# Steenbergen Pipe Flow with Swirl Data
# Wall Jet Case, Re=300,000
#
# Mean velocity
# x/D= 7.6
#
# r/R          U/Ub         W/Ub
 -0.97        0.798747     0.322405
 -0.95999     0.831688     0.335692
 -0.94999     0.86325      0.338562
 -0.93        0.89285      0.342402
 -0.91        0.913911     0.341327
 -0.88999     0.926225     0.337776
 -0.87        0.939256     0.335689
 -0.85        0.94982      0.332507
 -0.8         0.968183     0.322636
 -0.75        0.989457     0.312604
 -0.69999     1.008388     0.298705
 -0.64999     1.027584     0.278753
 -0.6         1.044507     0.252236
 -0.55        1.064836     0.221136
 -0.5         1.082439     0.19006
 -0.44999     1.102669     0.157449
 -0.4         1.124125     0.128078
 -0.34999     1.141154     0.100976
 -0.3         1.161677     0.083174
 -0.25        1.178279     0.067641
 -0.2         1.19209      0.055904
 -0.15        1.201867     0.04489
 -0.1         1.206319     0.038612
 -0.05        1.209011     0.032085
  0           1.200702     0.025589
  0.05        1.188269     0.015565
  0.1         1.172435     0.004312
  0.15        1.152571    -0.01321
  0.2         1.137815    -0.03374
  0.25        1.11726     -0.06131
  0.3         1.101549    -0.09192
  0.349999    1.084831    -0.12734
  0.4         1.074893    -0.15948
  0.449999    1.058544    -0.19833
  0.5         1.048922    -0.23555
  0.55        1.039101    -0.26098
  0.6         1.028709    -0.28563
  0.649999    1.021535    -0.29867
  0.699999    1.011804    -0.30609
  0.75        1.003751    -0.30693
  0.8         0.995798    -0.30858
  0.85        0.984185    -0.31159
  0.87        0.97671     -0.31475
  0.889999    0.969356    -0.3191
  0.91        0.954849    -0.31883
  0.93        0.938162    -0.32157
  0.949999    0.905904    -0.31696
  0.959999    0.878958    -0.31093
  0.97        0.842552    -0.29845