# Steenbergen Pipe Flow with Swirl Data # Wall Jet Case, Re=50,000 # # Mean velocity # x/D= 9.6 # # r/R U/Ub W/Ub -0.97 0.781691 0.266582 -0.95999 0.822491 0.280501 -0.94999 0.851583 0.286522 -0.93 0.895404 0.2872 -0.91 0.926708 0.289453 -0.88999 0.949337 0.286911 -0.87 0.962664 0.28229 -0.85 0.974774 0.277066 -0.8 1.008722 0.257943 -0.75 1.028653 0.236877 -0.69999 1.055923 0.219825 -0.64999 1.08105 0.199617 -0.6 1.099911 0.17958 -0.55 1.131234 0.162478 -0.5 1.151666 0.14742 -0.44999 1.16595 0.134403 -0.4 1.188341 0.122275 -0.34999 1.202144 0.110973 -0.3 1.215744 0.101209 -0.25 1.223289 0.090538 -0.2 1.228749 0.088647 -0.15 1.231266 0.080536 -0.1 1.227582 0.071419 -0.05 1.220053 0.060803 0 1.209485 0.050261 0.05 1.202813 0.030526 0.1 1.189516 0.013436 0.15 1.177491 -0.01134 0.2 1.16056 -0.03756 0.25 1.145764 -0.06283 0.3 1.130647 -0.08815 0.349999 1.11042 -0.11335 0.4 1.087478 -0.13793 0.449999 1.074502 -0.15737 0.5 1.050358 -0.17388 0.55 1.031528 -0.19157 0.6 1.009597 -0.20264 0.649999 0.994076 -0.21481 0.699999 0.980242 -0.23054 0.75 0.958443 -0.24432 0.8 0.945562 -0.25741 0.85 0.917073 -0.27275 0.87 0.906829 -0.28181 0.889999 0.89254 -0.28724 0.91 0.870739 -0.28718 0.93 0.848261 -0.28762 0.949999 0.812996 -0.28434 0.97 0.731957 -0.27503