Chemistry · Book 3 · Bachelor Year 2

University Chemistry — Year 2

University Chemistry — Year 2 · Bachelor Year 2

9Thermodynamics of Electrochemical Cells

A hydrogen fuel-cell bus carries a stack of a few hundred thin cells. In each, hydrogen and the oxygen of the air combine to water without a flame, and the energy comes out as an electric current. Two numbers govern such a stack, and both come straight from tables of Gibbs energies: no cell can give more than 1.23 V1.23\,\mathrm{V}, and no fuel cell, however perfect, turns all the energy of its hydrogen into electrical work. This chapter connects the voltage of a cell to the Gibbs energy of its reaction, derives the Nernst equation used since the Year 1 volume, and reads entropies and enthalpies of reaction off a voltmeter and a thermometer.

You already know

The Year 1 volume: cells, half-cells, anode and cathode, salt bridge, cell voltage, electrode potential, standard potential and the standard hydrogen electrode, the Nernst equation (admitted there), equilibrium constants from potentials. Chapter 2: ΔrG\Delta_r G, ΔrG∘\Delta_r G^\circ and ΔrG=ΔrG∘+RTln⁡Q\Delta_r G = \Delta_r G^\circ + RT\ln Q; the evolution criterion. Chapter 3: activities. The school volume: electrolysis.

A hydrogen fuel-cell bus at a stop: the hydrogen tanks are under the fairing on the roof, and the only exhaust is water, dripping under the bus.
A hydrogen fuel-cell bus at a stop: the hydrogen tanks are under the fairing on the roof, and the only exhaust is water, dripping under the bus.

9.1 Electrical work and the Faraday constant

Definition 9.1 (Faraday constant)

The Faraday constant is the electric charge of one mole of elementary charges, F=NAe=96 485.33 C/molF = N_A e = 96\,485.33\,\mathrm{C}/\mathrm{mol}.

Proposition 9.2 (Charge passed)

If the reaction of a cell, written with nn electrons exchanged, advances by Δξ\Delta\xi, the charge that flows through the external circuit is Q=nF ΔξQ = nF\,\Delta\xi.

Proof. An advancement Δξ\Delta\xi transfers n Δξn\,\Delta\xi moles of electrons from the anode to the cathode through the wire, each of charge ee in magnitude: Q=n Δξ NAeQ = n\,\Delta\xi\,N_A e. ∎

When a charge QQ is driven through a circuit by a voltage UU, the work received by the circuit is QUQU. Seen from the cell, which delivers that work, the electrical work it receives is δWel=−U δQ=−nFU dξ\delta W_{\text{el}} = -U\,\delta Q = -nFU\, d\xi.

A cell as a thermodynamic system at constant temperature and pressure: it exchanges heat with its surroundings and delivers electrical work through the external circuit. With the sign convention of the first law (work and heat received counted positive), W_ el = -nFU\,d.
A cell as a thermodynamic system at constant temperature and pressure: it exchanges heat with its surroundings and delivers electrical work through the external circuit. With the sign convention of the first law (work and heat received counted positive), δWel=−nFU dξ\delta W_{\text{el}} = -nFU\,d\xi.

9.2 The Gibbs energy of a cell reaction

Theorem 9.3 (Electrical work and Gibbs energy)

A cell working at constant TT and pp delivers an electrical work at most equal to the decrease of its Gibbs energy: for an advancement dξd\xi, nFU dξ≤−ΔrG dξnFU\,d\xi \leq -\Delta_r G\,d\xi. When it works reversibly (an infinitesimal current), the equality holds, and the cell voltage is the electromotive force

ΔrG=−nFE.\Delta_r G = -nFE .

Proof. First law at constant pressure, with the pressure work separated: dH=δQ+δWeldH = \delta Q + \delta W_{\text{el}}. Second law: dS≥δQ/TdS \geq \delta Q/T. At constant TT and pp, dG=dH−T dS≤δWel=−nFU dξdG = dH - T\,dS \leq \delta W_{\text{el}} = -nFU\,d\xi. With dG=ΔrG dξdG = \Delta_r G\,d\xi, ΔrG dξ≤−nFU dξ\Delta_r G\,d\xi \leq -nFU\,d\xi, that is nFU dξ≤−ΔrG dξnFU\,d\xi \leq -\Delta_r G\,d\xi. For a reversible change the inequality of the second law is an equality, and the voltage then measured, with no current, is EE: ΔrG=−nFE\Delta_r G = -nFE. ∎

A cell can thus run forward (dξ>0d\xi > 0, delivering work) only if ΔrG<0\Delta_r G < 0, that is E>0E > 0 with the poles chosen so that the reaction written runs from anode to cathode. A real cell, through which a current flows, delivers less work than −ΔrG-\Delta_r G: the difference is dissipated as heat in its resistance and at its electrodes (Chapter 10).

Example 9.4 (The Daniell cell)

For Zn+CuX2+→ZnX2++Cu\ce{Zn + Cu^2+ -> Zn^2+ + Cu}, ΔrG∘=ΔfG∘(ZnX2+)−ΔfG∘(CuX2+)=−147.06−65.49=−212.55 kJ/mol\Delta_r G^\circ = \Delta_f G^\circ(\ce{Zn^2+}) - \Delta_f G^\circ(\ce{Cu^2+}) = -147.06 - 65.49 = -212.55\,\mathrm{kJ}/\mathrm{mol}, and n=2n = 2: E∘=212 550/(2×96 485)=1.10 VE^\circ = 212\,550/(2 \times 96\,485) = 1.10\,\mathrm{V}, the voltage measured on a Daniell cell in standard conditions.

