd, Initial residual = 0.00762969, Final residual = 9.32449e-08, No Iterations 12
1809 CG: Solving for pd, Initial residual = 0.004076, Final residual = 6.32318e-08, No Iterations 12
1810 CG: Solving for pd, Initial residual = 0.00257299, Final residual = 8.8297e-08, No Iterations 11
1811 CG: Solving for pd, Initial residual = 0.0017689, Final residual = 9.06352e-08, No Iterations 11
1812 mag(U): max: 2.43694 avg: 0.200764
1813 time step continuity errors : sum local = 1.08837e-11, global = -2.31807e-13, cumulative = -3.09977e-11
1814 Calculating static pressure
1815 CG: Solving for p, Initial residual = 0.000235329, Final residual = 4.92552e-08, No Iterations 7
1816 Relaxation: p = 0.1
1817 BiCGStab: Solving for alpha1, Initial residual = 3.65663e-07, Final residual = 1.40348e-11, No Iterations 1
1818 Liquid phase volume fraction = 0.500415 Min(alpha1) = -0.00824412 Max(alpha1) = 1.00464
1819 ExecutionTime = 13.64 s ClockTime = 111 s
1821 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1822 Courant Number mean: 0.00404285 max: 0.38795 velocity magnitude: 1.16648
1823 deltaT = 0.000619355
1824 Time = 0.0338065
1826 BiCGStab: Solving for Ux, Initial residual = 0.000388526, Final residual = 3.56167e-09, No Iterations 1
1827 BiCGStab: Solving for Uy, Initial residual = 0.0044569, Final residual = 8.11733e-11, No Iterations 2
1828 CG: Solving for pd, Initial residual = 0.0587075, Final residual = 9.82057e-08, No Iterations 13
1829 CG: Solving for pd, Initial residual = 0.0364077, Final residual = 8.72628e-08, No Iterations 12
1830 CG: Solving for pd, Initial residual = 0.0237934, Final residual = 8.50631e-08, No Iterations 12
1831 CG: Solving for pd, Initial residual = 0.0162731, Final residual = 7.78478e-08, No Iterations 12
1832 CG: Solving for pd, Initial residual = 0.0116149, Final residual = 9.19886e-08, No Iterations 11
1833 CG: Solving for pd, Initial residual = 0.008653, Final residual = 8.30777e-08, No Iterations 11
1834 mag(U): max: 2.45499 avg: 0.201211
1835 time step continuity errors : sum local = 1.06756e-11, global = 5.49391e-13, cumulative = -3.04483e-11
1836 BiCGStab: Solving for alpha1, Initial residual = 5.93135e-06, Final residual = 8.04509e-11, No Iterations 1
1837 Liquid phase volume fraction = 0.500414 Min(alpha1) = -0.00832881 Max(alpha1) = 1.00474
1838 BiCGStab: Solving for Ux, Initial residual = 0.000369953, Final residual = 2.88652e-09, No Iterations 1
1839 BiCGStab: Solving for Uy, Initial residual = 0.00389281, Final residual = 4.9521e-12, No Iterations 2
1840 CG: Solving for pd, Initial residual = 0.0534999, Final residual = 8.79389e-08, No Iterations 12
1841 CG: Solving for pd, Initial residual = 0.0230082, Final residual = 5.00612e-08, No Iterations 13
1842 CG: Solving for pd, Initial residual = 0.00750512, Final residual = 8.3942e-08, No Iterations 11
1843 CG: Solving for pd, Initial residual = 0.00407788, Final residual = 9.27011e-08, No Iterations 11
1844 CG: Solving for pd, Initial residual = 0.00256115, Final residual = 7.21686e-08, No Iterations 11
1845 CG: Solving for pd, Initial residual = 0.00174229, Final residual = 8.64809e-08, No Iterations 11
1846 mag(U): max: 2.43561 avg: 0.200778
1847 time step continuity errors : sum local = 1.03457e-11, global = 1.35569e-13, cumulative = -3.03127e-11
1848 Calculating static pressure
