# Circular to Rectangular Transition Duct Reb=390,000 # Expt. data of Davis & Gessner # Total Pressure (Pt-Pi)/Qref, Station 1, Traverse y3 # y/R (Pt-Pi)/Qref 1.00000 0.00000 0.99851 0.14013 0.99726 0.25323 0.99602 0.29449 0.99478 0.33532 0.99353 0.35423 0.99229 0.37570 0.99104 0.39460 0.98856 0.41984 0.98607 0.45127 0.98358 0.47016 0.98109 0.48883 0.97861 0.50860 0.97612 0.52275 0.97363 0.53739 0.96866 0.56418 0.96368 0.58548 0.95871 0.60736 0.95373 0.62249 0.94876 0.64104 0.94378 0.66460 0.93881 0.67507 0.93383 0.69344 0.92886 0.70900 0.92388 0.72063 0.91891 0.73718 0.91393 0.75102 0.90896 0.76244 0.90398 0.78408 0.89900 0.79314 0.89403 0.80648 0.88408 0.83297 0.87413 0.86006 0.86418 0.88004 0.85423 0.91208 0.84428 0.93372 0.83433 0.95648 0.82438 0.97525 0.81443 0.99292 0.80448 1.02180 0.79453 1.03513 0.78458 1.05133 0.77463 1.06740 0.76468 1.08848 0.75473 1.09599 0.74478 1.12071 0.73483 1.12878 0.72488 1.13402 0.71493 1.13784 0.70498 1.14105 0.69502 1.15250 0.68507 1.14746 0.67512 1.15110 0.66269 1.15586 0.65025 1.15476 0.62537 1.16144 0.60050 1.15159 0.57562 1.16419 0.55075 1.16035 0.50100 1.14934 0.45124 1.15021 0.40149 1.14686 0.35174 1.14992 0.30199 1.15537 0.25224 1.15628 0.20249 1.16177 0.15274 1.15422 0.10299 1.15105 0.05323 1.14973 0.00000 1.14872