9.3 The Nernst equation and standard potentials

The Year 1 volume admitted the Nernst equation; it now follows from ΔrG=ΔrG∘+RTln⁡Q\Delta_r G = \Delta_r G^\circ + RT\ln Q.

Theorem 9.5 (The Nernst equation, derived)

For a half-reaction α Ox+n e−⇌β Red\alpha\,\mathrm{Ox} + n\,\mathrm e^- \rightleftharpoons \beta\,\mathrm{Red}, the potential of the electrode at temperature TT is

E=E∘+RTnFln⁡aOxαaRedβ,E = E^\circ + \frac{RT}{nF}\ln\frac{a_{\mathrm{Ox}}^{\alpha}}{a_{\mathrm{Red}}^{\beta}} ,

where the activities include those of every other species of the half-reaction (HX+\ce{H+}, water excepted), with their stoichiometric powers.

Proof. The potential of an electrode is the voltage of the cell made of the standard hydrogen electrode (anode) and that electrode (cathode). Its reaction is

α Ox+n2 HX2⟶β Red+n HX+,\alpha\,\mathrm{Ox} + \tfrac n2\,\ce{H2} \longrightarrow \beta\,\mathrm{Red} + n\,\ce{H+} ,

whose reaction quotient, with aHX+=1a_{\ce{H+}} = 1 and pHX2=p∘p_{\ce{H2}} = p^\circ at the standard hydrogen electrode, reduces to aRedβ/aOxαa_{\mathrm{Red}}^\beta/ a_{\mathrm{Ox}}^\alpha. From Theorem 9.3, E=−ΔrG/(nF)=−ΔrG∘/(nF)−(RT/nF)ln⁡QE = -\Delta_r G/(nF) = -\Delta_r G^\circ/(nF) - (RT/nF)\ln Q; with E∘=−ΔrG∘/(nF)E^\circ = -\Delta_r G^\circ/(nF) this is the formula. At 298.15 K298.15\,\mathrm{K}, RTln⁡10/F=0.0592 VRT\ln 10/F = 0.0592\,\mathrm{V}. ∎

Proposition 9.6 (Standard potentials from Gibbs energies)

With the conventions ΔfG∘(HX+,aq)=0\Delta_f G^\circ(\ce{H+}, \text{aq}) = 0 and ΔfG∘(HX2,g)=0\Delta_f G^\circ(\ce{H2}, \text{g}) = 0, the standard potential of a couple is E∘=−ΔrG∘/(nF)E^\circ = -\Delta_r G^\circ/(nF), where ΔrG∘\Delta_r G^\circ is the standard Gibbs energy of the half-reaction written as a reduction, the electrons counted as having zero Gibbs energy.

Proof. In the reaction against the hydrogen electrode, n2 HX2\tfrac n2\,\ce{H2} and n HX+n\,\ce{H+} contribute nothing to ΔrG∘\Delta_r G^\circ under those conventions: the standard Gibbs energy of the cell reaction is that of the half-reaction alone. ∎

Method 9.7 (A standard potential from tables)

  1. Write the half-reaction as a reduction, balanced with HX+\ce{H+} and HX2O\ce{H2O}, with nn electrons.
  2. Compute ΔrG∘=∑νiΔfGi∘\Delta_r G^\circ = \sum\nu_i\Delta_f G^\circ_i (products positive), with zero for the elements, HX+\ce{H+} and the electrons.
  3. E∘=−ΔrG∘/(nF)E^\circ = -\Delta_r G^\circ/(nF), in volts with ΔrG∘\Delta_r G^\circ in joules per mole.

Example 9.8 (The silver chloride electrode)

AgCl(s)+eX−→Ag(s)+ClX−\ce{AgCl(s) + e- -> Ag(s) + Cl^-}: ΔrG∘=−131.228−(−109.789)=−21.439 kJ/mol\Delta_r G^\circ = -131.228 - (-109.789) = -21.439\,\mathrm{kJ}/\mathrm{mol}, E∘=21 439/96 485=0.222 VE^\circ = 21\,439/96\,485 = 0.222\,\mathrm{V}. Its potential depends on the chloride activity only: in a saturated potassium chloride solution it is a stable reference electrode.

Proposition 9.9 (Combining potentials)

If a half-reaction (3), with n3n_3 electrons, is the sum of half-reactions (1) and (2), with n1n_1 and n2n_2 electrons, then

n3E3∘=n1E1∘+n2E2∘;n_3E_3^\circ = n_1E_1^\circ + n_2E_2^\circ ;

the potentials themselves do not add.

