Heterogeneous catalysis

From Wikipedia, the free encyclopedia
  (Redirected from Heterogeneous catalyst)
Jump to: navigation, search
Hydrogenation of ethene on a solid surface

In chemistry, heterogeneous catalysis refers to the form of catalysis where the phase of the catalyst differs from that of the reactants. Phase here refers not only to solid, liquid, vs gas, but also immiscible liquids, e.g. oil and water. The great majority of practical heterogeneous catalysts are solids and the great majority of reactants are gases or liquids.[1] Heterogeneous catalysis is of paramount importance in many areas of the chemical and energy industries. Heterogeneous catalysis has attracted Nobel prizes for Fritz Haber and Carl Bosch in 1918, Irving Langmuir in 1932, and Gerhard Ertl in 2007.[2][3][4][5][6]


Adsorption is commonly an essential first step in heterogeneous catalysis. Adsorption is when a molecule in the gas phase or in solution binds to atoms on the solid or liquid surface. The molecule that is binding is called the adsorbate, and the surface to which it binds is the adsorbent. The process of the adsorbate binding to the adsorbent is called adsorption. The reverse of this process (the adsorbate splitting from adsorbent) is called desorption. In terms of catalyst support, the catalyst is the adsorbate and the support is the adsorbent.

Types of adsorption[edit]

Two types of adsorption are recognized in heterogeneous catalysis, although many processes fall into an ambiguous range between the two extremes. In the first type, physisorption, induces only small changes to the electronic structure of the adsorbate. Typical energies for physisorption are from 2 to 10 kcal/mol. The second type is chemisorption, in which the adsorbate is strongly perturbed, often with bond-breaking. Energies for typical chemisorptions range from 15 to 100 kcal/mol.

For physisorption, adsorbate is attracted to the surface atoms by van der Waals forces. A mathematical model for physisorption was developed by London to predict the energies of basic physisorption of non-polar molecules. The analysis of physisorption for polar or ionic species is more complex.

Chemisorption results in the sharing of electrons between the adsorbate and the adsorbent. Chemisorption is traditionally described by the Lennard-Jones potential, which considers various cases, two of which are.

  • Molecular adsorption, where the adsorbate remains intact. An example is alkene binding by platinum.
  • In dissociation adsorption, one or more bonds break concomitantly with adsorption. In this case the barrier to dissociation affects the rate of adsorption. An example of this the binding of H2, where the H-H bond is broken upon adsorption [7] by hydrogen spillover.

Surface Reactions[edit]

With catalyst supports, the reaction that occurs often occurs on the surface of either the catalyst or the support. In terms of surface reactions there are three mechanisms.

  • Langmuir-Hinshelwood mechanism. The two molecules A and B both adsorb to the surface. While adsorbed to the surface, the A and B "meet," bond, and then the new molecule A-B desorbs.
  • Rideal-Eley mechanism. One of the two molecules, A, adsorbs to the surface. The second molecule, B, meets A on the surface, having never adsorbed to the surface, and they react and bind. Then the newly formed A-B desorbs.
  • Precursor mechanism. One of the two molecules, A, is adsorbed on the surface. The second molecule, B, collides with the surface, forming a mobile precursor state. The molecule B then collides with A on the surface, they react, bind and the new molecule desorbs.

Any surface reaction can be described as following one of these mechanisms, or some combination of these mechanisms. In addition, all of these above mechanisms can occur in reverse. In general, the pathway for a reaction on a surface is as follows. First the reactants adsorb onto the surface. Through a series of bonds being formed and being broken, adsorbed intermediates are produced and destroyed. Then the final product(s) is produced and it desorbs from the solid. Most metal surface reaction occur by chain propagation.[7]


In heterogeneous catalysis, the reactants diffuse to the catalyst surface and adsorb onto it, via the formation of chemical bonds. After reaction, the products desorb from the surface and diffuse away. Understanding the transport phenomena and surface chemistry such as dispersion is important. If diffusion rates are not taken into account, the reaction rates for various reactions on surfaces depend solely on the rate constants and reactant concentrations. For solid heterogeneous catalysts, the surface area of the catalyst is critical since it determines the availability of catalytic sites. Surface areas can be large, for example some mesoporous silicates have areas of 1000 m2/g. The most common approach to maximizing surface area is by the use of catalyst supports, which are the materials over which the catalysts are spread.

Classes of heterogeneous catalysts[edit]

Although the majority of heterogeneous catalysts are solids, many variations exist.

