% Kalpakli, A. and Örlü, R. (2013) 
% Turbulent pipe flow downstream a 90° pipe bend with and without 
% superimposed swirl, Int. J. Heat Fluid Flow, 41:103-110. 
% http://dx.doi.org/10.1007/s00348-013-1483-9  
% Contact: Ramis Örlü (ramis@mech.kth.se) 
% 
% Data corresponds to those shown in Fig. 2b and 2c (S=0 only) 
% Velocities are normalised using bulk velocity, Ub 
% and distances by the pipe radius, R 
% Hot-wire measurements done by: Sohrab S. Sattarzadeh (sohrab@mech.kth.se) 
% For experimental setup and measurement details see above reference 
% as well as http://kth.diva-portal.org/smash/get/diva2:430330/FULLTEXT01.pdf 
% in which further details regarding the hot-wire measurements are given. 
% Inner diameter D [mm]:	60.3 
% Curvature radius [mm]:	95.3 
% Version 1.0, 10-Dec-2014 
%
% Ubulk=3.53m/s,Re=14000   Ub=6.04m/s,Re=24000   Ub=8.56m/s,Re=34000 
% r/R W/Ub		r/R W/Ub		r/R W/Ub
-0.933 1.161 		 -0.933 1.176 		 -0.933 1.145 
-0.900 1.198 		 -0.900 1.207 		 -0.900 1.176 
-0.867 1.212 		 -0.867 1.215 		 -0.867 1.185 
-0.833 1.216 		 -0.833 1.220 		 -0.833 1.185 
-0.800 1.212 		 -0.800 1.221 		 -0.800 1.187 
-0.767 1.214 		 -0.767 1.221 		 -0.767 1.189 
-0.733 1.213 		 -0.733 1.222 		 -0.733 1.187 
-0.667 1.207 		 -0.667 1.220 		 -0.667 1.184 
-0.600 1.205 		 -0.600 1.212 		 -0.600 1.180 
-0.533 1.197 		 -0.533 1.204 		 -0.533 1.171 
-0.467 1.185 		 -0.467 1.191 		 -0.467 1.159 
-0.400 1.169 		 -0.400 1.175 		 -0.400 1.143 
-0.333 1.144 		 -0.333 1.152 		 -0.333 1.122 
-0.267 1.110 		 -0.267 1.123 		 -0.267 1.095 
-0.200 1.061 		 -0.200 1.079 		 -0.200 1.056 
-0.133 0.982 		 -0.133 1.016 		 -0.133 0.993 
-0.067 0.893 		 -0.067 0.922 		 -0.067 0.908 
0.000 0.795 		 0.000 0.820 		 0.000 0.802 
0.067 0.710 		 0.067 0.724 		 0.067 0.710 
0.133 0.645 		 0.133 0.658 		 0.133 0.647 
0.200 0.621 		 0.200 0.631 		 0.200 0.623 
0.267 0.618 		 0.267 0.633 		 0.267 0.627 
0.333 0.626 		 0.333 0.646 		 0.333 0.641 
0.400 0.640 		 0.400 0.660 		 0.400 0.661 
0.467 0.643 		 0.467 0.667 		 0.467 0.678 
0.533 0.640 		 0.533 0.673 		 0.533 0.686 
0.600 0.627 		 0.600 0.672 		 0.600 0.692 
0.667 0.614 		 0.667 0.668 		 0.667 0.692 
0.733 0.601 		 0.733 0.664 		 0.733 0.691 
0.767 0.594 		 0.767 0.661 		 0.767 0.688 
0.800 0.580 		 0.800 0.654 		 0.800 0.680 
0.833 0.583 		 0.833 0.645 		 0.833 0.672 
0.867 0.575 		 0.867 0.638 		 0.867 0.656 
0.900 0.561 		 0.900 0.620 		 0.900 0.638 
0.933 0.537 		 0.933 0.597 		 0.933 0.614