UFR 1-07 Test Case: Difference between revisions

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[[Image:UFR1-07_fig9.gif|center]]
[[Image:UFR1-07_fig9.gif|center|509px]]


<center>'''Figure 9 '''&nbsp;Boundary conditions for the O&lsquo;Hern&nbsp;''et al.''&nbsp;[[UFR_1-07_References#4|[4]]] experiments.</center>
<center>'''Figure 9 '''&nbsp;Boundary conditions for the O&lsquo;Hern&nbsp;''et al.''&nbsp;[[UFR_1-07_References#4|[4]]] experiments.</center>

Revision as of 08:20, 12 July 2010


Front Page

Description

Test Case Studies

Evaluation

Best Practice Advice

References

Unsteady Near-Field Plumes

Underlying Flow Regime 1-07


Test Case Study

Brief Description of the Study Test Case

  • A summary of the boundary conditions is shown in Figure 8.
  • A gas mixture mainly composed of helium is discharged through a circular orifice into ambient air.
  • The gas is composed of 96.4% helium, 1.7% acetone and 1.9% oxygen by volume.
  • The molecular weight of the gas released is 5.45 g/mol ±2.7%.
  • The mixture is discharged at a temperature of THe = 11°C ±3°C and the air is at Tair = 13°C ±3°C.
  • The circular plume source has diameter, D = 1 metre.
  • The helium is discharged at a Reynolds-averaged velocity V0 = 0.325 m/s ±1.3% and a Favre-averaged velocity of approximately 0.339 m/s.
  • The flow through the orifice is laminar.
  • The ambient pressure is 80.9 kPa ±0.4 kPa.
  • The measurements include:
    1. Time-history of vertical velocity at a point 0.5 m from the centreline and 0.5 m above the inlet, used to estimate the puffing frequency
    2. Measurements on a vertical plane through the plume from the plume source to a distance of one orifice diameter of:
      • Reynolds-averaged and Favre-averaged mean axial and radial velocities
      • Reynolds-averaged and Favre-averaged shear stresses, normal stresses and turbulent kinetic energy[1]
      • Favre-averaged helium concentrations
    3. Movies of helium concentration and velocities
    4. Profiles of the mean and RMS velocities, and mean and RMS helium concentrations at six measurement positions (0.1, 0.2, 0.3, 0.4, 0.5 and 0.6 m downstream of the plume source)

Item 1 is available in the O‘Hern et al. [4] paper, Items 2 and 3 can be obtained by contacting the authors of the study[2]. and Item 4 is presented by Chung & Devaud [39].

Test Case Experiments

UFR1-07 fig8.gif
Figure 8  Boundary conditions for the O‘Hern et al. [4] experiments.


UFR1-07 fig9.gif
Figure 9  Boundary conditions for the O‘Hern et al. [4] experiments.

CFD Methods

Footnotes

  1. Only velocities parallel to a two-dimensional plane were recorded. The turbulent kinetic energy, k, is calculated from the vertical and horizontal normal stresses (  and  ) by assuming that the horizontal component is the same in the out-of-plane direction (  ), i.e. assuming that .
  2. Dr. Tieszen (srtiesz@sandia.gov) or Dr. O‘Hern (tjohern@sandia.gov)


Front Page

Description

Test Case Studies

Evaluation

Best Practice Advice

References


Contributed by: Simon Gant — UK Health & Safety Laboratory

© copyright ERCOFTAC 2010