Two different equations showing the change in Gibbs free energy are given. The derivation of E ° as a function of temperature for the given equations, the graphical determination of Δ H ° and Δ S ° from measurements of E ° at different temperature and the property used for designing a reference half-cell that would produce a potential relatively stable with respect to temperature is to be stated. Concept introduction: Gibbs free energy is basically the maximum amount of non-expansion work done. Therefore, it is represented as, W max = Δ G ° The relationship between Gibbs free energy change and cell potential is given by the formula, Δ G ° = − n F E ° cell The relation between Δ G ° , Δ H ° and Δ S ° is given as, Δ G ° = Δ H ° − T Δ S ° To determine: The derivation of E ° as a function of temperature for the given equations, the graphical determination of Δ H ° and Δ S ° from measurements of E ° at different temperatures and the property used for designing a reference half-cell that would produce a potential relatively stable with respect to temperature. The relation obtained from the given equations is, E ° cell = T ( Δ S ° n F ) + ( − Δ H ° n F )
Two different equations showing the change in Gibbs free energy are given. The derivation of E ° as a function of temperature for the given equations, the graphical determination of Δ H ° and Δ S ° from measurements of E ° at different temperature and the property used for designing a reference half-cell that would produce a potential relatively stable with respect to temperature is to be stated. Concept introduction: Gibbs free energy is basically the maximum amount of non-expansion work done. Therefore, it is represented as, W max = Δ G ° The relationship between Gibbs free energy change and cell potential is given by the formula, Δ G ° = − n F E ° cell The relation between Δ G ° , Δ H ° and Δ S ° is given as, Δ G ° = Δ H ° − T Δ S ° To determine: The derivation of E ° as a function of temperature for the given equations, the graphical determination of Δ H ° and Δ S ° from measurements of E ° at different temperatures and the property used for designing a reference half-cell that would produce a potential relatively stable with respect to temperature. The relation obtained from the given equations is, E ° cell = T ( Δ S ° n F ) + ( − Δ H ° n F )
Solution Summary: The author explains that Gibbs free energy is basically the maximum amount of non-expansion work done.
Two different equations showing the change in Gibbs free energy are given. The derivation of
E° as a function of temperature for the given equations, the graphical determination of
ΔH° and
ΔS° from measurements of
E° at different temperature and the property used for designing a reference half-cell that would produce a potential relatively stable with respect to temperature is to be stated.
Concept introduction:
Gibbs free energy is basically the maximum amount of non-expansion work done. Therefore, it is represented as,
Wmax=ΔG°
The relationship between Gibbs free energy change and cell potential is given by the formula,
ΔG°=−nFE°cell
The relation between
ΔG°,
ΔH° and
ΔS° is given as,
ΔG°=ΔH°−TΔS°
To determine: The derivation of
E° as a function of temperature for the given equations, the graphical determination of
ΔH° and
ΔS° from measurements of
E° at different temperatures and the property used for designing a reference half-cell that would produce a potential relatively stable with respect to temperature.
The relation obtained from the given equations is,
(c) The following data have been obtained for the hydrolysis of sucrose, C12H22O11, to
glucose, C6H12O6, and fructose C6H12O6, in acidic solution:
C12H22O11 + H2O → C6H12O6 + C6H12O6
[sucrose]/mol dm³
t/min
0
0.316
14
0.300
39
0.274
60
0.256
80
0.238
110
0.211
(i) Graphically prove the order of the reaction and determine the rate constant of the
reaction.
(ii) Determine the half-life, t½ for the hydrolysis of sucrose.
(III) adsorbent
(b) Adsorption of the hexacyanoferrate (III) ion, [Fe(CN)6] ³, on y-Al2O3 from aqueous
solution was examined. The adsorption was modelled using a modified Langmuir
isotherm, yielding the following values of Kat pH = 6.5:
(ii)
T/K
10-10 K
280
2.505
295
1.819
310
1.364
325
1.050
Determine the enthalpy of adsorption, AadsHⓇ.
If the reported value of entropy of adsorption, Aads Se = 146 J K-1 mol-1 under the above
conditions, determine Aads Gº.
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