Thermodynamics: An Engineering Approach
Thermodynamics: An Engineering Approach
9th Edition
ISBN: 9781260048766
Author: CENGEL
Publisher: MCG
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Chapter 16.6, Problem 23P

(a)

To determine

The natural Logarithm equilibrium constant for the reaction at 298K.

Compare the results for the values of KP obtained from the equation of equilibrium constants and the equilibrium constant Table A-28.

(a)

Expert Solution
Check Mark

Answer to Problem 23P

The natural Logarithm equilibrium constant for the reaction at 298K is 103.81_.

The natural equilibrium constant obtained from the equilibrium constants of Table A-28 at 2298K is 103.76_.

Explanation of Solution

Express the standard-state Gibbs function change.

ΔG*(T)=vCO2g¯*CO2(T)vCOg¯*CO(T)vO2g¯*O2(T) (I)

Here, the Gibbs function of components CO2,CO,andO2 at 1 atm pressure and temperature T are g¯*CO2(T),g¯*CO(T),andg¯*O2(T) respectively, temperature of CO2,CO,andO2 are TCO2,TCO,andTO2,and stoichiometric coefficients of components CO2,CO,andO2 are vCO2,vCO,andvO2 respectively.

Write the equation to calculate the natural logarithms of equilibrium constant for the chemical equilibrium of ideal-gas mixtures.

lnKP=ΔG*(T)RuT (II)

Here, universal gas constant is Ru and temperature of Gibbs function of formation is T.

Conclusion:

From the equilibrium reaction, the values of vCO2,vCO,andvO2 are 1, 1, and 0.5 respectively.

Refer Table A-26, obtain the values of g¯*H2O,g¯*H2,andg¯*O2 as below:

g¯*CO2=394,360 kJ/kmolg¯*CO=137,150kJ/kmol g¯*O2=0kJ/kmol

Substitute 1 for vCO2, 1 for vCO, 0.5 for vO2, -394,360 kJ/kmol for g¯*CO2, 137,150kJ/kmol  for g¯*CO, and 0 for g¯*O2 in Equation (I).

ΔG*(T)=1(394,360 kJ/kmol/kmol)1(137,150kJ/kmol )0.5(0)=257,210 kJ/kmol

Substitute 257,210 kJ/kmol for ΔG*(T), 298 K for T, and 8.314kJ/kmolK for Ru in Equation (II).

lnKP=257,210 kJ/kmol(8.314kJ/kmolK)×298 K=103.81

Thus, the equilibrium constant obtained from the equilibrium reaction at 298 K is 103.81_.

From table A-28, “Natural logarithms of the equilibrium constant” obtain the equilibrium constant for the reaction at the temperature of 298 K as 103.76_.

The value obtained for equilibrium constant at 298 K from the definition of the equilibrium constant is 103.81 which is equal to the value obtained for equilibrium constant as 103.76 from the Table A-28.

(b)

To determine

The natural logarithm equilibrium constant for the reaction at 2000 K.

Compare the results for the values of KP obtained from the equilibrium constants of Table A-28.

(b)

Expert Solution
Check Mark

Answer to Problem 23P

The natural logarithm equilibrium constant for the reaction at 2000 K is 6.64_.

The natural Logarithm equilibrium constant obtained from the equilibrium constants of Table A-28 at 2000K is 6.635_

Explanation of Solution

Express the standard-state Gibbs function change.

ΔG*(T)=vCO2g¯*CO2(T)vCOg¯*CO(T)vO2g¯*O2(T)=vCO2(h¯Ts¯)CO2vCO(h¯Ts¯)COvO2(h¯Ts¯)O2=[vCO2(h¯fo,CO2+(h¯CO2h¯oCO2)Ts¯CO2)vH2(h¯f,COo+(h¯H2h¯oCO)Ts¯CO)vO2(h¯fo,O2+(h¯O2h¯oO2)Ts¯O2)] (III)

