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An inventor proposes to make a heat engine using water/ice as the working substance, taking advantage of the fact that water expands as it freezes. A weight to be lifted is placed on top of a piston over a cylinder of water at 1°C. The system is then placed in thermal contact with a low-temperature reservoir at -1°C until the water freezes into ice, lifting the weight. The weight is then removed and the ice is melted by putting it in contact with a high-temperature reservoir at 1°C. The inventor is pleased with this device because it can seemingly perform an unlimited amount of work while absorbing only a finite amount of heat. Explain the flaw in the inventor's reasoning, and use the Clausius-Clapeyron relation to prove that the maximum efficiency of this engine is still given by the Carnot formula, 1 -Te/Th

Short Answer

Expert verified

The maximum efficiency is1-TcTh

Step by step solution

01

Given information

The heat engine efficiency is given as

e=WQh

Where,

W is the work done

Qh is the heat absorbed from hot reservoir

The heat engine's working ingredient is either water or ice. The primary flaw in the inventor's logic is that when water freezes to ice, the weight it can lift is restricted.

The following is the reason for this. The weight of the water will exert pressure on the water, lowering the freezing point below - 1°C. As a result, the water did not freeze.

02

Concept

In a heat engine, the work done by the working substance is equal to the change in the potential energy of the water.

W=PE

Let hi be the starting water level in the cylinder. The height of the water climbs to hf once it freezes into ice. As a result, the change in water's potential energy is as follows.

ΔPE=mghf-hi

Where,

m is the mass of water

g is the acceleration due to gravity

Therefore,

W=mghf-hi

Heat absorbed will be

Qh=L

Where L is the latent heat of water into ice

Substitute mg (hf -hi)for W and L for Qh, in the equation e= e=WQh. to solve for e.

e=mghf-hiL

03

Explanation

Using the Clausius-Clapeyron relationship, the pressure added to the system as the freezing point drops below T is as follows:
dPdT=LThΔV

Where

Vis the change in volume of water

dT is the difference in temperature

ΔV=Vf-Vi

Where, Vfis final volume and Viis initial volume

dT=Th-Tc

Th is temperature of hot reservoir

Therefore, we have

role="math" localid="1646899721371" dPTh-Tc=LThVf-VidP=LThVf-ViTh-Tc

Cylinder's initial volume is

Vi=Ah1

Cylinder's final volume is

Vf=Ahf

Where, A is the area.

The extra pressure to the system is,

dP=mgA

Where, mg is water weight

04

Calculation

Substituting and solving

mgA=LThAhf-AhiTh-Tcmghf-hiL=Th-TcTh

Substitute, e=mghf-hiL

role="math" localid="1646900275148" e=Th-TcThe=1-TcTh

Therefore, the maximum efficiency isrole="math" localid="1646900319016" 1-TcTh

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Most popular questions from this chapter

Functions encountered in physics are generally well enough behaved that their mixed partial derivatives do not depend on which derivative is taken first. Therefore, for instance,
VUS=SUV

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TVS=-PSV

a nontrivial identity called a Maxwell relation. Go through the derivation of this relation step by step. Then derive an analogous Maxwell relation from each of the other three thermodynamic identities discussed in the text (for H, F, and G ). Hold N fixed in all the partial derivatives; other Maxwell relations can be derived by considering partial derivatives with respect to N, but after you've done four of them the novelty begins to wear off. For applications of these Maxwell relations, see the next four problems.


In the previous section I derived the formula (F/V)T=-P. Explain why this formula makes intuitive sense, by discussing graphs of F vs. V with different slopes.

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dlnKdT=ΔH°RT2

which gives the dependence of the equilibrium constant on temperature." Here H°is the enthalpy change of the reaction, for pure substances in their standard states (1 bar pressure for gases). Notice that if H°is positive (loosely speaking, if the reaction requires the absorption of heat), then higher temperature makes the reaction tend more to the right, as you might expect. Often you can neglect the temperature dependence ofH°; solve the equation in this case to obtain

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Consider a completely miscible two-component system whose overall composition is x, at a temperature where liquid and gas phases coexist. The composition of the gas phase at this temperature is xaand the composition of the liquid phase is xb. Prove the lever rule, which says that the proportion of liquid to gas is x-xa/xb-x. Interpret this rule graphically on a phase diagram.

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