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Langmuir Hinshelwood

Similar equations were written by Eley [204] for the exchange of N2 with N2 catalyzed by Fe or W, and mechanisms such as Eq. XVIII-33 have come to be known as Eley-Rideal mechanisms. Mechanisms such as that of Eq. XVIII-32 are now most commonly called Langmuir-Hinshelwood mechanisms (see... [Pg.721]

Ref. 205). The two mechanisms may sometimes be distinguished on the basis of the expected rate law (see Section XVni-8) one or the other may be ruled out if unreasonable adsorption entropies are implied (see Ref. 206). Molecular beam studies, which can determine the residence time of an adsorbed species, have permitted an experimental decision as to which type of mechanism applies (Langmuir-Hinshelwood in the case of CO + O2 on Pt(lll)—note Problem XVIII-26) [207,208]. [Pg.722]

The Langmuir-Hinshelwood picture is essentially that of Fig. XVIII-14. If the process is unimolecular, the species meanders around on the surface until it receives the activation energy to go over to product(s), which then desorb. If the process is bimolecular, two species diffuse around until a reactive encounter occurs. The reaction will be diffusion controlled if it occurs on every encounter (see Ref. 211) the theory of surface diffusional encounters has been treated (see Ref. 212) the subject may also be approached by means of Monte Carlo/molecular dynamics techniques [213]. In the case of activated bimolecular reactions, however, there will in general be many encounters before the reactive one, and the rate law for the surface reaction is generally written by analogy to the mass action law for solutions. That is, for a bimolecular process, the rate is taken to be proportional to the product of the two surface concentrations. It is interesting, however, that essentially the same rate law is obtained if the adsorption is strictly localized and species react only if they happen to adsorb on adjacent sites (note Ref. 214). (The apparent rate law, that is, the rate law in terms of gas pressures, depends on the form of the adsorption isotherm, as discussed in the next section.)... [Pg.722]

If reaction XVIII-42 is the slow step, the Langmuir-Hinshelwood rate law is... [Pg.725]

Rate laws have also been observed that correspond to there being two kinds of surface, one adsorbing reactant A and the other reactant B and with the rate proportional to 5a x 5b- For traditional discussions of Langmuir-Hinshelwood rate laws, see Refs. 240-242. Many catalytic systems involve a series of intermediates, and the simplifying assumption of steady-state equilibrium is usually made. See Boudart and co-workers [243-245] for a contemporary discussion of such complexities. [Pg.728]

Derive the probable rate law for the reaction CO + j02 = CO2 as catalyzed by a metal surface assuming (a) an Eley-Rideal mechanism and (b) a Langmuir-Hinshelwood mechanism. [Pg.741]

The desire to understand catalytic chemistry was one of the motivating forces underlying the development of surface science. In a catalytic reaction, the reactants first adsorb onto the surface and then react with each other to fonn volatile product(s). The substrate itself is not affected by the reaction, but the reaction would not occur without its presence. Types of catalytic reactions include exchange, recombination, unimolecular decomposition, and bimolecular reactions. A reaction would be considered to be of the Langmuir-Hinshelwood type if both reactants first adsorbed onto the surface, and then reacted to fonn the products. If one reactant first adsorbs, and the other then reacts with it directly from the gas phase, the reaction is of the Eley-Ridel type. Catalytic reactions are discussed in more detail in section A3.10 and section C2.8. [Pg.302]

Figure A3.9.1. Schematic illustrations of (a) the Langmuir-Hinshelwood and (b) Eley-Rideal mechanisms in gas-surface dynamics. Figure A3.9.1. Schematic illustrations of (a) the Langmuir-Hinshelwood and (b) Eley-Rideal mechanisms in gas-surface dynamics.
Rettner C T 1994 Reaction of an H-atom beam with Cl/Au(111)—dynamics of concurrent Eley-Rideal and Langmuir-Hinshelwood mechanisms J. Chem. Phys. 101 1529... [Pg.919]

The first step consists of the molecular adsorption of CO. The second step is the dissociation of O2 to yield two adsorbed oxygen atoms. The third step is the reaction of an adsorbed CO molecule with an adsorbed oxygen atom to fonn a CO2 molecule that, at room temperature and higher, desorbs upon fomiation. To simplify matters, this desorption step is not included. This sequence of steps depicts a Langmuir-Hinshelwood mechanism, whereby reaction occurs between two adsorbed species (as opposed to an Eley-Rideal mechanism, whereby reaction occurs between one adsorbed species and one gas phase species). The role of surface science studies in fomuilating the CO oxidation mechanism was prominent. [Pg.953]

