CHEMISTRY |
Class XII
Chapter 3
ELECTROCHEMISTRY
Electrochemical Cells ◆
Nernst Equation ◆ Conductance
◆ Electrolysis ◆
Faraday's Laws
1. Introduction to
Electrochemistry
Electrochemistry is the branch of chemistry that deals with the
relationship between electrical energy and chemical reactions. It encompasses
two fundamental processes: (1) spontaneous chemical reactions that generate
electrical energy (as in batteries and fuel cells), and (2) the use of
electrical energy to drive non-spontaneous chemical reactions (as in
electroplating and extraction of metals).
Electrochemistry plays a pivotal role in modern civilisation — from the
lithium-ion battery in your smartphone to the electrolytic refining of copper,
from the corrosion of iron bridges to the electroplating of jewellery, and from
hydrogen fuel cells to chlor-alkali industry. Understanding electrochemistry
requires a grasp of thermodynamics, equilibrium, kinetics, and the physics of
electric current.
Redox Reaction: All electrochemical processes are based on
oxidation-reduction (redox) reactions. In a redox reaction, one species loses
electrons (oxidation) and another gains electrons (reduction). The species that
loses electrons is the reducing agent; the species that gains electrons is the
oxidising agent.
2. Electrochemical Cells (Galvanic / Voltaic Cells)
An electrochemical cell (galvanic cell or voltaic cell) converts chemical
energy from a spontaneous redox reaction into electrical energy. It consists of
two half-cells — each containing an electrode dipped into its electrolyte
solution. The two half-cells are connected by (a) an external metallic wire
through which electrons flow, and (b) a salt bridge through which ions flow to
maintain electrical neutrality.
2.1 The Daniell Cell — A Classic Example
The Daniell cell (1836) is the most studied galvanic cell. It consists of
a zinc electrode dipped in zinc sulphate (ZnSO₄) solution (the anode half-cell)
and a copper electrode dipped in copper sulphate (CuSO₄) solution (the cathode
half-cell), connected by a salt bridge containing KCl or KNO₃.
Figure 1: Daniell Cell — Zinc (anode) is
oxidised, releasing electrons that flow through the external circuit to the
copper cathode where Cu²⁺ ions are reduced. EMF = 1.10 V.
|
Key Events in the Daniell Cell |
|
ANODE (−): Zn(s) → Zn²⁺(aq) +
2e⁻ [Oxidation — zinc dissolves] CATHODE (+): Cu²⁺(aq) + 2e⁻ →
Cu(s) [Reduction — copper deposits] NET REACTION: Zn(s) + Cu²⁺(aq)
→ Zn²⁺(aq) + Cu(s) [Spontaneous; ΔG
< 0] ELECTRONS flow through
external wire from Zn (anode) to Cu (cathode). CATIONS in salt bridge flow
from KCl solution toward the CuSO4 half-cell. ANIONS in salt bridge flow
from KCl solution toward the ZnSO4 half-cell. EMF of Daniell cell under
standard conditions = +1.10 V |
2.2 Cell Notation (Cell Representation)
An electrochemical cell is represented by a standardised notation (cell
diagram). By convention: the anode (oxidation half-cell) is written on the
left, the cathode (reduction half-cell) on the right. A single vertical line (
| ) represents a phase boundary (solid/liquid interface). A double vertical
line ( || ) represents the salt bridge.
|
Cell Notation for Daniell Cell |
Zn(s) |
Zn²⁺(aq) || Cu²⁺(aq) | Cu(s) |
Reading left to right: zinc solid in contact with zinc ion solution |
salt bridge | copper ion solution in contact with copper solid. The EMF is
always calculated as E(cathode) − E(anode).
2.3 Standard Electrode Potential (E°)
The electrode potential is the tendency of an electrode to gain or lose
electrons relative to a reference electrode. The Standard Hydrogen Electrode
(SHE) is universally chosen as the reference and is assigned a standard
electrode potential of exactly 0.00 V. The standard electrode potential of any
other electrode is measured relative to SHE under standard conditions (1 M
concentration, 1 atm gas pressure, 25°C = 298 K).
