# Steenbergen Pipe Flow with Swirl Data # Concentrated Vortex Case, Re=300,000 # # Mean velocity # x/D= 7.7 # # r/R U/Ub W/Ub -0.97 0.8674 0.2614 -0.96 0.9015 0.2612 -0.95 0.9246 0.2614 -0.93 0.9601 0.2588 -0.91 0.9846 0.2541 -0.89 1.001 0.2495 -0.87 1.019 0.2465 -0.85 1.025 0.2406 -0.8 1.056 0.242 -0.75 1.069 0.2473 -0.7 1.083 0.2574 -0.65 1.084 0.2731 -0.6 1.083 0.2932 -0.55 1.078 0.3175 -0.5 1.072 0.3428 -0.45 1.063 0.3769 -0.4 1.048 0.4099 -0.35 1.025 0.4477 -0.3 0.9851 0.4915 -0.25 0.9334 0.5404 -0.2 0.8467 0.5324 -0.15 0.7504 0.515 -0.1 0.662 0.3452 -0.05 0.6183 0.1004 0 0.6355 -0.1961 0.05 0.7025 -0.4036 0.1 0.7845 -0.4926 0.15 0.881 -0.516 0.2 0.9559 -0.4979 0.25 1.003 -0.4629 0.3 1.038 -0.4177 0.35 1.055 -0.3821 0.4 1.068 -0.3426 0.45 1.072 -0.315 0.5 1.075 -0.2907 0.55 1.076 -0.2687 0.6 1.074 -0.2501 0.65 1.072 -0.2347 0.7 1.067 -0.227 0.75 1.051 -0.2162 0.8 1.037 -0.215 0.85 1.013 -0.2165 0.87 0.9963 -0.2197 0.89 0.9814 -0.225 0.91 0.9619 -0.2281 0.93 0.9366 -0.2319 0.95 0.899 -0.2362 0.96 0.8656 -0.2376 0.97 0.8224 -0.2372 -0.2 0.8445 0.5261 -0.18 0.8103 0.5159 -0.16 0.7755 0.5018 -0.14 0.7314 0.4614 -0.12 0.7049 0.4165 -0.1 0.6625 0.3392 -0.08 0.6375 0.2583 -0.06 0.6213 0.1548 -0.04 0.6183 0.04576 -0.02 0.6228 -0.07291 0 0.6334 -0.194 0.02 0.6505 -0.266 0.04 0.677 -0.3945 0.06 0.7102 -0.4824 0.08 0.7485 -0.4834 0.1 0.7891 -0.4744 0.12 0.8263 -0.493 0.14 0.864 -0.5056 0.16 0.9003 -0.4961 0.18 0.932 -0.4942 0.2 0.9555 -0.4807