Proof. Standard Gibbs energies add, ΔrG3∘=ΔrG1∘+ΔrG2∘\Delta_r G_3^\circ = \Delta_r G_1^\circ + \Delta_r G_2^\circ, and the electron counts add, n3=n1+n2n_3 = n_1 + n_2. Divide each ΔrG∘\Delta_r G^\circ by −F-F. ∎

Example 9.10 (Iron in its two oxidation states)

FeX3++eX−→FeX2+\ce{Fe^3+ + e- -> Fe^2+} has E∘=(−78.90+4.7)/(−96.485)=0.77 VE^\circ = (-78.90 + 4.7)/(-96.485) = 0.77\,\mathrm{V} and FeX2++2 eX−→Fe\ce{Fe^2+ + 2e- -> Fe} has E∘=−78.90/(2×96.485)=−0.41 VE^\circ = -78.90/(2 \times 96.485) = -0.41\,\mathrm{V}. Hence FeX3++3 eX−→Fe\ce{Fe^3+ + 3e- -> Fe}: E∘=(0.77−0.82)/3=−0.02 VE^\circ = (0.77 - 0.82)/3 = -0.02\,\mathrm{V}, not the sum of the two.

9.4 Temperature, entropy and the efficiency of a fuel cell

Definition 9.11 (Temperature coefficient)

The temperature coefficient of a cell is the derivative (∂E/∂T)p(\partial E/\partial T)_p of its electromotive force with respect to temperature.

Proposition 9.12 (Entropy and enthalpy from cell data)

For the standard cell reaction,

ΔrS∘=nF dE∘dT,ΔrH∘=−nF(E∘−TdE∘dT),\Delta_r S^\circ = nF\,\frac{dE^\circ}{dT}, \qquad \Delta_r H^\circ = -nF\Big(E^\circ - T\frac{dE^\circ}{dT}\Big),

and a cell working reversibly at temperature TT receives from its surroundings the heat TΔrST\Delta_r S per mole of reaction.

Proof. ΔrS∘=−dΔrG∘/dT\Delta_r S^\circ = -d\Delta_r G^\circ/dT (from dG=−S dT+V dpdG = -S\,dT + V\,dp, differentiated with respect to ξ\xi) =nF dE∘/dT= nF\,dE^\circ/dT; then ΔrH∘=ΔrG∘+TΔrS∘\Delta_r H^\circ = \Delta_r G^\circ + T\Delta_r S^\circ. For the reversible change, δQ=T dS=TΔrS dξ\delta Q = T\,dS = T\Delta_r S\, d\xi. ∎

Method 9.13 (From cell data to the thermodynamics of the reaction)

  1. Measure EE at several temperatures; the slope is dE/dTdE/dT.
  2. ΔrG=−nFE\Delta_r G = -nFE, ΔrS=nF dE/dT\Delta_r S = nF\,dE/dT, ΔrH=ΔrG+TΔrS\Delta_r H = \Delta_r G + T\Delta_r S.
  3. Heat exchanged per mole when the cell works reversibly: TΔrST\Delta_r S; when it delivers a current at a voltage U<EU < E, the heat released is −ΔrH−nFU-\Delta_r H - nFU per mole.

For the hydrogen–oxygen cell producing liquid water, the CODATA key values give ΔrH∘=−285.83 kJ/mol\Delta_r H^\circ = -285.83\,\mathrm{kJ}/\mathrm{mol} and

ΔrS∘=69.95−130.68−12×205.15=−163.3 J/(K mol),\Delta_r S^\circ = 69.95 - 130.68 - \tfrac12 \times 205.15 = -163.3\,\mathrm{J}/(\mathrm{K}\,\mathrm{mol}) ,

so ΔrG∘=−237.14 kJ/mol\Delta_r G^\circ = -237.14\,\mathrm{kJ}/\mathrm{mol} and E∘=1.229 VE^\circ = 1.229\,\mathrm{V}; the temperature coefficient is ΔrS∘/(2F)=−0.85 mV/K\Delta_r S^\circ/(2F) = -0.85\,\mathrm{mV}/\mathrm{K}. A hydrogen fuel cell gives less voltage hot than cold.

The hydrogen–oxygen cell from the JANAF tables. Left: standard voltage - _r G /(2F) with liquid water (up to 500\, K, the liquid kept under its standard state) and with water vapour. Right: maximum efficiency _r G / _r H of the cell producing vapour, against the Carnot efficiency of a heat engine working between T and 298\, K; the engine wins only above about 1150\, K. The hydrogen–oxygen cell from the JANAF tables. Left: standard voltage - _r G /(2F) with liquid water (up to 500\, K, the liquid kept under its standard state) and with water vapour. Right: maximum efficiency _r G / _r H of the cell producing vapour, against the Carnot efficiency of a heat engine working between T and 298\, K; the engine wins only above about 1150\, K.
The hydrogen–oxygen cell from the JANAF tables. Left: standard voltage −ΔrG∘/(2F)-\Delta_r G^\circ/(2F) with liquid water (up to 500 K500\,\mathrm{K}, the liquid kept under its standard state) and with water vapour. Right: maximum efficiency ΔrG∘/ΔrH∘\Delta_r G^\circ/\Delta_r H^\circ of the cell producing vapour, against the Carnot efficiency of a heat engine working between TT and 298 K298\,\mathrm{K}; the engine wins only above about 1150 K1150\,\mathrm{K}.

Definition 9.14 (Thermodynamic efficiency of a fuel cell)

The thermodynamic efficiency of a fuel cell is the ratio of the electrical work it delivers to the heat its fuel would release by combustion at the same temperature, −ΔrH-\Delta_r H per mole.

