Level 4 — ApplicationRedox & Electrochemistry (Intro)

Redox & Electrochemistry (Intro)

50 marksprintable — key stays hidden on paper

Level: 4 (Application — novel problems, no hints) Time: 60 minutes Total Marks: 50

Useful data: F=96485 C mol1F = 96485\ \text{C mol}^{-1}, R=8.314 J K1mol1R = 8.314\ \text{J K}^{-1}\text{mol}^{-1}, T=298 KT = 298\ \text{K} unless stated. Use RTFln=0.0592log\dfrac{RT}{F}\ln = 0.0592\log at 298 K where convenient.

Standard reduction potentials (298 K):

Half-reaction EE^\circ / V
Ag++eAg\text{Ag}^+ + e^- \to \text{Ag} +0.80+0.80
Cu2++2eCu\text{Cu}^{2+} + 2e^- \to \text{Cu} +0.34+0.34
Fe2++2eFe\text{Fe}^{2+} + 2e^- \to \text{Fe} 0.44-0.44
Zn2++2eZn\text{Zn}^{2+} + 2e^- \to \text{Zn} 0.76-0.76
Ni2++2eNi\text{Ni}^{2+} + 2e^- \to \text{Ni} 0.25-0.25

Q1. (10 marks) A galvanic cell is built from a nickel electrode in 1.0 M Ni2+1.0\ \text{M Ni}^{2+} and a silver electrode in 1.0 M Ag+1.0\ \text{M Ag}^+.

(a) Write the two half-reactions, identify anode and cathode, and give the overall balanced cell reaction. (4) (b) Calculate EcellE^\circ_{\text{cell}}. (2) (c) Calculate ΔG\Delta G^\circ for the overall reaction (state units). (2) (d) Determine the equilibrium constant KK at 298 K. (2)


Q2. (10 marks) Consider the cell Zn(s)Zn2+(0.010 M)Cu2+(0.50 M)Cu(s)\text{Zn}(s)\,|\,\text{Zn}^{2+}(0.010\ \text{M})\,||\,\text{Cu}^{2+}(0.50\ \text{M})\,|\,\text{Cu}(s)

(a) Calculate EcellE^\circ_{\text{cell}}. (2) (b) Using the Nernst equation, calculate the actual cell EMF under these concentrations. (4) (c) The cell is discharged until it reaches equilibrium. State the value of EcellE_{\text{cell}} at that point and explain what "equilibrium" means for a battery in one sentence. (2) (d) Predict qualitatively how EcellE_{\text{cell}} would change if [Cu2+][\text{Cu}^{2+}] were reduced to 0.010 M0.010\ \text{M}. Justify without full calculation. (2)


Q3. (10 marks) A concentration cell is set up using two copper electrodes: Cu(s)Cu2+(x M)Cu2+(0.100 M)Cu(s)\text{Cu}(s)\,|\,\text{Cu}^{2+}(x\ \text{M})\,||\,\text{Cu}^{2+}(0.100\ \text{M})\,|\,\text{Cu}(s)

(a) Explain why Ecell=0E^\circ_{\text{cell}} = 0 for a concentration cell. (2) (b) The measured EMF is 0.0296 V0.0296\ \text{V} at 298 K. Determine xx, the unknown concentration, and state which half-cell is the anode. (6) (c) State one practical application of concentration-cell behaviour. (2)


Q4. (12 marks) An electrolysis plant purifies copper and, in a separate cell, produces aluminium.

(a) In an electrorefining cell, a current of 5.0 A5.0\ \text{A} passes for 2.0 hours2.0\ \text{hours} through CuSO4\text{CuSO}_4 solution. Calculate the mass of copper deposited at the cathode. (Cu: 63.5 g mol163.5\ \text{g mol}^{-1}) (4) (b) The same charge is passed through molten Al2O3\text{Al}_2\text{O}_3 (Hall–Héroult, Al: 27.0 g mol127.0\ \text{g mol}^{-1}). Calculate the mass of aluminium deposited. (3) (c) Explain, using Faraday's laws, why equal charge deposits different masses but chemically equivalent amounts of the two metals. (2) (d) In the Hall–Héroult process the carbon anodes are continuously consumed. Write the anode reaction that explains this and state why aluminium is not obtained from aqueous solution. (3)


Q5. (8 marks) Iron structures corrode electrochemically.

