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Chemistry · Ch 10 — Surface Chemistry

Theories of Catalysis

10.2.2

Theories of Catalysis

For any chemical reaction to occur, the reactant molecules must first be activated into an 'activated complex', and the minimum energy required to bring the reactants to this activated state is the activation energy. Activation energy can, in principle, always be supplied by simply raising the reaction temperature; a catalyst instead achieves the same activation at a LOWER temperature — in other words, a catalyst works by lowering the activation energy needed. Since lowering the activation energy allows a much larger fraction of reactant molecules to possess enough energy to react at a given temperature, the overall rate of reaction increases. Two complementary theories explain exactly how a catalyst manages to lower this barrier: the intermediate compound formation theory, which applies mainly to homogeneous catalysis, and the adsorption theory, which applies to heterogeneous (contact) catalysis.

The intermediate compound formation theory. Here, a catalyst C works by combining with one of the reactants to form a short-lived intermediate compound, which then reacts further with the remaining reactant(s) to give the final product, regenerating the catalyst unchanged at the end: for the overall reaction A+B→ABA + B \rightarrow AB, the catalysed pathway instead runs as A+C→ACA + C \rightarrow AC (the intermediate) followed by AC+B→AB+CAC + B \rightarrow AB + C. Crucially, the activation energies of these two catalysed steps are each LOWER than the activation energy of the original, uncatalysed single step A+B→ABA + B \rightarrow AB — it is exactly this lower activation-energy pathway, made available by the intermediate's formation and decomposition, that accelerates the overall reaction. Four worked illustrations from real chemistry: (1) in the Friedel–Crafts reaction of benzene with methyl chloride over anhydrous AlCl3\text{AlCl}_3, the catalyst first forms the intermediate [CH3+][AlCl4−][\text{CH}_3^+][\text{AlCl}_4^-] from CH3Cl+AlCl3\text{CH}_3\text{Cl} + \text{AlCl}_3, which then reacts with benzene to give toluene, HCl, and regenerated AlCl3\text{AlCl}_3; (2) the thermal decomposition of KClO3\text{KClO}_3 catalysed by MnO2\text{MnO}_2 proceeds via the intermediate KMnO4\text{KMnO}_4 (formed from KClO3\text{KClO}_3 and MnO2\text{MnO}_2), which decomposes to release O2\text{O}_2 and regenerate MnO2\text{MnO}_2; (3) the formation of water from H2\text{H}_2 and O2\text{O}_2 catalysed by copper proceeds via the intermediate Cu2O\text{Cu}_2\text{O}; and (4) the oxidation of HCl by air catalysed by CuCl2\text{CuCl}_2 proceeds via the intermediates Cu2Cl2\text{Cu}_2\text{Cl}_2 and Cu2OCl2\text{Cu}_2\text{OCl}_2. This theory successfully explains both the SPECIFICITY of a given catalyst (since only certain reactants can chemically combine with it to form the necessary intermediate) and the observed increase in reaction rate with increasing catalyst concentration (more catalyst means more intermediate can form). Its limitations, however, are real: it fails to explain the action of catalytic poisons and promoters/activators, and it cannot account for the mechanism of HETEROGENEOUS catalysed reactions, where the catalyst and reactants are not even in the same phase to form a chemical intermediate in the first place.

The adsorption theory. Langmuir explained heterogeneous catalysis — also called contact catalysis for exactly this reason — on the basis of adsorption: the reactant molecules are first adsorbed onto the catalyst's surface, forming an activated complex there, which then decomposes to release the product. The full mechanism runs through five steps: (1) reactant molecules diffuse from the bulk gas or solution phase to the catalyst surface; (2) the reactant molecules are adsorbed onto the catalyst surface; (3) the adsorbed molecules are activated and form an activated complex on the surface, which decomposes to give the products; (4) the product molecules are desorbed from the surface; and (5) the product molecules then diffuse away from the surface back into the bulk phase. …

Figure fig-10.3Figure 10.3 — Hydrogenation of ethylene on a nickel surface

What this figure shows. The diagram shows ethylene (CH2=CH2\text{CH}_2=\text{CH}_2) approaching a nickel metal surface and being adsorbed onto it. On adsorption, the double bond between the two carbon atoms weakens and partially breaks, freeing bonding capacity at the carbon atoms; hydrogen molecules are similarly adsorbed onto adjacent sites on the same nickel surface and are split into individual hydrogen atoms held to the metal. Because both reactants are now held close together on the same surface in an activated, bond-weakened state, hydrogen atoms migrate across the surface and add on to the activated ethylene, forming ethane (CH3−CH3\text{CH}_3-\text{CH}_3), which then desorbs from the nickel surface — freeing the active …

Figure fig-10.4Figure 10.4 — Finely divided catalyst is more effective due to increase in active centres

What this figure shows. The figure contrasts a single large block of catalyst with the same total mass of catalyst broken up into many small particles. Because the surface of a catalyst is never perfectly smooth — it carries steps, cracks and corners where atoms are co-ordinatively unsaturated and therefore carry residual force of attraction — these irregular locations, called active centres, are where adsorption and activation of the reactant actually occur. Reducing particle size increases the total exposed surface area for the same mass of catalyst, which multiplies the number of active centres available and hence increases the observed rate of the catalysed reaction — exactly why catalysts are used in finely divided or powde …