Standard Reduction Potential (E°red): The electrode potential
measured when the electrode reaction is written as a reduction (gain of
electrons). A positive E°red means the electrode is a better oxidising agent
than SHE; a negative E°red means it is a better reducing agent.
|
Standard Cell EMF |
E°cell =
E°cathode − E°anode
= E°reduction(cathode) −
E°reduction(anode) |
|
Spontaneity Criterion |
E°cell >
0 →
Spontaneous (ΔG < 0);
E°cell < 0 → Non-spontaneous (ΔG > 0) |
|
Relation with Gibbs Energy |
DeltaG° =
−nFE°cell [n = moles of
electrons; F = 96500 C/mol] |
|
Relation with Equilibrium Constant |
DeltaG° =
−RT ln Keq → E°cell
= (RT/nF) ln Keq =
(0.0592/n) log Keq [at 298 K] |
Figure 6: Standard Reduction Potential
(SRP) Series — Electrodes with more negative E° are stronger reducing agents;
more positive E° are stronger oxidising agents. E°cell = E°cathode − E°anode.
|
Electrode
Reaction |
E° (V) |
Nature |
|
Li⁺(aq) + e⁻ → Li(s) |
−3.05 |
Strongest reducing agent
(most active metal) |
|
K⁺(aq) + e⁻ → K(s) |
−2.93 |
Very strong reducing agent |
|
Na⁺(aq) + e⁻ → Na(s) |
−2.71 |
Very strong reducing agent |
|
Mg²⁺(aq) + 2e⁻ → Mg(s) |
−2.37 |
Strong reducing agent |
|
Al³⁺(aq) + 3e⁻ → Al(s) |
−1.66 |
Strong reducing agent |
|
Zn²⁺(aq) + 2e⁻ → Zn(s) |
−0.76 |
Moderate reducing agent |
|
Fe²⁺(aq) + 2e⁻ → Fe(s) |
−0.44 |
Moderate reducing agent |
|
2H⁺(aq) + 2e⁻ → H₂(g) |
0.00 |
Standard reference (SHE) |
|
Cu²⁺(aq) + 2e⁻ → Cu(s) |
+0.34 |
Moderate oxidising agent |
|
Ag⁺(aq) + e⁻ → Ag(s) |
+0.80 |
Strong oxidising agent
(noble metal) |
|
Cl₂(g) + 2e⁻ → 2Cl⁻(aq) |
+1.36 |
Very strong oxidising agent |
|
F₂(g) + 2e⁻ → 2F⁻(aq) |
+2.87 |
Strongest oxidising agent |
3. Nernst Equation
The standard electrode potential (E°) is measured at standard conditions
(1 M, 298 K, 1 atm). In real situations, concentrations may differ from 1 M.
The Nernst Equation gives the electrode potential (or cell EMF) at any
concentration. It was derived by Walther Nernst from thermodynamic principles.
|
Nernst Equation (Cell EMF) |
E_cell =
E°_cell − (RT / nF) ln Q =
E°_cell − (0.0592 / n) log Q [at 298 K] |
|
Reaction Quotient (Q) |
Q =
[Products] / [Reactants]
(same form as equilibrium constant K) |
|
At Equilibrium (E_cell = 0) |
E°_cell =
(0.0592 / n) log Keq → log Keq
= nE°_cell / 0.0592 |
At 298 K, RT/F = 0.02569 V ≈ 0.0257 V; and (RT ln 10)/F = 0.05916 V ≈
0.0592 V (used with log base 10).
Figure 2: Nernst Equation Graph — As
reaction proceeds (Q increases), E_cell decreases. At equilibrium, Q = Keq and
E_cell = 0. The cell is 'dead'.
Physical Meaning: When reactant concentrations are high (Q <
1), the cell has a higher EMF than E°. As the reaction proceeds, reactant
concentrations decrease and product concentrations increase (Q increases),
causing the EMF to decrease. Eventually, when Q = Keq, the cell reaches
equilibrium and E_cell = 0 — no more current flows (battery is 'dead').
