Part of PC-08 — Chemical Kinetics

Chemical Kinetics — Industrial & Applied Connections

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Haber Process (N2+3H22NH3\text{N}_2 + 3\text{H}_2 \rightarrow 2\text{NH}_3): Iron catalyst with K2O/Al2O3\text{K}_2\text{O}/\text{Al}_2\text{O}_3 promoters lowers EaE_a, dramatically increasing the rate at industrially manageable temperatures (~450 °C, 200 atm). Without the catalyst the reaction is practically too slow at any accessible temperature. Kinetics determines the optimal operating conditions — high pressure increases rate and shifts equilibrium toward product; temperature is a compromise between rate (needs heat) and equilibrium yield (exothermic, favoured at low T).

Contact Process for H2SO4\text{H}_2\text{SO}_4 (SO2SO3\text{SO}_2 \rightarrow \text{SO}_3): V2O5\text{V}_2\text{O}_5 catalyst. The catalyst undergoes a cyclic mechanism: V5+\text{V}^{5+} oxidises SO2\text{SO}_2 to SO3\text{SO}_3 and is reduced to V4+\text{V}^{4+}, then re-oxidised by O2\text{O}_2. This is an example of a homogeneous intermediate mechanism — the catalyst participates in the reaction but is regenerated.

Radioactive Decay (first order): 238U234Th+4He^{238}\text{U} \rightarrow ^{234}\text{Th} + ^4\text{He}; t1/2=4.5×109t_{1/2} = 4.5 \times 10^9 years. Carbon-14 dating exploits t1/2=5730t_{1/2} = 5730 years for 14C^{14}\text{C} to determine the age of organic material. The first-order nature (concentration-independent half-life) is what makes the dating reliable.

H2O2\text{H}_2\text{O}_2 Decomposition: 2H2O22H2O+O22\text{H}_2\text{O}_2 \rightarrow 2\text{H}_2\text{O} + \text{O}_2 — first-order in dilute solution. Used in rocket propulsion (high-test peroxide) and as a bleaching agent. Catalysed by MnO2\text{MnO}_2, KI\text{KI}, or enzymes (catalase in blood).

Enzyme Kinetics (Michaelis–Menten): At low substrate concentration, enzyme reactions follow first-order kinetics; at saturation (enzyme fully occupied), they become zero order in substrate — a direct application of surface-saturation kinetics.

Ozone Depletion: CFCshνCl\text{CFCs} \xrightarrow{h\nu} \text{Cl}^{\bullet}; then Cl+O3ClO+O2\text{Cl}^{\bullet} + \text{O}_3 \rightarrow \text{ClO}^{\bullet} + \text{O}_2. Cl acts as a homogeneous catalyst — it is consumed in one step but regenerated in another, lowering the activation energy for O3\text{O}_3 decomposition. Kinetics here determines the stratospheric lifetime of ozone.

Food Preservation: Low temperature slows spoilage reactions (microbial metabolism, lipid oxidation) because k=AeEa/RTk = Ae^{-E_a/RT} — reducing TT reduces kk exponentially. Refrigeration at 4 °C vs 25 °C slows reactions by a factor of roughly 22.142^{2.1} \approx 4 based on the temperature coefficient.

Catalytic Converters: Pt/Pd/Rh catalyst converts CO\text{CO}, unburnt hydrocarbons, and NOx\text{NO}_x in exhaust. Zero-order behaviour can occur at high exhaust concentrations when catalyst surface is saturated — explaining why efficiency drops under rich fuel conditions.

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