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A mixture of one part nitrogen and three parts hydrogen is heated, in the presence of a suitable catalyst, to a temperature of 500° C. What fraction of the nitrogen (atom for atom) is converted to ammonia, if the final total pressure is 400 atm? Pretend for simplicity that the gases behave ideally despite the very high pressure. The equilibrium constant at 500° C is 6.9 x 10-5. (Hint: You'l have to solve a quadratic equation.)

Short Answer

Expert verified

The fraction of nitrogen that is converted to ammonia is56.6%

Step by step solution

01

Given information

A mixture of one part nitrogen and three parts hydrogen is heated, in the presence of a suitable catalyst, to a temperature of 500° C.

The gases behave ideally despite the very high pressure.

The equilibrium constant at 500° C is 6.9 x 10-5

02

Explanation

Consider the following reaction: one part nitrogen and three parts hydrogen are heated to 500 degrees Celsius with a final pressure of 400 atmospheres.

N2+3H2→2NH3(1)

In terms of partial pressure, the equilibrium constant for this reaction may be represented as:

K=PNH3/P02PN2/P0PH2/P03

Where,

Pois atmospheric pressure

K=PNH32PN2PH23

At a temperature of 500 C, the constant is K=6.9×10-5so,

PNH32PN2PH23=6.9×10-5(2)

The total final pressure is:

PNH3+PN2+PH2=400atm(3)

03

Explanation

Because every part of N2 requires three parts of H2, the ratio of partial derivatives reactants remains constant during the reaction, we may write:

PN2PH2=13PH2=3PN2(4)

So we have three equations to solve for the three pressures: (2), (3), and (4). To eliminate PH2, first substitute from (4) to (3), as follows:

PNH3+PN2+3PN2=400atmPNH3+4PN2=400atm(5)

Substitute from from (4) into (2)

PNH3227PN24=6.9×10-5PNH32=1.863×10-3PN24PNH3=1.863×10-3PN22(6)

Substitute from (6) into (5), to eliminate PNH3

1.863×10-3PN22+4PN2=400atm1.863×10-3PN22+4PN2-400atm=0

Solving the above quadratic equation, we get

PN2=-4±16+41.863×10-3(400atm)21.863×10-3

Since the presSure cannot be negative, the accepted solution is:

PN2=60.50atm

Substitute into (4) to get,

PH2=3(60.50atm)=181.5atm

Substitute into (6), we get

PNH3=1.863×10-3(60.50atm)2=158atm

Substitute into (6) to get

PNH3=1.863×10-3(60.50atm)2=158atm

04

Conclusion

We must use the ideal gas law so: to convert these partial pressures to number of molecules.

N=VkTPN=CP

Where C is constant

role="math" localid="1647207370400" The number ofN2molecules is60.5CThe number of molecules ofNH3is158CThenumber of atoms ofN2is60.5C×2=121CThe number of atoms ofNH3is158The number of nitrogen atoms is121C+158C=279CHence,the fraction of the nitrogen atom which converted to ammonia is158C/279C=0.5663=56.6%

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Most popular questions from this chapter

In this problem you will derive approximate formulas for the shapes of the phase boundary curves in diagrams such as Figures 5.31 and 5.32, assuming that both phases behave as ideal mixtures. For definiteness, suppose that the phases are liquid and gas.

(a) Show that in an ideal mixture of A and B, the chemical potential of species A can be written μA=μA°+kTln(1-x)where A is the chemical potential of pure A (at the same temperature and pressure) and x=NB/NA+NB. Derive a similar formula for the chemical potential of species B. Note that both formulas can be written for either the liquid phase or the gas phase.

(b) At any given temperature T, let x1 and xgbe the compositions of the liquid and gas phases that are in equilibrium with each other. By setting the appropriate chemical potentials equal to each other, show that x1and xg obey the equations =1-xl1-xg=eΔGA°/RTandxlxg=eΔGB°/RT and where ΔG°represents the change in G for the pure substance undergoing the phase change at temperature T.

(c) Over a limited range of temperatures, we can often assume that the main temperature dependence of ΔG°=ΔH°-TΔS°comes from the explicit T; both ΔH°andΔS°are approximately constant. With this simplification, rewrite the results of part (b) entirely in terms of ΔHA°,ΔHB° TA, and TB (eliminating ΔGandΔS). Solve for x1and xgas functions of T.

(d) Plot your results for the nitrogen-oxygen system. The latent heats of the pure substances areΔHN2°=5570J/molandΔHO2°=6820J/mol. Compare to the experimental diagram, Figure 5.31.

(e) Show that you can account for the shape of Figure 5.32 with suitably chosenΔH° values. What are those values?

Compare expression 5.68 for the Gibbs free energy of a dilute solution to expression 5.61 for the Gibbs free energy of an ideal mixture. Under what circumstances should these two expressions agree? Show that they do agree under these circumstances, and identify the function f(T, P) in this case.

Below 0.3 K the slope of the °He solid-liquid phase boundary is negative (see Figure 5.13).

(a) Which phase, solid or liquid, is more dense? Which phase has more entropy (per mole)? Explain your reasoning carefully.

(b) Use the third law of thermodynamics to argue that the slope of the phase boundary must go to zero at T = 0. (Note that the *He solid-liquid phase boundary is essentially horizontal below 1 K.)

(c) Suppose that you compress liquid *He adiabatically until it becomes a solid. If the temperature just before the phase change is 0.1 K, will the temperature after the phase change be higher or lower? Explain your reasoning carefully.

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.)

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(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

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

a solubility gap.

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

Suppose you have a mole of water at 25°Cand atmospheric pressure. Use the data at the back of this book to determine what happens to its Gibbs free energy if you raise the temperature to30°C. To compensate for this change, you could increase the pressure on the water. How much pressure would be required?

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