Holden, M. S.          Axisymmetric Cone-Flare Data           AIAA Paper 84-1677

Run number = 8
Cone Angle of Attack (degrees) = 0
Angle of Cone (degrees) = 6
Length Along Cone (inches) = 104.6
Angle of Flare (degrees) = 30
Length of Flare (inches) = 9
Reservoir Total Pressure = 7234 PSIA
Reservoir Total Temperature = 2727 deg R
Freestream Mach number = 10.98
Freestream Velocity = 5931 ft/sec
Freestream Static Pressure = 0.09078 PSIA
Freestream Static Temperature = 121.3 deg R
Freestream Reynolds number = 3651000/ft
Wall Enthalpy (Cp*Tw) = 3183000 (Ft/sec)2

WALL PRESSURE & HEAT XFER DATA****BOUNDARY-LAYER DATA***************

Gage # X inches    Press. PSIA   Y inches  U/UE     MACH#     TT/TTE
P1     98.9105     2.366E-01      0.014    0.493    2.186     0.469
P3     100.1195    2.672E-01      0.028    0.572    2.613     0.535
P7     101.9185    2.700E-01      0.042    0.618    2.890     0.576
P9     102.5125    2.686E-01      0.056    0.651    3.105     0.607
P11    103.1135    2.803E-01      0.070    0.676    3.285     0.631
P13    103.7165    2.677E-01      0.084    0.697    3.444     0.652
P14    104.0165    2.669E-01      0.098    0.716    3.589     0.670
P16    104.6765    2.250E+00      0.112    0.731    3.725     0.687
P17    105.1835    5.297E+00      0.127    0.746    3.855     0.702
P18    105.6825    6.390E+00      0.141    0.760    3.981     0.716
P19    106.1825    1.043E+01      0.155    0.772    4.104     0.729
P20    106.6825    9.707E+00      0.169    0.784    4.226     0.742
P21    107.1835    "Null"         0.183    0.795    4.347     0.754
P22    107.6835    9.788E+00      0.197    0.806    4.469     0.766
P24    108.6805    1.063E+01      0.211    0.816    4.591     0.778
P26    109.6825    1.135E+01      0.225    0.826    4.715     0.789
P27    110.6825    9.166E+00      0.239    0.836    4.840     0.800
P28    111.6825    9.016E+00      0.253    0.845    4.967     0.810
P29    112.6825    8.899E+00      0.267    0.854    5.097     0.821
                                  0.281    0.863    5.229     0.831
Gage # X inches    BTU/FT2/SEC    0.295    0.871    5.363     0.841
HT1    98.9105     5.806E+00      0.309    0.880    5.500     0.851
HT5    101.3175    5.603E+00      0.323    0.887    5.639     0.860
HT6    101.6065    6.656E+00      0.337    0.895    5.781     0.869
HT7    101.9185    6.411E+00      0.351    0.902    5.925     0.877
HT8    102.2195    5.153E+00      0.366    0.910    6.072     0.886
HT9    102.5125    "Null"         0.380    0.916    6.221     0.895
HT10   102.8135    5.930E+00      0.394    0.923    6.371     0.902
HT11   103.1135    5.495E+00      0.408    0.929    6.523     0.910
HT12   103.4165    4.726E+00      0.422    0.935    6.677     0.917
HT13   103.7165    6.010E+00      0.436    0.941    6.831     0.924
HT14   104.0165    5.796E+00      0.450    0.946    6.985     0.931
HT16   104.6765    1.124E+02      0.464    0.952    7.140     0.938
HT17   105.1835    1.181E+02      0.478    0.956    7.294     0.944
HT18   105.6825    "Null"         0.492    0.961    7.447     0.950
HT19   106.1825    1.443E+02      0.506    0.965    7.597     0.955
HT20   106.6825    1.323E+02      0.520    0.969    7.746     0.960
HT21   107.1835    1.316E+02      0.534    0.973    7.891     0.965
HT22   107.6835    1.522E+02      0.548    0.976    8.033     0.970
HT23   108.1765    1.392E+02      0.562    0.980    8.170     0.974
HT24   108.6805    1.208E+02      0.576    0.983    8.301     0.978
HT25   109.1835    1.048E+02      0.590    0.986    8.427     0.981
HT26   109.6825    1.056E+02      0.605    0.988    8.547     0.985
HT27   110.6825    1.005E+02      0.619    0.991    8.659     0.988
HT28   111.6825    9.250E+01      0.633    0.993    8.763     0.990
HT29   112.6825    9.706E+01      0.647    0.995    8.859     0.993
                                  0.661    0.996    8.946     0.995
                                  0.675    0.998    9.024     0.997
                                  0.689    0.999    9.092     0.998
                                  0.703    1.000    9.150     1.000

