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A mixture of 2 mol of \(\mathrm{H}_{2} \mathrm{O}\) and \(3 \mathrm{mol}\) of \(\mathrm{O}_{2}\) is heated to \(3600 \mathrm{K}\) at a pressure of 8 atm. Determine the equilibrium composition of the mixture, assuming that only \(\mathrm{H}_{2} \mathrm{O}, \mathrm{OH}, \mathrm{O}_{2}\), and \(\mathrm{H}_{2}\) are present.

Short Answer

Expert verified
Based on the given data and the assumption that Reaction 1 is the most dominant, we could determine the equilibrium composition of the mixture if we had the temperature dependence of the equilibrium constant for Reaction 1. However, due to the lack of this information, we cannot solve the problem completely, and thus cannot determine the final equilibrium composition of the mixture containing H2O, OH, O2, and H2.

Step by step solution

01

Determine the chemical reactions and equilibrium constants

To begin, let's write the dissociation reactions involving the four given species, OH, O2, H2, and H2O: 1. \(\mathrm{H}_{2}\mathrm{O}\rightleftharpoons\mathrm{OH}+\mathrm{H}_{2}\) (Reaction 1) 2. \(\mathrm{H}_{2}\mathrm{O}\rightleftharpoons\mathrm{O}_{2}+\mathrm{H}_{2}\) (Reaction 2) Since the process takes place at high temperature, let's assume that dissociation of water molecule into its component particles is negligible. Furthermore, let's assume that reaction 1 is most dominant. Therefore, we will focus on Reaction 1. The equilibrium constant \(K_1\) for Reaction 1 can be expressed as follows: \(K_1 = \frac{[\mathrm{OH}][\mathrm{H}_2]}{[\mathrm{H}_2\mathrm{O}]}\) Next, we need to find the temperature dependence of the equilibrium constant. For that, we can use the van't Hoff equation: \(\Delta G^{\circ} = -RT\ln{K}\) where \(\Delta G^{\circ}\) is the standard Gibbs free energy of the reaction, \(R\) is the ideal gas constant, and \(T\) is the temperature in Kelvin. However, we need \(\Delta G^{\circ}\) for reaction 1 at \(3600K\), which isn't provided. Therefore, we need to make a simplifying assumption. Let's assume that the system is nearly ideal and the fugacities can be replaced with the partial pressures, then we can determine \(K_1\) by using \(KP\) instead of fugacity coefficients.
02

Set up a system of equations

First, let's convert the initial total number of moles into the partial pressures: \(P_{\mathrm{H}_2\mathrm{O}} = \frac{2\ mol}{8\ atm} = 0.25\ atm\) \(P_{\mathrm{O}_2} = \frac{3\ mol}{8\ atm} = 0.375\ atm\) Now, let's set up the equilibrium constant expression for Reaction 1: \(K_1 = \frac{(P_{\mathrm{OH}})(P_{\mathrm{H}_2})}{P_{\mathrm{H}_2\mathrm{O}}}\) Since only \(\mathrm{H}_{2}\mathrm{O}\) is consumed during reaction, we can write the change of partial pressures as follows: \(P_{\mathrm{H}_2\mathrm{O}} = 0.25 - x\) \(P_{\mathrm{OH}} = x\) \(P_{\mathrm{H}_2} = x\) Now, substitute these relationships into the equilibrium constant expression: \(K_1 = \frac{x^2}{0.25 - x}\)
03

Solve the equations for the equilibrium composition

In this case, we don't have the value of \(K_{1}\), given the lack of information on the temperature dependence of the equilibrium constant for Reaction 1. Nonetheless, if we had a numerical value for \(K_{1}\), we could proceed as follows: 1. Substitute the numerical value of \(K_{1}\) into the equation: \(K_{1} = \frac{x^2}{0.25 - x}\) 2. Solve this equation for \(x\). This can be done through algebraic manipulation or with the help of a numerical solver. 3. Obtain the final equilibrium composition of the mixture. The equilibrium partial pressures of \(\mathrm{H}_2\mathrm{O}\), \(\mathrm{OH}\), and \(\mathrm{H}_2\) can then be determined using the relationships \(P_{\mathrm{H}_2\mathrm{O}} = 0.25 - x\), \(P_{\mathrm{OH}} = x\), and \(P_{\mathrm{H}_2} = x\) This method allows us to determine the equilibrium composition of the mixture of species \(\mathrm{H}_{2}\mathrm{O}\), \(\mathrm{OH}\), \(\mathrm{O}_{2}\), and \(\mathrm{H}_{2}\) at the given temperature and pressure, assuming that Reaction 1 is the most dominant reaction in the system.

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Most popular questions from this chapter

Using the Gibbs function data, determine the equilibrium constant \(K_{P}\) for the dissociation process \(\mathrm{CO}_{2} \rightleftharpoons\) \(\mathrm{CO}+\frac{1}{2} \mathrm{O}_{2}\) at \((a) 298 \mathrm{K}\) and \((b) 1800 \mathrm{K} .\) Compare your results with the \(K_{P}\) values listed in Table \(\mathrm{A}-28\).

A constant-volume tank contains a mixture of 1 mol of \(\mathrm{H}_{2}\) and \(0.5 \mathrm{mol}\) of \(\mathrm{O}_{2}\) at \(25^{\circ} \mathrm{C}\) and 1 atm. The contents of the tank are ignited, and the final temperature and pressure in the tank are \(2800 \mathrm{K}\) and 5 atm, respectively. If the combustion gases consist of \(\mathrm{H}_{2} \mathrm{O}, \mathrm{H}_{2},\) and \(\mathrm{O}_{2},\) determine \((a)\) the equilibrium composition of the product gases and ( \(b\) ) the amount of heat transfer from the combustion chamber. Is it realistic to assume that no \(\mathrm{OH}\) will be present in the equilibrium mixture?

A gaseous mixture of 30 percent (by mole fraction) methane and 70 percent carbon dioxide is heated at 1 atm pressure to \(1200 \mathrm{K}\). What is the equilibrium composition (by mole fraction) of the resulting mixture? The natural logarithm of the equilibrium constant for the reaction \(\mathrm{C}+2 \mathrm{H}_{2} \rightleftharpoons \mathrm{CH}_{4}\) at \(1200 \mathrm{K}\) is 4.147.

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In absorption refrigeration systems, a two-phase equilibrium mixture of liquid ammonia \(\left(\mathrm{NH}_{3}\right)\) and water \(\left(\mathrm{H}_{2} \mathrm{O}\right)\) is frequently used. Consider a liquid-vapor mixture of ammonia and water in equilibrium at \(30^{\circ} \mathrm{C}\). If the composition of the liquid phase is 60 percent \(\mathrm{NH}_{3}\) and 40 percent \(\mathrm{H}_{2} \mathrm{O}\) by mole numbers, determine the composition of the vapor phase of this mixture. Saturation pressure of \(\mathrm{NH}_{3}\) at \(30^{\circ} \mathrm{C}\) is \(1167.4 \mathrm{kPa}\).

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