Proposition 9.15 (Maximum efficiency of a fuel cell)

The thermodynamic efficiency of a fuel cell is at most ΔrG/ΔrH\Delta_r G/\Delta_r H, reached when it works reversibly, and equal to (nFU)/(−ΔrH)(nFU)/(-\Delta_r H) at a working voltage UU. Unlike a heat engine, it is not limited by the Carnot efficiency 1−T0/T1 - T_0/T.

Proof. By Theorem 9.3 the work per mole is nFU≤−ΔrGnFU \leq -\Delta_r G; divide by −ΔrH-\Delta_r H. The cell converts chemical energy directly into work at a single temperature: no heat is taken from a hot source and partly given to a cold one, so the Carnot bound, which concerns such cycles, does not apply. Its own bound is set by TΔrST\Delta_r S, the heat the reversible cell must exchange. ∎

Where the energy of one mole of hydrogen goes in a fuel cell at 298\, K (liquid water). Top: the heat a flame would release. Middle: the reversible cell, which must give up -T _r S = 48.7\, kJ as heat whatever its design. Bottom: a real cell working at 0.70\, V.
Where the energy of one mole of hydrogen goes in a fuel cell at 298 K298\,\mathrm{K} (liquid water). Top: the heat a flame would release. Middle: the reversible cell, which must give up −TΔrS∘=48.7 kJ-T\Delta_r S^\circ = 48.7\,\mathrm{kJ} as heat whatever its design. Bottom: a real cell working at 0.70 V0.70\,\mathrm{V}.

History — Faraday’s laws of electrolysis

In 1834 Michael Faraday, measuring the products of electrolyses with a voltameter of his own design, stated that the mass of a substance produced at an electrode is proportional to the quantity of electricity passed, and that for a given quantity of electricity the masses of different substances are in the ratio of their chemical equivalents. He coined the words electrode, anode, cathode, ion, anion and cation. The constant that bears his name turns those laws into Q=nF ΔξQ = nF\,\Delta\xi. (Portrait by Thomas Phillips, 1842, public domain, Wikimedia Commons.)

9.5 Concentration cells

Definition 9.16 (Concentration cell)

A concentration cell is made of two half-cells of the same couple that differ only in the concentration (or pressure) of one species.

Proposition 9.17 (Voltage of a concentration cell)

Two electrodes of a metal M dipping into solutions of MXn+\ce{M^{n+}} at concentrations c1<c2c_1 < c_2, joined by a salt bridge, give a voltage

U=RTnFln⁡c2c1,U = \frac{RT}{nF}\ln\frac{c_2}{c_1} ,

the positive pole being the more concentrated side. The cell works until the two concentrations are equal.

Proof. By the Nernst equation each electrode has Ei=E∘+(RT/nF)ln⁡ciE_i = E^\circ + (RT/nF)\ln c_i (ideal dilute solutions); E∘E^\circ cancels in the difference. The reaction is MXn+\ce{M^{n+}}(side 2) →\to MXn+\ce{M^{n+}}(side 1): metal is deposited on the concentrated side (cathode) and dissolved on the dilute side (anode), which evens the concentrations out; ΔrG=RTln⁡(c1/c2)<0\Delta_r G = RT\ln(c_1/c_2) < 0 until they are equal. ∎

A silver concentration cell at 25 C. The dilute side is the anode: silver dissolves there and is deposited on the concentrated side, until the two concentrations are equal. U = 0.0592 (0.10/0.010) = 59\, mV.
A silver concentration cell at 25∘C25{}^{\circ}\mathrm{C}. The dilute side is the anode: silver dissolves there and is deposited on the concentrated side, until the two concentrations are equal. U=0.0592log⁡(0.10/0.010)=59 mVU = 0.0592\log(0.10/0.010) = 59\,\mathrm{mV}.

The same principle measures concentrations. A glass electrode, whose thin membrane separates a reference solution from the sample, develops a membrane potential of (RT/F)ln⁡10=59 mV(RT/F)\ln 10 = 59\,\mathrm{mV} per unit of pH difference at 25∘C25{}^{\circ}\mathrm{C}: the pH meter of the Year 1 volume is a concentration cell for HX+\ce{H+}. Across the membrane of a living cell, the unequal concentrations of KX+\ce{K+} create in the same way a potential of several tens of millivolts.

9.6 Exercises

Exercise 9.1 ★

From ΔfG∘(HX2O,l)=−237.14 kJ/mol\Delta_f G^\circ(\ce{H2O}, \text{l}) = -237.14\,\mathrm{kJ}/\mathrm{mol}, compute the standard voltage of the hydrogen–oxygen cell.

Solution

Solution of Exercise 9.1.

HX2+12 OX2→HX2O(l)\ce{H2 + 1/2O2 -> H2O(l)}, n=2n = 2: E∘=237 140/(2×96 485)=1.229 VE^\circ = 237\,140/(2 \times 96\,485) = 1.229\,\mathrm{V}.

Exercise 9.2 ★

A battery is rated 1.0 A h1.0\,\mathrm{A}\,\mathrm{h}. Compute the charge it holds, in coulombs, and the mass of zinc consumed at its anode (Zn→ZnX2++2 eX−\ce{Zn -> Zn^2+ + 2e-}) when it is fully discharged.

