Turbulent Flow in Diffuser: Exercise 7—Analyzing Results
This exercise describes how the results are analyzed during and after the simulation. To hide CAD surfaces (not the fluid domain), switch between
CAD Bodies and
Flow Analysis Bodies in the
Show group. Clear any variable display by selecting
No Selection in the
Legend drop-down. Click
XYPlot Panel to view the XY Plot.
| 1. To show/hide selected geometric entities, click Show in View Panel. 2. To change the color scheme, click on More in the Legend and select between Blue Red and Blue Purple. |
Viewing the Pressure Contours on a Section
| Pressure Pa |
1. In the
Post-processing group, click
Section View and create a section.
Section 02 appears under Derived Surfaces.
2. Select Section 02.
3. In the Properties panel, Model tab, set values for the options as listed below:
◦ Type — Plane Y
◦ Position — 0
4. In the Properties panel, View tab, for Surface, set values for the options as listed below:
◦ Grid—No
◦ Outline—Yes
◦ Variable — Pressure [Pa] : Flow
Viewing the Velocity Magnitude on a Section
| Velocity Magnitude m/s |
1. In the
Post-processing group, click
Section View and create a section.
Section 03 appears under Derived Surfaces.
2. Select Section 03.
3. In the Properties panel, Model tab, set values for the options as listed below:
◦ Type — Plane Y
◦ Position — 0
4. In the Properties panel, View tab, for Surface, set values for the options as listed below:
◦ Grid—No
◦ Outline—Yes
◦ Variable — Velocity Magnitude [m/s] : Flow
Plotting the Temperature at the Monitoring Point
1. In the Flow Analysis Tree, under Results, click Monitoring Points..
2. Select Point01 to Point10.
3. Click
XYPlot. A new entity
xyplot1 appears in the Flow Analysis Tree under >
4. Click xyplot1.
5. In the Properties panel, View tab, for Surface, set Variable to Pressure [Pa] : Flow.
Plotting the Temperature at the Monitoring Point
1. In the Flow Analysis Tree, under Results, click Monitoring Points..
2. Select Point10.
3. Click
XYPlot. A new entity
xyplot2 appears in the Flow Analysis Tree under >
4. The monitoring point Point10 is added to xyplot2.
Validation
The coefficient of pressure at diffuser wall is calculated as follows:
where,
P | Pressure at the diffuser walls (Pa): From monitoring points |
ρ | Density (kg/m3): 1.15758 |
Pdiffuser | Pressure at the diffuser outlet (Pa): -2.6066 |
u | Inlet velocity m/s: 18.06 |
The monitoring points in the simulation are used to measure the pressure close to the diffuser wall:
Points | X | X/D | Static Pressure (Pa) | Pressure at Diffuser Outlet (Pa) | Coefficient of Pressure Cp |
---|
Point01 | 3.500 | 0.000 | -170.453 | -2.293 | -0.891 |
Point02 | 3.575 | 0.738 | -106.429 | -2.293 | -0.552 |
Point03 | 3.650 | 1.476 | -72.543 | -2.293 | -0.372 |
Point04 | 3.725 | 2.215 | -51.002 | -2.293 | -0.258 |
Point05 | 3.800 | 2.953 | -36.504 | -2.293 | -0.181 |
Point06 | 3.875 | 3.691 | -26.172 | -2.293 | -0.126 |
Point07 | 3.950 | 4.429 | -18.522 | -2.293 | -0.086 |
Point08 | 4.025 | 5.167 | -12.885 | -2.293 | -0.056 |
Point09 | 4.100 | 5.906 | -8.056 | -2.293 | -0.031 |
Point10 | 4.218 | 7.067 | -2.293 | -2.293 | 0.000 |
where,
X/D= (X-3.5)/D and D (m) = 0.1016
The comparison of the coefficient of pressure from experiments and Creo Flow Analysis are as follows:
Reference: Azad, R. S., & Kassab, S. Z. (1989). Turbulent flow in a conical diffuser: Overview and implications. Physics of Fluids A: Fluid Dynamics, 1(3), 564–573.