# Steenbergen Pipe Flow with Swirl Data
# Wall Jet Case, Re=50,000
#
# Mean velocity
# x/D= 28.1
#
# r/R          U/Ub         W/Ub
 -0.97        0.720187     0.193464
 -0.95999     0.752354     0.199329
 -0.94999     0.785276     0.198986
 -0.93        0.8245       0.195338
 -0.91        0.843814     0.193551
 -0.88999     0.867963     0.191179
 -0.87        0.882478     0.183902
 -0.85        0.896992     0.181102
 -0.8         0.919388     0.162518
 -0.75        0.939758     0.144664
 -0.69999     0.951566     0.123997
 -0.64999     0.961336     0.108221
 -0.6         0.973553     0.087109
 -0.55        0.977768     0.068175
 -0.5         0.986229     0.052443
 -0.44999     1.000075     0.03945
 -0.4         1.002931     0.025153
 -0.34999     1.019607     0.014319
 -0.3         1.025219     0.005418
 -0.25        1.042354    -0.00226
 -0.2         1.05039     -0.0116
 -0.15        1.059879    -0.01572
 -0.1         1.080369    -0.01918
 -0.05        1.086497    -0.02311
  0           1.101163    -0.0317
  0.05        1.106864    -0.03485
  0.1         1.113719    -0.04013
  0.15        1.117309    -0.0446
  0.2         1.117796    -0.04875
  0.25        1.127557    -0.05517
  0.3         1.131971    -0.06117
  0.349999    1.128857    -0.06557
  0.4         1.136281    -0.07235
  0.449999    1.137876    -0.07934
  0.5         1.136436    -0.08568
  0.55        1.137353    -0.09348
  0.6         1.13529     -0.10445
  0.649999    1.132648    -0.11465
  0.699999    1.126747    -0.12429
  0.75        1.114805    -0.13355
  0.8         1.088679    -0.14209
  0.85        1.048591    -0.15036
  0.87        1.024098    -0.15265
  0.889999    0.999805    -0.15455
  0.91        0.966247    -0.15928
  0.93        0.925213    -0.16113
  0.949999    0.871832    -0.16335
  0.959999    0.83558     -0.15144
  0.97        0.775383    -0.15165