Matter is anything with mass that occupies space. An element cannot be broken into simpler substances by chemical means; a compound is two or more elements chemically combined in a fixed ratio (H₂O is always 2 H : 1 O); a mixture combines substances in variable ratio, separable physically.
Atoms are too small to count, so chemists use the mole — exactly \(6.022\times10^{23}\) entities (the Avogadro constant \(N_A\)), just as "a dozen" always means 12. The mole is defined so the mass of one mole in grams (the molar mass) numerically equals the atomic/molecular mass in \(u\). This links the atomic world to the weighable world:
$$ n = \frac{\text{given mass}}{\text{molar mass}} = \frac{N}{N_A} = \frac{V}{22.4\ \text{L}}\ (\text{gas at STP}) $$
One mole of any gas occupies \(22.4\ \text{L}\) at STP — a direct consequence of Avogadro's law.
The empirical formula is the simplest whole-number atom ratio; the molecular formula \(= \text{empirical} \times n\), where \(n = \dfrac{\text{molecular mass}}{\text{empirical formula mass}}\). In a reaction, the limiting reagent is found by comparing (moles ÷ coefficient) for each reactant — the smallest value runs out first and caps the product.
Non-zero digits and zeros between them are significant; leading zeros never are; trailing zeros count only after a decimal point. For addition/subtraction the result keeps the fewest decimal places; for multiplication/division it keeps the fewest significant figures.
| Model | Scientist | Key Feature | Limitation |
|---|---|---|---|
| Plum-pudding | Thomson (1904) | Electrons embedded in positive sphere | Couldn't explain α-scattering |
| Nuclear model | Rutherford (1911) | Tiny dense nucleus; electrons orbit | Couldn't explain atomic stability or line spectra |
| Planetary (quantised) | Bohr (1913) | Fixed circular orbits; energy quantised | Only valid for H-like atoms; ignored wave nature |
| Series | \(n_f\) | \(n_i\) | Region | First line (\(n_i = n_f+1\)) |
|---|---|---|---|---|
| Lyman | 1 | 2,3,4… | UV | n=2→1 (121.6 nm) |
| Balmer | 2 | 3,4,5… | Visible | n=3→2 (656.3 nm, red) |
| Paschen | 3 | 4,5,6… | Near IR | n=4→3 |
| Brackett | 4 | 5,6,7… | IR | n=5→4 |
| Pfund | 5 | 6,7,8… | Far IR | n=6→5 |
| QN | Symbol | Values | Describes |
|---|---|---|---|
| Principal | \(n\) | 1, 2, 3, … | Shell, energy level, size |
| Azimuthal | \(l\) | \(0\) to \(n-1\) | Sub-shell, shape (s,p,d,f) |
| Magnetic | \(m_l\) | \(-l\) to \(+l\) | Orientation in space |
| Spin | \(m_s\) | \(+\tfrac{1}{2}\) or \(-\tfrac{1}{2}\) | Spin of electron |
System: part under study. Surroundings: everything else. Universe = system + surroundings.
Types: Open (exchange mass+energy), Closed (energy only), Isolated (neither).
State functions: H, S, G, U, T, P, V — depend only on current state, not path. q and w are path functions.
ΔU = q + w (IUPAC sign: w = −PₑₓₜΔV for expansion)
For ideal gas: ΔU = nCᵥΔT (depends only on T).
Enthalpy: H = U + PV; ΔH = ΔU + ΔngRT for reactions involving gases (Δng = moles of gaseous products − reactants).
| Term | Symbol | Definition |
|---|---|---|
| Standard enthalpy of formation | ΔH°f | For 1 mol compound from elements in standard states; ΔH°f(elements) = 0 |
| Combustion | ΔH°c | Complete combustion of 1 mol in excess O₂ (always negative) |
| Atomisation | ΔH°at | 1 mol gaseous atoms from element in standard state (always +ve) |
| Bond dissociation | BE | Energy to break 1 mol bonds homolytically in gas phase (always +ve) |
| Lattice enthalpy | ΔH°L | 1 mol ionic solid → gaseous ions (always +ve; Born-Haber cycle) |
| Solution | ΔH°soln | ΔH°soln = ΔH°L + ΔH°hydration |
ΔH of a reaction is independent of the path — only depends on initial and final states.
ΔH°rxn = Σ ΔH°f(products) − Σ ΔH°f(reactants)
Flip a reaction → change sign of ΔH. Multiply by n → multiply ΔH by n.
ΔH°rxn = Σ BE(bonds broken) − Σ BE(bonds formed)
Bonds broken = reactants; bonds formed = products.
