Level 3 — ProductionRedox & Electrochemistry (Intro)

Redox & Electrochemistry (Intro)

45 minutes60 marksprintable — key stays hidden on paper

Level: 3 (Production — derivations, reasoning from memory, explain-out-loud) Time limit: 45 minutes Total marks: 60

Use F=96485 C mol1F = 96485\ \text{C mol}^{-1}, R=8.314 J mol1K1R = 8.314\ \text{J mol}^{-1}\text{K}^{-1}, T=298 KT = 298\ \text{K} unless told otherwise. Show all reasoning.


Question 1 — Derive the Nernst equation from first principles (10 marks)

Starting from memory with the thermodynamic relation ΔG=ΔG+RTlnQ\Delta G = \Delta G^\circ + RT\ln Q and the electrochemical link between free energy and cell potential:

(a) State the two founding equations and explain physically why the sign is negative in ΔG=nFE\Delta G = -nFE. (3)

(b) Derive the Nernst equation E=ERTnFlnQE = E^\circ - \dfrac{RT}{nF}\ln Q. (4)

(c) Convert it to the base-10 form valid at 298 K and show the numerical prefactor equals 0.0592/n0.0592/n V. (3)


Question 2 — Build a galvanic cell and compute its EMF (12 marks)

You are given the half-cells: Zn2++2eZn,E=0.76 V\text{Zn}^{2+} + 2e^- \rightarrow \text{Zn}, \quad E^\circ = -0.76\ \text{V} Ag++eAg,E=+0.80 V\text{Ag}^+ + e^- \rightarrow \text{Ag}, \quad E^\circ = +0.80\ \text{V}

(a) Identify anode and cathode and justify using the electrochemical series. (2)

(b) Write the balanced cell reaction and the standard cell notation (line diagram). (3)

(c) Compute EcellE^\circ_{\text{cell}}. (2)

(d) Compute EcellE_{\text{cell}} when [Zn2+]=0.10 M[\text{Zn}^{2+}] = 0.10\ \text{M} and [Ag+]=0.010 M[\text{Ag}^+] = 0.010\ \text{M}. (3)

(e) Compute ΔG\Delta G^\circ for the cell reaction (kJ). (2)


Question 3 — Equilibrium constant from EE^\circ (8 marks)

For the reaction in Question 2:

(a) Derive the relation lnK=nFERT\ln K = \dfrac{nFE^\circ}{RT} from the two founding equations. (3)

(b) Compute KK for the Zn/Ag cell (state nn used). (3)

(c) Interpret: is the reaction essentially complete? Explain in one sentence. (2)


Question 4 — Concentration cell (10 marks)

A concentration cell is built from two copper electrodes in Cu2+\text{Cu}^{2+} solutions of 0.001 M0.001\ \text{M} and 1.0 M1.0\ \text{M}.

(a) Explain out loud (in words) why this cell produces a voltage despite identical electrodes; identify which electrode is the cathode. (3)

(b) Write the Nernst expression for EcellE_{\text{cell}} and derive the simplified form for a concentration cell (where Ecell=0E^\circ_{\text{cell}} = 0). (3)

(c) Compute EcellE_{\text{cell}}. (4)


Question 5 — Faraday's laws & industrial electrolysis (12 marks)

(a) State Faraday's first law and derive m=MItnFm = \dfrac{MIt}{nF} from the definition of moles of electrons. (3)

(b) Molten Al2O3\text{Al}_2\text{O}_3 is electrolysed at 40,000 A40{,}000\ \text{A}. Calculate the mass of aluminium deposited in 1.0 hour. Take M(Al)=27 g mol1M(\text{Al}) = 27\ \text{g mol}^{-1}. (4)

(c) For the electrolysis of brine (aqueous NaCl), write the electrode reactions and name the three commercial products. (3)

(d) Explain why aqueous Na+\text{Na}^+ is not reduced at the cathode in brine electrolysis, referencing electrode potentials. (2)


Question 6 — Corrosion, protection & fuel cells (8 marks)

(a) Describe the electrochemical mechanism of iron rusting: identify anodic and cathodic regions and write both half-reactions. (3)

(b) Explain why galvanization (zinc coating) protects iron even if the coating is scratched — refer to the electrochemical series. (2)