Nernst Equation for Single Electrode: For a single reduction
half-cell M^n+ + ne⁻ → M, the Nernst equation gives: E = E° − (0.0592/n)
log(1/[M^n+]) = E° + (0.0592/n) log[M^n+]. The electrode potential increases
when the ion concentration increases.
4. Conductance of Electrolytic Solutions
When an electrolyte is dissolved in water, it dissociates into ions that
can carry electric current. The ability of an electrolytic solution to conduct
electricity is described by conductance and related quantities. Understanding
these terms is essential for studying ionic behaviour, determining degree of
dissociation, and finding solubility products.
4.1 Definitions and Units
Resistance (R): Opposition to flow of current. Unit: ohm (Ω). For
a conductor: R = ρ l/A where ρ =
resistivity, l = length, A = cross-sectional area.
Conductance (G): Reciprocal of resistance: G = 1/R. Unit: siemens
(S) or mho (Ω⁻¹).
Specific Conductance (κ, kappa): The conductance of a solution of
unit length (1 cm) and unit cross-section (1 cm²). κ = G × l/A = G × cell
constant. Unit: S cm⁻¹.
Molar Conductance (Λm): The conductance of a solution containing 1
mole of electrolyte when placed between two electrodes of unit area separated
by unit distance. Λm = κ/c (where c = concentration in mol/cm³) or Λm = (κ ×
1000)/M (where M = molarity in mol/L). Unit: S cm² mol⁻¹.
|
Specific Conductance |
kappa = G
× (l/A) = G × cell constant [S cm⁻¹] |
|
Molar Conductance (from κ and M) |
Lambda_m =
(kappa × 1000) / M [S cm²
mol⁻¹; M in mol/L] |
4.2 Variation of Molar Conductance with
Concentration
The molar conductance of both strong and weak electrolytes increases with
decreasing concentration (dilution). However, the pattern of increase is very
different for the two types — a distinction that is fundamental to
understanding electrolyte behaviour.
Figure 3: Molar Conductance vs √c —
Strong electrolytes show linear decrease with √c (Debye-Hückel); weak
electrolytes show a sharp rise at low concentration due to increased
dissociation.
Strong Electrolytes (e.g., KCl, NaCl, HCl, H₂SO₄): These are
completely dissociated at all concentrations. The increase in Λm with dilution
is because at high concentrations, interionic attractions slow down the ions
(Debye-Hückel-Onsager effect). On plotting Λm vs √c, a straight line is
obtained.
|
Debye-Hückel-Onsager Equation (Strong Electrolytes) |
Lambda_m =
Lambda°_m − b√c
(b = experimental constant) |
Weak Electrolytes (e.g., CH₃COOH, NH₄OH): These are partially
dissociated. At high concentrations, degree of dissociation (α) is very small.
As concentration decreases (dilution), α increases dramatically — causing Λm to
rise sharply. Λ°m cannot be determined by extrapolation and must be calculated
using Kohlrausch's Law.
4.3 Kohlrausch's Law of Independent Migration of Ions
At infinite dilution, all ions are completely free of interionic
interactions. Kohlrausch's Law states that the molar conductance at infinite
dilution (Λ°m) of an electrolyte is the sum of the limiting molar
conductivities of the individual ions (cation and anion), regardless of which
other ion is present.
|
Kohlrausch's Law |
Lambda°_m = v₊
× lambda°₊ + v₋ × lambda°₋ |
Here v₊ and v₋ are the number of cations and anions per formula unit, and
λ°₊ and λ°₋ are the limiting molar conductivities of cation and anion
respectively.
|
Example: Λ°m of CH₃COOH |
Lambda°_m(CH3COOH) =
Lambda°_m(CH3COONa) + Lambda°_m(HCl) − Lambda°_m(NaCl) |
Key Application — Degree of Dissociation: For a weak electrolyte,
the degree of dissociation α = Λm / Λ°m. This allows calculation of Ka: Ka =
cα² / (1−α) ≈ cα² for small α.
