Moran M.J., Shapiro H.N. Fundamentals of Engineering Thermodynamics

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446 Chapter 9 Gas Power Systems

9.3 At the beginning of the compression process of an air-

standard Otto cycle, p

 1 bar, T

 290 K, V

 400 cm

The maximum temperature in the cycle is 2200 K and the com-

pression ratio is 8. Determine

(a) the heat addition, in kJ.

(b) the net work, in kJ.

(d) the mean effective pressure, in bar.

(e) Develop a full accounting of the exergy transferred to the

air during the heat addition, in kJ.

(f) Devise and evaluate an exergetic efficiency for the cycle.

Let T

 290 K, p

 1 bar.

9.4 Plot each of the quantities specified in parts (a) through (d)

of Problem 9.3 versus the compression ratio ranging from

2to12.

9.5 Solve Problem 9.3 on a cold air-standard basis with spe-

cific heats evaluated at 300 K.

9.6 Consider the cycle in Problem 9.3 as a model of the

processes in each cylinder of a spark-ignition engine. If the en-

gine has four cylinders and the cycle is repeated 1200 times

per min in each cylinder, determine the net power output,

in kW.

9.7 An air-standard Otto cycle has a compression ratio of 7.5.

At the beginning of compression, p

 85 kPa and T

 32C.

The mass of air is 2 g, and the maximum temperature in the

cycle is 960 K. Determine

(a) the heat rejection, in kJ.

(b) the net work, in kJ.

(d) the mean effective pressure, in kPa.

9.8 Consider a modification of the air-standard Otto cycle in

which the isentropic compression and expansion processes are

each replaced with polytropic processes having n  1.3. The

compression ratio is 9 for the modified cycle. At the beginning

of compression, p

 1 bar and T

 300 K. The maximum

temperature during the cycle is 2000 K. Determine

(a) the heat transfer and work per unit mass of air, in kJ/kg,

for each process in the modified cycle.

(b) the thermal efficiency.

9.9 At the beginning of the compression process in an air-

standard Otto cycle, p

 1 bar and T

 300 K. The maximum

cycle temperature is 2000 K. Plot the net work per unit of mass,

in kJ/kg, the thermal efficiency, and the mean effective pres-

sure, in bar, versus the compression ratio ranging from 2 to 14.

9.10 Investigate the effect of maximum cycle temperature on

the net work per unit mass of air for air-standard Otto cycles

with compression ratios of 5, 8, and 11. At the beginning of

the compression process, p

 1 bar and T

 295 K. Let the

maximum temperature in each case vary from 1000 to 2200 K.

9.11 The pressure-specific volume diagram of the air-standard

Atkinson cycle is shown in Fig. P9.11. The cycle consists of

isentropic compression, constant volume heat addition, isen-

tropic expansion, and constant pressure compression. For a

particular Atkinson cycle, the compression ratio during

isentropic compression is 8.5. At the beginning of this

compression process, p

 100 kPa and T

 300 K. The con-

stant volume heat addition per unit mass of air is 1400 kJ/kg.

(a) Sketch the cycle on T–s coordinates. Determine (b) the net

work, in kJ per kg of air,

cle, and

(d) the mean effective pressure, in kPa. Compare your

answers with those obtained for the Otto cycle in Problem 9.1

and discuss.

9.12 On a cold air-standard basis, derive an expression for the

thermal efficiency of the Atkinson cycle (see Fig. P9.11)

in terms of the volume ratio during the isentropic compression,

the pressure ratio for the constant volume process, and the spe-

cific heat ratio. Compare the thermal efficiencies of the cold

air-standard Atkinson and Otto cycles, each having the same

compression ratio and maximum temperature. Discuss.

9.13 The pressure and temperature at the beginning of com-

pression of an air-standard Diesel cycle are 95 kPa and 300 K,

respectively. At the end of the heat addition, the pressure is

7.2 MPa and the temperature is 2150 K. Determine

(a) the compression ratio.

(b) the cutoff ratio.

(d) the mean effective pressure, in kPa.

9.14 Solve Problem 9.13 on a cold air-standard basis with spe-

cific heats evaluated at 300 K.

9.15 The conditions at the beginning of compression in an air-

standard Diesel cycle are fixed by p

 200 kPa, T

 380 K.

The compression ratio is 20 and the heat addition per unit mass

is 900 kJ/kg. Determine

(a) the maximum temperature, in K.

(b) the cutoff ratio.

(d) the thermal efficiency.

(e) the mean effective pressure, in kPa.

(f) To investigate the effects of varying compression ratio, plot

each of the quantities calculated in parts (a) through (e) for

compression ratios ranging from 5 to 25.

s = c

 Figure P9.11

Problems: Developing Engineering Skills 447

9.16 For the Diesel cycle of Problem 9.15 with a compression

ratio of 20 and a heat addition per unit mass of 900 kJ/kg

(a) evaluate the exergy transfers accompanying heat and work

for each process, in kJ/kg.

(b) devise and evaluate an exergetic efficiency for the cycle.

Let T

 300 K, p

 100 kPa.

