Homework Set 6

1. Air enters a compressor operating at steady state with

a pressure of 14.7 lbf/in^2 , a temperature of 80F, and a

volumetric flowrate of 1000 ft^3/min (cfm). At the exit,

the pressure is 100 lbf/in^2, and the temperature is 400F.

Find the diameter of the exit duct which gives rise to an

exit velocity of 700 ft/sec. Consider air to be an ideal gas.

Solution strategy:

There is a simple but important relationship between

the mass flowrate mdot (lbm/sec) and the volumetric flowrate

voldot (ft^3/sec). It is

mdot = (voldot)/v

where v is the specific volume. Since

mdot = (velocity x cross-sectional area)/v

it follows that

voldot = velocity x cross-sectional area

If there is steady flow and if there are no leaks in the wall

of a pipe or duct, then

mdot = constant

However, since v may vary with position along a pipe or duct,

it follows that

voldot is not a constant

To start the problem solution, we note that voldot = 1000

cfm at the inlet state (state 1). To find mdot, we calculate v1

from the ideal gas law:

v1 = R(T1)/(p1) = (53.33)(80 + 459.7)/(14.7)(144)

= 13.60 ft^3/lbm

and

mdot = [(voldot)1]/(v1) = 1000/13.60

= 1.225 lbm/sec

At the exit state (state 2), the same value of mdot prevails,

but there is a different value of voldot. First, we use the ideal

gas law to calculate v2:

v2 = R(T2)/(p2) = 3.18 ft^3/lbm

and

(voldot)2 = (mdot)(v2) = (1.225)(3.18)

= 3.89 ft^3/sec

= [velocity at 2] x [area at 2]

= (700 ft/sec) x [(pi)(D^2)/4]

Solve this equation for D in feet.

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2. Problem 4.24, page 157 in the 3rd edition and Problem

4.25, page 191 in the 4th edition.

For background on nozzles, read pages 131 - 133 in the

3rd edition and pages 157 - 160 in the 4th edition. These

readings contain a worked-out example.

A nozzle is a device whose main purpose is to change the

velocity in a pipe whose cross-sectional area varies in the

flow direction.

If 1 denotes the nozzle inlet and 2 denotes the nozzle exit,

the First Law for a flowing fluid reduces to (pages 132 and

158 in the respective editions):

0 = (Qdot)/(mdot) + (h1 - h2) + [(V1)^2 - (V2)^2]/2

where h is the specific enthalpy. The problem statement says

that the nozzle is well-insulated, so that Qdot = 0.

At state 1, p1 = 200 lbf/in^2 and T1 = 500F. The value of h1

can be read directly Table A-4E without interpolation. In

addition, the velocities at the inlet and the exit are given as

V1 = 200 ft/sec and 1700 ft/sec respectively. Also,

h2 = h1 + [(V1)^2 - (V2)^2]/2

The values of all the terms on the right-hand side of this

equation are known. However, the units must be carefully

dealt with. The units of h are Btu/lbm, while those of V^2

are (ft/sec)^2. Clearly, conversion factors are needed.

Let's see how to do this:

[(ft)^2]/[(sec)^2]} x 1 / 1

1 = (1/32.2){[(lb)f]/[(lb)m]}{[(sec)^2]/ft}

1 = 778.17 (ft-lbf)/Btu

So, to convert V^2 in (ft/sec)^2 to Btu/lbm divide by 32.2 and

778.17.

With this conversion factor, we can calculate h2. Then, with

this h2 and with p2 = 60 lbf/in^2, we have to go to Table A-4E

and look for T2.

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3. Problem 4.36, page 157 of the 3rd edition and problem 4.37,

page 192 of the 4th edition.

This problem is focused on turbines. A turbine is a power-

producing machine whose "product" is a rotating shaft.

Background material on turbines may be found on pages

133 - 135 of the 3rd edition and on pages 160 - 162 of the 4th

edition. The form of the energy equation for turbines is found

at the bottom of page 134 and at the bottom of page 161 in the

respective editions,

According to the problem statement, the turbine is well-

insulated, so that Qdot = 0. With this, the energy equation is

0 = (Wdot)/(mdot) + (h2 - h1) + [(V2)^2 - (V1)^2]/2

where Wdot is the power output of the rotating shaft. It is

given that Wdot = 10 MW = 10,000kW.

We begin by solving the energy equation for h1:

h1 = (Wdot)/(mdot) + h2 + [(V2)^2 - (V1)^2]/2

The value of h2 can be found from Table A-3 as hg at p =

0.06 bars. All other quantities on the right-hand side are

known, so that h1 can be found. With this value of h1 and

with T1 = 320C, Table A-4 is searched for p1.

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4. Problem 4.58, page 159 of the 3rd edition and problem 4.60,

page 194 of the 4th edition.

There are no work transfers in this problem and potential

energy changes are negligible. Also, since it was given that

cp = constant, it follows that

h2 - h1 = cp(T2 - T1)

The energy equation for this problem can then be written as:

(Qdot)/(mdot) = cp(T2 - T1) + [(V2)^2 - (V1)^2]/2

Before attempting to solve for Qdot, it is first necessary to

determine mdot. Since mdot is a constant (steady state, no

leaks), it may be evaluated anywhere along the pipe. It is

easiest to calculate mdot at the inlet (state 1). The essential

piece of information that is missing at state 1 is the specific

volume v1. From the ideal gas law,

v1 = R(T1)/p1

The molecular weight of carbon dioxide is 44.01 kg/kmole,

and R = (Rbar)/44.01. Once v1 has been found,

mdot = [(velocity)1][(pi)D^2/4]/v1

The last step in the solution is to evaluate the terms on the

right-hand side of the energy equation.

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