# Steenbergen Pipe Flow with Swirl Data
# Wall Jet Case, Re=50,000
#
# Mean velocity
# x/D= 4.4
#
# r/R          U/Ub         W/Ub
 -0.97        0.822402     0.278796
 -0.95999     0.865196     0.289214
 -0.94999     0.889444     0.294398
 -0.93        0.929124     0.305005
 -0.91        0.952346     0.310217
 -0.88999     0.971556     0.317036
 -0.87        0.982359     0.319729
 -0.85        0.990259     0.323362
 -0.8         0.990156     0.329416
 -0.75        0.987587     0.333114
 -0.69999     0.988552     0.330414
 -0.64999     0.989163     0.320852
 -0.6         1.007751     0.294596
 -0.55        1.01726      0.255752
 -0.5         1.039834     0.211805
 -0.44999     1.062549     0.164804
 -0.4         1.085514     0.119823
 -0.34999     1.119025     0.083295
 -0.3         1.152593     0.054129
 -0.25        1.195797     0.033363
 -0.2         1.223261     0.012544
 -0.15        1.259065     0.001116
 -0.1         1.288616    -0.00858
 -0.05        1.305327    -0.01628
  0           1.328096    -0.01667
  0.05        1.336444    -0.01644
  0.1         1.335139    -0.01379
  0.15        1.331708    -0.01784
  0.2         1.308228    -0.02104
  0.25        1.290592    -0.03183
  0.3         1.257462    -0.04404
  0.349999    1.219549    -0.06235
  0.4         1.177229    -0.08788
  0.449999    1.137387    -0.11614
  0.5         1.108644    -0.15373
  0.55        1.067231    -0.19358
  0.6         1.048498    -0.2308
  0.649999    1.021751    -0.2664
  0.699999    1.004812    -0.29268
  0.75        0.989834    -0.30748
  0.8         0.971727    -0.31384
  0.85        0.963097    -0.32159
  0.87        0.946566    -0.31859
  0.889999    0.939599    -0.32167
  0.91        0.922468    -0.32216
  0.93        0.89627     -0.32149
  0.949999    0.85623     -0.31891
  0.959999    0.823991    -0.31008
  0.97        0.779611    -0.29781