Experimental data for Case 1 (G_in = 474 kg/m^2s, q_w = 152.3 kW/m^2) by Lee et al. (2002).
All profiles are recorded at the axial location x = L_m.

(r-Ri)/(Ro-Ri) [-],	vapour volume fraction [-]
0.118,	0.255
0.182,	0.273
0.248,	0.240
0.312,	0.188
0.376,	0.148
0.442,	0.114
0.509,	0.079
0.572,	0.058
0.636,	0.036
0.700,	0.021
0.767,	0.010
0.830,	0.007
0.897,	0.005

(r-Ri)/(Ro-Ri) [-], axial liquid velocity [m/s]
0.120,	0.681
0.186,	0.691
0.249,	0.696
0.313,	0.668
0.377,	0.652
0.445,	0.635
0.509,	0.622
0.572,	0.599
0.638,	0.578
0.704,	0.548
0.768,	0.537
0.834,	0.517
0.897,	0.517

(r-Ri)/(Ro-Ri) [-],	axial vapour velocity [m/s]
0.115,	0.731
0.181,	0.741
0.248,	0.751
0.313,	0.751
0.377,	0.759
0.442,	0.756
0.506,	0.764
0.570,	0.771
0.637,	0.769
0.702,	0.754
0.766,	0.733
0.833,	0.713
0.895,	0.688


Experimental data for Case 2 (G_in = 1059.2 kg/m^2s, q_w = 251.5 kW/m^2) by Lee et al. (2002).
All profiles are recorded at the axial location x = L_m.

(r-Ri)/(Ro-Ri) [-],	vapour volume fraction [-]
0.116,	0.279
0.185,	0.207
0.246,	0.115
0.314,	0.058
0.377,	0.024
0.443,	0.009
0.509,	0.001
0.572,	0.001
0.638,	0.000
0.704,	0.000
0.767,	0.000
0.833,	0.000
0.899,	0.000
 
(r-Ri)/(Ro-Ri) [-],	axial liquid velocity [m/s]
0.117,	1.151
0.183,	1.204
0.249,	1.237
0.312,	1.265
0.378,	1.269
0.444,	1.265
0.507,	1.249
0.571,	1.237
0.634,	1.212
0.700,	1.188
0.766,	1.163
0.832,	1.135
0.898,	1.123

(r-Ri)/(Ro-Ri) [-],	axial vapour velocity [m/s]
0.116,	1.160
0.184,	1.216
0.249,	1.259
0.315,	1.299
0.378,	1.323
0.443,	1.347
0.508,	1.335