|
Degree of Dissociation (Weak Electrolyte) |
alpha =
Lambda_m / Lambda°_m |
4.4 Important Limiting Molar Conductivities
|
Ion |
λ° (S cm²
mol⁻¹) |
Ion |
λ° (S cm²
mol⁻¹) |
|
H⁺ (hydronium) |
349.6 |
OH⁻ |
198.0 |
|
K⁺ |
73.5 |
Cl⁻ |
76.3 |
|
Na⁺ |
50.1 |
NO₃⁻ |
71.5 |
|
Ca²⁺ |
119.0 |
SO₄²⁻ |
160.0 |
|
Mg²⁺ |
106.0 |
CH₃COO⁻ |
40.9 |
|
NH₄⁺ |
73.7 |
HCO₃⁻ |
44.5 |
Note: H⁺ and OH⁻ have anomalously high conductivities due to the
Grotthuss (proton-hopping) mechanism — protons hop along a chain of
hydrogen-bonded water molecules rather than physically migrating.
5. Electrolytic Cells and Electrolysis
An electrolytic cell is a device that uses electrical energy from an
external source (battery or DC power supply) to drive a non-spontaneous
chemical (redox) reaction. This process is called electrolysis. Unlike a
galvanic cell (which generates electricity from chemistry), an electrolytic
cell uses electricity to produce chemistry.
Figure 4: Electrolytic Cell —
Electrolysis of acidulated water. At cathode (−): H⁺ ions are reduced to H₂
gas. At anode (+): water is oxidised to O₂ gas.
|
Feature |
Galvanic /
Voltaic Cell |
Electrolytic
Cell |
|
Energy conversion |
Chemical → Electrical
energy |
Electrical → Chemical
energy |
|
Reaction type |
Spontaneous redox (ΔG <
0) |
Non-spontaneous (ΔG >
0), driven by ext. power |
|
External source |
Not needed (cell is the
source) |
External battery/DC source
required |
|
Anode charge |
Negative (−) |
Positive (+) |
|
Cathode charge |
Positive (+) |
Negative (−) |
|
Anode reaction |
Oxidation (metal dissolves) |
Oxidation (ion
discharge/oxidation) |
|
Cathode reaction |
Reduction (metal deposits) |
Reduction (cation
discharge) |
|
Salt bridge |
Required (to complete
circuit) |
Not required (both
electrodes in same electrolyte) |
|
Examples |
Daniell cell, Dry cell,
Lead storage battery |
Electrolysis of water,
brine; electroplating |
5.1 Products of Electrolysis — Preferential
Discharge
When multiple ions are present in an electrolytic cell, the ion that is
discharged (reduced at cathode or oxidised at anode) preferentially depends on
several factors: (1) Nature of electrode, (2) Concentration of ions, (3)
Overpotential (extra voltage needed beyond theoretical, especially for gas
evolution), and (4) Standard electrode potential (ions with higher SRP are
preferentially reduced at cathode).
◆
At cathode: The cation with the highest (most positive)
standard reduction potential is preferentially reduced. Exception: H₂ shows
large overpotential on mercury, so metals like Zn are deposited even though
E°(Zn) < E°(H₂).
◆
At anode: If the anode is active (Cu, Ag, Zn), it
dissolves preferentially. If anode is inert (Pt, graphite/carbon), the anion
with the lowest oxidation potential is discharged. OH⁻ is preferentially
discharged over SO₄²⁻ in dilute solutions.
