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Figure 5.35 (left) shows the free energy curves at one particular temperature for a two-component system that has three possible solid phases (crystal structures), one of essentially pure A, one of essentially pure B, and one of intermediate composition. Draw tangent lines to determine which phases are present at which values of x. To determine qualitatively what happens at other temperatures, you can simply shift the liquid free energy curve up or down (since the entropy of the liquid is larger than that of any solid). Do so, and construct a qualitative phase diagram for this system. You should find two eutectic points. Examples of systems with this behaviour include water + ethylene glycol and tin - magnesium.

Short Answer

Expert verified

Starting at x=0 on the left, the αphase and liquid phase are stable, then the liquid phase is stable, then the β phase and liquid phase are stable, then a small range of x where only the β phase is stable, and ultimately just the liquid phase is stable.

Step by step solution

01

Given information

The free energy curves at one particular temperature for a two-component system that has three possible solid phases (crystal structures), one of essentially pure A, one of essentially pure B, and one of intermediate composition.

02

Step 2: 

Consider the Gibbs free energy graph below, which shows a system with three solid phases: α,βandγ. One is a pure A substance, one is a pure B substance, and one is a mixture of the two.

03

Explanation 

First, as shown in the diagram, we draw three tangent lines from left to right: first, the αphase plus the liquid phase are stable, then the liquid phase is stable, then the βphase plus the liquid phase are stable, then a narrow range of x where only the βphase is stable, and finally only the liquid phase is stable.

04

Calculations

The Gibbs free energy is given by

G=U-TS+PV

At constant entropy and constant pressure, differentiate the Gibbs free energy to get:

role="math" localid="1647065790638" dG=dU-SdT+PdV

By increasing the temperature,

∂G∂T=-S

We can see from this equation that as the temperature rises, the stability ranges of αand β vanish. When we lower the temperature, the stability of γ plus the liquid appears, as seen in the previous figure for large x. As the temperature drops, the liquid's stable range narrows until it vanishes at two locations, which are known as the eutectic points (where all the liquid freezes).

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Most popular questions from this chapter

In a hydrogen fuel cell, the steps of the chemical reaction are

at-electrode:H2+2OH-⟶2H2O+2e-at+electrode:12O2+H2O+2e-⟶2OH-

Calculate the voltage of the cell. What is the minimum voltage required for electrolysis of water? Explain briefly.

Use a Maxwell relation from the previous problem and the third law of thermodynamics to prove that the thermal expansion coefficient β(defined in Problem 1.7) must be zero at T=0.

A formula analogous to that for CP-CVrelates the isothermal and isentropic compressibilities of a material:

κT=κS+TVβ2CP.

(Here κS=-(1/V)(∂V/∂P)Sis the reciprocal of the adiabatic bulk modulus considered in Problem 1.39.) Derive this formula. Also check that it is true for an ideal gas.

Problem 5.58. In this problem you will model the mixing energy of a mixture in a relatively simple way, in order to relate the existence of a solubility gap to molecular behaviour. Consider a mixture of A and B molecules that is ideal in every way but one: The potential energy due to the interaction of neighbouring molecules depends upon whether the molecules are like or unlike. Let n be the average number of nearest neighbours of any given molecule (perhaps 6 or 8 or 10). Let n be the average potential energy associated with the interaction between neighbouring molecules that are the same (4-A or B-B), and let uAB be the potential energy associated with the interaction of a neighbouring unlike pair (4-B). There are no interactions beyond the range of the nearest neighbours; the values of μoandμABare independent of the amounts of A and B; and the entropy of mixing is the same as for an ideal solution.

(a) Show that when the system is unmixed, the total potential energy due to neighbor-neighbor interactions is 12Nnu0. (Hint: Be sure to count each neighbouring pair only once.)

(b) Find a formula for the total potential energy when the system is mixed, in terms of x, the fraction of B.

(c) Subtract the results of parts (a) and (b) to obtain the change in energy upon mixing. Simplify the result as much as possible; you should obtain an expression proportional to x(1-x). Sketch this function vs. x, for both possible signs of uAB-u0.

(d) Show that the slope of the mixing energy function is finite at both end- points, unlike the slope of the mixing entropy function.

(e) For the case uAB>u0, plot a graph of the Gibbs free energy of this system

vs. x at several temperatures. Discuss the implications.

(f) Find an expression for the maximum temperature at which this system has

a solubility gap.

(g) Make a very rough estimate of uAB-u0for a liquid mixture that has a

solubility gap below 100°C.

(h) Use a computer to plot the phase diagram (T vs. x) for this system.

When plotting graphs and performing numerical calculations, it is convenient to work in terms of reduced variables, Rewrite the van der Waals equation in terms of these variables, and notice that the constants a and b disappear.

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