M a = 1.5

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M a = 1.5 supersonic subsonic ape along ceiling nd wall of super- onic nozzle. N O R M A L S H O C K

description

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 - PowerPoint PPT Presentation

Transcript of M a = 1.5

Page 1: M a  = 1.5

Ma = 1.5

supersonic subsonic

Tape along ceilingand wall of super-sonic nozzle.

NORMAL

SHOCK

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Ma = 1.5

supersonic subsonic

NORMAL

SHOCK

• 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

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Can occur in internal and external flow, must be between supersonic to subsonic, irreversible, “abrupt discontinuity” (0.2 microns ~ 10-5 in)

Ma = 1.7

Ma

=1.5

normal shock(irreversiblediscontinuity)

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

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Thickness is about 0.2 microns (10-5 inches)“treat” as abrupt discontinuity

p, , T can be very largeDecelerations may be of the order

of tens of millions of gs

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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

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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

Propertyrelationsfor idealgas withcv and cp

constant

Cons. Of Mass

Cons. of Momentum

Cons. of Energy

2nd Law of Thermodynamics

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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

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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

Shock width is extraordinarily thin so Rx is negligible;

dm/dt = VAp1 + 1V1

2 = p2 + 2V22

0

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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 ThermodynamicsConservation of Energy

No temperature gradients at stations 1 and 2 so adiabatic

h1 + V12 = h2 + V2

2 ; h01 = h02

0

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h1 + V12 = h2 + V2

2 h01 = h02

h = cp T h01 = c0T01

h02 = c0T02

T01 = T02

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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 ThermodynamicsConservation of Energy

No temperature gradients at stations 1 and 2 so adiabatic

s22V2A - s11V1A 0; s2 > s1

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Second Law of ThermodynamicsConservation of Energy

s22V2A - s11V1A 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)

Quasi-One-Dimensional, Steady, dWs/dt = 0, dWshear/dt = 0, dW/dtother = 0,

effects of gravity = 0, ideal gas, cv, cp is constant

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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

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(1)

(2)

(2)

(3)

(4)(5)

(6)

To recap:Major simplifying features ~Because so thin

A1 = A 2; Rx = 0Because boundaries of control volume are far from shockNo gradients of V, T, , p there

Q/dm = 0

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breath

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(1)

(2)

(2)

(3)

(4)(5)

(6)

6 unknowns: p1, 1, T1, s1, h1, and V1

6 equations:

and one constraint:

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(1)

(2)

(2)

(3)

(4)(5)

(6)

Fanno Line friction

Rayleigh Line heat tranfer

Normal shock must satisfy eqs: 1-6, so must lie on intersection of Fanno and Rayleigh lines.

IGNORE

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BREATH

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s1

h1

1

s2

h2

2

s2 > s1

Property Changes Across Shock

“explanation”

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To = constant

Entropy increases forirreversible process

1

23

4

56

7

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p02 < p01

T2 > T1

T = To/[1 + (k-1)M2/2]T2/T1 = [1 + (k-1)M1

2/2]/[1 + (k-1)M2

2/2]

p02 < p01 (prob. 11.2)

T2 > T1

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23

4

56

7

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Since T2 > T1, then h2 > h1

..so V2< V1

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Since V decreases across shock,then must increase for V to

remain constant.

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Since V is constant across shockand V decreases across shock, then

p must increase across shock.Can also see from Ts diagram.

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Since V decreases across shock and T increases across shock

then Ma = V / (kRT)1/2 must decrease supersonic – to – sonic across shock.

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?Make sure you

know what goes in here

GIVEN

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

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s1

h1

1

s2

h2

2

(1)

(2)

(2)

(3)

(4)(5)

(6)

6 equations 6 unknowns

Hard to solve, much easier if had ratios (e.g. p1/p2) in terms of M1

Ma1 Ma2

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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.

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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)

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To/T = 1 + {(k – 1)/2}M2

T01 = T02

1T2/T1 = f(M1, M2)

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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)

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V2/V1 = f(M1, M2)

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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)

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2/1 = f(M1, M2)

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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)

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p2/p1 = f(M1, M2)

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T2/T1 = f(M1, M2)

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M2 = f(M1)

=

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M2 = f(M1)

=

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M2 = f(M1)

Let: L = M12(1 + M1

2 (k-1)/2) / (1 +k M12)2

after much algebra(M2

2)2 ((1/2)(k-1) – k2L) + M22(1-2kL) – L = 0

Gas Dynamics - John

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ds > 0M1> 0

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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)

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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)

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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)

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

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

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EXAMPLE

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T1 = 0oCp1 = 60 kPa (abs)V1 = 497 m/s

T2 = 87oC

Find: M2, V2, P02

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T1 = 0oCp1 = 60 kPa (abs)V1 = 497 m/s

T2 = 87oC

Find: M2, V2, P02

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T1= 273o K , p1 = 60 kPa,V1 = 497 m/s, T2 = 360oKFind: M2,V2, p02,

M1 = V1/(kRT1) = 1.5M2 = 0.70

p02 = p010.93po1 /p1 = [1 + M1

2{(k – 1)/2}]k/(k-1)

p01= p13.67 = 220.2p02 = p010.93p02 = 205 kPa (abs)

V2 = V1/1.24 = 267 m/sOther ways ~ M1 = V1/(kRT1); T01= T1(1 + M1

2(k-1)/2); T01 = T02; M2 =[{2/(k-1)}{(T02/T2) – 1}]1/2

V2 = M2/(kRT2)p2 = p1 + 1V1(V1 – V2); 1 = p1/(RT1); p02 = p2[1 + M2

2(k-1)/2]k/(k-1)

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THE

END

REALLY