States of Matter
Build conceptual understanding of States of Matter. Focus on definitions, mechanisms, and core principles.
Concept Core
Matter exists in three principal states — solid, liquid, and gas — governed by the balance between kinetic energy and intermolecular forces. Intermolecular interactions increase in strength: dispersion (London) forces < dipole-dipole < hydrogen bonding. Stronger interactions lead to higher boiling points and lower vapour pressures.
Gas laws describe ideal gas behavior:
- Boyle's law: PV = constant (at constant T and n)
- Charles's law: V/T = constant (at constant P and n)
- Gay-Lussac's law: P/T = constant (at constant V and n)
- Avogadro's law: V ∝ n (at constant T and P)
These combine into the ideal gas equation: PV = nRT, where R = 0.0821 L·atm/(mol·K) = 8.314 J/(mol·K).
Dalton's law of partial pressures: = p₁ + p₂ + ...; partial pressure = × ( = mole fraction).
Graham's law of diffusion: r₁/r₂ = √(M₂/M₁) — rate inversely proportional to square root of molar mass.
Solved Example 1: Volume of 2 mol ideal gas at 27°C and 2 atm. V = nRT/P = (2 × 0.0821 × 300)/2 Dimensional analysis: mol × L·atm/(mol·K) × K / atm = L ✓ V = 24.63 L
Solved Example 2: Rate of diffusion of gas A is twice that of gas B ( = 64 g/mol). Find . = √() → 2 = √(64/) → 4 = 64/ → = 16 g/mol (likely CH₄)
Solved Example 3: Total pressure of 2 mol N₂ + 3 mol O₂ in 10 L at 300 K. = 5 mol; P = nRT/V = (5 × 0.0821 × 300)/10 = 12.315 atm ₂ = () × 12.315 = 4.926 atm; ₂ = () × 12.315 = 7.389 atm ✓
Kinetic molecular theory postulates random motion, elastic collisions, negligible intermolecular forces, and KE ∝ T. From PV = ()mnc², combined with PV = nRT:
Derivation of : PV = ()Nmc² and PV = nRT, so ()Nmc² = nRT.
Since N = nNₐ and m = M/Nₐ: ()(nNₐ)(M/Nₐ)c² = nRT → c² = 3RT/M → = √(3RT/M).
Molecular speeds: = √(3RT/M), = √(8RT/πM), = √(2RT/M). Order: > > (ratio 1.224 : 1.128 : 1 relative to ).
Real gases deviate from ideal behavior at high pressure and low temperature. The van der Waals equation accounts for this: (P + a/V²)(V − b) = RT (per mole), where 'a' corrects for intermolecular attraction and 'b' for molecular volume.
The compressibility factor Z = PV/(nRT): Z = 1 (ideal), Z < 1 (attractive forces dominate, gas more compressible than ideal), Z > 1 (repulsive forces dominate, gas less compressible). Exception: H₂ and He show Z > 1 at all pressures because their 'a' is very small.
Boyle temperature = a/(Rb) — the temperature at which a real gas behaves ideally over a wide pressure range.
Critical constants: = 8a/(27Rb), = a/(27b²), = 3b; relationship: = 3R/8.
Liquefaction requires high pressure and low temperature (below ). The Joule-Thomson effect cools gases on expansion below the inversion temperature. Andrews isotherms for CO₂ ( = 31.1°C) illustrate gas-liquid-supercritical behavior.
Liquid state properties: Vapour pressure increases with temperature (more molecules escape); surface tension decreases with temperature (weaker cohesive forces); viscosity decreases with temperature for liquids (more kinetic energy overcomes intermolecular forces).
The key testable concept is ideal gas equation numericals, Graham's law calculations, and the relationship between molecular speeds ( > > ).
Key Testable Concept
The key testable concept is **ideal gas equation numericals, Graham's law calculations, and the relationship between molecular speeds (v_rms > v_avg > v_mp)**.
Comparison Tables
A) Gas Laws
| Law | Statement | Formula | Constant Conditions | Graph Shape |
|---|---|---|---|---|
| Boyle's | Volume inversely proportional to pressure | PV = const or P₁V₁ = P₂V₂ | T, n constant | PV vs P: horizontal line; P vs V: hyperbola |
| Charles's | Volume directly proportional to temperature | V/T = const or V₁/T₁ = V₂/T₂ | P, n constant | V vs T(K): straight line through origin |
| Gay-Lussac's | Pressure directly proportional to temperature | P/T = const or P₁/T₁ = P₂/T₂ | V, n constant | P vs T(K): straight line through origin |
| Avogadro's | Volume proportional to moles | V ∝ n or V₁/n₁ = V₂/n₂ | T, P constant | V vs n: straight line through origin |
| Combined | Combines Boyle, Charles, Gay-Lussac | P₁V₁/T₁ = P₂V₂/T₂ | n constant | — |
| Ideal gas | General equation | PV = nRT | None (all variable) | — |
B) Molecular Speeds
| Speed | Formula | Ratio (relative to ) | Physical Meaning |
|---|---|---|---|
| Most probable () | √(2RT/M) | 1.000 | Speed possessed by maximum number of molecules |
| Average () | √(8RT/πM) | 1.128 | Arithmetic mean of all molecular speeds |
| Root mean square () | √(3RT/M) | 1.224 | Square root of mean of squares of speeds |
| Order | < < | 1 : 1.128 : 1.224 | Always in this order at any temperature |
C) Ideal vs Real Gas
| Property | Ideal Gas | Real Gas | Condition for Ideal Behavior |
|---|---|---|---|
| Intermolecular forces | None | Present (attractive + repulsive) | Low pressure, high temperature |
| Molecular volume | Negligible | Finite (correction 'b') | Very low pressure |
| Obeys gas laws | Perfectly | Deviates at high P, low T | T >> , P → 0 |
| Equation | PV = nRT | (P + an²/V²)(V − nb) = nRT | — |
| Compressibility factor Z | Always 1 | Z < 1 or Z > 1 | Z → 1 at low P, high T |
| Liquefaction | Cannot be liquefied | Can be liquefied below | — |
D) Liquid State Properties
| Property | Definition | Temperature Effect | Example |
|---|---|---|---|
| Vapour pressure | Pressure exerted by vapour in equilibrium with liquid | Increases with T | Water: 17.5 mmHg (20°C) → 760 mmHg (100°C) |
| Surface tension | Force per unit length at liquid surface | Decreases with T | Water has high surface tension (H-bonding) |
| Viscosity | Resistance to flow | Decreases with T (liquids) | Glycerol > water > diethyl ether |
| Boiling point | T where vapour pressure = external pressure | Decreases at lower external P | Water: 100°C at 1 atm, ~70°C on Everest |
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