1849 CG: Solving for p, Initial residual = 0.000226951, Final residual = 4.69597e-08, No Iterations 7
1850 Relaxation: p = 0.1
1851 BiCGStab: Solving for alpha1, Initial residual = 3.79892e-07, Final residual = 1.50686e-11, No Iterations 1
1852 Liquid phase volume fraction = 0.500414 Min(alpha1) = -0.0083047 Max(alpha1) = 1.00474
1853 ExecutionTime = 13.91 s ClockTime = 111 s
1855 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1856 Courant Number mean: 0.00404092 max: 0.387755 velocity magnitude: 1.16593
1857 deltaT = 0.000619355
1858 Time = 0.0344258
1860 BiCGStab: Solving for Ux, Initial residual = 0.000390305, Final residual = 3.06382e-09, No Iterations 1
1861 BiCGStab: Solving for Uy, Initial residual = 0.00452664, Final residual = 5.17194e-11, No Iterations 2
1862 CG: Solving for pd, Initial residual = 0.0594998, Final residual = 6.87326e-08, No Iterations 13
1863 CG: Solving for pd, Initial residual = 0.0366149, Final residual = 8.96656e-08, No Iterations 12
1864 CG: Solving for pd, Initial residual = 0.0238085, Final residual = 8.19343e-08, No Iterations 12
1865 CG: Solving for pd, Initial residual = 0.0161493, Final residual = 8.50013e-08, No Iterations 12
1866 CG: Solving for pd, Initial residual = 0.011514, Final residual = 9.15574e-08, No Iterations 11
1867 CG: Solving for pd, Initial residual = 0.00852933, Final residual = 8.13328e-08, No Iterations 11
1868 mag(U): max: 2.45348 avg: 0.201227
1869 time step continuity errors : sum local = 1.04606e-11, global = 9.90402e-14, cumulative = -3.02137e-11
1870 BiCGStab: Solving for alpha1, Initial residual = 5.94609e-06, Final residual = 8.25869e-11, No Iterations 1
1871 Liquid phase volume fraction = 0.500414 Min(alpha1) = -0.00838076 Max(alpha1) = 1.00484
1872 BiCGStab: Solving for Ux, Initial residual = 0.00036488, Final residual = 2.92179e-09, No Iterations 1
1873 BiCGStab: Solving for Uy, Initial residual = 0.00362302, Final residual = 5.62694e-12, No Iterations 2
1874 CG: Solving for pd, Initial residual = 0.0537963, Final residual = 8.57109e-08, No Iterations 12
1875 CG: Solving for pd, Initial residual = 0.0225311, Final residual = 8.75338e-08, No Iterations 12
1876 CG: Solving for pd, Initial residual = 0.00748418, Final residual = 7.34448e-08, No Iterations 11
1877 CG: Solving for pd, Initial residual = 0.00414501, Final residual = 7.5564e-08, No Iterations 12
1878 CG: Solving for pd, Initial residual = 0.00265213, Final residual = 6.80665e-08, No Iterations 12
1879 CG: Solving for pd, Initial residual = 0.00179588, Final residual = 9.51178e-08, No Iterations 10
1880 mag(U): max: 2.43408 avg: 0.200794
1881 time step continuity errors : sum local = 1.14197e-11, global = 3.82157e-13, cumulative = -2.98315e-11
1882 Calculating static pressure
1883 CG: Solving for p, Initial residual = 0.000216898, Final residual = 4.39835e-08, No Iterations 7
1884 Relaxation: p = 0.1
1885 BiCGStab: Solving for alpha1, Initial residual = 3.55326e-07, Final residual = 1.55564e-11, No Iterations 1
1886 Liquid phase volume fraction = 0.500414 Min(alpha1) = -0.00835531 Max(alpha1) = 1.00484
1887 ExecutionTime = 14.17 s ClockTime = 111 s
1889 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1890 Courant Number mean: 0.00403907 max: 0.38753 velocity magnitude: 1.16529
1891 deltaT = 0.000619355
1892 Time = 0.0350452