Mechanistic kinetic expressions are often used to represent the rate data obtained in laboratory studies, and to explain quantitatively the effects observed in the field. Several types of mechanisms have been proposed. These differ primarily in complexity, and on whether the mechanism assumes that one compound that is adsorbed on the catalyst surface reacts with the other compound in the gas phase, eg, the Eley-Rideal mechanism (23) or that both compounds are adsorbed on the catalyst surface before they react, eg, the Langmuir-Hinshelwood mechanism (25). [Pg.505]

Solid-catalyzed 7eactioixs. Some Langmuir-Hinshelwood mechanisms for the reference reaction A -I- B R -I- S (see also Tables 7.2, 7.3) ... [Pg.684]

Over the usual hmited range of conditions, a power law rate equation often appears to be as satisfactory a fit of the data as a more complex Langmuir-Hinshelwood equation. The example of the hydrogenation of oc tenes is shown in Fig. l-2d and l-2e, and another case follows. [Pg.692]

The first is ruled out because the constants physically cannot be negative. Although the other correlations are equally valid statistically, the Langmuir-Hinshelwood may be preferred to the power law form because it is more likely to be amenable to extrapolation. [Pg.693]

Boudart (1956) and Weller (1956) discussed the applicability and need of Langmuir-Hinshelwood kinetics to describe the rate of industrially... [Pg.120]

The model is intrinsically irreversible. It is assumed that both dissociation of the dimer and reaction between a pair of adjacent species of different type are instantaneous. The ZGB model basically retains the adsorption-desorption selectivity rules of the Langmuir-Hinshelwood mechanism, it has no energy parameters, and the only independent parameter is Fa. Obviously, these crude assumptions imply that, for example, diffusion of adsorbed species is neglected, desorption of the reactants is not considered, lateral interactions are ignored, adsorbate-induced reconstructions of the surface are not considered, etc. Efforts to overcome these shortcomings will be briefly discussed below. [Pg.392]

The catalytic reaction of NO and CO on single crystal substrates, under ultra-high vacuum conditions, has been extensively studied. Neglecting N2O formation and CO desorption, the Langmuir-Hinshelwood mechanism of the NO + CO reaction can be described by the following sequence of steps [16,17] ... [Pg.415]

A dimer-dimer (DD) surface reaction scheme of the type (1/2)A2 + B2 B2A has been proposed in order to mimic the catalytic oxidation of hydrogen A2 is O2, B2 is H2, AB is OH and B2A is H2O. The model reaction proceeds according to the Langmuir-Hinshelwood... [Pg.419]

The monomer-monomer (MM) model, for the reaction A -H B —> AB, assumes the following Langmuir-Hinshelwood reaction schema ... [Pg.421]

The reaction scheme of the ZGB-DD model is based upon the Langmuir-Hinshelwood mechanism. Thus, it is assumed that the reaction occurs according to the following steps ... [Pg.423]

If the rate of both single reactions is expressed separately, e.g. by means of the equations of Langmuir-Hinshelwood type (when written in a more general way and if the mechanism of both reactions with common reagent X will be the same), we obtain... [Pg.19]

The kinetics of a coupled catalytic reaction can be well described by equations of the Langmuir-Hinshelwood type, since these are able to express mutual influencing of single reactions. Power-law equations are not suitable for this purpose. [Pg.48]

The form of equations of the Langmuir-Hinshelwood type and the values of their constants, obtained by the study of isolated reactions, are valid also in the case of the coupled system, where more substances are present and a greater number of interactions is taking place simultaneously on the surface of the catalyst. [Pg.48]

On the other hand, the work of Roginski with manganese oxide suggested the Langmuir-Hinshelwood mechanism of (49)... [Pg.86]


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Adsorption Langmuir-Hinshelwood-type