Holden, M. S.          Axisymmetric Cone-Flare Data           AIAA Paper 84-1677

Run number = 4
Cone Angle of Attack (degrees) = 0
Angle of Cone (degrees) = 6
Length Along Cone (inches) = 104.6
Angle of Flare (degrees) = 36
Length of Flare (inches) = 9
Reservoir Total Pressure = 7001 PSIA
Reservoir Total Temperature = 2649 deg R
Freestream Mach number = 10.97
Freestream Velocity = 5836 ft/sec
Freestream Static Pressure = 0.08943 PSIA
Freestream Static Temperature = 117.8 deg R
Freestream Reynolds number = 3755000/ft
Wall Enthalpy (Cp*Tw) = 3183000 (Ft/sec)2

WALL PRESSURE & HEAT XFER DATA****BOUNDARY-LAYER DATA****************

Gage #  X inches   Press. PSIA       Y inches  U/UE    MACH#   TT/TTE
P1      98.9105     2.6728E-01       0.014     0.493   2.186   0.469
P3      100.1195    2.8851E-01       0.028     0.572   2.613   0.535
P7      101.9185    3.4467E-01       0.042     0.618   2.890   0.576
P9      102.5125    8.0524E-01       0.056     0.651   3.105   0.607
P11     103.1135   1.29314E+00       0.070     0.676   3.285   0.631
P13     103.7165   1.38824E+00       0.084     0.697   3.444   0.652
P14     104.0165   1.53297E+00       0.098     0.716   3.589   0.670
P16     104.6765   1.30152E+00       0.112     0.731   3.725   0.687
P17     105.1835   "Null"            0.127     0.746   3.855   0.702
P18     105.6825   "Null"            0.141     0.760   3.981   0.716
P19     106.1825   1.49127E+01       0.155     0.772   4.104   0.729
P20     106.6825   1.51135E+01       0.169     0.784   4.226   0.742
P21     107.1835   1.26621E+01       0.183     0.795   4.347   0.754
P22     107.6835   1.39913E+01       0.197     0.806   4.469   0.766
P24     108.6805   1.45225E+01       0.211     0.816   4.591   0.778
P26     109.6825   1.54217E+01       0.225     0.826   4.715   0.789
P27     110.6825   1.29523E+01       0.239     0.836   4.840   0.800
P28     111.6825   1.19923E+01       0.253     0.845   4.967   0.810
P29     112.6825   1.22768E+01       0.267     0.854   5.097   0.821
                                     0.281     0.863   5.229   0.831
Gage #  X inches   BTU/FT2/SEC       0.295     0.871   5.363   0.841
HT1     98.9105    5.85107E+00       0.309     0.880   5.500   0.851
HT5     101.3175   5.71897E+00       0.323     0.887   5.639   0.860
HT6     101.6065   5.80157E+00       0.337     0.895   5.781   0.869
HT7     101.9185   6.16079E+00       0.351     0.902   5.925   0.877
HT8     102.2195   9.01738E+00       0.366     0.910   6.072   0.886
HT9     102.5125   1.47118E+01       0.380     0.916   6.221   0.895
HT10    102.8135   1.46640E+01       0.394     0.923   6.371   0.902
HT11    103.1135   1.32007E+01       0.408     0.929   6.523   0.910
HT12    103.4165   1.33030E+01       0.422     0.935   6.677   0.917
HT13    103.7165   1.19369E+01       0.436     0.941   6.831   0.924
HT14    104.0165   1.74385E+01       0.450     0.946   6.985   0.931
HT16    104.6765   "Null"            0.464     0.952   7.140   0.938
HT17    105.1835   9.00276E+01       0.478     0.956   7.294   0.944
HT18    105.6825   1.72171E+02       0.492     0.961   7.447   0.950
HT19    106.1825   2.03513E+02       0.506     0.965   7.597   0.955
HT20    106.6825   1.97140E+02       0.520     0.969   7.746   0.960
HT21    107.1835   1.77999E+02       0.534     0.973   7.891   0.965
HT22    107.6835   1.75618E+02       0.548     0.976   8.033   0.970
HT23    108.1765   1.65347E+02       0.562     0.980   8.170   0.974
HT24    108.6805   1.46599E+02       0.576     0.983   8.301   0.978
HT25    109.1835   1.44159E+02       0.590     0.986   8.427   0.981
HT26    109.6825   1.36357E+02       0.605     0.988   8.547   0.985
HT27    110.6825   1.29164E+02       0.619     0.991   8.659   0.988
HT28    111.6825   1.04948E+02       0.633     0.993   8.763   0.990
HT29    112.6825   1.02294E+02       0.647     0.995   8.859   0.993
                                     0.661     0.996   8.946   0.995
                                     0.675     0.998   9.024   0.997
                                     0.689     0.999   9.092   0.998
                                     0.703     1.000   9.150   1.000

