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Modern Engineering Thermodynamics

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170 CHAPTER 6: First Law Open System Applications<br />

EXAMPLE 6.1<br />

Determine the mass flow energy transport rate of steam at 100. psia, 500.°F leaving a system through a 6.00-inch inside diameter<br />

pipe at a velocity of 300. ft/s at a height of 15.0 ft above the floor (the zero height potential).<br />

Solution<br />

First, draw a sketch of the system (Figure 6.2).<br />

6.00 inch ID pipe with<br />

steam at 100. psia<br />

and 500.°F<br />

15.0 ft<br />

300. ft/s<br />

FIGURE 6.2<br />

Example 6.1.<br />

This is an open system, and the unknown is _E mass : The material is steam.<br />

flow<br />

From the superheated steam table, Table C.3a in Thermodynamic Tables to accompany <strong>Modern</strong> <strong>Engineering</strong> <strong>Thermodynamics</strong>, we<br />

find that, at 100. psia and 500.°F,<br />

v = 5:587 ft 3 /lbm<br />

h = 1279:1 Btu/lbm<br />

Now, since ρ =1/v, we can find _m from Eq. (6.1):<br />

Then,<br />

_m = ρAV = AV v<br />

2<br />

π 3 12 ft<br />

2<br />

ð300: ft/sÞ<br />

=<br />

5:587 ft 3 = 10:5 lbm/s<br />

/lbm<br />

and<br />

ke = V2<br />

2g c<br />

=<br />

ð300:Þ 2 ft 2 /s 2<br />

<br />

2 32:174 lbm = 1398<br />

.ft<br />

ft .lbf<br />

lbm<br />

lbf .s 2<br />

<br />

= 1398 ft <br />

.lbf 1 Btu<br />

lbm 778:16 ft.lbf<br />

<br />

= 1:80 Btu<br />

lbm<br />

pe = gZ<br />

g c<br />

In this problem, we have only one flow stream, so<br />

= ð32:174 ft/s2 Þð15:0ftÞ<br />

32:174 lbm .ft<br />

lbf .s 2<br />

<br />

= 15:0 ft .lbf<br />

lbm<br />

_E mass<br />

flow<br />

<br />

1 Btu<br />

778:16 ft.lbf<br />

= − ½ _m ðh + ke + peÞŠ out<br />

= 15:0 ft .lbf<br />

lbm<br />

<br />

= 0:019 Btu/lbm<br />

= − ð10:5 lbm/sÞ½ð1279:1 + 1:80 + 0:019Þ Btu/lbmŠ<br />

= − 1:35 × 10 4 Btu/s<br />

Exercises<br />

1. Determine the percentage contribution to the mass flow energy transport rate in Example 6.1 of each of the following<br />

terms: (a) enthalpy, (b) kinetic energy, and (c) potential energy. Answers: (a) 99.86%, (b) 0.14%, and (c) 0.0015%.<br />

2. Determine the percent error incurred in the answer to Example 6.1 if the kinetic and potential energy terms are<br />

neglected. Answer: Percent error = 0.142%.<br />

3. Suppose the fluid leaving the system through the 6.00-inch pipe in Example 6.1 were saturated liquid water at 50.0°F,<br />

and determine the percentage error incurred in neglecting the kinetic and potential energies of the flow stream. Answer:<br />

Percent error = 9.14%.

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