5.2 Important Industrial Electrolytic Processes
|
Process |
Electrolyte |
Cathode
Product |
Anode
Product |
Application |
|
Electrolysis of water |
Dil. H₂SO₄ or NaOH |
H₂ gas |
O₂ gas |
Hydrogen production |
|
Electrolysis of brine
(NaCl) |
Concentrated NaCl |
H₂ gas |
Cl₂ gas |
Chlor-alkali industry
(NaOH, Cl₂, H₂) |
|
Electrolytic refining of Cu |
CuSO₄ solution |
Pure Cu (99.99%) |
Impure Cu dissolves |
Electronics, wiring |
|
Electroplating with Ag |
AgNO₃ solution |
Ag deposits on object |
Ag anode dissolves |
Jewellery, tableware |
|
Electroplating with Cr |
Chromic acid |
Cr deposits |
Inert Pt anode; O₂ |
Automotive parts |
|
Extraction of Al |
Molten Al₂O₃ (Bayer
process) |
Al metal |
O₂ gas; C anode burns |
Hall-Héroult process |
6. Faraday's Laws of Electrolysis
Michael Faraday (1833–34) formulated two quantitative laws relating the
amount of substance deposited or liberated at an electrode to the quantity of
electricity passed. These laws are valid for all electrolytic processes,
regardless of the nature of the electrolyte, electrode, or conditions.
Figure 5: Faraday's Laws — First Law
relates mass deposited to charge passed; Second Law relates masses deposited
for different substances to their equivalent weights. F = 96500 C/mol.
6.1 First Law of Electrolysis
The mass of substance deposited or liberated at an electrode during
electrolysis is directly proportional to the quantity of electricity (charge)
passed through the electrolyte.
|
First Law |
w = Z
× Q =
Z × I × t |
Here w = mass deposited (grams), Z = electrochemical equivalent (g/C), Q
= charge in coulombs, I = current in amperes, t = time in seconds. Z = E/F =
M/(nF), where E = equivalent weight, F = Faraday constant = 96500 C/mol.
|
Faraday's First Law (Quantitative Form) |
w = (M
× I × t) / (n × F) = (M × Q) / (n × F) |
Here M = molar mass (g/mol), n = number of electrons transferred per ion
(n-factor), F = 96500 C/mol, I = current (A), t = time (s). The formula can be
rearranged to find any one variable given the others.
6.2 Second Law of Electrolysis
When the same quantity of electricity passes through different
electrolytes connected in series, the masses of different substances deposited
or liberated are proportional to their equivalent weights (E = M/n, where n is
the n-factor).
|
Second Law |
w₁ /
w₂ =
E₁ / E₂ = (M₁/n₁) / (M₂/n₂) |
6.3 Faraday Constant — Key Values
|
Faraday Constant (F) |
F =
N_A × e = 6.022 × 10²³ × 1.6 × 10⁻¹⁹ =
96500 C/mol ≈ 96485 C/mol |
|
Equivalents Deposited |
Equivalents = Q
/ F =
(I × t) / F |
|
Volume of Gas at STP |
V = (Q
/ nF) × 22400 mL = (I × t / nF) × 22.4 L |
|
Step-by-Step Method for Faraday's Law
Problems |
|
Step 1: Find total charge Q =
I × t (in coulombs). If current varies, use Q = ∫I dt. Step 2: Find moles of
electrons = Q / F = Q / 96500. Step 3: Using stoichiometry of
the electrode reaction, find moles of substance deposited. (e.g., if Cu²⁺ + 2e⁻ → Cu, then 2
moles of electrons deposit 1 mole of Cu) Step 4: Multiply moles of
substance by its molar mass to get mass in grams. Step 5: For gas volume (at
STP), multiply moles by 22.4 L. Note: 1 Faraday = 96500 C =
charge required to deposit 1 gram-equivalent of any substance. |
7. Batteries — Commercial Electrochemical Cells
A battery is a combination of one or more galvanic cells connected in
series (to increase voltage) or in parallel (to increase current capacity).
Batteries are broadly classified into primary cells (non-rechargeable) and
secondary cells (rechargeable).
