# Steenbergen Pipe Flow with Swirl Data
# Concentrated Vortex Case, Re=300,000
#
# Mean velocity
# x/D= 34.9
#
# r/R          U/Ub         W/Ub
 -0.97        0.818495     0.184568
 -0.95999     0.855065     0.187475
 -0.94999     0.881783     0.188131
 -0.93        0.917149     0.185158
 -0.91        0.941051     0.183699
 -0.88999     0.964617     0.178042
 -0.87        0.975497     0.173443
 -0.85        0.985833     0.166353
 -0.8         1.009866     0.153084
 -0.75        1.025377     0.142073
 -0.69999     1.037882     0.133555
 -0.64999     1.047663     0.130459
 -0.6         1.057957     0.126419
 -0.55        1.060847     0.123567
 -0.5         1.065758     0.127684
 -0.44999     1.069506     0.132266
 -0.4         1.070564     0.140619
 -0.34999     1.064686     0.142224
 -0.3         1.065211     0.147502
 -0.25        1.059654     0.14613
 -0.2         1.054534     0.137382
 -0.15        1.045664     0.129201
 -0.1         1.036762     0.105715
 -0.05        1.032531     0.076999
  0           1.026078     0.092973
  0.05        1.031299     0.012734
  0.1         1.026243    -0.03408
  0.15        1.02555     -0.08512
  0.2         1.035227    -0.1127
  0.25        1.030268    -0.15708
  0.3         1.043722    -0.17811
  0.349999    1.05184     -0.18437
  0.4         1.052831    -0.18792
  0.449999    1.05951     -0.18233
  0.5         1.056824    -0.18219
  0.55        1.058276    -0.17112
  0.6         1.057288    -0.16709
  0.649999    1.047762    -0.16403
  0.699999    1.043316    -0.16189
  0.75        1.032359    -0.1614
  0.8         1.014823    -0.16371
  0.85        0.988008    -0.17267
  0.87        0.97652     -0.17518
  0.889999    0.957381    -0.17758
  0.91        0.94183     -0.18309
  0.93        0.915269    -0.18692
  0.949999    0.87704     -0.183
  0.959999    0.853736    -0.18177
  0.97        0.822319    -0.17885