9.17 The displacement volume of an internal combustion en-

gine is 5.6 liters. The processes within each cylinder of the

engine are modeled as an air-standard Diesel cycle with a cut-

off ratio of 2.4. The state of the air at the beginning of com-

pression is fixed by p

 95 kPa, T

 27C, and V

 6.0

liters. Determine the net work per cycle, in kJ, the power de-

veloped by the engine, in kW, and the thermal efficiency, if the

cycle is executed 1500 times per min.

9.18 The state at the beginning of compression of an air-

standard Diesel cycle is fixed by p

 100 kPa and T

 310 K.

The compression ratio is 15. For cutoff ratios ranging from

1.5 to 2.5, plot

(a) the maximum temperature, in K.

(b) the pressure at the end of the expansion, in kPa.

(d) the thermal efficiency.

9.19 An air-standard Diesel cycle has a maximum temperature

of 1800 K. At the beginning of compression, p

 95 kPa and

 300 K. The mass of air is 12 g. For compression ratios

ranging from 15 to 25, plot

(a) the net work of the cycle, in kJ.

(b) the thermal efficiency.

9.20 At the beginning of compression in an air-standard Diesel

cycle, p

 96 kPa, V

 0.016 m

, and T

 290 K. The com-

pression ratio is 15 and the maximum cycle temperature is

1290 K. Determine

(a) the mass of air, in kg.

(b) the heat addition and heat rejection per cycle, each in kJ.

9.21 At the beginning of the compression process in an air-

standard Diesel cycle, p

 1 bar and T

 300 K. For maximum

cycle temperatures of 1200, 1500, 1800, and 2100 K, plot the

heat addition per unit of mass, in kJ/kg, the net work per unit of

mass, in kJ/kg, the mean effective pressure, in bar, and the thermal

efficiency, each versus compression ratio ranging from 5 to 20.

9.22 An air-standard dual cycle has a compression ratio of 9.

At the beginning of compression, p

 100 kPa and T

 300

K. The heat addition per unit mass of air is 1400 kJ/kg, with

one half added at constant volume and one half added at con-

stant pressure. Determine

(a) the temperatures at the end of each heat addition process,

in K.

(b) the net work of the cycle per unit mass of air, in kJ/kg.

(d) the mean effective pressure, in kPa.

9.23 For the cycle in Problem 9.22, plot each of the quantities

calculated in parts (a) through (d) versus the ratio of constant-

volume heat addition to total heat addition varying from 0 to

1. Discuss.

9.24 Solve Problem 9.23 on a cold air-standard basis with spe-

cific heats evaluated at 300 K.

9.25 The thermal efficiency, , of a cold air-standard dual cy-

cle can be expressed as

where r is compression ratio, r

is cutoff ratio, and r

is the

pressure ratio for the constant volume heat addition. Derive

this expression.

9.26 An air-standard dual cycle has a compression ratio of 16

and a cutoff ratio of 1.15. At the beginning of compression,

 95 kPa and T

 300 K. The pressure increases by a fac-

tor of 2.2 during the constant volume heat addition process. If

the mass of air is 0.04 kg, determine

(a) the heat addition at constant volume and at constant pres-

sure, each in kJ.

(b) the net work of the cycle, in kJ.

(d) the thermal efficiency.

9.27 At the beginning of the compression process in an air-

standard dual cycle, p

 1 bar and T

 300 K. The total heat

addition is 1000 kJ/kg. Plot the net work per unit of mass, in

kJ/kg, the mean effective pressure, in bar, and the thermal ef-

ficiency versus compression ratio for different fractions of con-

stant volume and constant pressure heat addition. Consider

compression ratio ranging from 10 to 20.

Brayton Cycle

9.28 Air enters the compressor of an ideal air-standard Brayton

cycle at 100 kPa, 300 K, with a volumetric flow rate of 5 m

/s.

The compressor pressure ratio is 10. For turbine inlet temper-

atures ranging from 1000 to 1600 K, plot

(a) the thermal efficiency of the cycle.

(b) the back work ratio.

9.29 Air enters the compressor of an ideal air-standard Brayton

cycle at 100 kPa, 300 K, with a volumetric flow rate of 5 m

/s.

The turbine inlet temperature is 1400 K. For compressor pres-

sure ratios ranging from 2 to 20, plot

(a) the thermal efficiency of the cycle.

(b) the back work ratio.

9.30 Consider an ideal air-standard Brayton cycle with mini-

mum and maximum temperatures of 300 K and 1500 K, re-

spectively. The pressure ratio is that which maximizes the net

h  1 

k1

 1

 12 kr

 12

448 Chapter 9 Gas Power Systems

work developed by the cycle per unit mass of air flow. On a

cold air-standard basis, calculate

(a) the compressor and turbine work per unit mass of air flow,

each in kJ/kg.

(b) the thermal efficiency of the cycle.

perature ranging from 1200 to 1800 K.

9.31 On the basis of a cold air-standard analysis, show that the

back work ratio of an ideal air-standard Brayton cycle equals

the ratio of absolute temperatures at the compressor inlet and

the turbine outlet.