7.1 Primary Cells (Non-rechargeable)
|
Battery |
Anode |
Cathode |
Electrolyte |
EMF |
Application |
|
Leclanché (Dry cell, 1866) |
Zn |
MnO₂ + C (graphite) |
NH₄Cl + ZnCl₂ paste |
~1.5 V |
Torches, remotes, clocks |
|
Mercury cell |
Zn (in KOH) |
HgO |
KOH/ZnO paste |
~1.35 V |
Hearing aids, watches,
cameras |
|
Alkaline cell |
Zn powder |
MnO₂ |
KOH solution |
~1.5 V |
Higher capacity; longer
life than dry cell |
|
Lithium cell |
Li |
MnO₂ or SOCl₂ |
LiClO₄ in organic solvent |
~3.0 V |
Pacemakers, cameras, memory
backup |
7.2 Secondary Cells (Rechargeable)
|
Battery |
Anode
(discharge) |
Cathode
(discharge) |
Electrolyte |
EMF |
Key Features |
|
Lead Storage Battery (Car
battery) |
Pb (lead) |
PbO₂ |
38% H₂SO₄ (aq) |
~2.0 V/cell (12V for 6
cells) |
Heavy; reliable;
rechargeable; widely used in vehicles |
|
Nickel-Cadmium (NiCd) |
Cd |
NiO(OH) |
KOH solution |
~1.2 V |
Constant discharge; memory
effect; toxic Cd |
|
Nickel-Metal Hydride (NiMH) |
Metal hydride (MH) |
NiO(OH) |
KOH solution |
~1.2 V |
Higher capacity than NiCd;
no memory effect; used in hybrid cars |
|
Lithium-Ion (Li-ion) |
Graphite (Li intercalated) |
LiCoO₂ / LiFePO₄ |
LiPF₆ in organic solvent |
~3.6 V |
High energy density; no
memory effect; smartphones, laptops, EVs |
7.3 Lead Storage Battery — Detailed Chemistry
The lead-acid battery (invented by Gaston Planté in 1859) is the oldest
rechargeable battery and remains the most widely used for automotive
applications due to its high power output, reliability, and low cost. Each cell
generates about 2.0 V, so a standard 12 V car battery contains 6 cells in
series.
|
Discharge — Anode Reaction |
Pb(s) +
SO₄²⁻(aq) → PbSO₄(s) + 2e⁻
[Oxidation] |
|
Discharge — Cathode Reaction |
PbO₂(s) +
SO₄²⁻ + 4H⁺ + 2e⁻ → PbSO₄(s) + 2H₂O
[Reduction] |
|
Overall Discharge Reaction |
Pb + PbO₂ +
2H₂SO₄ → 2PbSO₄ + 2H₂O (discharge) |
During charging, the reactions are reversed — PbSO₄ is converted back to
Pb and PbO₂, and H₂SO₄ is regenerated. The density of H₂SO₄ increases during
charging and decreases during discharging — hydrometer measurement of H₂SO₄
density indicates the state of charge of the battery.
7.4 Fuel Cells
A fuel cell is a galvanic cell that generates electricity by the
continuous electrochemical reaction of a fuel (hydrogen, methanol,
hydrocarbons) with an oxidant (usually oxygen from air), as long as the
reactants are supplied. Unlike a battery, a fuel cell does not 'run down' — it
operates continuously like an engine. The only by-product of a hydrogen-oxygen
fuel cell is water — making it extremely clean.
|
H₂–O₂ Fuel Cell — Cathode (with KOH electrolyte) |
O₂(g) +
2H₂O(l) + 4e⁻ → 4OH⁻(aq) |
|
H₂–O₂ Fuel Cell — Anode |
H₂(g) +
2OH⁻(aq) → 2H₂O(l) + 2e⁻ |
|
Overall Reaction |
2H₂(g) +
O₂(g) → 2H₂O(l) + Electrical Energy |
Fuel cells have efficiency of up to 70–80% (much higher than internal
combustion engines at 25–35%). Applications include space shuttles (Apollo,
Space Shuttle), backup power systems, electric buses (hydrogen fuel cell buses
in many cities), and emerging passenger vehicles (Toyota Mirai, Hyundai Nexo).
8. Corrosion — An Electrochemical Process
Corrosion is the gradual deterioration of metals by chemical or
electrochemical reaction with the environment — particularly with oxygen and
moisture. Rusting of iron, tarnishing of silver, and the green patina on copper
are all forms of corrosion. It is estimated that corrosion costs the global
economy over USD 2.5 trillion per year.