Holden, M. S.           Axisymmetric Cone-Flare Data           AIAA Paper 84-1677

Run number = 7
Cone Angle of Attack (degrees) = 0
Angle of Cone (degrees) = 6
Length Along Cone (inches) = 104.6
Angle of Flare (degrees) = 30
Length of Flare (inches) = 9
Reservoir Total Pressure = 17230 PSIA
Reservoir Total Temperature = 3246 deg R
Freestream Mach number = 12.92
Freestream Velocity = 6634 ft/sec
Freestream Static Pressure = 0.07272 PSIA
Freestream Static Temperature = 109.7 deg R
Freestream Reynolds number = 4000000/ft
Wall Enthalpy (Cp*Tw) = 3183000 (Ft/sec)2

WALL PRESSURE & HEAT XFER DATA******BOUNDARY-LAYER DATA************

Gage #  X inches   Press. PSIA      Y inches U/UE    MACH#   TT/TTE
P1      98.9105     2.577E-01       0.015    0.486   2.266   0.445
P3      100.1195    3.032E-01       0.029    0.567   2.718   0.515
P7      101.9185    3.241E-01       0.044    0.614   3.014   0.559
P9      102.5125    3.040E-01       0.059    0.648   3.243   0.591
P11     103.1135    3.605E-01       0.074    0.674   3.437   0.617
P13     103.7165    3.650E-01       0.088    0.696   3.609   0.639
P14     104.0165    4.115E-01       0.103    0.714   3.766   0.659
P16     104.6765   "Null"           0.118    0.731   3.914   0.676
P17     105.1835    6.149E+00       0.133    0.746   4.056   0.692
P18     105.6825    7.350E+00       0.147    0.759   4.194   0.707
P19     106.1825    1.358E+01       0.162    0.772   4.329   0.722
P20     106.6825    1.243E+01       0.177    0.784   4.463   0.735
P21     107.1835   "Null"           0.191    0.795   4.598   0.748
P22     107.6835    1.218E+01       0.206    0.806   4.732   0.760
P24     108.6805    1.394E+01       0.221    0.817   4.869   0.772
P26     109.6825    1.431E+01       0.236    0.827   5.007   0.784
P27     110.6825    1.188E+01       0.250    0.837   5.148   0.795
P28     111.6825    1.175E+01       0.265    0.847   5.291   0.807
P29     112.6825    1.219E+01       0.280    0.856   5.437   0.817
                                    0.295    0.864   5.587   0.828
Gage #  X inches   BTU/FT2/SEC      0.309    0.873   5.740   0.838
HT1     98.9105    "Null"           0.324    0.881   5.896   0.848
HT5     101.3175    8.217E+00       0.339    0.889   6.056   0.858
HT6     101.6065    9.402E+00       0.353    0.897   6.220   0.867
HT7     101.9185    9.852E+00       0.368    0.904   6.387   0.877
HT8     102.2195    8.042E+00       0.383    0.911   6.557   0.885
HT9     102.5125    9.473E+00       0.398    0.918   6.731   0.894
HT10    102.8135    8.531E+00       0.412    0.925   6.907   0.902
HT11    103.1135    8.600E+00       0.427    0.931   7.086   0.910
HT12    103.4165    7.930E+00       0.442    0.937   7.268   0.918
HT13    103.7165    1.013E+01       0.457    0.943   7.451   0.925
HT14    104.0165    8.931E+00       0.471    0.948   7.636   0.932
HT16    104.6765    4.236E+02       0.486    0.953   7.821   0.938
HT17    105.1835    3.791E+02       0.501    0.958   8.006   0.944
HT18    105.6825   "Null"           0.515    0.962   8.191   0.950
HT19    106.1825    3.199E+02       0.530    0.966   8.374   0.955
HT20    106.6825    2.818E+02       0.545    0.970   8.555   0.960
HT21    107.1835    4.178E+02       0.560    0.974   8.733   0.965
HT22    107.6835    3.879E+02       0.574    0.978   8.907   0.970
HT23    108.1765    3.152E+02       0.589    0.981   9.076   0.974
HT24    108.6805    2.296E+02       0.604    0.984   9.239   0.978
HT25    109.1835    2.287E+02       0.619    0.987   9.395   0.981
HT26    109.6825    1.925E+02       0.633    0.989   9.543   0.985
HT27    110.6825    1.819E+02       0.648    0.991   9.683   0.988
HT28    111.6825    1.624E+02       0.663    0.993   9.814   0.990
HT29    112.6825    1.455E+02       0.677    0.995   9.934   0.993
                                    0.692    0.996   10.043  0.995
                                    0.707    0.998   10.141  0.997
                                    0.722    0.999   10.227  0.998
                                    0.736    1.000   10.300  1.000

Holden, M. S.           Axisymmetric Cone-Flare Data           AIAA Paper 84-1677