(c) For a H₂/O₂ fuel cell (alkaline), write both electrode reactions and give one reason it is preferred on spacecraft over a battery. (3)

Answer keyMark scheme & solutions

Question 1 (10)

(a) Founding equations: ΔG=nFE\Delta G = -nFE and ΔG=ΔG+RTlnQ\Delta G = \Delta G^\circ + RT\ln Q. (1 each) Sign is negative because a spontaneous cell (E>0E>0) does electrical work on the surroundings, releasing free energy (ΔG<0\Delta G<0); nFnF is positive charge transferred so nFE-nFE enforces ΔG<0\Delta G<0 when E>0E>0. (1)

(b) Substitute both: nFE=nFE+RTlnQ-nFE = -nFE^\circ + RT\ln Q. (2) Divide by nF-nF: E=ERTnFlnQE = E^\circ - \frac{RT}{nF}\ln Q (2)

(c) Convert: lnQ=2.303log10Q\ln Q = 2.303\log_{10}Q, so prefactor =2.303RTnF=\dfrac{2.303RT}{nF}. (1) Numerically: 2.303×8.314×29896485=0.05916 V\dfrac{2.303\times 8.314\times 298}{96485} = 0.05916\ \text{V}. (2) E=E0.0592nlog10QE = E^\circ - \frac{0.0592}{n}\log_{10}Q


Question 2 (12)

(a) Zn has more negative EE^\circ → more readily oxidised → anode. Ag → cathode. (2)

(b) Reaction: Zn+2Ag+Zn2++2Ag\text{Zn} + 2\text{Ag}^+ \rightarrow \text{Zn}^{2+} + 2\text{Ag} (2) (balance electrons: Zn gives 2e⁻, need 2 Ag⁺). Cell: ZnZn2+Ag+Ag\text{Zn}\,|\,\text{Zn}^{2+}\,\|\,\text{Ag}^+\,|\,\text{Ag} (1)

(c) Ecell=EcatEan=0.80(0.76)=1.56 VE^\circ_{\text{cell}} = E^\circ_{\text{cat}} - E^\circ_{\text{an}} = 0.80 - (-0.76) = 1.56\ \text{V} (2)

(d) n=2n=2, Q=[Zn2+][Ag+]2=0.10(0.010)2=1000Q = \dfrac{[\text{Zn}^{2+}]}{[\text{Ag}^+]^2} = \dfrac{0.10}{(0.010)^2} = 1000. (1) E=1.560.05922log10(1000)=1.560.0296×3=1.560.0888=1.471 VE = 1.56 - \dfrac{0.0592}{2}\log_{10}(1000) = 1.56 - 0.0296\times 3 = 1.56 - 0.0888 = 1.471\ \text{V} (2)

(e) ΔG=nFE=2×96485×1.56=301,033 J301 kJ\Delta G^\circ = -nFE^\circ = -2\times 96485\times 1.56 = -301{,}033\ \text{J} \approx -301\ \text{kJ} (2)


Question 3 (8)

(a) At equilibrium ΔG=0\Delta G=0, E=0E=0, Q=KQ=K. From ΔG=nFE\Delta G^\circ = -nFE^\circ and ΔG=RTlnK\Delta G^\circ = -RT\ln K: (2) RTlnK=nFElnK=nFERT-RT\ln K = -nFE^\circ \Rightarrow \ln K = \frac{nFE^\circ}{RT} (1)

(b) n=2n=2: lnK=2×96485×1.568.314×298=301,0332477.6=121.5\ln K = \dfrac{2\times 96485\times 1.56}{8.314\times 298} = \dfrac{301{,}033}{2477.6} = 121.5. (2) K=e121.55×1052K = e^{121.5} \approx 5\times 10^{52}. (1)

(c) KK is astronomically large → reaction goes essentially to completion. (2)


Question 4 (10)

(a) Both electrodes/reactions identical, but potential depends on ion concentration (Nernst). The dilute side has a lower Cu²⁺ potential and undergoes oxidation (anode); the concentrated side is reduced (cathode = 1.0 M side). The system drives toward equalising concentrations. (3)

