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Modern Engineering Thermodynamics

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310 CHAPTER 9: Second Law Open System Applications<br />

FINAL COMMENTS ON THE SECOND LAW<br />

In Chapter’s 7, 8, and 9, we deal with the fundamentals of the second law of thermodynamics for nonequilibrium<br />

systems. This law introduces the new thermodynamic property entropy, which is not conserved in any real engineering<br />

process. The second law of thermodynamics states that entropy must always be produced in any irreversible<br />

process; however, a positive entropy production does not mean that the net system entropy must necessarily<br />

increase, because entropy may be transported out of a system faster than it is produced within the system; therefore,<br />

the entropy level of the entire system can either increase or decrease in any real process.<br />

In Chapter 8 we investigate closed system applications of the second law of thermodynamics for both reversible<br />

and irreversible processes. In so doing, we expand the first law examples given in Chapter 5 to include an<br />

entropy balance analysis. Since entropy production is a direct consequence of system losses that lead to diminished<br />

operating efficiency, many of the examples in this chapter focus on determining the entropy production<br />

or its rate to gain further insight into the causes of system inefficiency. This is done by using either the auxiliary<br />

entropy production equations (the direct method) or an appropriate entropy balance equation (the indirect<br />

method).<br />

In this chapter, we use the second law of thermodynamics in the analysis of open systems. We use the entropy<br />

balance to determine the entropy production rates for a variety of common engineering devices (nozzles, diffusers,<br />

throttles, heat exchangers, etc.). We also look at how different processes that achieve the same end<br />

states affect the amount of entropy produced by the system during those processes. This allows us to choose<br />

the process or method of changing the state that is the least dissipative and consequently the most efficient.<br />

Determining processes that minimize the entropy production produces economic and productivity rewards to<br />

the user.<br />

Problems (* indicates problems in SI units)<br />

1. An inventor claims to have a steady state, steady flow system<br />

with an isentropic flow stream (i.e., s in = s out ) that requires heat<br />

addition. Show whether or not this system violates the second<br />

law of thermodynamics.<br />

2. The inventor in Example 9.1 now claims to have a system that<br />

generates heat by pumping water through a pipe isothermally<br />

(i.e., T in = T out ). Show whether or not this system violates the<br />

second law of thermodynamics.<br />

3.* Suppose the inventor in Example 9.1 filed a new patent claim<br />

that said the heater was 20.0 kW and the heat transfer boundary<br />

temperature was 100ºC. What are the water flow rate and entropy<br />

production rate under these conditions?<br />

4.* The inventor in Example 9.1 needs to know the heat transfer<br />

rate and entropy production rate required to heat 5.00 kg/s from<br />

15ºC to50ºC. You are the engineer, so what are the answers?<br />

5.* The inventor in Example 9.1 now wants to patent a<br />

water cooling system that cools 0.500 kg/s of water from 50ºC<br />

to 15ºC by removing heat with a heat transfer boundary<br />

temperature of 10.0ºC. What is (a) the heat transfer rate and<br />

(b) the entropy production rate for this process.<br />

6. An inventor reports that she has a refrigeration compressor that<br />

receives saturated Refrigerant-134a vapor at 0.00°F and delivers<br />

it at 150. psia and 120.°F. The compression process is adiabatic.<br />

Determine whether or not this process violates the second law<br />

of thermodynamics.<br />

7.* A 1.00 MW steam power plant operates on the simple reversible<br />

thermodynamic cycle shown Figure 9.23.<br />

a. What is its thermal efficiency?<br />

b. What is the steam mass flow rate in this system?<br />

c. What is its thermal efficiency if it is operated on a Carnot cycle?<br />

8.* A steam turbine is limited to a maximum inlet temperature of<br />

800.°C. The exhaust pressure is 0.0100 MPa, and the moisture<br />

in the turbine exhaust is not to exceed 9.00%.<br />

T(K)<br />

FIGURE 9.23<br />

Problem 7.<br />

700<br />

650<br />

600<br />

550<br />

500<br />

1.0 1.1 1.2 1.3 1.4<br />

s (kJ/kg •K)<br />

a. What is the maximum allowable turbine inlet pressure if the<br />

flow is adiabatic and reversible?<br />

b. What is the maximum power output per unit mass flow rate?<br />

9.* A steam turbine receives steam at 1.00 MPa and 700.°C and<br />

exhausts at 0.100 MPa. If the turbine can be considered to<br />

operate as a steady flow, reversible, adiabatic machine, what is<br />

the work done per pound of steam flowing? Neglect any<br />

changes in kinetic or potential energy.<br />

10. Saturated mercury vapor enters a steady flow turbine of a highpressure<br />

auxiliary power system at 600. psia and emerges as a<br />

mixture of liquid and vapor at a pressure of 1.00 psia. What<br />

must be the flow rate if the power output is to be 10.0 kW?<br />

Assume the turbine is reversible and adiabatic, and neglect any<br />

changes in kinetic or potential energy.<br />

11.* In the year 2138, a law requires certain limits on the production<br />

of entropy of any marketable piece of technology. This law is<br />

similar in nature to the old air pollution laws of the 20th<br />

century. It sets an upper limit of 1.00 × 10 –3 kJ/(kg · K · s) on the

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