# Measured turbulence kinetic energy profiles as compiled by
#   Patel, Rodi, and Scheuerer AIAA Journal Vol. 23, No. 9, 1985.
#   Digitized from figure 4.
# This data represents an "average" t.k.e. profile for the data
# obtained by
#   D. Coles "A Model for Flow in the Viscous Sublayer,"
#     Proceedings of the Workshop on Coherent Structure of
#     Turbulent Boundary Layers, Lehigh Univ., Bethlehem PA 1978.
#   M.M.M.El Telbany & A.J.Reynolds "Turbulence in Plane Channel
#     Flows," Journal of Fluid Mechanics, Vol. 111, pp.283-318, 1981.
# eps+     = (Total Diss)
# Prod_Dis = Prod / (Total) Diss
# D+       = (Total Diss)+ - (Chien Diss)+
Variables="y+","u+","k+","eps+","-uv+","Prod_Dis","D+"
Zone T="Patel", F=POINT
 2.6  0.0  0.31  0.0  0.0  0.0  0.0
 5.3  0.0  1.23  0.0  0.0  0.0  0.0
 7.7  0.0  2.80  0.0  0.0  0.0  0.0
 9.9  0.0  4.07  0.0  0.0  0.0  0.0
12.4  0.0  4.46  0.0  0.0  0.0  0.0
14.9  0.0  4.48  0.0  0.0  0.0  0.0
17.4  0.0  4.47  0.0  0.0  0.0  0.0
19.9  0.0  4.42  0.0  0.0  0.0  0.0
22.2  0.0  4.37  0.0  0.0  0.0  0.0
24.9  0.0  4.31  0.0  0.0  0.0  0.0
27.6  0.0  4.25  0.0  0.0  0.0  0.0
29.9  0.0  4.16  0.0  0.0  0.0  0.0
32.3  0.0  4.07  0.0  0.0  0.0  0.0
34.9  0.0  3.99  0.0  0.0  0.0  0.0
37.3  0.0  3.90  0.0  0.0  0.0  0.0
39.8  0.0  3.81  0.0  0.0  0.0  0.0
42.4  0.0  3.73  0.0  0.0  0.0  0.0
44.8  0.0  3.62  0.0  0.0  0.0  0.0
47.2  0.0  3.53  0.0  0.0  0.0  0.0
49.7  0.0  3.46  0.0  0.0  0.0  0.0
52.2  0.0  3.40  0.0  0.0  0.0  0.0
54.8  0.0  3.36  0.0  0.0  0.0  0.0
57.4  0.0  3.31  0.0  0.0  0.0  0.0
59.6  0.0  3.32  0.0  0.0  0.0  0.0
62.2  0.0  3.32  0.0  0.0  0.0  0.0
64.6  0.0  3.30  0.0  0.0  0.0  0.0
67.0  0.0  3.29  0.0  0.0  0.0  0.0
69.7  0.0  3.29  0.0  0.0  0.0  0.0
72.2  0.0  3.29  0.0  0.0  0.0  0.0
74.8  0.0  3.29  0.0  0.0  0.0  0.0
77.3  0.0  3.29  0.0  0.0  0.0  0.0
79.8  0.0  3.29  0.0  0.0  0.0  0.0
82.3  0.0  3.30  0.0  0.0  0.0  0.0
84.8  0.0  3.30  0.0  0.0  0.0  0.0
87.3  0.0  3.32  0.0  0.0  0.0  0.0
89.7  0.0  3.31  0.0  0.0  0.0  0.0
92.4  0.0  3.31  0.0  0.0  0.0  0.0
94.6  0.0  3.31  0.0  0.0  0.0  0.0
97.4  0.0  3.30  0.0  0.0  0.0  0.0
99.9  0.0  3.28  0.0  0.0  0.0  0.0