Breaking bonds requires energy (+); forming bonds releases energy (−). Used when ΔH°f data is unavailable.
Entropy (S): measure of disorder/randomness. \(\Delta S = q_{rev}/T\). For universe: \(\Delta S_{univ} = \Delta S_{sys} + \Delta S_{surr} \ge 0\) (always for spontaneous processes).
G = H − TS; ΔG = ΔH − TΔS (at constant T, P)
ΔG < 0: spontaneous; ΔG = 0: equilibrium; ΔG > 0: non-spontaneous.
ΔG° = −RT ln K = −nFE°cell
Standard free energy of formation: ΔG°rxn = Σ ΔG°f(products) − Σ ΔG°f(reactants)
| ΔH | ΔS | ΔG = ΔH−TΔS | Spontaneity |
|---|---|---|---|
| − | + | Always − | Spontaneous at all T |
| + | − | Always + | Non-spontaneous at all T |
| − | − | − at low T | Spontaneous at low T only |
| + | + | − at high T | Spontaneous at high T only |
At equilibrium: rate of forward = rate of reverse reaction. Concentrations are constant (not necessarily equal).
For aA+bB ⇌ cC+dD:
Kc = [C]ᶜ[D]^d / [A]ᵃ[B]^b (concentrations)
Kp \(= (pC)ᶜ(pD)^d / (pA)ᵃ(pB)^b\) (partial pressures)
\(Kp = Kc(RT)^\Delta ng\) where Δng = (c+d)−(a+b) for gases only
Pure solids and liquids excluded from K expression.
Q has same form as K but uses non-equilibrium concentrations.
Q < K: reaction proceeds forward (→)
Q > K: reaction proceeds reverse (←)
Q = K: system is at equilibrium
System at equilibrium subjected to a stress shifts to partially relieve that stress.
ΔG° = −RT ln K
K > 1 → ΔG° < 0 (products favoured)
K < 1 → ΔG° > 0 (reactants favoured)
K = 1 → ΔG° = 0
\(K_w = [\mathrm{H}^+][\mathrm{OH}^-] = 10^{-14}\) at 25°C; pH + pOH = 14
\(\text{pH} = -\log[\mathrm{H}^+]\); \(\text{pOH} = -\log[\mathrm{OH}^-]\)
Acid: pH < 7; Base: pH > 7; Neutral: pH = 7 (at 25°C)
For weak acid HA ⇌ H⁺+A⁻: \(K_a = [\mathrm{H}^+][\mathrm{A}^-]/[\mathrm{HA}]\)
\([\mathrm{H}^+] = \sqrt{K_a \cdot C}\) (if \(\alpha \ll 1\))
\(\text{pH} = \tfrac{1}{2}(\text{p}K_a - \log C)\)
Degree of dissociation: \(\alpha = \sqrt{K_a/C}\)
\(K_a\times K_b = K_w\) for conjugate pair
Henderson-Hasselbalch: \(\text{pH} = \text{p}K_a + \log([\mathrm{A}^-]/[\mathrm{HA}])\)
Maximum buffer capacity when \([\mathrm{A}^-]=[\mathrm{HA}]\), i.e. \(\text{pH} = \text{p}K_a\).
Acidic buffer: weak acid + its salt. Basic buffer: weak base + its salt.
For \(A_m B_n\)(s) ⇌ \(m\mathrm{A}^{n+} + n\mathrm{B}^{m-}\):
\(K_{sp} = [\mathrm{A}^{n+}]^m [\mathrm{B}^{m-}]^n\)
Solubility s: \(K_{sp} = m^m \cdot n^n \cdot s^{m+n}\)
Common ion effect: adding common ion decreases solubility (shifts equilibrium left).
Galvanic: spontaneous redox → electrical energy. Anode (oxidation, −ve), Cathode (reduction, +ve). E°cell = E°cathode − E°anode.
Electrolytic: electrical energy → non-spontaneous redox. External EMF applied. Anode = +ve, Cathode = −ve.
Measured against SHE (Standard Hydrogen Electrode, E° = 0 V by convention).
More positive E° → stronger oxidising agent (reduced at cathode). More negative E° → stronger reducing agent.
E°cell = E°cathode(reduction) − E°anode(reduction)
Spontaneous cell: E°cell > 0 (ΔG° = −nFE°cell < 0).
