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Solver Refinement
Refinement: Disabled
Results Saving
Save before refinement
On
Periodic saving
Units: Iterations
Period: 100
Advanced Control Options
Flow Freezing
Flow freezing strategy
Disabled
Manual time step: Off
RESULTS
General Info
Iterations: 200
Physical time: 0.0896829479 s
CPU time: 154 s
Calculation Mesh
Basic Mesh Dimensions
Number of cells in X
12
Number of cells in Y
6
Number of cells in Z
14
Number Of Cells
Total cells
6104
Fluid cells
2288
Solid cells
1288
Partial cells
2528
Irregular cells
0
Trimmed cells
56
Maximum refinement level: 1
Goals
Name
Unit
Value
Progress
Use in con-
vergence
Delta
Criteria
PG Total
Pressure 1
Pa
104126
100
On
38.4383518
296.566087
PG Tem-
perature of
Fluid 1
K
691.346
100
On
0.11968398
4
0.27450490
5
PG Density
1
kg/m^3
0.77457
100
On
0.00015556
7149
0.00123414
674
PG Veloci-
ty 1
m/s
85.1618
100
On
0.60744538
3
3.26501782
PG Turbu-
lent Vis-
Pa*s
0.0308409
100
On
0.00019641
1107
0.00425956
837
Solver Refinement Refinement: Disabled Results Saving Save before refinement On Periodic saving Units: Iterations Period: 100 Advanced Control Options Flow Freezing Flow freezing strategy Disabled Manual time step: Off RESULTS General Info Iterations: 200 Physical time: 0.0896829479 s CPU time: 154 s Calculation Mesh Basic Mesh Dimensions Number of cells in X 12 Number of cells in Y 6 Number of cells in Z 14 Number Of Cells Total cells 6104 Fluid cells 2288 Solid cells 1288 Partial cells 2528 Irregular cells 0 Trimmed cells 56 Maximum refinement level: 1 Goals Name Unit Value Progress Use in con- Delta Criteria vergence PG Total Pa 104126 100 On 38.4383518 296.566087 Pressure 1 PG Tem- K 691.346 100 On 0.11968398 0.27450490 perature of 4 5 Fluid 1 PG Density kg/m^3 0.77457 100 On 0.00015556 0.00123414 1 7149 674 PG Veloci- m/s 85.1618 100 On 0.60744538 3.26501782 ty 1 3 PG Turbu- Pa*s 0.0308409 100 On 0.00019641 0.00425956 lent Vis- 1107 837