9.32 The compressor inlet temperature for an ideal Brayton cy-

cle is T

and the turbine inlet temperature is T

. Using a cold

air-standard analysis, show that the temperature T

at the com-

pressor exit that maximizes the net work developed per unit

mass of air flow is T

 (T

)

12

9.33 Reconsider Problem 9.29, but include in the analysis that

the turbine and compressor each have isentropic efficiencies

of 90, 80, and 70%. The compressor pressure ratio varies over

the same range as in Problem 9.29. Plot, for each value of isen-

tropic efficiency

(a) the thermal efficiency.

(b) the back work ratio.

(d) the rates of exergy destruction in the compressor and tur-

bine, respectively, each in kW, for T

 300 K.

9.34 The compressor and turbine of a simple gas turbine each

have isentropic efficiencies of 90%. The compressor pressure

ratio is 12. The minimum and maximum temperatures are

290 K and 1400 K, respectively. On the basis of an air-standard

analysis, compare the values of

(a) the net work per unit mass

of air flowing, in kJ/kg, (b) the heat rejected per unit mass of

air flowing, in kJ/kg, and (c) the thermal efficiency to the same

quantities evaluated for an ideal cycle.

9.35 Air enters the compressor of a simple gas turbine at 100

kPa, 300 K, with a volumetric flow rate of 5 m

/s. The com-

pressor pressure ratio is 10 and its isentropic efficiency is 85%.

At the inlet to the turbine, the pressure is 950 kPa, and the tem-

perature is 1400 K. The turbine has an isentropic efficiency of

88% and the exit pressure is 100 kPa. On the basis of an air-

standard analysis,

(a) develop a full accounting of the net exergy increase of the

air passing through the gas turbine combustor, in kW.

(b) devise and evaluate an exergetic efficiency for the gas tur-

bine cycle.

Let T

 300 K, p

 100 kPa.

Regeneration, Reheat, and Compression

with Intercooling

9.36 Reconsider Problem 9.33, but incorporate a regenerator

with an effectiveness of 80% into the cycle. Plot

(a) the thermal efficiency.

(b) the back work ratio.

(d) the rate of exergy destruction in the regenerator, in kW,

for T

 300 K.

9.37 Reconsider Problem 9.34, but include a regenerator in the

cycle. For regenerator effectiveness values ranging from 0 to

100%, plot

(a) the heat addition per unit mass of air flowing, in kJ/kg.

(b) the thermal efficiency.

9.38 On the basis of a cold air-standard analysis, show that the

thermal efficiency of an ideal regenerative gas turbine can be

expressed as

where r is the compressor pressure ratio, and T

and T

denote

the temperatures at the compressor and turbine inlets, respectively.

9.39 A regenerative gas turbine power plant is shown in Fig.

P9.39. Air enters the compressor at 1 bar, 27C with a mass flow

rate of 0.562 kg/s and is compressed to 4 bar. The isentropic

efficiency of the compressor is 80%, and the regenerator effec-

tiveness is 90%. All the power developed by the high-pressure

turbine is used to run the compressor. The low-pressure turbine

provides the net power output. Each turbine has an isentropic

efficiency of 87% and the temperature at the inlet to the high-

pressure turbine is 1200 K. Determine

(a) the net power output, in kW.

(b) the thermal efficiency.

h  1  a

b 1r2

1k 12



High-pressure

turbine

Low-pressure turbine

1 bar

= 1200 K

net

1 bar, 27°C

Compressor

Combustor

Regenerator

= 4 bar

 Figure P9.39

9.40 Air enters the turbine of a gas turbine at 1200 kPa, 1200 K,

and expands to 100 kPa in two stages. Between the stages, the

Problems: Developing Engineering Skills 449

air is reheated at a constant pressure of 350 kPa to 1200 K.

The expansion through each turbine stage is isentropic. De-

termine, in kJ per kg of air flowing

(a) the work developed by each stage.

(b) the heat transfer for the reheat process.

expansion with no reheat.

9.41 Reconsider Problem 9.40 and include in the analysis that

each turbine stage might have an isentropic efficiency less than

100%. Plot each of the quantities calculated in parts (a) through

ing from 100 to 1200 kPa and for isentropic efficiencies of

100%, 80%, and 60%.

9.42 Consider a two-stage turbine operating at steady state with

reheat at constant pressure between the stages. Show that the

maximum work is developed when the pressure ratio is the

same across each stage. Use a cold air-standard analysis, as-

suming the inlet state and the exit pressure are specified, each

expansion process is isentropic, and the temperature at the inlet

to each turbine stage is the same. Kinetic and potential energy

effects can be ignored.

9.43 Modify the cycle of Problem 9.36 to include a two-stage

turbine expansion with reheat to 1400 K at constant pressure be-

tween the stages. The regenerator effectiveness is 80%, and the

pressure ratio is the same across each turbine stage. The stages

have equal isentropic efficiencies. Construct the same plots as

requested in parts (a) through (c) of Problem 9.36 for turbine

stage isentropic efficiencies of 100%, 90%, 80%, and 70%.

