Heterogeneous catalysis

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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.

Contents

[edit] Concepts

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.

[edit] Classes of heterogeneous catalysts

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

Reacting phases Examples 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

[edit] Examples

Many examples exist, the table emphasizes large-scale industrial processes,[2] 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 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

[edit] Other examples

Nitrile hydrogenation
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. This process can occur with any of the hydrocarbons, but most commonly is performed with petrol or diesel.

2 C6H6 + 15 O2 → 12 CO2 + 6 H2O
Ethylbenzene + 1/2 O2Styrene + H2O
Acrolein + 1/2 O2Acrylic acid

[edit] See also

[edit] References

  1. ^ Gadi Rothenberg, Catalysis: Concepts and green applications, Wiley-VCH: Weinheim, ISBN 978-3-527-31824-7
  2. ^ Zhen Ma, Francisco Zaera "Heterogeneous Catalysis by Metals" in Encyclopedia of Inorganic Chemistry, 2006, John Wiley. doi:10.1002/0470862106.ia084
  3. ^ Organic Syntheses, Coll. Vol. 3, p.720 (1955); Vol. 23, p.71 (1943). http://orgsynth.org/orgsyn/pdfs/CV4P0603.pdf
  4. ^ Heitbaum, Glorius, Escher, Asymmetric heterogeneous catalysis, Angew. Chem. Int. Ed. 2006, 45, 4732.
  5. ^ 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. doi:10.1126/science.1161916. 
  6. ^ 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. 
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