Reactions on surfaces
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Reactions on surfaces are reactions in which at least one of the steps of the reaction mechanism is the adsorption of one or more reactants. The mechanisms for these reactions, and the rate equations are of extreme importance for heterogeneous catalysis. Via scanning tunneling microscopy, it is possible to observe reactions at the solid|gas interface in real space, if the time scale of the reaction is in the correct range. Reactions at the solid|gas interface are in some cases related to catalysis.
If a reaction occurs through these steps:
- A + S ⇌ AS → Products
where A is the reactant and S is an adsorption site on the surface and the respective rate constants for the adsorption, desorption and reaction are k1, k−1 and k2, then the global reaction rate is:
- r is the rate, m−2s−1
- is the surface concentration of occupied sites, m−2
- is the surface coverage, dimensionless
- is the total number of sites (occupied or not), m−2
- t is time, s
- k2 is the kinetic constant for the surface reaction, s−1.
is highly related to the total surface area of the adsorbent: the greater the surface area, the more sites and the faster the reaction. This is the reason why heterogeneous catalysts are usually chosen to have great surface areas (in the order of a hundred m2/gram)
If we apply the steady state approximation to AS, then:
Note that, with , the formula was divided by .
The result is completely equivalent to the Michaelis–Menten kinetics. The rate equation is complex, and the reaction order is not clear. In experimental work, usually two extreme cases are looked for in order to prove the mechanism. In them, the rate-determining step can be:
- Limiting step: adsorption/desorption
- Limiting step: reaction
which is just Langmuir isotherm and .
Depending on the concentration of the reactant the rate changes:
- Low concentrations, then , that is to say a first order reaction in component A.
- High concentration, then . It is a zeroth order reaction in component A.
In this mechanism, suggested by Irving Langmuir in 1921 and further developed by Cyril Hinshelwood in 1926, two molecules adsorb on neighboring sites and the adsorbed molecules undergo a bimolecular reaction:
- A + S ⇌ AS
- B + S ⇌ BS
- AS + BS → Products
The rate constants are now ,,, and for adsorption/desorption of A, adsorption/desorption of B, and reaction. The rate law is:
Proceeding as before we get , where is the fraction of empty sites, so . Let us assume now that the rate limiting step is the reaction of the adsorbed molecules, which is easily understood: the probability of two adsorbed molecules colliding is low. Then , with , which is nothing but Langmuir isotherm for two adsorbed gases, with adsorption constants and . Calculating from and we finally get
The rate law is complex and there is no clear order respect to any of the reactants but we can consider different values of the constants, for which it is easy to measure integer orders:
- Both molecules have low adsorption
That means that , so . The order is one respect to both the reactants
- One molecule has very low adsorption
In this case , so . The reaction order is 1 respect to B. There are two extreme possibilities now:
- At low concentrations of A, , and the order is one respect to A.
- At high concentrations, . The order is minus one respect to A. The higher the concentration of A, the slower the reaction goes, in this case we say that A inhibits the reaction.
- One molecule has very high adsorption
One of the reactants has very high adsorption and the other one doesn't adsorb strongly.
, so . The reaction order is 1 with respect to B and −1 with respect to A. Reactant A inhibits the reaction at all concentrations.
The following reactions follow a Langmuir–Hinshelwood mechanism:
- 2 CO + O2 → 2 CO2 on a platinum catalyst.
- CO + 2H2 → CH3OH on a ZnO catalyst.
- C2H4 + H2 → C2H6 on a copper catalyst.
- N2O + H2 → N2 + H2O on a platinum catalyst.
- C2H4 + ½ O2 → CH3CHO on a palladium catalyst.
- CO + OH → CO2 + H+ + e− on a platinum catalyst.
In this mechanism, proposed in 1938 by D. D. Eley and E. K. Rideal, only one of the molecules adsorbs and the other one reacts with it directly from the gas phase, without adsorbing ("nonthermal surface reaction"):
- A(g) + S(s) ⇌ AS(s)
- AS(s) + B(g) → Products
Constants are and and rate equation is . Applying steady state approximation to AS and proceeding as before (considering the reaction the limiting step once more) we get . The order is one respect to B. There are two possibilities, depending on the concentration of reactant A:
- At low concentrations of A, , and the order is one with respect to A.
- At high concentrations of A, , and the order is zero with respect to A.
The following reactions follow an Eley–Rideal mechanism:
- C2H4 + ½ O2 (adsorbed) → H2COCH2 The dissociative adsorption of oxygen is also possible, which leads to secondary products carbon dioxide and water.
- CO2 + H2 (ads.) → H2O + CO
- 2NH3 + 1½ O2 (ads.) → N2 + 3H2O on a platinum catalyst
- C2H2 + H2 (ads.) → C2H4 on nickel or iron catalysts
- Wintterlin, J.; Völkening, S.; Janssens, T. V. W.; Zambelli, T.; Ertl, G. (1997). "Atomic and Macroscopic Reaction Rates of a Surface-Catalyzed Reaction". Science 278: 1931–4. doi:10.1126/science.278.5345.1931. PMID 9395392.
- Waldmann, T.; et al. (2012). "Oxidation of an Organic Adlayer: A Bird's Eye View". Journal of the American Chemical Society 134: 8817–8822. doi:10.1021/ja302593v.
- Keith J. Laidler and John H. Meiser Physical Chemistry (Benjamin/Cummings 1982) p.780 ISBN 0-8053-5682-7
- Grolmuss, Alexander. "A 7: Mechanismen in der heterogenen Katalyse" [A7: Mechanisms in Heterogeneous Catalysis] (in German). Archived from the original on 3 October 2016.