9.44 If the inlet state and the exit pressure are specified for a two-

stage turbine with reheat between the stages and operating at

steady state, show that the maximum total work output is ob-

tained when the pressure ratio is the same across each stage. Use

a cold air-standard analysis assuming that each compression

process is isentropic, there is no pressure drop through the re-

heater, and the temperature at the inlet to each turbine stage is

the same. Kinetic and potential energy effects can be ignored.

9.45 A two-stage air compressor operates at steady state, com-

pressing 10 m

/min of air from 100 kPa, 300 K, to 1200 kPa.

An intercooler between the two stages cools the air to 300 K

at a constant pressure of 350 kPa. The compression processes

are isentropic. Calculate the power required to run the com-

pressor, in kW, and compare the result to the power required

for isentropic compression from the same inlet state to the same

final pressure.

9.46 Reconsider Problem 9.45 and include in the analysis that

each compressor stage might have an isentropic efficiency less

than 100%. Plot, in kW, (a) the power input to each stage,

(b) the heat transfer rate for the intercooler, and (c) the decrease

in power input as compared to a single stage of compression

with no intercooling, for values of interstage pressure ranging

from 100 to 1200 kPa and for isentropic efficiencies of 100%,

80%, and 60%.

9.47 Modify the cycle of Problem 9.36 to include a two-stage

compressor with intercooling to 300 K at constant pressure

between the stages. The regenerator effectiveness is 80%, and

the pressure ratios are the same across each compressor stage.

The stages have equal isentropic efficiencies. Construct the

same plots as requested in parts (a) through (c) of Problem 9.36

for compressor stage isentropic efficiencies of 100%, 90%,

80%, and 70%.

9.48 Referring to Example 9.10, show that if T

 T

the pres-

sure ratios across the two compressor stages are related by

9.49 Rework Example 9.10 for the case of a three-stage com-

pressor with intercooling between stages.

9.50 Modify the cycle of Problem 9.36 to include two-stage

compression and expansion, with intercooling to 300 K and

reheat to 1400 K, respectively, between the stages. The

regenerator effectiveness is 80%, and the pressure ratios are

the same across each compressor stage. The intercooler and

reheater both operate at the same pressure. The compressor

and turbine stages all have equal isentropic efficiencies. Con-

struct the same plots as requested in parts (a) through (c) of

Problem 9.36 for stage isentropic efficiencies of 100%, 90%,

80%, and 70%.

9.51 Air enters the compressor of a gas turbine at 100 kPa,

300 K. The air is compressed in two stages to 900 kPa, with

intercooling to 300 K between the stages at a pressure of

300 kPa. The turbine inlet temperature is 1480 K and the ex-

pansion occurs in two stages, with reheat to 1420 K between

the stages at a pressure of 300 kPa. The compressor and tur-

bine stage efficiencies are 84 and 82%, respectively. The net

power developed is 1.8 MW. Determine

(a) the volumetric flow rate, in m

/s, at the inlet of each com-

pressor stage.

(b) the thermal efficiency of the cycle.

9.52 Reconsider Problem 9.51 but include a regenerator with

an effectiveness of 75%.

Other Gas Power System Applications

9.53 Air at 22 kPa, 220 K, and 250 m/s enters a turbojet en-

gine in flight at an altitude of 10,000 m. The pressure ratio

across the compressor is 12. The turbine inlet temperature

is 1400 K, and the pressure at the nozzle exit is 22 kPa. The

diffuser and nozzle processes are isentropic, the compressor

and turbine have isentropic efficiencies of 85 and 88%,

respectively, and there is no pressure drop for flow through

the combustor. On the basis of an air-standard analysis,

determine

(a) the pressures and temperatures at each principal state, in

kPa and K, respectively.

(b) the velocity at the nozzle exit, in m/s.

Neglect kinetic energy except at the diffuser inlet and the

nozzle exit.

 a

b a



1k 12

450 Chapter 9 Gas Power Systems

9.54 For the turbojet in Problem 9.54, plot the velocity at the

nozzle exit, in m/s, the pressure at the turbine exit, in kPa, and

the rate of heat input to the combustor, in kW, each as a func-

tion of compressor pressure ratio in the range of 6 to 14. Re-

peat for turbine inlet temperatures of 1200 K and 1000 K.

9.55 Consider the addition of an afterburner to the turbojet in

Problem 9.54 that raises the temperature at the inlet of the nozzle

to 1300 K. Determine the velocity at the nozzle exit, in m/s.

9.56 Air enters the diffuser of a ramjet engine at 40 kPa, 240 K,

with a velocity of 2500 km/h and decelerates to negligible ve-

locity. On the basis of an air-standard analysis, the heat addition

is 1080 kJ per kg of air passing through the engine. Air exits

the nozzle at 40 kPa. Determine

(a) the pressure at the diffuser exit, in kPa.

(b) the velocity at the nozzle exit, in m/s.

Neglect kinetic energy except at the diffuser inlet and the noz-

zle exit.