(b) E=E0.0592nlog[Cu2+]anode/dilute[Cu2+]cathode/concE = E^\circ - \dfrac{0.0592}{n}\log\dfrac{[\text{Cu}^{2+}]_{\text{anode/dilute}}}{[\text{Cu}^{2+}]_{\text{cathode/conc}}}; with E=0E^\circ=0: E=0.05922log[dilute][conc]=0.05922log[conc][dilute]E = -\frac{0.0592}{2}\log\frac{[\text{dilute}]}{[\text{conc}]} = \frac{0.0592}{2}\log\frac{[\text{conc}]}{[\text{dilute}]} (3)

(c) n=2n=2: E=0.05922log1.00.001=0.0296×3=0.0888 VE = \dfrac{0.0592}{2}\log\dfrac{1.0}{0.001} = 0.0296\times 3 = 0.0888\ \text{V} (4)


Question 5 (12)

(a) First law: mass deposited ∝ charge passed. Moles of electrons =ItF= \dfrac{It}{F}; moles of metal =ItnF= \dfrac{It}{nF}; mass =MItnF= \dfrac{MIt}{nF}. (3)

(b) Al3++3eAl\text{Al}^{3+}+3e^-\rightarrow\text{Al}, n=3n=3. Q=It=40000×3600=1.44×108 CQ = It = 40000\times 3600 = 1.44\times 10^8\ \text{C}. (1) m=27×1.44×1083×96485=3.888×109289455=13,432 g13.4 kgm = \dfrac{27\times 1.44\times 10^8}{3\times 96485} = \dfrac{3.888\times 10^9}{289455} = 13{,}432\ \text{g} \approx 13.4\ \text{kg} (3)

(c) Cathode: 2H2O+2eH2+2OH2\text{H}_2\text{O}+2e^-\rightarrow \text{H}_2 + 2\text{OH}^-; Anode: 2ClCl2+2e2\text{Cl}^-\rightarrow \text{Cl}_2 + 2e^-. (2) Products: H₂, Cl₂, NaOH. (1)

(d) E(Na+/Na)=2.71 VE^\circ(\text{Na}^+/\text{Na}) = -2.71\ \text{V} is far more negative than water reduction (~0.83-0.83 V at pH 7); water is preferentially reduced, so H₂ evolves not Na. (2)


Question 6 (8)

(a) Anodic region: FeFe2++2e\text{Fe}\rightarrow \text{Fe}^{2+}+2e^-. Cathodic region (in presence of O₂/water): O2+2H2O+4e4OH\text{O}_2 + 2\text{H}_2\text{O}+4e^-\rightarrow 4\text{OH}^-. Fe²⁺ further oxidised → hydrated Fe₂O₃ (rust). (3)

(b) Zn is more electronegative (more negative E=0.76E^\circ = -0.76 V vs Fe 0.44-0.44 V), so Zn acts as sacrificial anode and is oxidised preferentially, protecting iron even when scratched (cathodic protection). (2)

(c) Anode: H2+2OH2H2O+2e\text{H}_2 + 2\text{OH}^-\rightarrow 2\text{H}_2\text{O}+2e^-; Cathode: O2+2H2O+4e4OH\text{O}_2 + 2\text{H}_2\text{O}+4e^-\rightarrow 4\text{OH}^-. (2) Preferred on spacecraft: continuous power as long as fuel supplied (no recharge needed), and by-product water is drinkable. (1)


[
  {"claim":"Q2c E_cell standard = 1.56 V","code":"Ec=0.80-(-0.76); result=abs(Ec-1.56)<1e-9"},
  {"claim":"Q2d E_cell at given conc = 1.471 V","code":"import math; E=1.56-(0.0592/2)*math.log10(0.10/(0.010**2)); result=abs(E-1.471)<1e-3"},
  {"claim":"Q2e dG standard approx -301 kJ","code":"dG=-2*96485*1.56; result=abs(dG/1000+301)<1"},
  {"claim":"Q3b lnK approx 121.5","code":"import math; lnK=2*96485*1.56/(8.314*298); result=abs(lnK-121.5)<0.5"},
  {"claim":"Q4c concentration cell E = 0.0888 V","code":"import math; E=(0.0592/2)*math.log10(1.0/0.001); result=abs(E-0.0888)<1e-3"},
  {"claim":"Q5b Al mass approx 13.4 kg","code":"m=27*40000*3600/(3*96485); result=abs(m/1000-13.4)<0.1"}
]