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M a = 1.5

supersonic. subsonic. N O R M A L. S H O C K. Tape along ceiling and wall of super- sonic nozzle. M a = 1.5. supersonic. subsonic. N O R M A L. S H O C K. M a = 1.5. can occur if converging, diverging and constant area channels

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M a = 1.5

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  1. supersonic subsonic N O R M A L S H O C K Tape along ceiling and wall of super- sonic nozzle. Ma = 1.5

  2. supersonic subsonic N O R M A L S H O C K Ma = 1.5 • can occur if converging, diverging and constant area channels • shock wave involves supersonic to subsonic flow • associated with rapid deceleration, pressure and entropy rise • only To is constant across shock

  3. normal shock (irreversible discontinuity) Ma = 1.5 Ma = 1.7 Can occur in internal and external flow, must be between supersonic to subsonic, irreversible, “abrupt discontinuity” (0.2 microns ~ 10-5 in) Interested in changes across shock rather than what’s happening in shock Important for design of inlets for high performance aircraft and supersonic wind tunnels

  4. p, , T can be very large Decelerations may be of the order of tens of millions of gs Thickness is about 0.2 microns (10-5 inches) “treat” as abrupt discontinuity

  5. Look at fundamental equations: cons. of mass, momentum and energy, 2nd Law of thermodynamics, property relations for an ideal gas with constant specific heats Because shock so thin, A1 = A 2 and Rx = 0; because control volume boundaries are far from shock, no gradients so no heat transfer

  6. Quasi-One-Dimensional, Steady, FBx = 0, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0, effects of gravity = 0, ideal gas, cv, cp is constant Cons. Of Mass Cons. of Momentum Cons. of Energy Property relations for ideal gas with cv and cp constant 2nd Law of Thermodynamics

  7. Quasi-One-Dimensional, Steady, FBx = 0, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0, effects of gravity = 0, ideal gas, cv, cp is constant Conservation of Mass Shock width is extraordinarily thin so A1 = A2 1V1 = 2V2 = (dm/dt)/A

  8. Quasi-One-Dimensional, Steady,FBx = 0, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0, effects of gravity = 0, ideal gas, cv, cp is constant Momentum Equation 0 Shock width is extraordinarily thin so Rx is negligible; dm/dt = VA p1+ 1V12 = p2+ 2V22

  9. Quasi-One-Dimensional, Steady, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0, effects of gravity = 0, ideal gas, cv, cp is constant First Law of Thermodynamics Conservation of Energy 0 No temperature gradients at stations 1 and 2 so adiabatic h1+ V12 = h2+ V22 ; h01 = h02

  10. h1+ V12 = h2+ V22 h01 = h02 h = cp T h01 = c0T01 h02 = c0T02 T01 = T02

  11. Quasi-One-Dimensional, Steady, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0, effects of gravity = 0, ideal gas, cv, cp is constant Second Law of Thermodynamics Conservation of Energy No temperature gradients at stations 1 and 2 so adiabatic s22V2A - s11V1A  0; s2 > s1

  12. Quasi-One-Dimensional, Steady, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0, effects of gravity = 0, ideal gas, cv, cp is constant Second Law of Thermodynamics Conservation of Energy s22V2A - s11V1A  0; s2 > s1 2nd Law by itself is little help in calculating entropy. To calculate entropy use 1st and 2nd Laws, ideal gas, constant cp to get: s2 – s1 = cpln(T2/T1) – Rln(p2/p1)

  13. Quasi-One-Dimensional, Steady, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0, effects of gravity = 0, ideal gas, cv, cp is constant Equation of State ~ Ideal Gas

  14. (1) (2) (2) (3) (4) (5) (6) To recap: Major simplifying features ~ Because so thin A1 = A 2; Rx = 0 Because boundaries of control volume are far from shock No gradients of V, T, , p there Q/dm = 0

  15. breath

  16. (1) (2) (2) (3) (4) (5) (6) 6 unknowns: p1, 1, T1, s1, h1, and V1 6 equations: and one constraint:

  17. (1) (2) (2) (3) (4) (5) (6) Rayleigh Line heat tranfer IGNORE Fanno Line friction Normal shock must satisfy eqs: 1-6, so must lie on intersection of Fanno and Rayleigh lines.