Rusting of Iron — Electrochemical Mechanism: Rusting is an
electrochemical process requiring both water and oxygen. The surface of iron
acts like a galvanic cell — impurities or stress points on the iron surface
become cathodic (more noble), while the main iron surface becomes anodic
(corrodes). The overall reaction produces rust, which is hydrated iron(III)
oxide: Fe₂O₃·xH₂O.
|
Rusting — Anode (Fe is oxidised) |
Fe(s) →
Fe²⁺(aq) + 2e⁻ E° = +0.44 V |
|
Rusting — Cathode (O₂ is reduced) |
O₂(g) +
2H₂O + 4e⁻ → 4OH⁻(aq) E° = +0.40 V |
|
Final Rust Formation |
4Fe(OH)₂ +
O₂ → 2Fe₂O₃.H₂O (rust) + 2H₂O |
8.1 Prevention of Corrosion
◆
Barrier Protection: Painting, oiling, greasing, or
coating with plastic prevents contact of iron with moisture and O₂.
◆
Galvanisation: Coating iron with zinc (a more reactive
metal, E° = −0.76 V vs Fe = −0.44 V). Even if the zinc coating is scratched,
zinc corrodes preferentially (sacrificial protection) because Zn has lower SRP
than Fe.
◆
Cathodic Protection (Sacrificial Anode Method): A more
reactive metal (Mg, Zn, Al) is connected to the iron structure. The sacrificial
metal is oxidised instead of iron — protecting underground pipelines, ship
hulls, and oil rigs.
◆
Alloying: Making stainless steel (Fe + Cr + Ni) creates
a passive Cr₂O₃ layer that prevents further corrosion.
◆
Tin Plating: Used for food cans. Tin (Sn, E° = −0.14 V)
is less reactive than Fe (E° = −0.44 V) — acts as barrier but NOT sacrificially
(once scratched, Fe corrodes faster).
◆
Electroplating: Depositing noble metals (Cr, Ni, Au,
Ag) on the surface by electrolysis — decorative and protective.
9. Master Formula Table — Electrochemistry
|
Formula /
Concept |
Expression |
Key Notes |
|
Standard
Cell EMF |
E°cell = E°cathode − E°anode |
Both are
standard reduction potentials |
|
Gibbs
Energy & EMF |
ΔG° = −nFE°cell |
n = moles of
electrons; F = 96500 C/mol |
|
EMF &
Equilibrium K |
E°cell = (0.0592/n) log Keq |
At 298 K; log
base 10 |
|
Nernst
Equation |
E = E° − (0.0592/n) log Q |
Q = reaction
quotient |
|
Nernst
(single electrode) |
E = E° + (0.0592/n) log[M^n+] |
For Mn+ + ne⁻
→ M electrode |
|
Spontaneity |
E°cell > 0 → ΔG < 0 → spontaneous |
E°cell < 0
→ non-spontaneous |
|
Conductance |
G = 1/R (S or Ω⁻¹) |
Reciprocal of
resistance |
|
Specific
Conductance |
κ = G × (l/A) = G × cell constant |
Unit: S cm⁻¹ |
|
Molar
Conductance |
Λm = (κ × 1000) / M |
M in mol/L;
unit: S cm² mol⁻¹ |
|
Kohlrausch's
Law |
Λ°m = v₊λ°₊ + v₋λ°₋ |
For strong
& weak electrolytes |
|
D-H-O
Equation |
Λm = Λ°m − b√c |
Strong
electrolytes only |
|
Degree of
Dissociation |
α = Λm / Λ°m |
For weak
electrolytes |
|
Faraday
1st Law |
w = (M × I × t) / (n × F) |
w in grams; I
in A; t in s |
|
Faraday
2nd Law |
w₁/w₂ = E₁/E₂ = (M₁/n₁)/(M₂/n₂) |
Same Q
through electrolytes in series |
|
Faraday
Constant |
F = 96500 C/mol |
Charge per
mole of electrons |
|
Charge
Quantity |
Q = I × t (coulombs) |
1 coulomb = 1
