Thermodynamics: An Engineering Approach
Thermodynamics: An Engineering Approach
9th Edition
ISBN: 9781259822674
Author: Yunus A. Cengel Dr., Michael A. Boles
Publisher: McGraw-Hill Education
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Chapter 9.12, Problem 133P

a)

To determine

The pressure at the turbine exit.

a)

Expert Solution
Check Mark

Answer to Problem 133P

The pressure at the turbine exit is 55.2psia.

Explanation of Solution

Draw the Ts diagram for pure jet engine as shown in Figure (1).

Thermodynamics: An Engineering Approach, Chapter 9.12, Problem 133P

Consider that the aircraft is stationary, and the velocity of air moving towards the aircraft is V1=900ft/s, the air will leave the diffuser with a negligible velocity (V20).

Diffuser (For process 1-2):

Write the expression for the energy balance equation for the diffuser.

E˙inE˙out=ΔE˙system (I)

Here, the rate of energy entering the system is E˙in, rate of energy leaving the system is E˙out, and the rate of change in the energy of the system is ΔE˙system.

Write the temperature and pressure relation for the process 1-2.

P2=P1(T2T1)k/(k1) (II)

Here, the specific heat ratio of air is k, pressure at state 1 is P1, pressure at state 2 is P2, temperature at state 1 is T1 and temperature at state 2 is T2.

Compressor (For process 2-3)

Write the pressure relation using the pressure ratio for the process 2-3.

P3=P4=(rp)(P2) (III)

Here, the pressure ratio is rp, pressure at state 3 is P3 and pressure at state 4 is P4.

Write the temperature and pressure relation for the process 2-3.

T3=T2(P3P2)(k1)/kT3=T2(rp(k1)/k) (IV)

Here, temperate at state 3 is T3.

Turbine (For process 4-5)

Write the temperature relation for the compressor and turbine.

wcomp,in=wturb,outh3h2=h4h5cp(T3T2)=cp(T4T5)

T3T2=T4T5T5=T4T3+T2 (V)

Here, the specific heat at constant pressure is cp, enthalpy at state 2 is h2, enthalpy at state 3 is h3, enthalpy at state 4 is h4, enthalpy at state 5 is h5, work input to the compressor is wcomp,in, work output from turbine is wturb,out, temperature at state 4 is T4 and temperature at state 5 is T5.

Write the temperature and pressure relation for the process 4-5.

P5=P4(T5T4)k/(k1) (VI).

Conclusion:

From Table A-2E, “Ideal-gas specific heats of various common gases”, obtain the following values for air at room temperature.

k=1.4cp=0.24Btu/lbmR

The rate of change in the energy of the system (ΔE˙system) is zero for the steady state system.

Substitute 0 for ΔE˙system in Equation (I).

E˙inE˙out=0

E˙in=E˙outh1+V122=h2+V2220=h2h1+V22V1220=cp(T2T1)V22V122 (VII).

Here, inlet velocity is V1 or Vinlet , velocity at state 2 is V2 , temperate at state 2 is T2 and temperate at state 1 is T1.

Substitute 0 for V2, 10°F for T1, 900ft/s for V1, and 0.24Btu/lbmR for cp in Equation (VII).

0=0.24Btu/lbmR(T2(10°F))(0)(900ft/s)22T2=(10+460)R+(900ft/s)2(2)(0.24Btu/lbmR)(1Btu/lbm25,037ft2/s2)T2=537.4R

Substitute 7psia for P1, 537.3 R for T2, 10°F for T1, and 1.4 for k in Equation (II).

P2=(7psia)(537.3R10°F)1.4/1.41=(7psia)(537.3R(10+460)R)1.4/1.41=11.19psia

Substitute 13 for rp, and 11.19psia for P2 in Equation (III).

P3=P4=(13)(11.19psia)=145psia

Substitute 537.4 R for T2, 1.4 for k, and 13 for rp in Equation (IV).