(a) Write the anode and cathode half-reactions for the rusting of iron in the presence of water and oxygen, and identify which region acts as anode. (3) (b) Zinc (E=0.76 VE^\circ = -0.76\ \text{V}) is coated onto iron (E=0.44 VE^\circ = -0.44\ \text{V}) as "galvanization." Using electrode potentials, explain why zinc protects iron even if the coating is scratched. (3) (c) Name and briefly describe one other method of cathodic protection for a buried steel pipeline. (2)

Answer keyMark scheme & solutions

Q1 (10)

(a) Ni has lower (more negative) EE^\circ → oxidised (anode); Ag reduced (cathode).

  • Anode: NiNi2++2e\text{Ni} \to \text{Ni}^{2+} + 2e^- (1)
  • Cathode: Ag++eAg\text{Ag}^+ + e^- \to \text{Ag} (1)
  • Balance electrons (×2 on Ag): overall Ni+2Ag+Ni2++2Ag\text{Ni} + 2\text{Ag}^+ \to \text{Ni}^{2+} + 2\text{Ag} (1) correct balancing; (1) correct anode/cathode ID.

(b) Ecell=EcathodeEanode=0.80(0.25)=+1.05 VE^\circ_{\text{cell}} = E^\circ_{\text{cathode}} - E^\circ_{\text{anode}} = 0.80 - (-0.25) = +1.05\ \text{V}. (2)

(c) n=2n = 2. ΔG=nFE=(2)(96485)(1.05)=2.026×105 J=202.6 kJ\Delta G^\circ = -nFE^\circ = -(2)(96485)(1.05) = -2.026\times10^5\ \text{J} = -202.6\ \text{kJ}. (2) (–ve → spontaneous.)

(d) lnK=nFERT=2×96485×1.058.314×298=81.79\ln K = \dfrac{nFE^\circ}{RT} = \dfrac{2\times96485\times1.05}{8.314\times298} = 81.79 K=e81.792.5×1035K = e^{81.79} \approx 2.5\times10^{35}. (2) (very large → reaction essentially complete.)

Q2 (10)

(a) Ecell=0.34(0.76)=+1.10 VE^\circ_{\text{cell}} = 0.34 - (-0.76) = +1.10\ \text{V}. (2)

(b) Reaction: Zn+Cu2+Zn2++Cu\text{Zn} + \text{Cu}^{2+} \to \text{Zn}^{2+} + \text{Cu}, n=2n=2. Q=[Zn2+][Cu2+]=0.0100.50=0.020Q = \dfrac{[\text{Zn}^{2+}]}{[\text{Cu}^{2+}]} = \dfrac{0.010}{0.50} = 0.020. (1) E=E0.05922logQ=1.100.0296log(0.020)E = E^\circ - \dfrac{0.0592}{2}\log Q = 1.10 - 0.0296\log(0.020) (2) log(0.020)=1.699\log(0.020) = -1.699; E=1.100.0296(1.699)=1.10+0.0503=1.150 VE = 1.10 - 0.0296(-1.699) = 1.10 + 0.0503 = 1.150\ \text{V}. (1)

(c) At equilibrium Ecell=0E_{\text{cell}} = 0. (1) Equilibrium = the cell is "dead"; forward and reverse rates equal, Q=KQ=K, no net current/no more usable work. (1)

(d) Lowering [Cu2+][\text{Cu}^{2+}] raises QQ, so 0.05922logQ-\frac{0.0592}{2}\log Q becomes more negative → EcellE_{\text{cell}} decreases. (2)

Q3 (10)

(a) Both electrodes are the same metal/couple, so Ecathode=EanodeE^\circ_{\text{cathode}} = E^\circ_{\text{anode}}; their difference is 00. EMF arises solely from concentration difference. (2)

