A numerical study of a prototypical vortex controlled diffuser is performed. The basic diffuser geometry consists of a step expansion in a pipe of area ratio 2.25:1. The incompressible Reynolds averaged Navier-Stokes equations, employing the RNG based κ − ∈ turbulence model, are solved. Results are presented for bleed rates ranging from 1 to 7 percent. Diffuser efficiencies in excess of 80 percent were obtained. These results are in good qualitative agreement with previous experimental work. The results do not confirm previous suggestions that the increases in effectiveness of the VCD over a step expansion result from an inhibition of flow separation due to the generation and downstream convection of extremely high levels of turbulence generated in the region of the bleed gap. The results do indicate that the effectiveness of the diffuser is a consequence of the turning of the flow toward the outer wall due to the influence of the low pressure vortex chamber. Calculations employing the RNG based turbulence model were able to capture the abrupt increase in diffuser effectiveness that has been shown experimentally to occur at low bleed rates. Calculations employing the standard κ − ∈ model were unable to predict this occurrence.

1.
Adkins
R. C.
,
1975
, “
A Short Diffuser With Low Pressure Loss
,”
JOURNAL OF FLUIDS ENGINEERING
, Vol.
97
, pp.
297
302
.
2.
Adkins
R. C.
,
Martharu
D. S.
, and
Yost
J. O.
,
1981
, “
The Hybrid Diffuser
,”
ASME Journal of Engineering Power
, Vol.
103
, pp.
229
236
.
3.
Busnaina, A. A., and Lilley, D. G., 1982, “A Simple Finite Difference Procedure for the Vortex Controlled Diffuser,” AIAA-82-0109, AIAA 20th Aerospace Sciences Meeting, Jan. 11–14, Orlando, FL.
4.
Heskestad
G.
,
1965
, “
An Edge Suction Effect
,”
AIAA Journal
, Vol.
3
, pp.
1958
1961
.
5.
Heskestad
G.
,
1968
, “
A Suction Scheme Applied to Flow Through a Sudden Enlargement
,”
ASME Journal of Basic Engineering
, Vol.
90
, pp.
541
544
.
6.
Heskestad
G.
,
1970
, “
Further Experiments with Suction at a Sudden Enlargement in a Pipe
,”
ASME Journal of Basic Engineering
, Vol.
XX
, pp.
437
449
.
7.
Leonard
B. P.
,
1979
, “
A Stable and Accurate Convective Modeling Procedure Based on Quadratic Upstream Interpolation
,”
Methods in Applied Mechanical Engineering
, Vol.
19
, pp.
59
98
.
8.
Nallasamy
M.
,
1987
, “
Turbulence Models and Their Applications to the Prediction of Internal Flows: A Review
,”
Computers & Fluids
, Vol.
15
, pp.
151
194
.
9.
Patankar, S. V., 1980, Numerical Heat Transfer and Fluid Flow, Hemisphere Publishing Corp., Washington, D.C.
10.
Sullerey
R. K.
,
Ashok
V.
, and
Shantharam
K. V.
,
1992
, “
Effect of Inlet Flow Distortion on Performance of Vortex Controlled Diffusers
,”
ASME JOURNAL OF FLUIDS ENGINEERING
, Vol.
114
, pp.
191
197
.
11.
Yakhot
V.
,
Orzag
S. A.
,
Thangam
S.
,
Gatski
T. B.
, and
Speziale
T. B.
,
1992
, “
Development of Turbulence Models for Shear Flows by a Double Expansion Technique
,”
Physics of Fluids A
, Vol.
4
, pp.
1510
1520
.
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