# Steenbergen Pipe Flow with Swirl Data
# Wall Jet Case, Re=300,000
#
# Mean velocity
# x/D= 9.6
#
# r/R          U/Ub         W/Ub
 -0.97        0.811999     0.295449
 -0.95999     0.846825     0.305024
 -0.94999     0.869976     0.31085
 -0.93        0.903416     0.314268
 -0.91        0.924302     0.313387
 -0.88999     0.94002      0.310844
 -0.87        0.952318     0.307306
 -0.85        0.961784     0.302726
 -0.8         0.981373     0.291161
 -0.75        0.997355     0.280869
 -0.69999     1.013912     0.270623
 -0.64999     1.03143      0.256758
 -0.6         1.046994     0.242218
 -0.55        1.0627       0.222034
 -0.5         1.079929     0.202843
 -0.44999     1.094997     0.179626
 -0.4         1.109351     0.156044
 -0.34999     1.126031     0.131968
 -0.3         1.138209     0.11008
 -0.25        1.15274      0.090525
 -0.2         1.163076     0.073506
 -0.15        1.175967     0.05767
 -0.1         1.18099      0.045402
 -0.05        1.184469     0.034646
  0           1.182548     0.022222
  0.05        1.179863     0.0103
  0.1         1.172901    -0.00616
  0.15        1.159764    -0.0228
  0.2         1.148556    -0.04451
  0.25        1.135477    -0.06795
  0.3         1.119447    -0.09585
  0.349999    1.107316    -0.12535
  0.4         1.094928    -0.15605
  0.449999    1.080839    -0.18464
  0.5         1.066174    -0.21187
  0.55        1.051233    -0.2324
  0.6         1.035804    -0.25213
  0.649999    1.023414    -0.26572
  0.699999    1.008891    -0.27847
  0.75        0.994217    -0.2862
  0.8         0.979985    -0.29769
  0.85        0.962022    -0.30872
  0.87        0.954206    -0.31283
  0.889999    0.942476    -0.32155
  0.91        0.933734    -0.32593
  0.93        0.915213    -0.32708
  0.949999    0.893208    -0.32835
  0.959999    0.875514    -0.32513
  0.97        0.851188    -0.31547