(b) E=0.05922log[dilute][conc]E = -\dfrac{0.0592}{2}\log\dfrac{[\text{dilute}]}{[\text{conc}]} where the dilute side is the anode. Cell drives ions from low→high implicitly; use E=0.05922log[Cu2+]cathode[Cu2+]anodeE = \dfrac{0.0592}{2}\log\dfrac{[\text{Cu}^{2+}]_{\text{cathode}}}{[\text{Cu}^{2+}]_{\text{anode}}}. (1) 0.0296=0.05922log0.100x0.0296 = \dfrac{0.0592}{2}\log\dfrac{0.100}{x} (1) 0.0296=0.0296log0.100xlog0.100x=10.0296 = 0.0296\log\dfrac{0.100}{x} \Rightarrow \log\dfrac{0.100}{x} = 1 (2) 0.100x=10x=0.010 M\dfrac{0.100}{x} = 10 \Rightarrow x = 0.010\ \text{M}. (1) The dilute half-cell (x=0.010 Mx = 0.010\ \text{M}) is the anode (oxidation raises its ion concentration). (1)

(c) e.g. ion-selective electrodes / pH meters use concentration-cell EMF to measure unknown ion concentrations. (2)

Q4 (12)

(a) Q=It=5.0×(2.0×3600)=36000 CQ = It = 5.0 \times (2.0\times3600) = 36000\ \text{C}. (1) Cu2++2eCu\text{Cu}^{2+} + 2e^- \to \text{Cu}, so n=2n=2. m=QMnF=36000×63.52×96485=11.85 gm = \dfrac{Q\,M}{nF} = \dfrac{36000\times63.5}{2\times96485} = 11.85\ \text{g}. (3)

(b) Al3++3eAl\text{Al}^{3+} + 3e^- \to \text{Al}, n=3n=3. m=36000×27.03×96485=3.36 gm = \dfrac{36000\times27.0}{3\times96485} = 3.36\ \text{g}. (3)

(c) By Faraday's laws mass \propto equivalent weight M/nM/n. Same charge → same number of moles of electrons → chemically equivalent (mole-electrons) amounts, but different nn and MM give different masses. (2)

(d) Anode reaction: C+O2CO2/CO+electrons\text{C} + \text{O}^{2-} \to \text{CO}_2/\text{CO} + \text{electrons}, e.g. C+2O2CO2+4e\text{C} + 2\text{O}^{2-} \to \text{CO}_2 + 4e^- — oxygen released oxidises the carbon anode, consuming it. (2) Al cannot come from aqueous solution because water/H+\text{H}^+ is reduced in preference to Al3+\text{Al}^{3+} (Al is far more negative than the H reduction), so hydrogen forms instead of aluminium. (1)

Q5 (8)

(a) Anode (oxidation): FeFe2++2e\text{Fe} \to \text{Fe}^{2+} + 2e^- (1) Cathode (reduction): O2+2H2O+4e4OH\text{O}_2 + 2\text{H}_2\text{O} + 4e^- \to 4\text{OH}^- (1) The region of the iron that is oxidised (often less oxygenated area) is the anode. (1)

(b) Zn has more negative EE^\circ (−0.76 V) than Fe (−0.44 V), so Zn is oxidised preferentially — it is the sacrificial anode and Fe becomes the cathode (protected). This holds even if scratched, so the whole surface is protected, not just coverage. (3)

(c) Sacrificial anode / impressed-current cathodic protection: connect a more reactive metal (Mg, Zn) to the pipe so it corrodes instead; or apply an external DC to force the pipe to be cathode. (2)

[
 {"claim":"Q1b E_cell = 1.05 V","code":"E=0.80-(-0.25); result = abs(E-1.05)<1e-9"},
 {"claim":"Q1c dG = -202.6 kJ","code":"dG=-2*96485*1.05/1000; result = abs(dG-(-202.6))<0.5"},
 {"claim":"Q1d ln K approx 81.79","code":"lnK=2*96485*1.05/(8.314*298); result = abs(lnK-81.79)<0.1"},
 {"claim":"Q2b E = 1.150 V","code":"E=1.10-(0.0592/2)*log(0.010/0.50,10); result = abs(E-1.150)<0.005"},
 {"claim":"Q3b x = 0.010 M","code":"from sympy import symbols,solve,log,Eq;x=symbols('x',positive=True);sol=solve(Eq(0.0296,(0.0592/2)*log(0.100/x,10)),x);result = abs(float(sol[0])-0.010)<1e-4"},
 {"claim":"Q4a Cu mass 11.85 g","code":"m=36000*63.5/(2*96485); result = abs(m-11.85)<0.05"},
 {"claim":"Q4b Al mass 3.36 g","code":"m=36000*27.0/(3*96485); result = abs(m-3.36)<0.05"}
]