Redox Reactions & Electrochemistry
Apply concepts from Redox Reactions & Electrochemistry to problem-solving. Focus on numerical practice and real-world applications.
Concept Core
Electrochemistry bridges thermodynamics and redox chemistry through quantitative relationships. Oxidation is loss of electrons (increase in oxidation number); reduction is gain of electrons (decrease in oxidation number). Key oxidation number rules: free element = 0, F always = −1, O = −2 (except peroxides −1, OF₂ +2), H = +1 (except metal hydrides −1), and the sum of oxidation numbers equals the charge on the species.
Galvanic (voltaic) cells are spontaneous (ΔG < 0, E°cell > 0). The anode (oxidation) is the negative terminal, and the cathode (reduction) is the positive terminal. Electron flow: anode → external circuit → cathode. A salt bridge (KCl in agar) maintains electrical neutrality.
Electrolytic cells are non-spontaneous (require external power). Here, the anode is positive and the cathode is negative — opposite sign convention from galvanic cells.
Standard electrode potential E° is measured against the SHE (E° = 0.00 V). More positive E° = stronger oxidizing agent; more negative E° = stronger reducing agent.
Cell EMF: E°cell = E°cathode − E°anode (always cathode minus anode).
Solved Example 1: Daniell cell: Zn(s)|Zn²⁺(aq)||Cu²⁺(aq)|Cu(s). E°(Zn²⁺/Zn) = −0.76 V, E°(Cu²⁺/Cu) = +0.34 V E°cell = E°cathode − E°anode = 0.34 − (−0.76) = 1.10 V
Nernst equation: E = E° − (RT/nF) ln Q. At 25°C: E = E° − (0.0592/n) log Q. At equilibrium, E = 0, so E° = (0.0592/n) log K (derivation: setting E = 0 in the Nernst equation and Q = K at equilibrium).
Solved Example 2: EMF with [Zn²⁺] = 0.1 M and [Cu²⁺] = 0.01 M at 25°C. E = 1.10 − (0.) log(0..01) = 1.10 − 0.0296 × log(10) = 1.10 − 0.0296 = 1.0704 V
Gibbs energy and EMF: ΔG° = −nFE° (F = 96485 C/mol ≈ 96500 C/mol).
Conductance: Specific conductance κ = 1/ρ (S/cm). Molar conductivity Λm = κ × 1000/M (S·cm²/mol, M = molarity). For strong electrolytes: Λm = Λ°m − A√C (Debye-Huckel-Onsager; slight increase on dilution). For weak electrolytes: Λm increases sharply at high dilution; degree of dissociation α = Λm/Λ°m.
Kohlrausch's law: Λ°m = ν₊λ°₊ + ν₋λ°₋. Application: Λ°m(CH₃COOH) = Λ°m(CH₃COONa) + Λ°m(HCl) − Λ°m(NaCl) (adding and canceling common ions).
Faraday's laws of electrolysis: First law: w = ZIt, where Z = M/(nF) (electrochemical equivalent). Combined: w = MIt/(nF), where M = molar mass, I = current (A), t = time (s), n = electrons transferred. Dimensional analysis: (g/mol × A × s) / (mol⁻¹ × C/mol) → g/mol × C / (C/mol) = g ✓ (since A·s = C) 1 Faraday = 96485 C = charge of 1 mol electrons.
Solved Example 3: Copper deposited by 2 A for 1 hour through CuSO₄ solution. w = MIt/(nF) = (63.5 × 2 × 3600) / (2 × 96500) = = 2.37 g
Batteries: Dry cell (Leclanché, 1.5 V, non-rechargeable), lead storage battery (Pb/PbO₂, 2 V/cell, rechargeable), fuel cells (H₂-O₂, continuous feed, ~70% efficiency). Corrosion is an electrochemical process: Fe oxidizes at anodic spots, O₂ reduces at cathodic spots, forming rust (Fe₂O₃·xH₂O). Prevention: galvanization (Zn coating), cathodic protection, painting.
The key testable concept is Nernst equation calculations for non-standard conditions and Faraday's law numericals for mass deposition in electrolysis.
Key Testable Concept
The key testable concept is **Nernst equation calculations for non-standard conditions and Faraday's law numericals for mass deposition in electrolysis**.
Comparison Tables
A) Galvanic vs Electrolytic Cell
| Feature | Galvanic (Voltaic) | Electrolytic |
|---|---|---|
| Spontaneity | Spontaneous (ΔG < 0) | Non-spontaneous (ΔG > 0) |
| E°cell | Positive | Negative (requires external EMF) |
| Energy conversion | Chemical → Electrical | Electrical → Chemical |
| Anode polarity | Negative (−) | Positive (+) |
| Cathode polarity | Positive (+) | Negative (−) |
| Anode reaction | Oxidation | Oxidation |
| Cathode reaction | Reduction | Reduction |
| Salt bridge | Present | Not needed (single container) |
| Example | Daniell cell | Electrolysis of NaCl |
B) Electrochemical Series (Key Values)
| Electrode | E° (V) | Reducing/Oxidizing Power |
|---|---|---|
| Li⁺/Li | −3.04 | Strongest reducing agent |
| K⁺/K | −2.93 | Very strong reducing agent |
| Na⁺/Na | −2.71 | Strong reducing agent |
| Al³⁺/Al | −1.66 | Moderate reducing agent |
| Zn²⁺/Zn | −0.76 | Moderate reducing agent |
| Fe²⁺/Fe | −0.44 | Weak reducing agent |
| H⁺/H₂ (SHE) | 0.00 | Reference electrode |
| Cu²⁺/Cu | +0.34 | Weak oxidizing agent |
| Ag⁺/Ag | +0.80 | Moderate oxidizing agent |
| Au³⁺/Au | +1.50 | Strong oxidizing agent |
| F₂/F⁻ | +2.87 | Strongest oxidizing agent |
C) Conductance Types
| Type | Symbol | Formula | Unit | Relationship |
|---|---|---|---|---|
| Conductance | G | 1/R | S (siemens, Ω⁻¹) | Reciprocal of resistance |
| Specific conductance | κ | G × (l/A) = G × cell constant | S/cm or S/m | Conductance per unit dimensions |
| Molar conductivity | Λm | κ × 1000/M | S·cm²/mol | Conductance of all ions from 1 mol in solution |
| Equivalent conductivity | Λeq | κ × 1000/N | S·cm²/eq | Per equivalent |
| Limiting molar conductivity | Λ°m | ν₊λ°₊ + ν₋λ°₋ | S·cm²/mol | At infinite dilution (Kohlrausch) |
D) Battery Comparison
| Cell Type | Anode | Cathode | EMF | Rechargeable? |
|---|---|---|---|---|
| Dry cell (Leclanché) | Zn | MnO₂ + C (graphite rod) | 1.5 V | No |
| Lead storage | Pb (spongy) | PbO₂ | 2.0 V per cell (6 cells = 12 V) | Yes |
| H₂-O₂ Fuel cell | H₂ (Pt electrode) | O₂ (Pt electrode) | ~1.23 V | Continuous feed |
| Mercury cell | Zn-Hg amalgam | HgO | 1.35 V | No |
| Nickel-cadmium | Cd | NiO(OH) | 1.2 V | Yes |
Study Materials
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