Simulation Stats

Test Case Name
pipe-tutorial
Number of Points [ – ]
3
Machine Type
stator
Rotation Speed [ RPM ]
0
Number of Components [ – ]
(topology)
1
Mesh Size [ cells ]
(details)
pipe : 46858
Total : 46858
Average y+ at walls [ – ]
details
Wall-clock time [ hh:mm:ss ]
00:00:07 (meshing)
00:02:20 (calculation)
Parallel Processors [ – ]
2
Fluid Name
water
Physical Model
incompressible
Numerical order
second
Turbulence model
kOmegaSST

Efficiency

1:pipe-inlet — 1:pipe-outlet
Point Nr.
Flow Rate [ l/s ]
Efficiency [ – ]
1
2.00000
0.998319
2
5.00000
0.992108
3
10.0000
0.974421

Total Pressure Difference

1:pipe-inlet — 1:pipe-outlet
Point Nr.
Flow Rate [ l/s ]
Total Pressure Difference [ Pa ]
1
2.00000
-171.360
2
5.00000
-828.058
3
10.0000
-2948.02

Total Pressure per Interfaces

Point Nr.
Interface Name
Flow Rate [ l/s ]
Total Pressure [ Pa ]
1
pipe-in
2.00000
101946.
1
pipe-out
2.00000
101775.
2
pipe-in
5.00000
104919.
2
pipe-out
5.00000
104091.
3
pipe-in
10.0000
115252.
3
pipe-out
10.0000
112304.

Velocity Magnitude per Interfaces

Point Nr.
Interface Name
Flow Rate [ l/s ]
Velocity Magnitude [ m/s ]
1
pipe-in
2.00000
0.917668
1
pipe-out
2.00000
0.940025
2
pipe-in
5.00000
2.29417
2
pipe-out
5.00000
2.33606
3
pipe-in
10.0000
4.58834
3
pipe-out
10.0000
4.65859