  18. B R E A T H

  19. s2 > s1 Property Changes Across Shock “explanation” s1 h1 1 s2 h2 2

  20. To = constant Entropy increases for irreversible process 1 2 3 4 5 6 7 8

  21. p02 < p01 T2 > T1 T = To/[1 + (k-1)M2/2] T2/T1 = [1 + (k-1)M12/2]/ [1 + (k-1)M22/2] p02 < p01(prob. 11.2) T2 > T1 1 2 3 4 5 6 7 8

  22. Since T2 > T1, then h2 > h1 ..so V2< V1 1 2 3 4 5 6 7 8

  23. Since V decreases across shock, then  must increase for V to remain constant. 1 2 3 4 5 6 7 8

  24. Since V is constant across shock and V decreases across shock, then p must increase across shock. Can also see from Ts diagram. 1 2 3 4 5 6 7 8

  25. Since V decreases across shock and T increases across shock then Ma = V / (kRT)1/2 must decrease supersonic – to – sonic across shock. 1 2 3 4 5 6 7 8

  26. G I V E N ? Make sure you know what goes in here

  27. Want: p02/p01 = f(M1); T2/T1 = f(M1); p2/p1 = f(M1); V2/V1 = f(M1); M2 = f(M1); 2/ 1 = f (M1)

  28. 6 unknowns 6 equations (1) (2) (2) (3) (4) (5) (6) Ma1 Ma2 s2 h2 2 s1 h1 1 Hard to solve, much easier if had ratios (e.g. p1/p2) in terms of M1

  29. Strategy ~ Step #1: Obtain property ratios, p1/p2, T1/T2, etc. in terms of M1 and M2. Step #2: Develop relationship between M1 and M2. Step #3: Recast property ratios, p1/p2, T1/T2, etc. in terms of M1.

  30. Want: p02/p01 = f(M1, M2); T2/T1 = f(M1,M2); p2/p1 = f(M1,M2); V2/V1 = f(M1,M2); M2 = f(M1); 2/ 1 = f (M1, M2)

  31. 1 T2/T1 = f(M1, M2) To/T = 1 + {(k – 1)/2}M2 T01 = T02

  32. Want: p02/p01 = f(M1, M2); T2/T1 = f(M1,M2); p2/p1 = f(M1,M2); V2/V1 = f(M1,M2); M2 = f(M1); 2/ 1 = f (M1, M2)

  33. V2/V1 = f(M1, M2)

  34. Want: p02/p01 = f(M1, M2); T2/T1 = f(M1,M2); p2/p1 = f(M1,M2); V2/V1 = f(M1,M2); M2 = f(M1); 2/ 1 = f (M1, M2)

  35. 2/1 = f(M1, M2)

  36. Want: p02/p01 = f(M1, M2); T2/T1 = f(M1,M2); p2/p1 = f(M1,M2); V2/V1 = f(M1,M2); M2 = f(M1); 2/ 1 = f (M1, M2)

  37. p2/p1 = f(M1, M2)

  38. T2/T1 = f(M1, M2)

  39. M2 = f(M1) =

  40. M2 = f(M1) =

  41. M2 = f(M1) Let: L = M12(1 + M12 (k-1)/2) / (1 +k M12)2 after much algebra (M22)2 ((1/2)(k-1) – k2L) + M22(1-2kL) – L = 0 Gas Dynamics - John

  42. ds > 0 M1> 0

  43. Want: p02/p01 = f(M1, M2); T2/T1 = f(M1,M2); p2/p1 = f(M1,M2); V2/V1 = f(M1,M2); M2 = f(M1); 2/ 1 = f (M1, M2)

  44. Have: T2/T1, V2/V1, 2/1, p2 /p1 = f(M1,M2); M2= f(M1) Still need: p02/p01 = ? po/p = [1 + M2{(k – 1)/2}]k/(k-1)

  45. Want: p02/p01 = f(M1, M2); T2/T1 = f(M1,M2); p2/p1 = f(M1,M2); V2/V1 = f(M1,M2); M2 = f(M1); 2/ 1 = f (M1, M2)

  46. Have: T2/T1, V2/V1, 2/1, p2 /p1 = f(M1,M2); M2= f(M1) Still need: p02/p01 = ?

  47. And similarly can substitute for M2 = f(M1) for other properties to get:

  48. E X A M P L E

  49. T1 = 0oC p1 = 60 kPa (abs) V1 = 497 m/s T2 = 87oC Find: M2, V2, P02

  50. T1 = 0oC p1 = 60 kPa (abs) V1 = 497 m/s T2 = 87oC Find: M2, V2, P02

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