Use the definition of enthalpy to calculate the change in enthalpy between points 1 and 2 of the Rankine cycle, for the same numerical parameters as used in the text. Recalculate the efficiency using your corrected value ofH2, and comment on the accuracy of the approximationH2≈H1.

Short Answer

Expert verified

The efficiency of the Rankine cycle could not result in efficiency even closer to 1because of some heat and pressure losses that are encountered during the process. The efficiency of the cycle is0.4775.

Step by step solution

01

Step 1. Introduction

To evaluate the Rankine cycle's efficiency, one must first compute the enthalpy energy change at various points throughout the cycle, i.e., the amount of heat absorbed or rejected by the system at constant pressure at various times.

The Rankine cycle's efficiency is:

e=1-H4-H1H3-H2

where

H1=Enthalpyatpoint1H2=Enthalpyatpoint2H3=Enthalpyatpoint3H4=Enthalpyatpoint4

02

Step 2. Calculation

The expression which relates the enthalpy change to the change in internal energy, volume and pressure is dH=dU+PdV+VdP.

By second law of thermodynamics dU=TdS-PdV+μdN.

Putting the value of dUin the first expression.

dH=TdS-PdV+μdN+PdV+VdP.

Here μdNis ignored as the amount of fluid is not changing. So, the value gives 0.

And entropy for the points 1and 2is also zero. So, dSis also ignored.

Hence the expression becomes dH=VdP.

Calculating the change in enthalpy change by assuming the pressure condition of 200 bars, then ΔH12=VΔP.

Substituting values of

V=1dm3=10-3m3P=298×105N/m2

So, ΔH12=10-3m3298×105N/m2=29.8KJ

Using the expression,

H2=H1+ΔH12=84KJ+29.8KJ=113.8KJ

03

Step 3. Calculating efficiency

As,

H1=84KJH2=113.8KJH3=3444KJH4=1824KJ

So,

e=1-H4-H1H3-H2=1-1824-843444-113.8=0.4775

04

Step 4. Conclusion

Thus efficiency of the cycle is 0.4775.

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Most popular questions from this chapter

Consider an ideal Hampson-Linde cycle in which no heat is lost to the environment.

(a) Argue that the combination of the throttling valve and the heat exchanger is a constant-enthalpy device, so that the total enthalpy of the fluid coming out of this combination is the same as the enthalpy of the fluid going in.

(b) Let xbe the fraction of the fluid that liquefies on each pass through the cycle. Show that

x=Hout-HinHout-Hliq,

where Hinis the enthalpy of each mole of compressed gas that goes into the heat exchanger, Houtis the enthalpy of each mole of low-pressure gas that comes out of the heat exchanger, and Hliqis the enthalpy of each mole of liquid produced.

(c) Use the data in Table 4.5to calculate the fraction of nitrogen liquefied on each pass through a Hampson-Linde cycle operating between 1 bar and 100 bars, with an input temperature of 300K. Assume that the heat exchanger works perfectly, so the temperature of the low-pressure gas coming out of it is the same as the temperature of the high-pressure gas going in. Repeat the calculation for an input temperature of 200K.

In an absorption refrigerator, the energy driving the process is supplied not as work, but as heat from a gas flame. (Such refrigerators commonly use propane as fuel, and are used in locations where electricity is unavailable.* ) Let us define the following symbols, all taken to be positive by definition:
Qf= heat input from flame
Qc= heat extracted from inside refrigerator
Qr= waste heat expelled to room
Tf= temperature of flame
Tc= temperature inside refrigerator
Tr= room temperature

(a) Explain why the "coefficient of performance" (COP) for an absorption refrigerator should be defined as Qc / Qf.
(b) What relation among Qf, Qc, and Qr is implied by energy conservation alone? Will energy conservation permit the COP to be greater than 1 ?
(c) Use the second law of thermodynamics to derive an upper limit on the COP, in terms of the temperatures Tf, Tc, and Tr alone.

It has been proposed to use the thermal gradient of the ocean to drive a heat engine. Suppose that at a certain location the water temperature is 22°Cat the ocean surface and 4°Cat the ocean floor.

(a) What is the maximum possible efficiency of an engine operating between these two temperatures?

(b) If the engine is to produce 1GWof electrical power, what minimum volume of water must be processed (to suck out the heat) in every second?

Consider a household refrigerator that uses HFC-134a as the refrigerant, operating between the pressures of 1.0barand 10bars.

(a) The compression stage of the cycle begins with saturated vapor at 1 bar and ends at 10 bars. Assuming that the entropy is constant during compression, find the approximate temperature of the vapor after it is compressed. (You'll have to do an interpolation between the values given in Table 4.4.)

(b) Determine the enthalpy at each of the points 1,2,3 and 4 , and calculate the coefficient of performance. Compare to the COP of a Carnot refrigerator operating between the same extreme temperatures. Does this temperature range seem reasonable for a household refrigerator? Explain briefly.

(c) What fraction of the liquid vaporizes during the throttling step?

A heat pump is an electrical device that heats a building by pumping heat in from the cold outside. In other words, it's the same as a refrigerator, but its purpose is to warm the hot reservoir rather than to cool the cold reservoir (even though it does both). Let us define the following standard symbols, all taken to be positive by convention:
Th=temperature inside buildingTc=temperature outsideQh=heat pumped into building in1dayQc=heat taken from outdoors in1dayW=electrical energy used by heat pump in1day
(a) Explain why the "coefficient of performance" (COP) for a heat pump should be defined as Qh / W.
(b) What relation among Qh , Qc, and W is implied by energy conservation alone? Will energy conservation permit the COP to be greater than 1 ?
(c) Use the second law of thermodynamics to derive an upper limit on the COP, in terms of the temperatures Th and Tc alone.
(d) Explain why a heat pump is better than an electric furnace, which simply converts electrical work directly into heat. (Include some numerical estimates.)

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