# Steenbergen Pipe Flow with Swirl Data
# Wall Jet Case, Re=300,000
#
# Mean velocity
# x/D= 4.4
#
# r/R          U/Ub         W/Ub
 -0.97        0.871563     0.285197
 -0.95999     0.906244     0.292217
 -0.94999     0.932783     0.301783
 -0.93        0.954022     0.310634
 -0.91        0.980952     0.318673
 -0.88999     0.989349     0.323539
 -0.87        0.993066     0.328847
 -0.85        0.995352     0.333282
 -0.8         0.989972     0.342438
 -0.75        0.984865     0.349869
 -0.69999     0.981346     0.350171
 -0.64999     0.980129     0.343279
 -0.6         0.984306     0.321358
 -0.55        0.989487     0.283397
 -0.5         0.999846     0.238559
 -0.44999     1.013255     0.185044
 -0.4         1.032886     0.135895
 -0.34999     1.063639     0.093795
 -0.3         1.095261     0.061069
 -0.25        1.127952     0.036139
 -0.2         1.15816      0.017666
 -0.15        1.188215     0.003745
 -0.1         1.217823    -0.0049
 -0.05        1.23995     -0.0124
  0           1.256549    -0.01702
  0.05        1.261496    -0.01724
  0.1         1.262535    -0.01845
  0.15        1.252851    -0.02193
  0.2         1.23364     -0.02883
  0.25        1.205257    -0.03821
  0.3         1.17391     -0.05579
  0.349999    1.14456     -0.07871
  0.4         1.104109    -0.10477
  0.449999    1.076784    -0.13999
  0.5         1.046604    -0.18121
  0.55        1.024111    -0.22269
  0.6         1.009407    -0.26182
  0.649999    0.99702     -0.29404
  0.699999    0.991045    -0.31782
  0.75        0.985321    -0.32744
  0.8         0.981085    -0.33484
  0.85        0.971151    -0.33605
  0.87        0.964112    -0.33872
  0.889999    0.954064    -0.34103
  0.91        0.942986    -0.34314
  0.93        0.922841    -0.34613
  0.949999    0.891503    -0.34249
  0.959999    0.867143    -0.33605
  0.97        0.825582    -0.32066