Here, the Gibbs function of components CO2,CO,andO2 at 1 atm pressure and temperature T are g¯*CO2(T),g¯*CO(T),andg¯*O2(T) respectively, enthalpy on the unit mole basis of H2,O2,andH2O are h¯H2,h¯O2,andh¯H2O respectively, absolute entropy of CO2,CO,andO2 are s¯CO2,s¯CO,ands¯O2, temperature of CO2,CO,andO2 are TCO,TCO,andTO2, sensible enthalpy at the specified state of CO2,CO,andO2 are h¯CO2h¯CO,andh¯O2, the sensible enthalpy at the standard reference state of 25°C and 1 atm of CO2,CO,andO2 are h¯CO2o,h¯COo,andh¯O2o, the enthalpy of formation at a specified states of 25°C and 1 atm for the components CO2,CO,andO2 are h¯f,CO2o,h¯f,COo,andh¯f,O2o, stoichiometric coefficients of components CO2,CO,andO2 are vCO2,vCO,andvO2 respectively.

Write the equation to calculate the natural logarithms of equilibrium constant for the chemical equilibrium of ideal-gas mixtures.

lnKP=ΔG*(T)RuT (IV)

Here, universal gas constant is Ru and temperature of Gibbs function of formation is T.

Conclusion:

From the equilibrium reaction, the values of vCO2,vCO,andvO2 are 1, 1, and 0.5 respectively.

Refer Table A-26, obtain the values of h¯f,H2o,h¯f,O2o,andh¯f,H2Oo as below:

h¯f,CO2o=393,520 kJ/kmolh¯f,COo=110,530 kJ/kmolh¯f,O2o=0kJ/kmol

Refer Table A-20, obtain the value of h¯CO2o at temperature of 298K.

h¯CO2o=9634kJ/kmol

Refer Table A-20, obtain the value of h¯CO2 and s¯CO2 at temperature of 2000K.

h¯CO2=100,804 kJ/kmols¯CO2=309.210kJ/kmolK

Refer Table A-21, obtain the value of h¯COo at temperature of 298K.

h¯COo=8669kJ/kmol

Refer Table A-21, obtain the value of h¯CO and s¯CO at temperature of 2000K.

h¯CO=65,408kJ/kmols¯CO=258.600kJ/kmolK

Refer Table A-19, obtain the value of h¯O2o at temperature of 298K.

h¯O2o=8682 kJ/kmol

Refer to Table A-19, obtain the value of h¯H2O and s¯H2O at temperature of 2000 K.

h¯O2o=67,881 kJ/kmols¯O2=268.655 kJ/kmolK

Substitute 1 for vH2O, 241,820kJ/kmol for h¯fo,H2O, 82593 kJ/kmol for h¯H2O, 9904kJ/kmol for h¯oH2O, 2000 K for T, 264.571 kJ/kmolK for s¯H2O, 1 for vH2, 0 for h¯f,H2o, 61,400 kJ/kmol for h¯H2, 8468kJ/kmol for h¯oH2, 188.297 kJ/kmolK for Ts¯H2, 0.5 for vO2, 0 for h¯fo,O2, 67881 kJ/kmol for h¯O2, 8682 kJ/kmol for h¯oO2, 268.655 kJ/kmolK for s¯O2 in Equation (III).

ΔG*(T)=[1(393,520 kJ/kmol+100,804 kJ/kmol9634kJ/kmol2000 K×309.210kJ/kmolK)CO21(110,530 kJ/kmol+65,408kJ/kmol8669kJ/kmol2000K×258.600kJ/kmolK)H20.5(0+(67881 kJ/kmol8682 kJ/kmol)2000K×268.655 kJ/kmolK)O2]=110.409 kJ/kmol

Substitute 110.409kJ/kmol for ΔG*(T), 2000 K for T, and 1.986Btu/lbmolR for Ru in Equation (IV).

lnKP=110.409kJ/kmol(1.986kJ/kmolK)×2000K=6.64

Thus, the natural logarithm equilibrium constant obtained from the equilibrium reaction at 2000K is 6.64_.

Refer Table A-28, “Natural logarithms of the equilibrium constant” obtain the equilibrium constant for the reaction by interpolating for the temperature of 2000 K as 6.635.

The value obtained for equilibrium constant at 2000K from the definition of the equilibrium constant is 6.64 which is almost equal to the value obtained for equilibrium constant as 6.635 from the Table A-28.

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Chapter 16 Solutions

Thermodynamics: An Engineering Approach

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