# Steenbergen Pipe Flow with Swirl Data # Concentrated Vortex Case, Re=300,000 # # Mean velocity # x/D= 11.5 # # r/R U/Ub W/Ub -0.97 0.8524 0.2554 -0.96 0.8838 0.2543 -0.95 0.9087 0.2546 -0.93 0.9442 0.2496 -0.91 0.9561 0.2538 -0.89 0.9753 0.2491 -0.87 0.9882 0.244 -0.85 1.004 0.2406 -0.8 1.03 0.2379 -0.75 1.05 0.243 -0.7 1.061 0.2508 -0.65 1.064 0.2633 -0.6 1.068 0.2809 -0.55 1.067 0.3013 -0.5 1.066 0.3268 -0.45 1.059 0.3532 -0.4 1.052 0.3863 -0.35 1.034 0.4273 -0.3 1.006 0.4684 -0.25 0.9641 0.5169 -0.2 0.903 0.5404 -0.15 0.8238 0.5562 -0.1 0.7753 0.4569 -0.05 0.7679 0.1434 0 0.7869 -0.2271 0.05 0.8083 -0.4446 0.1 0.8645 -0.5052 0.15 0.9424 -0.4984 0.2 0.9965 -0.4734 0.2 0.997 -0.4655 0.25 1.037 -0.4197 0.3 1.055 -0.3778 0.35 1.07 -0.3392 0.4 1.078 -0.3059 0.45 1.084 -0.2799 0.5 1.082 -0.2592 0.55 1.081 -0.2394 0.6 1.077 -0.2241 0.65 1.065 -0.2109 0.7 1.049 -0.2045 0.75 1.034 -0.2055 0.8 1.015 -0.2137 0.85 0.9861 -0.2292 0.87 0.9748 -0.2359 0.89 0.9573 -0.2438 0.91 0.9424 -0.2536 0.93 0.9199 -0.2513 0.95 0.8844 -0.2594 0.96 0.8523 -0.2596 -0.96 0.8623 0.2535 -0.94 0.9108 0.2522 -0.92 0.9413 0.2469 -0.9 0.9613 0.2428 -0.85 0.9994 0.2337 -0.8 1.027 0.2298 -0.75 1.043 0.2321 -0.14 0.8168 0.5341 -0.12 0.7985 0.4746 -0.1 0.7908 0.4129 -0.08 0.7255 0.4211 -0.06 0.7523 0.2442 -0.04 0.7569 0.07433 -0.02 0.7527 -0.1139 0 0.756 -0.2493 0.02 0.7338 -0.4035 0.04 0.7919 -0.3923 0.06 0.8126 -0.4534 0.08 0.8329 -0.4814 0.1 0.8632 -0.5015 0.12 0.8848 -0.5025 0.14 0.9173 -0.5024 0.16 0.9409 -0.4921 0.18 0.97 -0.476 0.2 0.9868 -0.458 0.22 1.005 -0.4427 0.24 1.018 -0.4227 0.26 1.032 -0.4031 0.7 1.044 -0.1982 0.75 1.029 -0.2009 0.8 1.007 -0.2041 0.85 0.9816 -0.2179 0.9 0.9472 -0.2373 0.92 0.9289 -0.2444 0.94 0.8964 -0.2494 0.96 0.8493 -0.2583