11.7.5: Figures and Tables
- Page ID
- 817
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\(\dfrac{4\,f\,L}{D}\) | 785.97 | 439.33 | 279.06 | 192.12 | 139.79 | 105.89 | 82.7040 | 66.1599 | 13.9747 | 7.9925 | 4.8650 | 3.0677 | 1.9682 | 1.2668 | 0.80732 | 0.50207 | 0.29895 | 0.16552 | 0.08085 | 0.03095 | 0.00626 | 0.00371 | 0.00205 | 0.000896 | 0.000220 | 0.0 |
\(\dfrac{P}{P^{\star}}\) | 28.1718 | 21.1289 | 16.9031 | 14.0859 | 12.0736 | 10.5644 | 9.3906 | 8.4515 | 4.2258 | 3.3806 | 2.8172 | 2.4147 | 2.1129 | 1.8781 | 1.6903 | 1.5366 | 1.4086 | 1.3002 | 1.2074 | 1.1269 | 1.056 | 1.043 | 1.032 | 1.021 | 1.011 | 1.000 |
\(\dfrac{P_{0}} (click for details) \) Callstack:
at (Bookshelves/Civil_Engineering/Book:_Fluid_Mechanics_(Bar-Meir)/11:_Compressible_Flow_One_Dimensional/11.70_Isothermal_Flow/11.7.5:_Figures_and_Tables), /content/body/table/tbody/tr[4]/td[1]/span, line 1, column 5
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17.6651 | 13.2553 | 10.6109 | 8.8493 | 7.5920 | 6.6500 | 5.9181 | 5.3334 | 2.7230 | 2.2126 | 1.8791 | 1.6470 | 1.4784 | 1.3524 | 1.2565 | 1.1827 | 1.1259 | 1.0823 | 1.0495 | 1.0255 | 1.009 | 1.007 | 1.005 | 1.003 | 1.001 | 1.000 |
\(\dfrac{\rho}{\rho^{\star}}\) | 28.1718 | 21.1289 | 16.9031 | 14.0859 | 12.0736 | 10.5644 | 9.3906 | 8.4515 | 4.2258 | 3.3806 | 2.8172 | 2.4147 | 2.1129 | 1.8781 | 1.6903 | 1.5366 | 1.4086 | 1.3002 | 1.2074 | 1.1269 | 1.056 | 1.043 | 1.032 | 1.021 | 1.011 | 1.000 |
\(\dfrac{T_{0}} (click for details) \) Callstack:
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0.87516 | 0.87528 | 0.87544 | 0.87563 | 0.87586 | 0.87612 | 0.87642 | 0.87675 | 0.88200 | 0.88594 | 0.89075 | 0.89644 | 0.90300 | 0.91044 | 0.91875 | 0.92794 | 0.93800 | 0.94894 | 0.96075 | 0.97344 | 0.98700 | 0.98982 | 0.99232 | 0.99485 | 0.99741 | 1.000 |
Contributors and Attributions
Dr. Genick Bar-Meir. Permission is granted to copy, distribute and/or modify this document under the terms of the GNU Free Documentation License, Version 1.2 or later or Potto license.