E = E° − (RT/nF)ln Q = E° − (0.0592/n)log Q (at 25°C)
E = 0 when Q = K (cell has fully discharged).
$$ ∴ E^{\circ} = (0.0592/n)\log K = RT/nF \times \ln K $$
Combined: ΔG° = −nFE° = −RT ln K
Both electrodes same metal but different concentrations: E° = 0.
E = (0.0592/n)log([higher]/[lower])
Reaction proceeds until concentrations equalise.
Arranging electrodes by their standard reduction potential (E°) gives the electrochemical series. A more positive E° means a stronger oxidising agent (readily reduced); a more negative E° means a stronger reducing agent (readily oxidised).
Mass deposited ∝ charge passed: m = ZQ = ZIt
Z = electrochemical equivalent (g/C) = M/nF where M = molar mass, n = electrons.
Same charge deposits masses in ratio of their equivalent weights (M/n).
m = (M/nF)×Q | 1 Faraday = 96500 C ≈ 1 mol electrons.
| Term | Formula | Units |
|---|---|---|
| Resistance \(R\) | \(R = \rho\cdot l/A\) | Ω |
| Conductance \(G\) | \(G = 1/R\) | S (siemens) |
| Specific conductance \(\kappa\) | \(\kappa = 1/\rho = G\cdot(l/A)\) | S·m⁻¹ |
| Molar conductance \(\Lambda_m\) | \(\Lambda_m = \kappa/C\) (C in mol/m³) | S·m²·mol⁻¹ |
| Kohlrausch's law | \(\Lambda^\circ_m = \Sigma\, \lambda^\circ(\text{ions})\) (at infinite dilution) | additive |
For aA+bB→cC+dD: Rate = −(1/a)d[A]/dt = −(1/b)d[B]/dt = +(1/c)d[C]/dt = +(1/d)d[D]/dt
Rate = k[A]^m[B]^n (determined experimentally, not from stoichiometry)
Order = m+n (overall); m = order w.r.t A; n w.r.t B.
Units of k: \((\mathrm{mol/L})^{1-n}\cdot s^{-1}\) where n = overall order.
One reactant in large excess → its concentration is effectively constant.
Hydrolysis of ester in dilute acid: Rate = k'[ester] — pseudo first-order (water in excess).
k' = k[H₂O] — pseudo rate constant.
| Order | Rate law | Integrated form | Half-life t½ | Units of k |
|---|---|---|---|---|
| Zero | \(\text{Rate} = k\) | \([A] = [A]_0 - kt\) | \(t_{1/2} = [A]_0/2k\) | mol·L⁻¹·s⁻¹ |
| First | \(\text{Rate} = k[A]\) | \(\ln[A] = \ln[A]_0 - kt\) or \([A]=[A]_0 e^{-kt}\) | \(t_{1/2} = \ln 2/k = 0.693/k\) | s⁻¹ |
| Second | \(\text{Rate} = k[A]^2\) | \(1/[A] = 1/[A]_0 + kt\) | \(t_{1/2} = 1/(k[A]_0)\) | L·mol⁻¹·s⁻¹ |
\(k = A\cdot e^{-E_a/RT}\)
ln k = ln A − Ea/RT
$$ \ln(k_{2}/k_{1}) = \frac{Ea}{R}(1/T_{1} - 1/T_{2}) $$
A = frequency factor (pre-exponential); Ea = activation energy (J/mol)
Rule of thumb: rate doubles for every 10°C rise (temperature coefficient \(\mu \approx 2\)).
Higher \(E_a\) → rate more sensitive to temperature.
Catalyst lowers \(E_a\) → increases \(k\) (doesn't change \(\Delta H\) or equilibrium).
Rate = Z_AB·f·p where Z_AB = collision frequency, \(f = e^{-E_a/RT}\) (fraction with enough energy), p = steric factor.
Not all collisions are effective — need correct orientation AND energy ≥ Ea.
Rate-determining step (RDS) = slowest step → determines overall rate law.
Intermediates cancel out; only species present before RDS appear in rate law.
Molecularity = number of species in elementary step (1, 2, or 3). Order = from experiment.
| Term | Formula | Units |
|---|---|---|
| Molarity (M) | moles of solute / volume of solution (L) | mol L⁻¹ |
| Molality (m) | moles of solute / mass of solvent (kg) | mol kg⁻¹ |
| Mole fraction (\(\chi\)) | \(n_A / (n_A + n_B)\); \(\chi_A + \chi_B = 1\) | dimensionless |
| Mass fraction (w) | mass of solute / total mass | dimensionless |
| ppm | mass of solute / total mass \(\times 10^6\) | mg kg⁻¹ |
For a volatile solute in a volatile solvent:
\(p_A = \chi_A \cdot p_A^\circ\) (partial pressure = mole fraction × vapour pressure of pure component)
Total pressure: \(P = p_A + p_B = \chi_A p_A^\circ + \chi_B p_B^\circ\)
For a non-volatile solute: \(p_{solution} = \chi_{solvent} \cdot p^\circ_{solvent}\)
\((p^\circ - p) / p^\circ = \chi_{solute} = n_2 / (n_1 + n_2)\)
For dilute solutions: \(\approx n_{2}/n_{1} = w_{2}M_{1} / (w_{1}M_{2})\)
RLVP is a colligative property — depends only on number of solute particles, not their nature.