Solution

Solution of Exercise 9.2.

Q=1.0×3600=3.6×103 CQ = 1.0 \times 3600 = 3.6 \times 10^{3}\,\mathrm{C}; n(Zn)=3600/(2×96 485)=1.87×10−2 moln(\ce{Zn}) = 3600/(2 \times 96\,485) = 1.87 \times 10^{-2}\,\mathrm{mol}, that is 1.22 g1.22\,\mathrm{g}.

Exercise 9.3 ★

A Daniell cell delivers 1.10 V1.10\,\mathrm{V} with no current. Compute ΔrG\Delta_r G for one mole of zinc and the maximum electrical work for 10.0 g10.0\,\mathrm{g} of zinc.

Solution

Solution of Exercise 9.3.

ΔrG=−2×96 485×1.10=−212 kJ/mol\Delta_r G = -2 \times 96\,485 \times 1.10 = -212\,\mathrm{kJ}/\mathrm{mol}. For 10.0 g10.0\,\mathrm{g}, 10.0/65.38=0.153 mol10.0/65.38 = 0.153\,\mathrm{mol}: at most 32.5 kJ32.5\,\mathrm{kJ}.

Exercise 9.4 ★

Two copper electrodes dip into copper(II) sulfate solutions of 1.0×10−3 mol/L1.0 \times 10^{-3}\,\mathrm{mol}/\mathrm{L} and 0.10 mol/L0.10\,\mathrm{mol}/\mathrm{L}. Compute the voltage at 25∘C25{}^{\circ}\mathrm{C} and name the poles.

Solution

Solution of Exercise 9.4.

U=(0.0592/2)log⁡(0.10/1.0×10−3)=0.059 VU = (0.0592/2)\log(0.10/1.0 \times 10^{-3}) = 0.059\,\mathrm{V}; the positive pole (cathode) is the electrode in the 0.10 mol/L0.10\,\mathrm{mol}/\mathrm{L} solution.

Exercise 9.5 ★★

A cell (n=2n = 2) has E∘=1.015 VE^\circ = 1.015\,\mathrm{V} and dE∘/dT=−4.0×10−4 V/KdE^\circ/dT = -4.0 \times 10^{-4}\,\mathrm{V}/\mathrm{K} at 298 K298\,\mathrm{K} (exercise data). Compute ΔrG∘\Delta_r G^\circ, ΔrS∘\Delta_r S^\circ and ΔrH∘\Delta_r H^\circ.

Solution

Solution of Exercise 9.5.

ΔrG∘=−2×96 485×1.015=−195.9 kJ/mol\Delta_r G^\circ = -2 \times 96\,485 \times 1.015 = -195.9\,\mathrm{kJ}/\mathrm{mol}; ΔrS∘=2×96 485×(−4.0×10−4)=−77.2 J/(K mol)\Delta_r S^\circ = 2 \times 96\,485 \times (-4.0 \times 10^{-4}) = -77.2\,\mathrm{J}/(\mathrm{K}\,\mathrm{mol}); ΔrH∘=−195.9+298×(−0.0772)=−218.9 kJ/mol\Delta_r H^\circ = -195.9 + 298 \times (-0.0772) = -218.9\,\mathrm{kJ}/\mathrm{mol}.

Exercise 9.6 ★★

The cell of Exercise 9.5 discharges one mole of reaction (a) reversibly; (b) at 0.90 V0.90\,\mathrm{V}. Compute in each case the electrical work and the heat exchanged with the surroundings.

Solution

Solution of Exercise 9.6.

(a) Work delivered 195.9 kJ195.9\,\mathrm{kJ}; heat TΔrS=−23.0 kJT\Delta_r S = -23.0\,\mathrm{kJ}: 23.0 kJ23.0\,\mathrm{kJ} released. (b) Work 2×96 485×0.90=173.7 kJ2 \times 96\,485 \times 0.90 = 173.7\,\mathrm{kJ}; heat released −ΔrH−173.7=218.9−173.7=45.2 kJ-\Delta_r H - 173.7 = 218.9 - 173.7 = 45.2\,\mathrm{kJ}. The extra 22.2 kJ22.2\,\mathrm{kJ} is the work lost to the current.

Exercise 9.7 ★★

Compute E∘(FeX3+/Fe)E^\circ(\ce{Fe^3+}/\ce{Fe}) from the Gibbs energies of formation (FeX2+\ce{Fe^2+} −78.90 kJ/mol-78.90\,\mathrm{kJ}/\mathrm{mol}, FeX3+\ce{Fe^3+} −4.7 kJ/mol-4.7\,\mathrm{kJ}/\mathrm{mol}) and check that it equals (E1∘+2E2∘)/3(E_1^\circ + 2E_2^\circ)/3.

Solution

Solution of Exercise 9.7.

FeX3++3 eX−→Fe\ce{Fe^3+ + 3e- -> Fe}: ΔrG∘=+4.7 kJ/mol\Delta_r G^\circ = +4.7\,\mathrm{kJ}/\mathrm{mol}, E∘=−4700/(3×96 485)=−0.016 VE^\circ = -4700/(3 \times 96\,485) = -0.016\,\mathrm{V}. With E1∘=0.769E_1^\circ = 0.769 and E2∘=−0.409 VE_2^\circ = -0.409\,\mathrm{V}: (0.769−0.818)/3=−0.016 V(0.769 - 0.818)/3 = -0.016\,\mathrm{V}.

