# Steenbergen Pipe Flow with Swirl Data # Concentrated Vortex Case, Re=300,000 # # Mean velocity # x/D= 4.3 # # r/R U/Ub W/Ub -0.97 0.8472 0.2428 -0.96 0.8791 0.2435 -0.95 0.9006 0.2413 -0.93 0.9361 0.239 -0.91 0.9571 0.2327 -0.89 0.9749 0.2307 -0.87 0.9926 0.2278 -0.85 1.004 0.2249 -0.8 1.038 0.2245 -0.75 1.058 0.2276 -0.7 1.082 0.2376 -0.65 1.099 0.2514 -0.6 1.107 0.2711 -0.55 1.114 0.2968 -0.5 1.113 0.325 -0.45 1.114 0.3583 -0.4 1.105 0.4017 -0.35 1.093 0.448 -0.3 1.063 0.5051 -0.25 1.011 0.5676 -0.2 0.9312 0.6275 -0.15 0.8063 0.6636 -0.1 0.637 0.7268 -0.05 0.4176 0.4567 0 0.2911 0.1192 0.05 0.3094 -0.216 0.1 0.4552 -0.4824 0.15 0.6525 -0.6735 0.2 0.8154 -0.6639 0.25 0.9363 -0.6311 0.3 1.008 -0.5683 0.35 1.064 -0.5081 0.4 1.082 -0.452 0.45 1.094 -0.4056 0.5 1.103 -0.3615 0.55 1.104 -0.331 0.6 1.097 -0.3035 0.65 1.086 -0.2805 0.7 1.073 -0.2624 0.75 1.057 -0.248 0.8 1.037 -0.2372 0.85 1.013 -0.2325 0.87 0.9942 -0.2326 0.89 0.9865 -0.2309 0.91 0.9647 -0.2333 0.93 0.9409 -0.2342 0.95 0.9001 -0.236 0.96 0.8763 -0.2347 0.97 0.8384 -0.2372 -0.2 0.9341 0.6382 -0.18 0.8904 0.6657 -0.16 0.8183 0.6525 -0.14 0.7731 0.7044 -0.12 0.6947 0.6992 -0.1 0.6191 0.688 -0.08 0.5355 0.6196 -0.06 0.4754 0.6817 -0.04 0.3987 0.4822 -0.02 0.3432 0.3323 0 0.3055 0.1305 0.02 0.2993 -0.0569 0.04 0.3171 -0.2385 0.06 0.3596 -0.4668 0.08 0.4196 -0.683 0.1 0.4808 -0.5537 0.1 0.4814 -0.6237 0.12 0.5663 -0.7167 0.14 0.6432 -0.7354 0.16 0.7103 -0.7276 0.18 0.776 -0.7098 0.2 0.8261 -0.681