Ideal: \(\Delta H_{mix} = 0\), \(\Delta V_{mix} = 0\); obeys Raoult's law at all concentrations. A-B interactions = A-A = B-B.
Positive deviation: A-B < A-A/B-B; p > Raoult prediction. Examples: ethanol-water, acetone-CS₂.
Negative deviation: A-B > A-A/B-B; p < Raoult prediction. Examples: HCl-water, acetone-chloroform.
\(p = K_H \cdot \chi\) where \(K_H\) = Henry's law constant (large \(K_H\) → low solubility).
Solubility of gas ↑ with ↑ pressure and ↓ temperature.
Applications: carbonated drinks (CO₂ under pressure), scuba diving (N₂ narcosis), oxygen in blood.
Depend only on the number of solute particles in solution, not their identity.
| Property | Formula | Key point |
|---|---|---|
| Relative lowering of VP | \((p^{\circ}-p)/p^{\circ} = \chi_{2}\) | χ₂ = mole fraction of solute |
| Elevation of boiling point | \(\Delta T_b = K_b \cdot m\) | \(K_b\) = ebullioscopic constant (solvent property) |
| Depression of freezing point | \(\Delta T_f = K_f \cdot m\) | \(K_f\) = cryoscopic constant; larger than \(K_b\) |
| Osmotic pressure | \(\pi = CRT = \frac{n}{V}RT\) | Van't Hoff equation; C in mol/L |
i = observed colligative property / expected colligative property = actual moles / formula moles
| Case | i value | Example |
|---|---|---|
| No association/dissociation | i = 1 | Glucose, urea in water |
| Dissociation (electrolytes) | i > 1 | NaCl → Na⁺ + Cl⁻ → i = 2 (ideal); KCl, MgCl₂ |
| Association | i < 1 | Acetic acid in benzene: 2CH₃COOH ⇌ (CH₃COOH)₂ → i = 0.5 |
Modified formula: ΔT_f = i · K_f · m; \(\pi = i \cdot CRT\)
For α degree of dissociation into n ions: \(i = 1 + \alpha(n - 1)\)
| Law | Relation | Constant |
|---|---|---|
| Boyle's Law | PV = constant → P₁V₁ = P₂V₂ | T, n fixed |
| Charles's Law | V/T = constant → V₁/T₁ = V₂/T₂ | P, n fixed |
| Gay-Lussac's Law | P/T = constant → P₁/T₁ = P₂/T₂ | V, n fixed |
| Avogadro's Law | V ∝ n at constant T, P | T, P fixed |
| Combined Gas Law | PV/T = constant → \(P_{1}V_{1}/T_{1} = P_{2}V_{2}/T_{2}\) | n fixed |
PV = nRT
R = 8.314 J mol⁻¹ K⁻¹ = 0.0821 L·atm mol⁻¹ K⁻¹ = 2 cal mol⁻¹ K⁻¹
Molar mass from ideal gas: \(M = mRT/PV = \rho RT/P\) (where ρ = density, m = mass)
Dalton's Law of Partial Pressures: P_total = p₁ + p₂ + p₃ + … ; pᵢ = χᵢ · P_total
u_rms = \(\sqrt{3RT/M}\) (root mean square)
ū = \(\sqrt{8RT/(\pi M)}\) (mean/average)
u_mp = \(\sqrt{2RT/M}\) (most probable)
Ratio: \(u_{mp} : \bar{u} : u_{rms} = \sqrt2 : \sqrt{8/\pi} : \sqrt3 = 1 : 1.128 : 1.225\)
All \(\propto \sqrt T\) and \(\propto 1/\sqrt M\)
Rate of diffusion \(\propto 1/\sqrt M\) (at same T and P)
$$ r_{1}/r_{2} = \sqrt{M_{2}/M_{1}} = \sqrt{d_{2}/d_{1}} $$
Used to compare diffusion rates of gases and to identify unknown gases by rate comparison.