1894 BiCGStab: Solving for Ux, Initial residual = 0.000393683, Final residual = 2.84554e-09, No Iterations 1
1895 BiCGStab: Solving for Uy, Initial residual = 0.00451072, Final residual = 1.75752e-11, No Iterations 2
1896 CG: Solving for pd, Initial residual = 0.0596959, Final residual = 8.37981e-08, No Iterations 13
1897 CG: Solving for pd, Initial residual = 0.0366264, Final residual = 8.40568e-08, No Iterations 12
1898 CG: Solving for pd, Initial residual = 0.0236334, Final residual = 7.19802e-08, No Iterations 12
1899 CG: Solving for pd, Initial residual = 0.0160718, Final residual = 6.44359e-08, No Iterations 12
1900 CG: Solving for pd, Initial residual = 0.0114468, Final residual = 8.18817e-08, No Iterations 11
1901 CG: Solving for pd, Initial residual = 0.00847032, Final residual = 8.39762e-08, No Iterations 11
1902 mag(U): max: 2.45178 avg: 0.201245
1903 time step continuity errors : sum local = 1.08274e-11, global = -4.77754e-13, cumulative = -3.03093e-11
1904 BiCGStab: Solving for alpha1, Initial residual = 5.96509e-06, Final residual = 8.27172e-11, No Iterations 1
1905 Liquid phase volume fraction = 0.500414 Min(alpha1) = -0.0084212 Max(alpha1) = 1.00494
1906 BiCGStab: Solving for Ux, Initial residual = 0.00035993, Final residual = 2.89518e-09, No Iterations 1
1907 BiCGStab: Solving for Uy, Initial residual = 0.00340573, Final residual = 6.61368e-12, No Iterations 2
1908 CG: Solving for pd, Initial residual = 0.0540624, Final residual = 8.39849e-08, No Iterations 12
1909 CG: Solving for pd, Initial residual = 0.0220144, Final residual = 8.22456e-08, No Iterations 12
1910 CG: Solving for pd, Initial residual = 0.00728245, Final residual = 9.76279e-08, No Iterations 10
1911 CG: Solving for pd, Initial residual = 0.00403774, Final residual = 7.28853e-08, No Iterations 12
1912 CG: Solving for pd, Initial residual = 0.00257082, Final residual = 6.67316e-08, No Iterations 12
1913 CG: Solving for pd, Initial residual = 0.00175229, Final residual = 9.38369e-08, No Iterations 10
1914 mag(U): max: 2.43231 avg: 0.200813
1915 time step continuity errors : sum local = 1.14016e-11, global = 3.78398e-13, cumulative = -2.99309e-11
1916 Calculating static pressure
1917 CG: Solving for p, Initial residual = 0.00021659, Final residual = 4.3326e-08, No Iterations 7
1918 Relaxation: p = 0.1
1919 BiCGStab: Solving for alpha1, Initial residual = 3.75425e-07, Final residual = 1.54483e-11, No Iterations 1
1920 Liquid phase volume fraction = 0.500414 Min(alpha1) = -0.00839418 Max(alpha1) = 1.00494
1921 ExecutionTime = 14.43 s ClockTime = 112 s
1923 Volume: new = 0.0221905 old = 0.0221905 change = 0 ratio = 0
1924 Courant Number mean: 0.00403752 max: 0.387263 velocity magnitude: 1.16456
1925 deltaT = 0.000619355
1926 Time = 0.0356645
1928 BiCGStab: Solving for Ux, Initial residual = 0.000397175, Final residual = 2.764e-09, No Iterations 1
1929 BiCGStab: Solving for Uy, Initial residual = 0.00440275, Final residual = 8.61165e-11, No Iterations 2
1930 CG: Solving for pd, Initial residual = 0.0594632, Final residual = 7.5398e-08, No Iterations 13
1931 CG: Solving for pd, Initial residual = 0.0366966, Final residual = 8.25306e-08, No Iterations 12
1932 CG: Solving for pd, Initial residual = 0.0237798, Final residual = 7.6062e-08, No Iterations 12
1933 CG: Solving for pd, Initial residual = 0.0162009, Final residual = 9.71794e-08, No Iterations 11