9.57 A turboprop engine consists of a diffuser, compressor,

combustor, turbine, and nozzle. The turbine drives a propeller

as well as the compressor. Air enters the diffuser with a volu-

metric flow rate of 83.7 m

/s at 40 kPa, 240 K, and a velocity

of 180 m/s, and decelerates essentially to zero velocity. The

compressor pressure ratio is 10 and the compressor has an

isentropic efficiency of 85%. The turbine inlet temperature is

1140 K, and its isentropic efficiency is 85%. The turbine exit

pressure is 50 kPa. Flow through the diffuser and nozzle is

isentropic. Using an air-standard analysis, determine

(a) the power delivered to the propeller, in MW.

(b) the velocity at the nozzle exit, in m/s.

Neglect kinetic energy except at the diffuser inlet and the noz-

zle exit.

9.58 Air enters the compressor of a combined gas turbine–vapor

power plant (Fig. 9.23) at 1 bar, 25C. The isentropic com-

pressor efficiency is 85% and the compressor pressure ratio is

14. The air passing through the combustor receives energy by

heat transfer at a rate of 50 MW with no significant decrease

in pressure. At the inlet to the turbine the air is at 1250C. The

air expands through the turbine, which has an isentropic effi-

ciency of 87%, to a pressure of 1 bar. Then, the air passes

through the interconnecting heat exchanger and is finally dis-

charged at 200C, 1 bar. Steam enters the turbine of the vapor

cycle at 12.5 MPa, 500C, and expands to a condenser pres-

sure of 0.1 bar. Water enters the pump as a saturated liquid at

0.1 bar. The turbine and pump have isentropic efficiencies of

90 and 100%, respectively. Cooling water enters the condenser

at 20C and exits at 35C. Determine

(a) the mass flow rates of the air, steam, and cooling water,

each in kg/s.

(b) the net power developed by the gas turbine cycle and the

vapor cycle, respectively, each in MW.

(d) the net rate at which exergy is carried out with the exhaust

air, in MW.m

air

e

 e

,

(e) the net rate at which exergy is carried out with the cool-

ing water, in MW.

Let T

 20C, p

 1 bar.

9.59 A combined gas turbine–vapor power plant (Fig. 9.23) has

a net power output of 100 MW. Air enters the compressor of

the gas turbine at 100 kPa, 300 K, and is compressed to

1200 kPa. The isentropic efficiency of the compressor is 84%.

The conditions at the inlet to the turbine are 1200 kPa and

1400 K. Air expands through the turbine, which has an

isentropic efficiency of 88%, to a pressure of 100 kPa. The air

then passes through the interconnecting heat exchanger, and is

finally discharged at 480 K. Steam enters the turbine of the

vapor power cycle at 8 MPa, 400C, and expands to the con-

denser pressure of 8 kPa. Water enters the pump as saturated

liquid at 8 kPa. The turbine and pump have isentropic effi-

ciencies of 90 and 80%, respectively. Determine

(a) the mass flow rates of air and steam, each in kg/s.

(b) the thermal efficiency of the combined cycle.

ing through the combustor of the gas turbine,

in MW. Discuss.

Let T

 300 K, p

 100 kPa.

9.60 Air enters the compressor of an Ericsson cycle at 300 K,

1 bar, with a mass flow rate of 5 kg/s. The pressure and tem-

perature at the inlet to the turbine are 10 bar and 1400 K, re-

spectively. Determine

(a) the net power developed, in kW.

(b) the thermal efficiency.

9.61 For the cycle in Problem 9.60, plot the net power devel-

oped, in kW, for compressor pressure ratios ranging from 2

to 15. Repeat for turbine inlet temperatures of 1200 K and

1000 K.

9.62 Nitrogen (N

) is the working fluid of a Stirling cycle with

a compression ratio of nine. At the beginning of the isother-

mal compression, the temperature, pressure, and volume are

310 K, 1 bar, and 0.008 m

, respectively. The temperature dur-

ing the isothermal expansion is 1000 K. Determine

(a) the net work, in kJ.

(b) the thermal efficiency.

Compressible Flow

9.63 If the mass flow rate of air for the cycle in Problem 9.54

is 50 kg/s, calculate the thrust developed by the engine, in kN.

9.64 Referring to the turbojet in Problem 9.54 and the modi-

fied turbojet in Problem 9.56, calculate the thrust developed

by each engine, in kN, if the mass flow rate of air is 50 kg/s.

Discuss.

9.65 Air enters the diffuser of a turbojet engine at 18 kPa,

216 K, with a volumetric flow rate of 230 m

/s and a veloc-

ity of 265 m/s. The compressor pressure ratio is 15, and its

air

e

 e

,

Problems: Developing Engineering Skills 451

isentropic efficiency is 87%. Air enters the turbine at 1360 K

and the same pressure as at the exit of the compressor. The

turbine isentropic efficiency is 89%, and the nozzle isentropic

efficiency is 97%. The pressure at the nozzle exit is 18 kPa.

On the basis of an air-standard analysis, calculate the thrust,

in kN.

9.67 Calculate the ratio of the thrust developed to the mass flow

rate of air, in N per kg/s, for the ramjet engine in Problem 9.57.