Exercise 9.8 ★★

Compute the standard potential of the couple AgCl\ce{AgCl}/Ag\ce{Ag}, then the potential of a silver chloride electrode dipping into 0.10 mol/L0.10\,\mathrm{mol}/\mathrm{L} potassium chloride.

Solution

Solution of Exercise 9.8.

E∘=0.222 VE^\circ = 0.222\,\mathrm{V} (as in the chapter). E=0.222−0.0592log⁡0.10=0.281 VE = 0.222 - 0.0592\log 0.10 = 0.281\,\mathrm{V}.

Exercise 9.9 ★★

Zinc–air cells use 2 Zn+OX2→2 ZnO\ce{2Zn + O2 -> 2ZnO} (ΔfG∘(ZnO)=−318.30 kJ/mol\Delta_f G^\circ(\ce{ZnO}) = -318.30\,\mathrm{kJ}/\mathrm{mol}). Compute the standard voltage and the maximum electrical energy, in kW h\mathrm{kW}\,\mathrm{h}, per kilogram of zinc.

Solution

Solution of Exercise 9.9.

ΔrG∘=2(−318.30)=−636.6 kJ\Delta_r G^\circ = 2(-318.30) = -636.6\,\mathrm{kJ} for n=4n = 4: E∘=636 600/(4×96 485)=1.65 VE^\circ = 636\,600/(4 \times 96\,485) = 1.65\,\mathrm{V}. Per kilogram of zinc, 1000/65.38=15.3 mol1000/65.38 = 15.3\,\mathrm{mol}, 15.3×318.3=4.87 MJ15.3 \times 318.3 = 4.87\,\mathrm{MJ}, that is 1.35 kW h1.35\,\mathrm{kW}\,\mathrm{h}.

Exercise 9.10 ★★★

A direct methanol fuel cell runs CHX3OH(l)+32 OX2→COX2+2 HX2O(l)\ce{CH3OH(l) + 3/2O2 -> CO2 + 2H2O(l)}. From ΔfH∘\Delta_f H^\circ (kJ/mol\mathrm{kJ}/\mathrm{mol}): CHX3OH(l)\ce{CH3OH(l)} −239-239, COX2\ce{CO2} −393.51-393.51, HX2O(l)\ce{H2O(l)} −285.83-285.83; and S∘S^\circ (J/(K mol)\mathrm{J}/(\mathrm{K}\,\mathrm{mol})): CHX3OH(l)\ce{CH3OH(l)} 127.2, COX2\ce{CO2} 213.8, HX2O(l)\ce{H2O(l)} 69.95, OX2\ce{O2} 205.15, compute nn, E∘E^\circ and the maximum efficiency.

Solution

Solution of Exercise 9.10.

Carbon goes from −2-2 to +4+4: n=6n = 6. ΔrH∘=−393.51+2(−285.83)+239=−726.2 kJ/mol\Delta_r H^\circ = -393.51 + 2(-285.83) + 239 = -726.2\,\mathrm{kJ}/\mathrm{mol}; ΔrS∘=213.8+2(69.95)−127.2−1.5×205.15=−81.2 J/(K mol)\Delta_r S^\circ = 213.8 + 2(69.95) - 127.2 - 1.5 \times 205.15 = -81.2\,\mathrm{J}/(\mathrm{K}\,\mathrm{mol}); ΔrG∘=−726.2+298.15×0.0812=−702.0 kJ/mol\Delta_r G^\circ = -726.2 + 298.15 \times 0.0812 = -702.0\,\mathrm{kJ}/\mathrm{mol}. E∘=702 000/(6×96 485)=1.21 VE^\circ = 702\,000/(6 \times 96\,485) = 1.21\,\mathrm{V}; maximum efficiency 702.0/726.2=0.967702.0/726.2 = 0.967. (Real methanol cells work far below this voltage.)

Exercise 9.11 ★★★

A cell (n=2n = 2) has E=0.500 VE = 0.500\,\mathrm{V} and dE/dT=+3.0×10−4 V/KdE/dT = +3.0 \times 10^{-4}\,\mathrm{V}/\mathrm{K} at 298 K298\,\mathrm{K} (exercise data). Show that, working reversibly, it delivers more electrical work than −ΔrH-\Delta_r H, and explain where the extra energy comes from.

Solution

Solution of Exercise 9.11.

ΔrG=−2×96 485×0.500=−96.5 kJ\Delta_r G = -2 \times 96\,485 \times 0.500 = -96.5\,\mathrm{kJ}; ΔrS=+57.9 J/K\Delta_r S = +57.9\,\mathrm{J}/\mathrm{K}; ΔrH=−96.5+298×0.0579=−79.2 kJ\Delta_r H = -96.5 + 298 \times 0.0579 = -79.2\,\mathrm{kJ}. The work, 96.5 kJ96.5\,\mathrm{kJ}, exceeds −ΔrH=79.2 kJ-\Delta_r H = 79.2\,\mathrm{kJ}: the cell absorbs TΔrS=17.3 kJT\Delta_r S = 17.3\,\mathrm{kJ} of heat from its surroundings and turns it into work as well. The second law is not violated, since the entropy of the reaction increases by as much.

