# Steenbergen Pipe Flow with Swirl Data
# Concentrated Vortex Case, Re=50,000
#
# Mean velocity
# x/D= 28.1
#
# r/R          U/Ub         W/Ub
 -0.97        0.755997     0.151041
 -0.95999     0.795001     0.154533
 -0.94999     0.827372     0.155784
 -0.93        0.869319     0.15759
 -0.91        0.906096     0.155072
 -0.88999     0.931761     0.156967
 -0.87        0.952504     0.152436
 -0.85        0.967583     0.144773
 -0.8         0.998988     0.136254
 -0.75        1.026309     0.12693
 -0.69999     1.034354     0.117523
 -0.64999     1.057026     0.10978
 -0.6         1.06701      0.105643
 -0.55        1.069421     0.099911
 -0.5         1.076595     0.102649
 -0.44999     1.080293     0.09635
 -0.4         1.087731     0.100301
 -0.34999     1.086828     0.09744
 -0.3         1.092701     0.095528
 -0.25        1.091559     0.090411
 -0.2         1.098891     0.088809
 -0.15        1.094965     0.080028
 -0.1         1.099672     0.077506
 -0.05        1.099181     0.066144
  0           1.09485      0.045896
  0.05        1.095046     0.032338
  0.1         1.092958     0.016603
  0.15        1.090226     0.000441
  0.2         1.084502    -0.02798
  0.25        1.088882    -0.04256
  0.3         1.082923    -0.06437
  0.349999    1.083546    -0.07993
  0.4         1.078351    -0.10494
  0.449999    1.079642    -0.11172
  0.5         1.072874    -0.12572
  0.55        1.06588     -0.13327
  0.6         1.063814    -0.14125
  0.649999    1.051004    -0.1471
  0.699999    1.042334    -0.15672
  0.75        1.034526    -0.16291
  0.8         1.011038    -0.16884
  0.85        0.976511    -0.18166
  0.87        0.965502    -0.18537
  0.889999    0.944508    -0.18903
  0.91        0.91553     -0.18988
  0.93        0.88625     -0.18976
  0.949999    0.834226    -0.19445
  0.959999    0.813275    -0.19443
  0.97        0.776431    -0.18756