Chemical Kinetics
Apply concepts from Chemical Kinetics to problem-solving. Focus on numerical practice and real-world applications.
Concept Core
Chemical kinetics deals with reaction rates and the factors that influence them. The rate of reaction for aA + bB → cC + dD is: rate = −(1/a)d[A]/dt = −(1/b)d[B]/dt = (1/c)d[C]/dt = (1/d)d[D]/dt. Factors affecting rate include concentration, temperature (a 10°C rise roughly doubles the rate), pressure (for gases), catalyst, surface area, and nature of reactants.
The rate law is experimentally determined: rate = k[A]^m[B]^n, where m and n are orders (NOT stoichiometric coefficients). Overall order = m + n. Units of k depend on order: for nth order, k has units (mol/L)^(1−n) × s⁻¹. So: zero order = mol/(L·s), first order = s⁻¹, second order = L/(mol·s).
Order vs Molecularity — critical distinction: Order is experimental, can be 0, fractional, or integer, applies to overall or elementary reactions, and can change with conditions. Molecularity is theoretical, always a positive integer (1, 2, or 3), applies only to elementary steps, and cannot change. The rate-determining step (slowest step) controls the overall rate.
Zero order kinetics: Integrated equation: [A] = [A]₀ − kt (linear decrease) Half-life: t₁/₂ = [A]₀/(2k) — depends on initial concentration Example: NH₃ decomposition on Pt surface at high pressure.
First order kinetics: Integrated equation: ln[A] = ln[A]₀ − kt, or equivalently k = (2.303/t) log([A]₀/[A]) Half-life derivation: At t₁/₂, [A] = [A]₀/2. Substituting: k × t₁/₂ = ln([A]₀/([A]₀/2)) = ln 2 = 0.693. Therefore t₁/₂ = 0.693/k — independent of initial concentration. Examples: radioactive decay, H₂O₂ decomposition, N₂O₅ decomposition.
Solved Example 1: First-order reaction with k = 6.93 × 10⁻³ s⁻¹. t₁/₂ = 0.693/k = 0.693/(6.93 × 10⁻³) = 100 s For 75% completion: [A] = 0.25[A]₀ t = (2.303/k) × log([A]₀/0.25[A]₀) = (2..93×10⁻³) × log 4 = 332.3 × 0.602 = 200 s = 2 × t₁/₂ ✓
Pseudo first-order reactions occur when one reactant is in large excess, making the reaction appear first order. Example: hydrolysis of ethyl acetate (SMILES: CC(=O)OCC) in excess water: CH₃COOC₂H₅ + H₂O → CH₃COOH + C₂H₅OH (SMILES products: CC(=O)O + CCO).
Arrhenius equation: k = Ae^(−Ea/RT), where A = frequency/pre-exponential factor, Ea = activation energy. Two-temperature form: log(k₂/k₁) = (Ea/2.303R)(1/T₁ − 1/T₂) Graph: ln k vs 1/T gives a straight line with slope = −Ea/R.
Solved Example 2: k at 300 K = 2.5 × 10⁻³ s⁻¹, k at 310 K = 5.0 × 10⁻³ s⁻¹. Find Ea. log(k₂/k₁) = (Ea/2.303R)(1/T₁ − 1/T₂) log(5.0×10⁻³/2.5×10⁻³) = (Ea/(2.303 × 8.314))( − ) 0.301 = (Ea/19.147)() = Ea × 5.616 × 10⁻⁶ Ea = 0..616 × 10⁻⁶ = 53,596 J/mol ≈ 53.6 kJ/mol
Activation energy: Ea(forward) − Ea(backward) = ΔH. A catalyst lowers Ea by providing an alternative pathway but does NOT change ΔH or the equilibrium constant.
Solved Example 3: Zero-order reaction, k = 0.01 mol/(L·s), [A]₀ = 0.5 M. Time for complete decomposition: t = [A]₀/k = 0..01 = 50 s t₁/₂ = [A]₀/(2k) = 0.5/(2 × 0.01) = 25 s
Dimensional analysis for rate constant units: Rate = k[A]^n → mol/(L·s) = k × (mol/L)^n → k = (mol/L)^(1−n) × s⁻¹ ✓
The key testable concept is first-order half-life calculations (t₁/₂ = 0.693/k, independent of concentration) and Arrhenius equation activation energy determination.
Key Testable Concept
The key testable concept is **first-order half-life calculations (t₁/₂ = 0.693/k, independent of concentration) and Arrhenius equation activation energy determination**.
Comparison Tables
A) Order Comparison
| Property | Zero Order | First Order | Second Order |
|---|---|---|---|
| Rate law | rate = k | rate = k[A] | rate = k[A]² |
| Integrated equation | [A] = [A]₀ − kt | ln[A] = ln[A]₀ − kt | 1/[A] = 1/[A]₀ + kt |
| Half-life (t₁/₂) | [A]₀/(2k) | 0.693/k | 1/(k[A]₀) |
| t₁/₂ depends on | [A]₀ (proportional) | Independent of [A]₀ | [A]₀ (inversely) |
| Units of k | mol/(L·s) | s⁻¹ | L/(mol·s) |
| Linear plot | [A] vs t | ln[A] vs t | 1/[A] vs t |
| Slope of linear plot | −k | −k | k |
B) Order vs Molecularity
| Feature | Order | Molecularity |
|---|---|---|
| Determination | Experimental | Theoretical (from mechanism) |
| Value range | 0, fractional, integer | Only positive integer (1, 2, 3) |
| Applies to | Overall and elementary reactions | Elementary reactions only |
| Can change? | Yes (with conditions) | No (fixed for a given step) |
| Zero value | Possible (zero order) | Not possible |
| Fractional value | Possible (e.g., 1.5) | Not possible |
C) Arrhenius Equation Forms
| Form | Equation | Use Case | Graph |
|---|---|---|---|
| Exponential | k = Ae^(−Ea/RT) | Direct calculation | k vs T (exponential curve) |
| Logarithmic (ln) | ln k = ln A − Ea/RT | Graph: slope = −Ea/R | ln k vs 1/T (straight line) |
| Logarithmic (log) | log k = log A − Ea/(2.303RT) | Numerical calculations | log k vs 1/T (straight line) |
| Two-temperature | log(k₂/k₁) = (Ea/2.303R)(1/T₁ − 1/T₂) | Finding Ea from 2 data points | — |
D) Common Reactions by Order
| Reaction | Order | Example | SMILES |
|---|---|---|---|
| NH₃ decomposition on Pt (high P) | Zero | 2NH₃ → N₂ + 3H₂ on Pt | N, [H][H] |
| Radioactive decay | First | ²³⁸U → ²³⁴Th + ⁴He | — |
| H₂O₂ decomposition | First | 2H₂O₂ → 2H₂O + O₂ | OO |
| N₂O₅ decomposition | First | 2N₂O₅ → 4NO₂ + O₂ | — |
| Ethyl acetate hydrolysis (excess H₂O) | Pseudo first | CH₃COOC₂H₅ + H₂O → CH₃COOH + C₂H₅OH | CC(=O)OCC |
| NO₂ decomposition | Second | 2NO₂ → 2NO + O₂ | — |
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