Reacting phases Examples given Comment
solid + gas Ammonia synthesis from N2 + H2 over iron catalysts
solid + solution hydrogenation of fatty acids with nickel used for the production of margarine
immiscible liquid phases hydroformylation of propene catalyst in aqueous phase, reactants and products mainly in nonaqueous phase


Many examples exist, the table emphasizes large-scale industrial processes,[8] although diverse examples are known.

Process Reactants, product(s) Catalyst Comment
Sulfuric acid synthesis (Contact process) SO2 + O2, SO3 vanadium oxides hydration of SO3 gives H2SO4
Ammonia synthesis (Haber–Bosch process) N2 + H2, NH3 iron oxides on alumina(Al2O3) consumes 1% of world's industrial energy budget
Nitric acid synthesis (Ostwald process) NH3 + O2, HNO3 unsupported Pt-Rh gauze direct routes from N2 are uneconomical
Hydrogen production by Steam reforming CH4 + H2O, H2 + CO2 Nickel or K2O Greener routes to H2 by water splitting actively sought
Ethylene oxide synthesis C2H4 + O2, C2H4O silver on alumina, with many promotors poorly applicable to other alkenes
Hydrogen cyanide synthesis (Andrussov oxidation) NH3 + O2 + CH4, HCN Pt-Rh Related ammoxidation process converts hydrocarbons to nitriles
Olefin polymerization Ziegler–Natta polymerization propylene, polypropylene TiCl3 on MgCl2 many variations exist, including some homogeneous examples
Desulfurization of petroleum (hydrodesulfurization) H2 + R2S (idealized organosulfur impurity), RH + H2S Mo-Co on alumina produces low-sulfur hydrocarbons, sulfur recovered via the Claus process

Other examples[edit]

Nitrile hydrogenation
The oxidation of carbon monoxide to carbon dioxide:
2CO(g) + O2(g) → 2CO2(g)
The reduction of nitrogen monoxide back to nitrogen:
2NO(g) + 2CO(g) → N2(g) + 2CO2(g)
The oxidation of hydrocarbons to water and carbon dioxide:
2 C6H6 + 15 O2 → 12 CO2 + 6 H2O
This process can occur with any of the hydrocarbons, but most commonly is performed with petrol or diesel.
Ethylbenzene + 1/2 O2Styrene + H2O
Acrolein + 1/2 O2Acrylic acid
  • Gas streams with strongly nonequilibrium gas phase concentrations can be achieved via epicatalysis[13]

See also[edit]


  1. ^ Gadi Rothenberg, Catalysis: Concepts and green applications, Wiley-VCH: Weinheim, ISBN 978-3-527-31824-7
  2. ^ Swathi, R.S. and Sebastian, K.L. Molecular mechanism of heterogeneous catalysis. Resonance Vol. 13 Issue 6 (2008) p. 548-560.
  3. ^ Fritz Haber - Biographical
  4. ^ Carl Bosch - Biographical
  5. ^ Irving Langmuir - Biographical
  6. ^ Gerhard Ertl - Biographical
  7. ^ a b R. I. Masel, “Principles of Adsorption and Reaction on Solid Surfaces”, Wiley Series in Chemical Engineering, Wiley-Interscience, New York, USA, 1996, ISBN 978-0-471-30392-3
  8. ^ Zhen Ma, Francisco Zaera "Heterogeneous Catalysis by Metals" in Encyclopedia of Inorganic Chemistry, 2006, John Wiley. doi:10.1002/0470862106.ia084
  9. ^ Organic Syntheses, Coll. Vol. 3, p.720 (1955); Vol. 23, p.71 (1943). http://wayback.archive.org/web/20120315000000*/http://orgsynth.org/orgsyn/pdfs/CV4P0603.pdf
  10. ^ Heitbaum, Glorius, Escher, Asymmetric heterogeneous catalysis, Angew. Chem. Int. Ed. 2006, 45, 4732.
  11. ^ Zhang, J.; Liu, X.; Blume, R.; Zhang, A.; Schlögl, R.; Su, D. S. (2008). "Surface-Modified Carbon Nanotubes Catalyze Oxidative Dehydrogenation of n-Butane". Science. 322 (5898): 73–77. Bibcode:2008Sci...322...73Z. PMID 18832641. doi:10.1126/science.1161916. 
  12. ^ Frank, B.; Blume, R.; Rinaldi, A.; Trunschke, A.; Schlögl, R. (2011). "Oxygen Insertion Catalysis by sp2 Carbon". Angew. Chem. Int. Ed. 50 (43): 10226–10230. doi:10.1002/anie.201103340. 
  13. ^ Sheehan, D.P., Nonequilibrium heterogeneous catalysis in the long mean-free-path regime, Phys. Rev. E 88 032125 (2013).