$$ \lambda = RT / (\sqrt2 \cdot \pi d^{2} \cdot N_{a} \cdot P) $$
λ ↑ as P ↓ (fewer collisions) and T ↑
λ ↓ as molecular size (d) ↑
Collision frequency \(Z \propto P^2/\sqrt T\)
Ideal gas deviates at high P and low T. Two corrections:
$$ (P + an^{2}/V^{2})(V - nb) = nRT $$
| Constant | Corrects for | Effect |
|---|---|---|
| a (pressure correction) | Intermolecular attractions | Observed P < ideal; add a/V² to correct |
| b (volume correction) | Finite volume of molecules | Observed V > free space; subtract nb |
Compressibility factor Z = PV/nRT
| Z value | Behaviour | Dominant effect |
|---|---|---|
| Z = 1 | Ideal gas | — |
| Z < 1 (low P) | More compressible than ideal | Intermolecular attractions (a dominates) |
| Z > 1 (high P) | Less compressible than ideal | Finite volume of molecules (b dominates) |
Boyle temperature T_B = a/(Rb) — temperature at which a real gas behaves ideally over a wide pressure range (Z ≈ 1).
Surface chemistry deals with phenomena occurring at interfaces — solid-gas, solid-liquid, and liquid-liquid — including adsorption, catalysis, colloids, and emulsions.
Adsorption: accumulation of a substance (adsorbate) on the surface of another (adsorbent). Surface phenomenon.
Absorption: uniform distribution throughout the bulk of the absorbing material.
Sorption: both adsorption and absorption occurring simultaneously.
| Property | Physisorption | Chemisorption |
|---|---|---|
| Force | van der Waals | Chemical bonds |
| ΔH | 20–40 kJ/mol | 40–400 kJ/mol |
| Reversibility | Reversible | Irreversible |
| Specificity | Non-specific | Highly specific |
| Layers | Multilayer | Monolayer only |
| Temp effect | Decreases with T | Initially increases, then decreases |
Freundlich isotherm: x/m = k·\(P^{1/n}\) (empirical; n > 1)
log(x/m) = log k + (1/n) log P — straight line graph; 1/n = slope
Langmuir isotherm: P/(x/m) = 1/(ab) + P/a — monolayer, homogeneous surface
At low P: x/m ∝ P (linear); At high P: x/m → constant (saturation)
Catalyst and reactants in the same phase.
Example: SO₂ oxidation — 2SO₂ + O₂ → 2SO₃ (catalyst: NO in gas phase)
Mechanism: catalyst forms intermediate compound with reactant; intermediate decomposes to give product and regenerate catalyst
Ea is lowered → rate increases without changing thermodynamics.
Catalyst and reactants in different phases. Reaction occurs on catalyst surface.
Steps: (1) Diffusion to surface → (2) Adsorption → (3) Reaction → (4) Desorption → (5) Diffusion away
Examples: Haber process (Fe catalyst); Contact process (V₂O₅); Hydrogenation of oils (Ni)
Promoters: enhance catalyst activity (e.g., Mo in Haber process)
Poisons: reduce activity (e.g., CO poisons Fe in Haber process)
Biological catalysts; highly specific (lock-and-key model).
Properties: colloidal in nature; specific; greatly accelerate reaction; optimum temperature and pH; destroyed by high T or pH extremes
Michaelis-Menten kinetics: rate = \(V_{max}\)[S] / (\(K_{m}\) + [S])
At [S] << \(K_{m}\): first order; At [S] >> \(K_{m}\): zero order (saturation)
Particle size: 1–1000 nm (intermediate between true solution and suspension)
| Type | Particle size | Visibility |
|---|---|---|
| True solution | <1 nm | Not visible |
| Colloidal sol | 1–1000 nm | Ultramicroscope |
| Suspension | >1000 nm | Naked eye |
By interaction with medium:
Dispersed phase / Dispersion medium combinations:
Dispersion methods: Bredig's arc (metals), peptization (adding electrolyte to precipitate)
Condensation methods: double decomposition (As₂S₃ from H₃AsO₃ + H₂S), reduction (Au/Ag sol), oxidation
Purification:
O/W (oil in water): oil droplets dispersed in water — milk, cold cream. Emulsifier: soap, protein
W/O (water in oil): water droplets dispersed in oil — butter, cream. Emulsifier: heavy metal soaps
Emulsifiers: stabilise emulsions by adsorbing at interface and reducing surface tension
Demulsification: breaking emulsion by heating, centrifugation, adding demulsifier, or electric field