T3=(537.4R)(13)1.41/1.4=1118.3R

Substitute 2400R for T4, 1118.3 R for T3, and 537.4 R for T2 in Equation (V).

T5=(2400R1118.3R+537.4R)=1819.1R

Substitute 1819.1R for T5, 2400R for T4, 145.5psia for P4, and 1.4 for k in Equation (VI).

P5=(145.5psia)(1819.1R2400R)1.4/1.41P5=Pexit=55.2psia

Thus, the pressure at the turbine exit is 55.2psia.

b)

To determine

The exit velocity of the exhaust gases.

b)

Expert Solution
Check Mark

Answer to Problem 133P

The exit velocity of the exhaust gases is 3121ft/s.

Explanation of Solution

Nozzle (For process 5-6)

Write the temperature and pressure relation for the isentropic process 4-6.

T6=T4(P6P4)(k1)/k (VIII)

Here, pressure at state 6 is P6 and temperature at state 6 is T6.

Write the energy balance equation for the nozzle.

E˙inE˙out=ΔE˙system (IX)

Conclusion:

Substitute 1819.1R for T5, 1.4 for k, 7psia for P6, and 55.2psia for P5 in Equation(VIII).

T6=(1819.1R)(7psia55.2psia)1.41/1.4=1008.4R

The rate of change in the energy of the system (ΔE˙system) is zero for the steady state system.

Substitute 0 for ΔE˙system Equation (IX).

E˙in=E˙outh5+V522=h6+V6220=h6h5+V62V5220=cp(T6T5)V62V522 (X)

Here, velocity at stat 5 is V5, exit velocity is V6 or Vexit and temperate at state 6 is T6.

Since, V5=V2

Substitute 1819.1R for T5, 1008.6R for T6, and 0.24Btu/lbmR for cp in Equation (X).

0=0.24Btu/lbmR(1819.1R1008.6R)V6202

V6=(2)(0.24Btu/lbmR)(1819.1R1008.6R)(25,037ft2/s21Btu/lbm)V6=Vexit=3121ft/s

Thus, the exit velocity of the exhaust gases is 3121ft/s.

c)

To determine

The propulsive efficiency of the turbojet engine.

c)

Expert Solution
Check Mark

Answer to Problem 133P

The propulsive efficiency of the turbojet engine is 25.9%.

Explanation of Solution

Write the expression to calculate the propulsive work done per unit mass by the turbojet engine (wp).

wp=(VexitVinlet)Vaircraft (XI).

Here, the velocity of the aircraft is Vaircraft, the velocity of the inlet air is Vinlet, and the exit velocity of the exhaust gases is Vexit.

Write the expression to calculate the heating value of the fuel per unit mass for the turbojet engine (qin).

qin=h4h3=cp(T4T3) (XII).

Here, temperature at state 4 is T4 , temperature at state 3 is T3 , enthalpy at state 4 is h4 and enthalpy at state 3 is h3.

Write the expression to calculate the propulsive efficiency of the turbojet engine (ηp).

ηp=wpqin (XIII).

Conclusion.

Substitute 3121ft/s for Vexit, 900ft/s for Vinlet, and 900ft/s for Vaircraft in Equation (XI).

wp=(3121ft/s900ft/s)×(900ft/s)=(2221ft/s)×(900ft/s)=1998900ft2/s2(1Btu/lbm25,037ft2/s2)=79.83Btu/lbm

Substitute 0.24Btu/lbmR for cp, 1118.3R for T3, and 2400R for T4 in Equation (XII).

qin=(0.24Btu/lbmR)(2400R1118.3R)=307.6Btu/lbm

Substitute 307.6Btu/lbm for qin, and 79.8Btu/lbm for wp in Equation (XIII).

ηp=79.8Btu/lbm307.6Btu/lbm=0.259×100%=25.9%

Thus, the propulsive efficiency of the turbojet engine is 25.9%.

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Chapter 9 Solutions

Thermodynamics: An Engineering Approach

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