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Suppose you are told to design a household air conditioner using

HFC-134a as its working substance. Over what range of pressures would you have it operate? Explain your reasoning. Calculate the COP for your design, and compare to the COP of an ideal Carnot refrigerator operating between the same extreme temperatures.

Short Answer

Expert verified

The household air conditioner will be operated between pressures of 4 and 12 bar, with a COP of 5.67 for the design and 7.54 for an ideal Carnot refrigerator running between the same reservoir temperatures, which is higher than the design's COP.

Step by step solution

01

To find

The range of pressures over which the household air conditioner will be operated and the COP for the design.Comparison of COP for design to the COP for an ideal Carnot refrigerator operating between the same reservoir temperatures.

02

Explanation

Given:

HFC-134a is used as a working substance to design a household air conditioner.

Formula: Tables 4.3 and 4.4 can be used to select the high temperature, which must be higher than the temperature outside the room, and the low temperature, which must be lower than the temperature outside the room, as 46.3°and 8.9°, respectively. Table 4.3 shows that the pressure at high temperature is 12 bar and the pressure at low temperature is 4 bar.

The enthalpy at the low temperature is 252kJ/kgand the enthalpy at the high temperature is 116kJ/kgfrom table 4.3.

Since the process is assumed to be adiabatic along the compression path, the entropy at the beginning and end is the same. From table 4.3, it has a value of 0.915kJ/K·kg, which corresponds to the temperature 50°from table 4.4. The corresponding enthalpy can be calculated as 276kJ/kg.

The expression of COP for the design

COP=H1-H3H2-H1…(1)

Where, H1is enthalpy at low temperature,

H3is enthalpy at high temperature and

H2is enthalpy at temperature 50°for the compression path.

The expression of the maximum COP for a Carnot air conditioner

COPmax=TcoldTboc-Tcold…..(2)

Where,Tcoldis the temperature of the cold reservoir andThotis the temperature of hot reservoir.

03

Calculation

Calculation:

SubstituteH1=252kJ/kgH2=276kJ/kgH3=116kJ/kgin equation (1)

COP=(252kJ/kg)-(116kJ/kg)(276kJ/kg)-(252kJ/kg)=5.67

SubstituteTcold=8.9andThot=46.3°forin equation (2)

COPmax=((8.9+273)K)((46.3+273)K)-((8.9+273)K)=7.54

Hence The household air conditioner will be operated between pressures of 4 and 12 bar, with a COP of 5.67 for the design and 7.54 for an ideal Carnot refrigerator running between the same reservoir temperatures, which is higher than the design's COP.

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Most popular questions from this chapter

What is the maximum possible COP for a cyclic refrigerator operating between a high-temperature reservoir at 1K and a low-temperature reservoir at 0.01 K ?

To get more than an infinitesimal amount of work out of a Carnot engine, we would have to keep the temperature of its working substance below that of the hot reservoir and above that of the cold reservoir by non-infinitesimal amounts. Consider, then, a Carnot cycle in which the working substance is at temperatureThwas it absorbs heat from the hot reservoir, and at temperatureTcwas it expels heat to the cold reservoir. Under most circumstances the rates of heat transfer will be directly proportional to the temperature differences:

QhΔt=KTh-ThwandQcΔt=KTcw-Tc

I've assumed here for simplicity that the constants of proportionality Kare the same for both of these processes. Let us also assume that both processes take the

same amount of time, so theΔt''s are the same in both of these equations.*

aAssuming that no new entropy is created during the cycle except during the two heat transfer processes, derive an equation that relates the four temperaturesTh,Tc,Thwand Tcw

bAssuming that the time required for the two adiabatic steps is negligible, write down an expression for the power (work per unit time) output of this engine. Use the first and second laws to write the power entirely in terms of the four temperatures (and the constant K), then eliminateTcwusing the result of part a.

cWhen the cost of building an engine is much greater than the cost of fuel (as is often the case), it is desirable to optimize the engine for maximum power output, not maximum efficiency. Show that, for fixed Thand Tc, the expression you found in part bhas a maximum value at Thw=12Th+ThTc. (Hint: You'll have to solve a quadratic equation.) Find the correspondingTcw.

dShow that the efficiency of this engine is 1-Tc/ThEvaluate this efficiency numerically for a typical coal-fired steam turbine with Th=600°CandTc=25°C, and compare to the ideal Carnot efficiency for this temperature range. Which value is closer to the actual efficiency, about 40%, of a real coal-burning power plant?

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.

In a real turbine, the entropy of the steam will increase somewhat. How will this affect the percentages of liquid and gas at point4in the cycle? How will the efficiency be affected?

Can you cool off your kitchen by leaving the refrigerator door open? Explain.

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