# Steenbergen Pipe Flow with Swirl Data # Concentrated Vortex Case, Re=50,000 # # Mean velocity # x/D= 4.3 # # r/R U/Ub W/Ub -0.97 0.8368 0.2422 -0.96 0.8759 0.2408 -0.95 0.906 0.2406 -0.93 0.9429 0.2373 -0.91 0.9695 0.2336 -0.89 0.9976 0.234 -0.87 1.011 0.231 -0.85 1.032 0.2303 -0.8 1.056 0.2273 -0.75 1.076 0.2295 -0.7 1.089 0.2339 -0.65 1.094 0.2422 -0.6 1.099 0.2565 -0.55 1.097 0.2696 -0.5 1.097 0.2863 -0.45 1.094 0.3036 -0.4 1.081 0.3257 -0.35 1.073 0.351 -0.3 1.052 0.3776 -0.25 1.018 0.3982 -0.2 0.9662 0.4089 -0.15 0.8929 0.3839 -0.1 0.8183 0.3283 -0.05 0.7461 0.2038 0 0.7062 0.02544 0.05 0.7122 -0.1185 0.1 0.7642 -0.2748 0.15 0.8365 -0.3813 0.2 0.9081 -0.4254 0.25 0.9652 -0.4374 0.3 1.011 -0.4209 0.35 1.038 -0.3999 0.4 1.056 -0.3686 0.45 1.073 -0.3429 0.5 1.082 -0.3183 0.55 1.086 -0.2985 0.6 1.088 -0.2812 0.65 1.08 -0.2627 0.7 1.074 -0.2522 0.75 1.061 -0.2443 0.8 1.032 -0.2387 0.85 1 -0.2436 0.87 0.9826 -0.2478 0.89 0.9696 -0.2509 0.91 0.9438 -0.2566 0.93 0.9074 -0.2543 0.95 0.8721 -0.2566 0.96 0.8357 -0.2665 0.97 0.7858 -0.2446 0 0.7272 0.03533 0.02 0.7145 -0.03456 0.04 0.7171 -0.1159 0.06 0.7377 -0.1793 0.08 0.7524 -0.2369 0.1 0.7769 -0.2886 0.12 0.7993 -0.3367 0.14 0.8323 -0.3737 0.16 0.8492 -0.397 0.18 0.8836 -0.4176 0.2 0.913 -0.4303