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Modern Engineering Thermodynamics

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7.5 The Absolute Temperature Scale 215<br />

The results of Example 7.1 are highly unrealistic since no real heat engine can ever be<br />

reversible. The irreversibilities within modern heat engines limit their actual operating<br />

thermal energy conversion efficiency to around 30%.<br />

Exercises<br />

1. Rework Example 7.1 for a flame temperature of 2500.°C and an environmental<br />

temperature of 20.0°C. Answer: (η T ) max = 89.4%.<br />

2. If the engine described in Example 7.1 has a maximum (reversible or Carnot) thermal<br />

efficiency of 60.0% when the environmental temperature is 70.0°F, determine the<br />

flame temperature of the combustion process. Answer: T flame = T H = 1324 R = 865°F.<br />

Burning fuel<br />

at 4000.°F<br />

Heat engine<br />

Environment<br />

at 70.0°F<br />

Heat from combustion<br />

Exhaust<br />

Work<br />

v7 = ?<br />

max<br />

possible<br />

FIGURE 7.7<br />

Example 7.1.<br />

EXAMPLE 7.2<br />

A coal-fired electrical power plant produces 5.00 MW of electrical power while exhausting 8.00 MW of thermal energy to a<br />

nearby river at 10.0°C. The power plant requires an input power of 100. kW to drive the boiler feed pump.<br />

Determine<br />

a. The actual thermal efficiency of the power plant.<br />

b. The equivalent heat source temperature if the plant operated on a reversible Carnot cycle.<br />

Solution<br />

First, draw a sketch of the system (Figure 7.8).<br />

Q H (from the combustion of coal)<br />

Boiler<br />

Boiler feed<br />

pump<br />

Turbine<br />

Electrical<br />

generator<br />

W E = 5.00 MW<br />

W P =−1.00 kW<br />

Condenser<br />

Q L (to river at 10.0°C) = 8.00 MW<br />

FIGURE 7.8<br />

Example 7.2.<br />

The unknowns are the actual thermal efficiency of the power plant and the equivalent heat source temperature if the plant operates<br />

on a reversible Carnot cycle. If we construct the system boundary as shown in the sketch, the power plant is a closed system.<br />

a. The actual thermal efficiency of this system is given by Eq. (7.9) as<br />

η T = ð _W out Þ net W<br />

= _ E − j _W P j Q<br />

= _ H − j _Q L j<br />

_Q in<br />

_Q H<br />

_Q H<br />

and the energy rate balance (ERB) for the steady state operation of this system is<br />

or<br />

_Q H − j _Q L j − ð _W E − j _W P jÞ = 0<br />

_Q H = j _Q L j + ð _W E − j _W P jÞ<br />

= j−8:00 MW j + ð5:00 MW − j− 0:100 MWjÞ<br />

= 12:9MW<br />

(Continued )

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