Domů

2500 solved problems in fluid mechanics hydraulics - 781

APPENDIXES D 771
T ABLE A-17 One-dimensional normal-shock relations!
"Ml

El Pi 1.000 1.047 1.095 1.144 1.194 1.245 1.297 1.350 1.403 1.458 1.513 1.570 1.627 1.686 1.745 1.805 1.866 1.928 1.991 2.055 2.120 2.186 2.253 2.320 2.389 2.458 2.529 2.600 2.673 2.746 2.820 2.895 2.971 3.048 3.126 3.205 3.285 3.366 3.447 3.530 3.613 3.698 3.783 3.869 3.957 4.045 4.134 4.224 4.315 4.407 4.500 4.594

72

Ti 1.000 1.013 1.026 1.039 1.052 1.065 1.078 1.090 1.103 1.115 1.128 1.140 1.153 1.166 1.178 1.191 1.204 1.216 1.229 1.242 1.255 1.268 1.281 1.294 1.307 1.320 1.334 1.347 1.361 1.374 1.388 1.402 1.416 1.430 1.444 1.458 1.473 1.487 1.502 1.517 1.532 1.547 1.562 1.577 1.592 1.608 1.624 1.639 1.655 1.671 1.688 1.704

(Po)2 (P0)l 1.000 1.000 1.000 1.000 0.999 0.999 0.998 0.997 0.996 0.995 0.993 0.991 0.988 0.986 0.983 0.979 0.976 0.972 0.968 0.963 0.958 0.953 0.948 0.942 0.936 0.930 0.923 0.917 0.910 0.903 0.895 0.888 0.880 0.872 0.864 0.856 0.847 0.839 0.830 0.821 0.813 0.804 0.795 0.786 0.777 0.767 0.758 0.749 0.740 0.730 0.721 0.711

Nm 2.04 2.06 2.08 2.10 2.12 2.14 2.16 2.18 2.20 2.22 2.24 2.26 2.28 2.30 2.32 2.34 2.36 2.38 2.40 2.42 2.44 2.46 2.48 2.50 2.52 2.54 2.56 2.58 2.60 2.62 2.64 2.66 2.68 2.70 2.72 2.74 2.76 2.78 2.80 2.82 2.84 2.86 2.88 2.90 2.92 2.94 2 .% 2.98 3.00

N*2 0.571 0.567 0.564 0.561 0.558 0.555 0.553 0.550 0.547 0.544 0.542 0.539 0.537 0.534 0.532 0.530 0.527 0.525 0.523 0.521 0.519 0.517 0.515 0.513 0.511 0.509 0.507 0.506 0.504 0.502 0.500 0.499 0.497 0.496 0.494 0.493 0.491 0.490 0.488 0.487 0.485 0.484 0.483 0.481 0.480 0.479 0.478 0.476 0.475

P2 Pi 4.689 4.784 4.881 4.978 5.077 5.176 5.277 5.378 5.480 5.583 5.687 5.792 5.898 6.005 6.113 6.222 6.331 6.442 6.553 6.666 6.779 6.894 7.009 7.125 7.242 7.360 7.479 7.599 7.720 7.842 7.965 8.088 8.213 8.338 8.465 8.592 8.721 8.850 8.980 9.111 9.243 9.376 9.510 9.645 9.781 9.918 10.055 10.194 10.333

72

Ti 1.720 1.737 1.754 1.770 1.787 1.805 1.822 1.839 1.857 1.875 1.892 1.910 1.929 1.947 1.965 1.984 2.003 2.021 2.040 2.060 2.079 2.098 2.118 2.138 2.157 2.177 2.198 2.218 2.238 2.260 2.280 2.301 2.322 2.343 2.364 2.396 2.407 2.429 2.451 2.473 2 .4% 2.518 2.541 2.563 2.586 2.609 2.632 2.656 2.679

(Poh 0.702 0.693 0.683 0.674 0.665 0.656 0.646 0.637 0.628 0.619 0.610 0.601 0.592 0.583 0.575 0.566 0.557 0.549 0.540 0.532 0.523 0.515 0.507 0.499 0.491 0.483 0.475 0.468 0.460 0.453 0.445 0.438 0.431 0.424 0.417 0.410 0.403 0.396 0.389 0.383 0.376 0.370 0.364 0.358 0.352 0.346 0.340 0.334 0.328

1.00 1.02 1.04 1.06 1.08 1.10 1.12 1.14 1.16 1.18 1.20 1.22 1.24 1.26 1.28 1.30 1.32 1.34 1.36 1.38 1.40 1.42 1.44 1.46 1.48 1.50 1.52 1.54 1.56 1.58 1.60 1.62 1.64 1.66 1.68 1.70 1.72 1.74 1.76 1.78 1.80 1.82 1.84 1.86 1.88 1.90 1.92 1.94 1.96 1.98 2.00 2.02

1.000 0.980 0.962 0.944 0.928 0.912 0.896 0.882 0.868 0.855 0.842 0.830 0.818 0.807 0.796 0.786 0.776 0.766 0.757 0.748 0.740 0.731 0.723 0.716 0.708 0.701 0.694 0.687 0.681 0.675 0.668 0.663 0.657 0.651 0.646 0.641 0.635 0.631 0.626 0.621 0.617 0.612 0.608 0.604 0.600 0.596 0.592 0.588 0.584 0.581 0.577 0.574

t For a perfect gas with k = 1.4.

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