Simulation results for Case 1 (G_in = 474 kg/m^2s, q_w = 152.3 kW/m^2) by Yeoh & Tu (2005). All profiles are recorded at the axial location x = L_m. (r-Ri)/(Ro-Ri) [-], vapour volume fraction [-] 0.042, 0.281 0.059, 0.304 0.074, 0.323 0.086, 0.338 0.098, 0.352 0.111, 0.362 0.120, 0.366 0.130, 0.366 0.147, 0.359 0.170, 0.348 0.187, 0.337 0.199, 0.323 0.214, 0.305 0.233, 0.285 0.248, 0.267 0.256, 0.251 0.278, 0.229 0.297, 0.207 0.327, 0.178 0.354, 0.151 0.381, 0.132 0.410, 0.111 0.450, 0.093 0.479, 0.079 0.523, 0.062 0.553, 0.047 0.590, 0.033 0.631, 0.021 0.683, 0.011 0.720, 0.007 0.771, 0.001 0.808, 0.001 0.855, 0.000 (r-Ri)/(Ro-Ri) [-], axial liquid velocity [m/s] 0.044, 0.691 0.083, 0.691 0.122, 0.691 0.169, 0.688 0.220, 0.678 0.267, 0.668 0.333, 0.650 0.394, 0.629 0.452, 0.606 0.504, 0.594 0.545, 0.576 0.594, 0.560 0.643, 0.540 0.682, 0.525 0.719, 0.509 0.768, 0.491 0.814, 0.479 0.858, 0.461 0.892, 0.443 0.929, 0.420 0.958, 0.397 (r-Ri)/(Ro-Ri) [-], axial vapour velocity [m/s] 0.038, 0.870 0.062, 0.878 0.091, 0.891 0.115, 0.901 0.143, 0.898 0.184, 0.896 0.222, 0.881 0.265, 0.860 0.301, 0.853 0.344, 0.843 0.372, 0.835 0.427, 0.820 0.463, 0.807 0.516, 0.792 0.558, 0.777 0.616, 0.759 0.678, 0.738 0.718, 0.721 0.761, 0.700 0.800, 0.672 0.835, 0.632 0.866, 0.581 0.893, 0.548 0.924, 0.517 0.943, 0.502 0.959, 0.484 Simulation results for Case 2 (G_in = 1059.2 kg/m^2s, q_w = 251.5 kW/m^2) by Yeoh & Tu (2005). All profiles are recorded at the axial location x = L_m. (r-Ri)/(Ro-Ri) [-], vapour volume fraction [-] 0.035, 0.311 0.056, 0.297 0.073, 0.288 0.086, 0.280 0.101, 0.271 0.114, 0.259 0.129, 0.242 0.141, 0.225 0.159, 0.199 0.174, 0.178 0.189, 0.156 0.215, 0.126 0.237, 0.108 0.270, 0.086 0.303, 0.064 0.333, 0.048 0.356, 0.037 0.396, 0.024 0.429, 0.016 0.475, 0.009 0.523, 0.005 0.568, 0.003 0.609, 0.001 0.659, 0.000 0.715, 0.000 0.790, 0.000 0.856, 0.000 0.929, 0.000 0.995, 0.000 (r-Ri)/(Ro-Ri) [-], axial liquid velocity [m/s] 0.039, 1.314 0.083, 1.322 0.129, 1.326 0.166, 1.330 0.215, 1.326 0.263, 1.318 0.322, 1.302 0.368, 1.293 0.412, 1.273 0.471, 1.253 0.520, 1.232 0.566, 1.216 0.602, 1.196 0.646, 1.172 0.693, 1.147 0.744, 1.119 0.788, 1.086 0.824, 1.062 0.861, 1.021 0.895, 0.981 0.920, 0.940 0.939, 0.899 0.961, 0.855 (r-Ri)/(Ro-Ri) [-], axial vapour velocity [m/s] 0.039, 1.501 0.085, 1.517 0.128, 1.529 0.174, 1.533 0.218, 1.537 0.262, 1.537 0.295, 1.525 0.341, 1.517 0.390, 1.505 0.426, 1.493 0.475, 1.469 0.525, 1.453 0.571, 1.430 0.605, 1.410 0.627, 1.394 0.654, 1.362 0.680, 1.327 0.702, 1.291 0.722, 1.251 0.755, 1.220 0.785, 1.196 0.814, 1.168 0.845, 1.133 0.867, 1.117 0.896, 1.073 0.918, 1.034 0.935, 1.006 0.954, 0.966 0.964, 0.954