Exercise 9.12 ★★★

Two hydrogen electrodes (1 bar1\,\mathrm{bar} of HX2\ce{H2}) dip into a reference solution of pH 7.00 and into a sample. The voltage is 0.177 V0.177\,\mathrm{V} at 25∘C25{}^{\circ}\mathrm{C}, the reference being the positive pole. Find the pH of the sample, and explain why the result does not depend on any standard potential.

Solution

Solution of Exercise 9.12.

Each hydrogen electrode has E=−0.0592 pHE = -0.0592\,\mathrm{pH}: U=0.0592 (pHs−7.00)=0.177U = 0.0592\,(\mathrm{pH}_s - 7.00) = 0.177, pHs=10.0\mathrm{pH}_s = 10.0. The two electrodes are of the same couple: the standard potential cancels, as in any concentration cell.

9.7 Problem: The Fuel-Cell Bus

Problem 9.1

Weekend problem — the standard voltage of the hydrogen–oxygen cell from Gibbs energies, its temperature coefficient, the efficiency and heat of a real stack, and the energy in a tank of hydrogen

A fuel-cell stack has 400 cells in series, each with a proton-exchange membrane (acidic electrolyte). Data at 298.15 K298.15\,\mathrm{K} (CODATA, JANAF): ΔfH∘(HX2O,l)=−285.83 kJ/mol\Delta_f H^\circ(\ce{H2O}, \text{l}) = -285.83\,\mathrm{kJ}/\mathrm{mol}, ΔfG∘(HX2O,l)=−237.14 kJ/mol\Delta_f G^\circ(\ce{H2O}, \text{l}) = -237.14\,\mathrm{kJ}/\mathrm{mol}, ΔfG∘(HX2O,g)=−228.58 kJ/mol\Delta_f G^\circ(\ce{H2O}, \text{g}) = -228.58\,\mathrm{kJ}/\mathrm{mol}; S∘S^\circ (J/(K mol)\mathrm{J}/(\mathrm{K}\,\mathrm{mol})): HX2O(l)\ce{H2O(l)} 69.95, HX2\ce{H2} 130.68, OX2\ce{O2} 205.15. F=96 485 C/molF = 96\,485\,\mathrm{C}/\mathrm{mol}; M(HX2)=2.016 g/molM(\ce{H2}) = 2.016\,\mathrm{g}/\mathrm{mol}.

Part I — The standard voltage.

  1. Write the half-reactions at the anode and at the cathode, and the cell reaction.
  2. How many electrons are exchanged per molecule of hydrogen?
  3. Compute E∘E^\circ when the water is formed as a liquid.
  4. Compute it when the water leaves as vapour.
  5. Explain the difference with the Gibbs energy of vaporisation of water.
  6. Compute ΔrH∘\Delta_r H^\circ and the maximum efficiency at 298 K298\,\mathrm{K}.

Part II — Temperature.

  1. Compute ΔrS∘\Delta_r S^\circ for liquid water.
  2. Deduce dE∘/dTdE^\circ/dT.
  3. Estimate E∘E^\circ at 80∘C80{}^{\circ}\mathrm{C}, the working temperature of the stack.
  4. Compare your method with the JANAF value at 400 K400\,\mathrm{K}, ΔfG∘(HX2O,l)=−221.01 kJ/mol\Delta_f G^\circ(\ce{H2O}, \text{l}) = -221.01\,\mathrm{kJ}/\mathrm{mol}.
  5. What heat does the reversible cell exchange per mole of hydrogen at 298 K298\,\mathrm{K}? Is it received or released?
  6. Estimate the maximum efficiency at 80∘C80{}^{\circ}\mathrm{C}.

Part III — The real stack at 0.70 V0.70\,\mathrm{V} per cell.

  1. Compute the electrical work per mole of hydrogen.
  2. Compute the efficiency referred to ΔrH∘\Delta_r H^\circ and to ΔrG∘\Delta_r G^\circ.
  3. Compute the heat released per mole of hydrogen.
  4. How much of it is unavoidable, and how much is due to the current?
  5. The stack delivers 300 A300\,\mathrm{A}. Compute the hydrogen consumption of one cell, then of the stack, in moles and grams per second.
  6. Compute the electrical power of the stack.
  7. Compute the heat power the cooling circuit must remove.

Part IV — The tank.

  1. What amount of hydrogen is in 5.0 kg5.0\,\mathrm{kg}?
  2. What charge passes through the cells, counted over all of them, when this hydrogen is oxidised?
  3. Compute the electrical energy delivered by the stack, with each cell at 0.70 V0.70\,\mathrm{V}.
  4. Convert it to kilowatt-hours.
  5. For how long can the stack deliver its power of question 18?
  6. State the electrical energy delivered by 5.0 kg5.0\,\mathrm{kg} of hydrogen at 0.70 V0.70\,\mathrm{V} per cell.
Solution

Solution of Problem 9.1.

