# Circular to Rectangular Transition Duct Reb=390,000
# Expt. data of Davis & Gessner
# Total Pressure (Pt-Pi)/Qref, Station 1, Traverse y4
#    y/R      (Pt-Pi)/Qref
  1.00000  0.00000
  0.99851  0.13520
  0.99726  0.25732
  0.99602  0.30518
  0.99478  0.33902
  0.99353  0.36541
  0.99229  0.37786
  0.99104  0.39931
  0.98856  0.43090
  0.98607  0.45499
  0.98358  0.47378
  0.98109  0.49100
  0.97861  0.51210
  0.97612  0.52515
  0.97363  0.53880
  0.96866  0.56464
  0.96368  0.58457
  0.95871  0.60624
  0.95373  0.62923
  0.94876  0.64456
  0.94378  0.66261
  0.93881  0.68096
  0.93383  0.69971
  0.92886  0.70679
  0.92388  0.72497
  0.91891  0.74049
  0.91393  0.75132
  0.90896  0.76831
  0.90398  0.78068
  0.89900  0.79766
  0.89403  0.80952
  0.88905  0.82303
  0.88408  0.83481
  0.87413  0.86518
  0.86418  0.88874
  0.85423  0.91021
  0.84428  0.93729
  0.83433  0.95947
  0.82438  0.98589
  0.81443  1.01053
  0.80448  1.03082
  0.79453  1.04721
  0.78458  1.05786
  0.77463  1.09058
  0.76468  1.09926
  0.75473  1.11024
  0.74478  1.13253
  0.73483  1.14001
  0.72488  1.14624
  0.71244  1.14804
  0.70000  1.15106
  0.68756  1.15756
  0.67512  1.16793
  0.66269  1.16194
  0.65025  1.15944
  0.62537  1.16244
  0.60050  1.15987
  0.57562  1.15744
  0.55075  1.15542
  0.50100  1.15771
  0.45124  1.15826
  0.40149  1.15937
  0.35174  1.15838
  0.30199  1.16038
  0.25224  1.15914
  0.20249  1.15881
  0.15274  1.15936
  0.10299  1.15899
  0.05323  1.15912
  0.00000  1.15936