# Steenbergen Pipe Flow with Swirl Data
# Wall Jet Case, Re=300,000
#
# Mean velocity
# x/D= 28.1
#
# r/R          U/Ub         W/Ub
 -0.97        0.866286     0.241944
 -0.95999     0.903622     0.240208
 -0.94999     0.928023     0.242139
 -0.93        0.96649      0.238794
 -0.91        0.993887     0.236255
 -0.88999     1.011835     0.233658
 -0.87        1.025832     0.227643
 -0.85        1.036594     0.223537
 -0.8         1.047295     0.209925
 -0.75        1.057422     0.192491
 -0.69999     1.056079     0.173287
 -0.64999     1.062363     0.15827
 -0.6         1.059387     0.137653
 -0.55        1.066539     0.119083
 -0.5         1.066177     0.103976
 -0.44999     1.068551     0.087299
 -0.4         1.069056     0.073143
 -0.34999     1.074032     0.059741
 -0.3         1.074266     0.047288
 -0.25        1.075205     0.033004
 -0.2         1.074335     0.021381
 -0.15        1.076912     0.01165
 -0.1         1.075678     0.000157
 -0.05        1.074963    -0.00754
  0           1.077072    -0.01752
  0.05        1.074482    -0.0272
  0.1         1.075074    -0.03272
  0.15        1.071989    -0.04044
  0.2         1.069188    -0.04775
  0.25        1.064758    -0.05568
  0.3         1.061544    -0.06312
  0.349999    1.056159    -0.07246
  0.4         1.053316    -0.0823
  0.449999    1.048336    -0.0935
  0.5         1.044147    -0.105
  0.55        1.033712    -0.11679
  0.6         1.030972    -0.13305
  0.649999    1.023182    -0.15106
  0.699999    1.017498    -0.16326
  0.75        1.012831    -0.1838
  0.8         0.998756    -0.19687
  0.85        0.979381    -0.21212
  0.87        0.975189    -0.21974
  0.889999    0.960377    -0.22303
  0.91        0.94607     -0.2284
  0.93        0.916559    -0.23294
  0.949999    0.880194    -0.22914
  0.959999    0.849624    -0.22165
  0.97        0.808426    -0.21676