9.68 Air flows at steady state through a horizontal, well-insulated,

constant-area duct of diameter 0.25 m. At the inlet,

 2.4 bar, T

 430 K. The temperature of the air leaving

the duct is 370 K. The mass flow rate is 600 kg/min. Determine

the magnitude, in N, of the net horizontal force exerted by the

duct wall on the air. In which direction does the force act?

9.69 Air flows at steady state through a horizontal, well-

insulated duct of varying cross-sectional area, entering at

15 bar, 340 K, with a velocity of 20 m/s. At the exit, the pres-

sure is 9 bar and the temperature is 300 K. The diameter of

the exit is 1 cm. Determine

(a) the net force, in N, exerted by the air on the duct in the

direction of flow.

(b) the rate of exergy destruction, in kW. Let T

 300 K and

 1 bar.

9.70 A flash of lightning is sighted and 3 seconds later thun-

der is heard. Approximately how far away was the lightning

strike?

9.71 Using data from Table A-4, estimate the sonic velocity, in

m/s, of steam of 60 bar, 360C. Compare the result with the

value predicted by the ideal gas model.

9.72 Plot the Mach number of carbon dioxide at 1 bar, 460 m/s,

as a function of temperature in the range 250 to 1000 K.

9.73 For Problem 9.70, determine the values of the Mach num-

ber, the stagnation temperature, in K, and the stagnation pres-

sure, in bar, at the inlet and exit of the duct, respectively.

9.74 Steam flows through a passageway, and at a particular lo-

cation the pressure is 3 bar. The corresponding stagnation state

is fixed by a stagnation pressure of 7 bar and a stagnation tem-

perature of 400C. Determine the specific enthalpy, in kJ/kg,

and the velocity, in m/s.

9.75 For the isentropic flow of an ideal gas with constant spe-

cific heat ratio k, the ratio of the temperature T* to the stag-

nation temperature T

is T*T

 2(k  1). Develop this

relationship.

9.76 A gas expands isentropically through a converging nozzle

from a large tank at 8 bar, 500 K. Assuming ideal gas behavior,

determine the critical pressure p*, in bar, and the corresponding

temperature, in K, if the gas is

(a) air.

(b) carbon dioxide (CO

9.77 Steam expands isentropically through a converging noz-

zle operating at steady state from a large tank at 1.83 bar,

280C. The mass flow rate is 2 kg/s, the flow is choked, and

the exit plane pressure is 1 bar. Determine the diameter of the

nozzle, in cm, at locations where the pressure is 1.5 bar, and

1 bar, respectively.

9.78 An ideal gas mixture with k  1.31 and a molecular weight

of 23 is supplied to a converging nozzle at p

 5 bar, T



700 K, which discharges into a region where the pressure is 1

bar. The exit area is 30 cm

. For steady isentropic flow through

the nozzle, determine

(a) the exit temperature of the gas, in K.

(b) the exit velocity of the gas, in m/s.

9.79 Air at p

 1.4 bar, T

 280 K expands isentropically

through a converging nozzle and discharges to the atmosphere

at 1 bar. The exit plane area is 0.0013 m

(a) Determine the mass flow rate, in kg/s.

(b) If the supply region pressure, p

, were increased to 2 bar,

what would be the mass flow rate, in kg/s.?

9.80 Air as an ideal gas with k  1.4 enters a diffuser operat-

ing at steady state at 4 bar, 290 K, with a velocity of 512 m/s.

Assuming isentropic flow, plot the velocity, in m/s, the Mach

number, and the area ratio AA* for locations in the flow cor-

responding to pressures ranging from 4 to 14 bar.

9.81 A converging–diverging nozzle operating at steady state has

a throat area of 3 cm

and an exit area of 6 cm

. Air as an ideal

gas with k  1.4 enters the nozzle at 8 bar, 400 K, and a Mach

number of 0.2, and flows isentropically throughout. If the noz-

zle is choked, and the diverging portion acts as a supersonic

nozzle, determine the mass flow rate, in kg/s, and the Mach

number, pressure, in bar, and temperature, in K, at the exit. Re-

peat if the diverging portion acts as a supersonic diffuser.

9.82 For the nozzle in Problem 9.81, determine the back pres-

sure, in bar, for which a normal shock would stand at the exit

plane.

9.83 For the nozzle in Problem 9.81, a normal shock stands in

the diverging section at a location where the pressure is 2 bar.

The flow is isentropic, except where the shock stands. Deter-

mine the back pressure, in bar.

9.84 Air as an ideal gas with k  1.4 undergoes a normal shock.

The upstream conditions are p

 0.5 bar, T

 280 K, and

 1.8. Determine

(a) the pressure p

, in bar.

(b) the stagnation pressure p

, in bar.

, in K.

(d) the change in specific entropy across the shock, in kJ/kg K.

(e) Plot the quantities of parts (a)–(d) versus M

ranging from

1.0 to 2.0. All other upstream conditions remain the same.