Run number = 6
Cone Angle of Attack (degrees) = 0
Angle of Cone (degrees) = 6
Length Along Cone (inches) = 104.6
Angle of Flare (degrees) = 36
Length of Flare (inches) = 9
Reservoir Total Pressure = 17600 PSIA
Reservoir Total Temperature = 3104 deg R
Freestream Mach number = 13.10
Freestream Velocity = 6458 ft/sec
Freestream Static Pressure = 0.07345 PSIA
Freestream Static Temperature = 102.6 deg R
Freestream Reynolds number = 5090000/ft
Wall Enthalpy (Cp*Tw) = 3183000 (Ft/sec)2

WALL PRESSURE & HEAT XFER DATA******BOUNDARY-LAYER DATA************

Gage #  X inches   Press. PSIA      Y inches U/UE    MACH#   TT/TTE
P1      98.9105     2.8474E-01      0.015    0.486   2.266   0.445
P3      100.1195    2.9218E-01      0.029    0.567   2.718   0.515
P7      101.9185    4.9656E-01      0.044    0.614   3.014   0.559
P9      102.5125    9.9969E-01      0.059    0.648   3.243   0.591
P11     103.1135    1.3961E+00      0.074    0.674   3.437   0.617
P13     103.7165    1.5696E+00      0.088    0.696   3.609   0.639
P14     104.0165    1.7067E+00      0.103    0.714   3.766   0.659
P16     104.6765    1.5295E+00      0.118    0.731   3.914   0.676
P17     105.1835    5.0433E+00      0.133    0.746   4.056   0.692
P18     105.6825   "Null            0.147    0.759   4.194   0.707
P19     106.1825    1.8144E+01      0.162    0.772   4.329   0.722
P20     106.6825    2.1674E+01      0.177    0.784   4.463   0.735
P21     107.1835   "Null"           0.191    0.795   4.598   0.748
P22     107.6835    1.7335E+01      0.206    0.806   4.732   0.760
P24     108.6805    1.8623E+01      0.221    0.817   4.869   0.772
P26     109.6825    2.0844E+01      0.236    0.827   5.007   0.784
P27     110.6825    1.4811E+01      0.250    0.837   5.148   0.795
P28     111.6825    1.6215E+01      0.265    0.847   5.291   0.807
P29     112.6825    1.6687E+01      0.280    0.856   5.437   0.817
                                    0.295    0.864   5.587   0.828
Gage #  X inches   BTU/FT2/SEC      0.309    0.873   5.740   0.838
HT1     98.9105     8.8680E+00      0.324    0.881   5.896   0.848
HT5     101.3175    7.2142E+00      0.339    0.889   6.056   0.858
HT6     101.6065    7.6842E+00      0.353    0.897   6.220   0.867
HT7     101.9185    1.0260E+01      0.368    0.904   6.387   0.877
HT8     102.2195    1.3595E+01      0.383    0.911   6.557   0.885
HT9     102.5125    1.7688E+01      0.398    0.918   6.731   0.894
HT10    102.8135    1.9199E+01      0.412    0.925   6.907   0.902
HT11    103.1135    2.0174E+01      0.427    0.931   7.086   0.910
HT12    103.4165    1.7752E+01      0.442    0.937   7.268   0.918
HT13    103.7165    2.1149E+01      0.457    0.943   7.451   0.925
HT14    104.0165    2.3570E+01      0.471    0.948   7.636   0.932
HT16    104.6765    1.9627E+02      0.486    0.953   7.821   0.938
HT17    105.1835    2.0182E+02      0.501    0.958   8.006   0.944
HT18    105.6825   "Null"           0.515    0.962   8.191   0.950
HT19    106.1825    4.3151E+02      0.530    0.966   8.374   0.955
HT20    106.6825    3.8457E+02      0.545    0.970   8.555   0.960
HT21    107.1835    4.3251E+02      0.560    0.974   8.733   0.965
HT22    107.6835    4.5576E+02      0.574    0.978   8.907   0.970
HT23    108.1765    3.1065E+02      0.589    0.981   9.076   0.974
HT24    108.6805    3.5936E+02      0.604    0.984   9.239   0.978
HT25    109.1835    3.2652E+02      0.619    0.987   9.395   0.981
HT26    109.6825    2.4472E+02      0.633    0.989   9.543   0.985
HT27    110.6825    2.1926E+02      0.648    0.991   9.683   0.988
HT28    111.6825    1.6218E+02      0.663    0.993   9.814   0.990
HT29    112.6825    1.7518E+02      0.677    0.995   9.934   0.993
                                    0.692    0.996   10.043  0.995
                                    0.707    0.998   10.141  0.997
                                    0.722    0.999   10.227  0.998
                                    0.736    1.000   10.300  1.000
*******************END OF FILE************************************
