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Modern Engineering Thermodynamics

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10.11 Energy Efficiency Based on the Second Law 339<br />

The entrance and exit specific flow availabilities are given by Eq. (10.20) (neglecting all flow stream kinetic and potential<br />

energy terms as per the problem statement) as<br />

so<br />

a f = h − h 0 − T 0 ðs − s 0 Þ<br />

and<br />

a f 1 = h 1 − h 0 − ðT 0 Þðs 1 − s 0 Þ = ð3456:5 − 83:9 kJ/kgÞ− ð20:0 + 273:15 KÞð7:2346 − 0:2965 kJ/kg .KÞ = 1339 kJ/kg<br />

a f 2 = h 2 − h 0 − ðT 0 Þðs 2 − s 0 Þ = ð2488:9 − 83:9 kJ/kgÞ− ð20:0 + 273:15 KÞð7:8509 − 0:2965 kJ/kg .KÞ = 190:4 kJ/kg<br />

Then, Eq. (10.27), for a reversible process, gives the required heat transfer as<br />

or<br />

_Q =<br />

_ W + _mða f 2 − a f 1 Þ<br />

1 − T 0<br />

T b<br />

_Q = 20:0 × 103 kJ/s + ð18:0kg/sÞð190:4 − 1339 kJ/kgÞ<br />

= −1260 kJ/s = −1260 kW<br />

20:0 + 273:15 K<br />

1 −<br />

350: + 273:15 K<br />

Exercises<br />

25. Determine the heat loss from the turbine in Example 10.9 if it is not reversible but instead has a power output of<br />

15.0 × 10 3 kW with an isentropic efficiency of 88.0%. Assume all the other variables remain unchanged.<br />

Answer: _Q = 6840 kJ/s:<br />

26. If we lower the surface temperature on the turbine in Example 10.9 from 350.°C to 100.°C, determine the new heat loss<br />

rate from the turbine, assuming all the other variables remain unchanged. Answer: _Q = 3120 kJ/s.<br />

27. An error was made in reporting the steam mass flow rate in Example 10.9. The actual mass flow rate is 20.0 kg/s not<br />

18.0 kg/s. Determine the heat loss rate now, assuming all the other variables remain unchanged.<br />

Answer: _Q = 5600 kJ/s.<br />

10.11 ENERGY EFFICIENCY BASED ON THE SECOND LAW<br />

The common work and thermal energy conversion efficiencies defined in Chapters 4 and 7 for fluid pumps and<br />

compressors, heat engines, heat pumps, air conditioners, refrigerators, and so forth are based on energy transport<br />

ratios for these technologies. Such efficiencies do not reveal the source of the losses within these devices, because<br />

they have no term containing the irreversibilities within the system. Consequently, these efficiencies are often<br />

called first law energy conversion efficiencies and are described by Eq. (4.70).<br />

10.11.1 First Law (Energy) Efficiency<br />

η E <br />

Desired energy result<br />

Required energy input<br />

For example, in Chapter 7, we introduce the first law (thermal) energy efficiency of a heat engine as<br />

(4.70)<br />

η T <br />

Net work output<br />

Total heat input = ðW outÞ net<br />

ðQ in Þ total<br />

= ð _W out Þ net<br />

ð _Q in Þ total<br />

(7.5)<br />

Equation (4.70) tells us that the energy conversion efficiency is the ratio of the magnitude of the energy that has<br />

been converted divided by the magnitude of energy initially present that could be converted. Since energy is<br />

conserved, if the energy conversion process is not 100%, then some of the energy initially present must have<br />

been converted into a form different from that desired. This energy is said to be “lost” to the system, since it did<br />

not end up in the proper energy form.<br />

All technology can be categorized into four broad genres:<br />

1. Those that output some form of energy (such as an engine) as their primary function.<br />

2. Those that absorb energy (such as a pump) as their primary function.

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