9.85 Air at 3.4 bar, 530 K, and a Mach number of 0.4 enters a

converging–diverging nozzle operating at steady state. A nor-

mal shock stands in the diverging section at a location where

the Mach number is M

 1.8. The flow is isentropic, except

where the shock stands. If the air behaves as an ideal gas with

k  1.4, determine

452 Chapter 9 Gas Power Systems

(a) the stagnation temperature T

, in K.

(b) the stagnation pressure p

, in bar.

(d) the pressure p

, in bar.

(e) the stagnation pressure p

, in bar.

(f) the stagnation temperature T

, in K.

If the throat area is 7.6  10

4

, and the exit plane pressure

is 2.4 bar, determine the mass flow rate, in kg/s, and the exit

area, in m

9.86 Derive the following expressions: (a) Eq. 9.55, (b) Eq.

9.56, (c) Eq. 9.57.

9.87 Using Interactive Thermodynamics: IT, generate tables of

the same isentropic flow functions as in Table 9.1 for specific

heat ratios of 1.2, 1.3, 1.4, and 1.67 and Mach numbers

ranging from 0 to 5.

9.88 Using Interactive Thermodynamics: IT, generate tables of

the same normal shock functions as in Table 9.2 for specific

heat ratios of 1.2, 1.3, 1.4, and 1.67 and Mach numbers ranging

from 1 to 5.

Design & Open Ended Problems: Exploring Engineering Practice

9.1D

With the development of high-strength metal–ceramic

materials, internal combustion engines can now be built with

no cylinder wall cooling. These adiabatic engines operate with

cylinder wall temperatures as high as 930C. What are the im-

portant considerations for adiabatic engine design? Are adia-

batic engines likely to find widespread application? Discuss.

9.2D An important factor leading to the increase in perform-

ance of gas turbines over the years has been the use of turbine

blade cooling to allow higher turbine inlet temperatures. With

the aid of diagrams, explain the various methods of turbine

blade cooling that are commonly used. What are some of the

most important research issues in gas turbine blade technol-

ogy today? Discuss.

9.3D Steam-injected gas turbines use hot turbine exhaust gases

to produce steam that is injected directly into the gas turbine

system. Figure P9.3D illustrates two possible approaches to

steam injection. In one approach, steam is injected directly into

the combustor. In the other approach, steam is injected into the

low-pressure turbine stages.

(a) What are the relative advantages and disadvantages of

these steam injection approaches? How does steam injec-

tion lead to better power cycle performance?

(b) Each of the steam injection approaches is inherently simpler

than combined cycles like the one illustrated in Fig. 9.23.

What are the other advantages and disadvantages of direct

steam injection compared to combined cycles?

9.4D Closed Brayton power systems, receiving their energy in-

put from radioisotopes, nuclear reactors, or solar collectors,

have been suggested for meeting space vehicle power require-

ments. What are the advantages and disadvantages of closed

Brayton cycles for spaceflight applications? What mission-

specific design criteria might determine the selection of the

system and the energy source?

9.5D Factories requiring compressed air and process heat com-

monly run electrically-driven air compressors and natural gas-

fired boilers to meet these respective needs. As an alternative,

commercially available natural gas-fueled engine-driven com-

pressor systems can simultaneously provide for both needs.

Determine if utility rates in your locale are favorable for the

adoption of such systems. Prepare a memorandum explaining

your conclusions.

9.6D Inlet air temperature and pressure can have significant im-

pact on gas turbine performance. Investigate the effect on the

power developed by a General Electric LM 6000 gas turbine

when the inlet air temperature and pressure vary about base-

line values of 10C and 1 bar, respectively. What are some ways

that could be used to alter the inlet air temperature and pres-

sure, and what are the economic implications? Prepare a mem-

orandum summarizing your findings.

9.7D A manufacturing company currently purchases 2.4 

MW h of electricity annually from the local utility com-

pany. An aging boiler on the premises annually provides 4 

kg of process steam at 20 bar. Consider the feasibility of

acquiring a cogeneration system to meet these needs. The sys-

tem would employ a natural gas–fueled gas turbine to produce

High-pressure

steam

Low-

pressure

steam

Air in

Heat

recovery

boiler

Turbine

exhaust

Water

supply

Combustor

 Figure P9.3D

Design & Open Ended Problems: Exploring Engineering Practice 453

the electricity and a heat-recovery steam generator to produce

the steam. Using thermoeconomic principles, investigate the

economic issues that should be considered in making a rec-

ommendation about the proposed cogeneration system. Write

a report of your findings.

9.8D The Stirling engine was first patented in 1816 but has not

been widely commercialized. Still, efforts continue to develop

Stirling engine technology for practical uses such as vehicle

propulsion. Prepare a memorandum summarizing the status of

Stirling engine technology. Discuss the advantages and disad-

vantages of Stirling engines and assess the likelihood that they

will be more widely used in the future.

9.9D The inlet to a gas turbine aircraft engine must provide air

to the compressor with as little a drop in stagnation pressure

and with as small a drag force on the aircraft as possible. The

inlet also serves as a diffuser to raise the pressure of the air

entering the compressor while reducing the air velocity. Write

a paper discussing the most common types of inlet designs for

subsonic and supersonic applications. Include a discussion of

how engine placement affects diffuser performance.

