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A Survey of Unsteady Hypersonic Flow Problems

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- 18 -<br />

Then the transformed velocity cconponent u' will be <strong>of</strong> the same<br />

order <strong>of</strong> magnitude as the components v and w, and gradients <strong>of</strong> flow<br />

quantities in terms <strong>of</strong> x1 will be <strong>of</strong> the same order <strong>of</strong> magnitude as those<br />

in the y and z directions. Substituting these transformed quantities into<br />

the equations <strong>of</strong> continuity, momentum and entropy (with isentropic conditions<br />

along the streamlines) we obtain<br />

and<br />

aP ap ah-4 ah)-+uus+-+-<br />

at a9 ay a2<br />

auf auf au* au* ap<br />

- + us-++-++-+at<br />

axI ay a2 pa+<br />

av av av av 1 ap<br />

- + us -+v-- +w--+-at<br />

a9 ay as P ay<br />

aw an an aw 1 ap<br />

- + us-+v- +w-+-dt<br />

axI ay az P a=<br />

as as as as<br />

- + U6 ---4-v-- +w-at<br />

ad ay az<br />

a(puf)<br />

= -p t . . . (2.8)<br />

ad<br />

au'<br />

= -6%'-, . . . (2.9)<br />

ax*<br />

av<br />

= #,f -<br />

axa 3<br />

. . . (2.10)<br />

an<br />

= -6% -3 . . . (2.11)<br />

a9<br />

as<br />

= #U - . 9.. (2.12)<br />

ai+<br />

where S is the entropy, and is given by S = C, log(p/py) + constant, where<br />

CV is the specific heat at constant volume. If the right-hand sides <strong>of</strong> these<br />

equations are neglected as they are <strong>of</strong> second order <strong>of</strong> smallness, the equations<br />

for v, w, p and p are decoupled from that for u'. The significance <strong>of</strong> this<br />

is seen more clearly if the equations are now transformed to axes fixed in the<br />

fluid, for if<br />

and<br />

F=t.<br />

2 = x' - mt-3<br />

a a<br />

-=ax'<br />

a2<br />

then equations (2.8) to (2.12) beome:<br />

a a a '<br />

- = -- us -<br />

at a? a2 I<br />

ap abd ah-d<br />

-+-+- =G 0<br />

a% ay az<br />

ih* tit au* 1 ap<br />

-+v-+w-+-- = 0<br />

aZ a;P az p aF<br />

. . . (2.13)<br />

. . . (2.G)<br />

. . . (2.15)<br />

. . . (2.16)

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