ampere × 1 second |
|
Moles of
electrons |
n_e = Q / F = It / 96500 |
Used in all
Faraday calculations |
|
Gas Volume
at STP |
V = (I×t / nF) × 22400 mL |
n = electrons
per molecule of gas |
|
Electrochemical
Eq. |
Z = M / (n × F) = E / F |
E =
equivalent weight = M/n |
10. Quick Revision — Key Points
|
Electrochemical Cells & EMF — Must Know |
|
* Galvanic cell: spontaneous
redox → electrical energy. Anode (−): oxidation. Cathode (+): reduction. * Cell notation: Anode |
electrolyte || electrolyte | Cathode. Left = anode always. * E°cell = E°cathode − E°anode
(both as standard REDUCTION potentials). * E°cell > 0 → ΔG < 0 →
spontaneous. ΔG° = −nFE°cell. * E°cell = (0.0592/n) log Keq
at 298 K. Larger E°cell → larger Keq (more complete reaction). * Nernst: E = E° −
(0.0592/n)logQ. At equilibrium: E = 0, Q = Keq. * Daniell cell: E° =
E°(Cu²⁺/Cu) − E°(Zn²⁺/Zn) = 0.34−(−0.76) = +1.10 V. |
|
Conductance — Must Know |
|
* κ (specific conductance) = G
× cell constant. Unit: S cm⁻¹. Increases with concentration. * Λm (molar conductance) = (κ
× 1000)/M. Unit: S cm² mol⁻¹. Increases with dilution. * Strong electrolytes: Λm =
Λ°m − b√c (linear). Λ°m by extrapolation. * Weak electrolytes: Λm rises
sharply with dilution. Λ°m by Kohlrausch's Law. * Kohlrausch: Λ°m(CH₃COOH) =
Λ°m(CH₃COONa) + Λ°m(HCl) − Λ°m(NaCl). * H⁺ has highest λ° (349.6)
and OH⁻ next (198.0) due to Grotthuss proton-hopping mechanism. * Degree of dissociation α =
Λm / Λ°m (for weak electrolytes). Then Ka = cα²/(1−α). |
|
Electrolysis & Faraday's Laws — Must
Know |
|
* Electrolytic cell:
electrical energy → chemical reaction (non-spontaneous). Anode = (+), Cathode
= (−). * At cathode: cation with
highest SRP is preferentially reduced. * At anode (inert): anion with
lowest oxidation potential is preferentially oxidised. * Faraday 1st Law: w =
MIt/(nF). Find Q = It → moles e⁻ = Q/F → moles substance → mass. * Faraday 2nd Law: w₁/w₂ =
E₁/E₂. Masses ∝ equivalent weights (M/n). * F = 96500 C/mol. 1 Faraday
deposits 1 gram-equivalent of any substance. * Gas volume at STP = (It/nF)
× 22400 mL. e.g., 96500 C through water gives 11200 mL H₂ and 5600 mL O₂. |
|
Batteries & Corrosion — Must Know |
|
* Primary cell:
non-rechargeable (dry cell 1.5V, mercury cell 1.35V, Li cell 3V). * Secondary cell:
rechargeable. Lead acid: Pb/PbO₂/H₂SO₄, 2V/cell, 12V total. * During discharge of lead
battery: both electrodes form PbSO₄; H₂SO₄ is consumed. * Li-ion cell: 3.6 V, highest
energy density, no memory effect → smartphones, EVs. * H₂-O₂ fuel cell: continuous
supply of H₂ and O₂; product = water only; 70-80% efficient. * Rusting: electrochemical
process needing water + O₂. Fe acts as anode; impurity as cathode. * Galvanisation (Zn coating) →
sacrificial protection. Tin plating → barrier only (not sacrificial). * Cathodic protection: connect
Mg/Zn block to iron — Mg/Zn corrodes preferentially. |
— End of Chapter 3:
Electrochemistry (Chemistry) —