9.10D In what ways must the compressible flow analysis pre-

sented in this chapter be modified to model the flow through

steam turbines? What special design considerations arise be-

cause of the possibility of condensation occurring within the

blade rows and nozzles of steam turbines?

9.11D End of Cheap Oil in View, Experts Say (see box

Sec. 9.2). Considering the likelihood of oil scarcity in years

ahead, investigate alternatives to conventional oil for meet-

ing our transportation needs without excessive costs or en-

vironmental impacts. Write a report including at least three

references.

9.12D New Power Plant Breaks Imagined Barrier (see box

Sec. 9.10). Investigate technical innovations that might allow

the thermal efficiency of future combined-cycle power plants

to exceed the 60% value of the H System

. Write a report

including at least three references.

454

Refrigeration and

Heat Pump

Systems

ENGINEERING CONTEXT Refrigeration systems for food preser-

vation and air conditioning play prominent roles in our everyday lives. Heat pumps also

are used for heating buildings and for producing industrial process heat. There are

many other examples of commercial and industrial uses of refrigeration, including air

separation to obtain liquid oxygen and liquid nitrogen, liquefaction of natural gas, and

production of ice.

The objective of this chapter is to describe some of the common types of refrigeration

and heat pump systems presently in use and to illustrate how such systems can be mod-

eled thermodynamically. The three principal types described are the vapor-compression,

absorption, and reversed Brayton cycles. As for the power systems studied in Chaps. 8

and 9, both vapor and gas systems are considered. In vapor systems, the refrigerant is

alternately vaporized and condensed. In gas refrigeration systems, the refrigerant remains

a gas.



10.1 Vapor Refrigeration Systems

The purpose of a refrigeration system is to maintain a cold region at a temperature below

the temperature of its surroundings. This is commonly achieved using the vapor refrigera-

tion systems that are the subject of the present section.

CARNOT REFRIGERATION CYCLE

To introduce some important aspects of vapor refrigeration, let us begin by considering a

Carnot vapor refrigeration cycle. This cycle is obtained by reversing the Carnot vapor power

cycle introduced in Sec. 5.6. Figure 10.1 shows the schematic and accompanying T–s dia-

gram of a Carnot refrigeration cycle operating between a region at temperature T

and an-

other region at a higher temperature T

. The cycle is executed by a refrigerant circulating

steadily through a series of components. All processes are internally reversible. Also, since

heat transfers between the refrigerant and each region occur with no temperature differences,

there are no external irreversibilities. The energy transfers shown on the diagram are positive

in the directions indicated by the arrows.

chapter objective 

10.1 Vapor Refrigeration Systems 455

Let us follow the refrigerant as it passes steadily through each of the components in

the cycle, beginning at the inlet to the evaporator. The refrigerant enters the evaporator

as a two-phase liquid–vapor mixture at state 4. In the evaporator some of the refrigerant

changes phase from liquid to vapor as a result of heat transfer from the region at tem-

perature T

to the refrigerant. The temperature and pressure of the refrigerant remain

constant during the process from state 4 to state 1. The refrigerant is then compressed

adiabatically from state 1, where it is a two-phase liquid–vapor mixture, to state 2, where

it is a saturated vapor. During this process, the temperature of the refrigerant increases

from T

to T

, and the pressure also increases. The refrigerant passes from the compres-

sor into the condenser, where it changes phase from saturated vapor to saturated liquid

as a result of heat transfer to the region at temperature T

. The temperature and pressure

remain constant in the process from state 2 to state 3. The refrigerant returns to the state

at the inlet of the evaporator by expanding adiabatically through a turbine. In this process,

from state 3 to state 4, the temperature decreases from T

to T

, and there is a decrease

in pressure.

Since the Carnot vapor refrigeration cycle is made up of internally reversible processes,

areas on the T–s diagram can be interpreted as heat transfers. Applying Eq. 6.51, area

1–a–b–4–1 is the heat added to the refrigerant from the cold region per unit mass of refrig-

erant flowing. Area 2–a–b–3–2 is the heat rejected from the refrigerant to the warm region

per unit mass of refrigerant flowing. The enclosed area 1–2–3–4–1 is the net heat transfer

from the refrigerant. The net heat transfer from the refrigerant equals the net work done on

the refrigerant. The net work is the difference between the compressor work input and the

turbine work output.

The coefficient of performance  of any refrigeration cycle is the ratio of the refrigera-

tion effect to the net work input required to achieve that effect. For the Carnot vapor refrig-

eration cycle shown in Fig. 10.1, the coefficient of performance is

(10.1)

This equation, which corresponds to Eq. 5.9, represents the maximum theoretical coefficient

of performance of any refrigeration cycle operating between regions at T

and T



 T



area 1–a–b–4–1

area 1–2–3–4–1



 s

 T

21s

 s

max





 W



 Figure 10.1 Carnot vapor refrigeration cycle.

Condenser

Evaporator

Compressor

out

4 1

Turbine

Cold region at T

Warm region at T