1. Anode: HX2→2 HX++2 eX−\ce{H2 -> 2H+ + 2e-}; cathode: 12 OX2+2 HX++2 eX−→HX2O\ce{1/2O2 + 2H+ + 2e- -> H2O}; cell: HX2+12 OX2→HX2O\ce{H2 + 1/2O2 -> H2O}. 2. Two. 3. E∘=237 140/(2×96 485)=1.229 VE^\circ = 237\,140/(2 \times 96\,485) = 1.229\,\mathrm{V}. 4. 228 580/192 970=1.185 V228\,580/192\,970 = 1.185\,\mathrm{V}. 5. ΔrG∘\Delta_r G^\circ differs by ΔvapG∘(HX2O)=−228.58+237.14=8.56 kJ/mol\Delta_{\text{vap}}G^\circ(\ce{H2O}) = -228.58 + 237.14 = 8.56\,\mathrm{kJ}/\mathrm{mol} at 298 K298\,\mathrm{K}: vapour is less stable than liquid there, and the voltage is lower by 8560/192 970=0.044 V8560/192\,970 = 0.044\,\mathrm{V}. 6. ΔrH∘=−285.83 kJ/mol\Delta_r H^\circ = -285.83\,\mathrm{kJ}/\mathrm{mol}; 237.14/285.83=0.830237.14/285.83 = 0.830. 7. ΔrS∘=69.95−130.68−102.58=−163.3 J/(K mol)\Delta_r S^\circ = 69.95 - 130.68 - 102.58 = -163.3\,\mathrm{J}/(\mathrm{K}\,\mathrm{mol}). 8. dE∘/dT=−163.3/192 970=−8.46×10−4 V/KdE^\circ/dT = -163.3/192\,970 = -8.46 \times 10^{-4}\,\mathrm{V}/\mathrm{K}. 9. 1.229−8.46×10−4×55=1.182 V1.229 - 8.46 \times 10^{-4} \times 55 = 1.182\,\mathrm{V}. 10. The same estimate at 400 K400\,\mathrm{K} gives 1.229−8.46×10−4×101.85=1.143 V1.229 - 8.46 \times 10^{-4} \times 101.85 = 1.143\,\mathrm{V}; JANAF gives 221 010/192 970=1.145 V221\,010/192\,970 = 1.145\,\mathrm{V}: treating ΔrS∘\Delta_r S^\circ as constant costs only 2 mV2\,\mathrm{mV}. 11. TΔrS∘=298.15×(−163.3)=−48.7 kJT\Delta_r S^\circ = 298.15 \times (-163.3) = -48.7\,\mathrm{kJ} per mole: 48.7 kJ48.7\,\mathrm{kJ} released. 12. ΔrG∘(353)≈−237.14+55×0.1633=−228.2 kJ\Delta_r G^\circ(353) \approx -237.14 + 55 \times 0.1633 = -228.2\,\mathrm{kJ}; with ΔrH∘\Delta_r H^\circ nearly unchanged, 228.2/285.8=0.80228.2/285.8 = 0.80. 13. 2×96 485×0.70=135.1 kJ2 \times 96\,485 \times 0.70 = 135.1\,\mathrm{kJ}. 14. 135.1/285.83=0.47135.1/285.83 = 0.47; 135.1/237.14=0.57135.1/237.14 = 0.57. 15. 285.83−135.1=150.7 kJ285.83 - 135.1 = 150.7\,\mathrm{kJ}. 16. 48.7 kJ48.7\,\mathrm{kJ} would be released even by a reversible cell; the other 102.0 kJ102.0\,\mathrm{kJ} come from the losses due to the current (resistance and electrode overpotentials). 17. One cell: 300/(2×96 485)=1.55×10−3 mol/s300/(2 \times 96\,485) = 1.55 \times 10^{-3}\,\mathrm{mol}/\mathrm{s}; the stack: 400×1.55×10−3=0.622 mol/s400 \times 1.55 \times 10^{-3} = 0.622\,\mathrm{mol}/\mathrm{s}, 1.25 g/s1.25\,\mathrm{g}/\mathrm{s}. 18. 400×0.70×300=84 kW400 \times 0.70 \times 300 = 84\,\mathrm{kW}. 19. 0.622×150.7=93.7 kW0.622 \times 150.7 = 93.7\,\mathrm{kW}: more heat than electricity. 20. 5000/2.016=2.48×103 mol5000/2.016 = 2.48 \times 10^{3}\,\mathrm{mol}. 21. 2×2480×96 485=4.79×108 C2 \times 2480 \times 96\,485 = 4.79 \times 10^{8}\,\mathrm{C}. 22. Each coulomb passing through a cell gives 0.70 J0.70\,\mathrm{J}: 4.79×108×0.70=3.35×108 J4.79 \times 10^8 \times 0.70 = 3.35 \times 10^{8}\,\mathrm{J}. 23. 3.35×108/3.6×106=93 kW h3.35 \times 10^8/3.6 \times 10^6 = 93\,\mathrm{kW}\,\mathrm{h}. 24. 93/84=1.1 h93/84 = 1.1\,\mathrm{h} at full power. 25. 5.0 kg5.0\,\mathrm{kg} of hydrogen at 0.70 V0.70\,\mathrm{V} per cell deliver ≈93 kW h\boldsymbol{\approx 93\,\mathrm{kW}\,\mathrm{h}} of electrical energy.

Terms defined in this chapter

See all 852 terms in the glossary