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Modern Engineering Thermodynamics

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9.5 Nozzles, Diffusers, and Throttles 287<br />

EXAMPLE 9.3<br />

Suppose 0.800 kg/s of argon flows at 93.0 m/s through an insulated diffuser from 97.0 kPa, 80.0°C to 101.3 kPa. Assuming<br />

the argon to be an ideal gas with constant specific heats, determine the rate of entropy production within the diffuser.<br />

Solution<br />

First, draw a sketch of the system (Figure 9.3).<br />

The unknown is _S P = ?, and the material is argon gas. The<br />

thermodynamic station conditions are<br />

Station 1<br />

p 1 = 97:0kPa<br />

T 1 = 80:0°C<br />

Diffuser<br />

ƒƒƒ!<br />

process Station 2<br />

p 2 = 101:3kPa<br />

The modified energy rate balance equation for this system is<br />

<br />

_Q − _W = 0 = _m h 2 − h 1 + V2 2 − <br />

V2 1<br />

2g c<br />

Assuming V 2 ≈ 0, and using the ideal gas auxiliary formula (Eq. (6.22)) with data for argon from Table C.13b,we<br />

find that<br />

Then, Eq. (9.18) gives<br />

<br />

_S P = _m c p ln T 2<br />

− R ln p <br />

2<br />

T 1 p 1<br />

= 2:47 J/ðs.KÞ = 2:47 W/K<br />

T 2 = T 1 + V2 1<br />

ð93:0 m/sÞ 2<br />

= ð80:0 + 273:15 KÞ+<br />

2g c c p 21 ð Þ½523 J/ ðkg.KÞŠ<br />

= 353:15 + 8:27 = 361:42 K<br />

= ð0:800 kg/s<br />

h<br />

Þ ½523 J/ ðkg.KÞŠln 361:42<br />

<br />

353:15 − ½ 208 J/ ð kg .KÞŠln 101:3 i<br />

97:0<br />

In this example, both the pressure and the temperature of the gas increase as it passes through the diffuser.<br />

Exercises<br />

7. Determine the entropy production rate in Example 9.3 when the mass flow rate of the argon is increased from 0.800 kg/s<br />

to 1.30 kg/s. Keep the values of all the other variables the same as they are in Example 9.3. Answer: _S P = 4:01 W/K.<br />

8. Determine the entropy production rate in Example 9.3 as the inlet velocity is increased from 93.0 m/s to 155 m/s. Keep<br />

the values of all the other variables the same as they are in Example 9.3. Answer: _S P = 19:1 W/K.<br />

9. Could the gas in Example 9.3 be changed from argon to air, keeping the values of all the other variables (except c p and<br />

R) the same as they are in Example 9.3? Hint: Check the sign of _S P . Answer: No. When the values of c p and R for air are<br />

used along with the values of the other variables given in Example 9.3, Eq. (9.18) gives _S P = −0:187. Since _S P < 0 in this<br />

case, the process as described in Example 9.3 with air replacing argon cannot occur.<br />

1<br />

V 1 = 93.0 m/s<br />

FIGURE 9.3<br />

Example 9.3.<br />

S P = ?<br />

Diffuser<br />

2<br />

System boundary<br />

m = 0.800 kg/s<br />

of argon<br />

EXAMPLE 9.4<br />

Suppose 0.100 lbm/s of Refrigerant-134a is throttled across the expansion valve in a refrigeration unit. The R-134a enters the valve<br />

as a saturated liquid at 100.°F and exits at 20.0°F with a quality of 53.0%. If the inlet and exit velocities are equal, determine<br />

a. The entropy production rate inside the valve if the valve is not insulated and has an isothermal external surface<br />

temperature of 60.0°F.<br />

b. The entropy production rate inside the valve if it is insulated and assuming it has the same inlet conditions and exit<br />

temperature as just stated.<br />

c. The percent decrease in the entropy production rate of part a brought about by adding the insulation in part b.<br />

Solution<br />

First, draw a sketch of the system (Figure 9.4).<br />

<br />

The unknowns are _S P uninsulated , _S P<br />

insulated , and the percent decrease in _S P due to the insulation. The material is R-134a.<br />

The thermodynamic station conditions are<br />

Station 1<br />

x 1 = 0:00 kPa<br />

T 1 = 100:°F<br />

Throttling<br />

ƒƒƒ ƒ!<br />

process<br />

Station 2<br />

x 2 = 0:530 ðonly in part aÞ<br />

T 2 = 20:0°F<br />

(Continued )

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