Adsorption Langmuir-Hinshelwood-type mechanism

Bonding Langmuir-Hinshelwood mechanism

Catalysis Langmuir-Hinshelwood mechanism

Catalytic Processes Langmuir-Hinshelwood Mechanism

Catalytic reactions rate models, Langmuir-Hinshelwood

Chemical adsorption Langmuir-Hinshelwood mechanism

Chemical reactors Langmuir-Hinshelwood model

Dispersion Langmuir-Hinshelwood model

Dual site Langmuir Hinshelwood model

Effectiveness Factor Bimolecular Langmuir-Hinshelwood Kinetics

Eley-Rideal or Langmuir-Hinshelwood

Heterogeneous Langmuir—Hinshelwood model

Heterogeneously Langmuir-Hinshelwood mechanism

Heterogeneously Langmuir-Hinshelwood-Hougen-Watson

Hinshelwood

Hydrogen Langmuir-Hinshelwood kinetics

Isothermic processes Langmuir-Hinshelwood isotherms

Kinetic Parameters from Fitting Langmuir-Hinshelwood Models

L-H = Langmuir-Hinshelwood

Langmuir and Hinshelwood

Langmuir-Hinshelwood (LH) Kinetics

Langmuir-Hinshelwood -type

Langmuir-Hinshelwood -type mechanism

Langmuir-Hinshelwood Dual Site Dissociative

Langmuir-Hinshelwood Kinetics and Intraparticle Temperature Gradients

Langmuir-Hinshelwood Kinetics in a Ring-shaped Catalyst

Langmuir-Hinshelwood adsorption

Langmuir-Hinshelwood approach

Langmuir-Hinshelwood approach to oxygen

Langmuir-Hinshelwood approach to oxygen quenching

Langmuir-Hinshelwood concept

Langmuir-Hinshelwood equation

Langmuir-Hinshelwood expression

Langmuir-Hinshelwood formalism

Langmuir-Hinshelwood formulation

Langmuir-Hinshelwood isotherm

Langmuir-Hinshelwood kinetic

Langmuir-Hinshelwood kinetic expressions

Langmuir-Hinshelwood kinetic model

Langmuir-Hinshelwood kinetics

Langmuir-Hinshelwood kinetics catalytic reaction rate data

Langmuir-Hinshelwood kinetics single-site mechanisms

Langmuir-Hinshelwood kinetics steps

Langmuir-Hinshelwood mechanism

Langmuir-Hinshelwood mechanism equilibrium constants

Langmuir-Hinshelwood mechanism isotherm

Langmuir-Hinshelwood or Eley-Rideal Mechanisms

Langmuir-Hinshelwood process

Langmuir-Hinshelwood rate

Langmuir-Hinshelwood rate equations (

Langmuir-Hinshelwood rate law

Langmuir-Hinshelwood reaction

Langmuir-Hinshelwood reaction mechanism

Langmuir-Hinshelwood relation

Langmuir-Hinshelwood steps

Langmuir-Hinshelwood type catalytic

Langmuir-Hinshelwood type catalytic reactions

Langmuir-Hinshelwood type reactions

Langmuir-Hinshelwood types of rate equations

Langmuir-Hinshelwood-Hougen-Watson

Langmuir-Hinshelwood-Hougen-Watson LHHW) model

Langmuir-Hinshelwood-Hougen-Watson LHHW) rate equations

Langmuir-Hinshelwood-Hougen-Watson kinetics

Langmuir-Hinshelwood-Hougen-Watson models

Langmuir—Hinshelwood mechanism, for

Langmuir—Hinshelwood model

Langmuir—Hinshelwood recombination

Langmuir—Hinshelwood recombination mechanism

Langmuir—Hinshelwood—Hougen—Watson LHHW) formulations

Langmuir—Hinshelwood—Hougen—Watson kinetic equation

Langmuir—Hinshelwood—Hougen—Watson reaction mechanism

Laws Langmuir-Hinshelwood rate expression

Photocatalysis Langmuir-Hinshelwood

Rate Langmuir-Hinshelwood models

Rate expression, adsorption limiting Langmuir-Hinshelwood

Rate expressions Langmuir-Hinshelwood

Rates, chemical reactions Langmuir-Hinshelwood mechanism

Reaction rate equations Langmuir-Hinshelwood

Surface Langmuir-Hinshelwood mechanism

Temperature Langmuir-Hinshelwood isotherms

The Case for a Langmuir-Hinshelwood Mechanism

The Langmuir-Hinshelwood Formalism

Transfer mechanism Langmuir-Hinshelwood

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