Consider the adsorption of a non-reacting gas onto the surface of a catalyst. Adsorption data are frequently reported in the form of adsorption isotherms. Isotherms portray the amount of a gas adsorbed on a solid at different pressures but at one temperature. A typical adsorption isotherm, shown in Figure R10.1-1, is taken from the classic study of Ward, 1 who adsorbed hydrogen on powdered copper at 25°C (see Table R10.1-1). The data appear to be quite precise. Only one point is slightly off a smooth curve, and there is no hysteresis because the points taken while the pressure was being gradually increased lie on the same curve as those taken while the pressure was decreased. |
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Figure R10.1-1 |
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Postulate models, then see which one(s) fit(s) the data |
This isotherm can be used to gain insight into the adsorption process. An equation for the curve in Figure R10.1-1 will be derived, and the derivation will reveal significant properties of the hydrogen-copper system. First, a model system is proposed and then the isotherm obtained from the model is compared with the experimental data shown on the curve. If the curve predicted by the model agrees with the experimental curve, the model may reasonably describe what is occurring physically in the real system. If the predicted curve does not agree with that obtained experimentally, the model fails to match the physical situation in at least one important characteristic, and perhaps more. To describe Ward's data, two models will be postulated--one in which hydrogen is adsorbed as molecules, H 2 , on copper powder, and the other in which hydrogen is adsorbed as atoms, H, instead of molecules. |
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Two models: |
The former is called molecular or nondissociated (e.g., H 2 ) adsorption and the latter is called dissociative adsorption. Whether a molecule adsorbs nondissociatively or dissociatively depends on the metal (M) surface. For example, CO undergoes dissociative adsorption on iron and molecular adsorption on nickel. |
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A. Molecular Adsorption
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(R10.1-1) |
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In obtaining a rate law for the rate of adsorption, the reaction in Equation (R10.1-1) can be treated as an elementary reaction. The rate of attachment of the hydrogen molecules to the surface is proportional to the number of collisions that these molecules make with the surface per second. In other words, a specific fraction of the molecules that strike the surface become adsorbed. The collision rate is, in turn, directly proportional to the hydrogen partial pressure,. Because hydrogen molecules can adsorb only on vacant sites and not on sites already occupied by other hydrogen molecules, the rate of attachment is also directly proportional to the concentration of vacant sites, C. Combining these two facts means that the rate of attachment of hydrogen molecules to the surface is directly proportional to the product of the partial pressure of H and the concentration of vacant sites: |
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rate of attachment |
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The rate of detachment of molecules from the surface can be a first-order process; that is, the detachment of hydrogen molecules from the surface is usually directly proportional to the concentration of sites occupied by the molecules, |
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rate of detachment |
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The net rate of adsorption is equal to the rate of molecular attachment to the surface minus the rate of detachment from the surface. If k A and k -A are the constants of proportionality for the attachment and detachment processes, then |
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(R10.1-2) |
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( The ratio K A = k A / k - A is the adsorption equilibrium constant. Using it to rearrange Equation (R10.1-2) gives |
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(R10.1-3) |
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The parameters k A , k -A , and K A are all functions of temperature, exhibiting an exponential temperature dependence. The forward and reverse specific reaction rates, k A and k -A increase with increasing temperature, while the adsorption equilibrium constant, K A , decreases with increasing temperature. At a single temperature, in this case 25°C, they are, of course, constant in the absence of any catalyst deactivation. |
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Because hydrogen is the only material adsorbed on the catalyst, the site balance gives |
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(R10.1-4) |
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The points plotted in Figure R10.1-1 were taken at equilibrium conditions. The experimental details present in the original work support this fact, and the absence of hysteresis confirms it. At equilibrium, the net rate of adsorption equals zero. Setting the right-hand side of Equation (R10.1-3) equal to zero and solving for the concentration of H 2 adsorbed on the surface, we get |
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(R10.1-5) |
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Using Equation (R10.1-4) to give C in terms ofand the total number of sites Ct we can solve forin terms of constants and the pressure of hydrogen: |
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Rearranging gives us |
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(R10.1-6) |
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Langmuir isotherm for adsorption of molecular hydrogen |
This equation thus givesas a function of
the partial pressure of hydrogen, and so is an equation for the adsorption isotherm.
This particular type of isotherm equation is called a Langmuir isotherm.
2 |
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(R10.1-7) |
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and the linearity of a plot ofas a function ofwill determine if the data conform to a Langmuir single-site isotherm. The data in Figure R10.1-1 are replotted in Figure R10.1-2 in the form suggested by Equation (R10.1-7). The data indicate a slight but definite curvature. Thus there is a significant question as to whether these data really conform to a model of hydrogen adsorbing as molecules. |
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B. Dissociative Adsorption
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When the hydrogen molecule dissociates upon adsorption, it is referred to as the dissociative adsorption of hydrogen. As in the case of molecular adsorption, the rate of adsorption here is proportional to the pressure of hydrogen in the system, because this rate governs the number of gaseous collisions with the surface. For a molecule to dissociate as it adsorbs, however, two adjacent vacant active sites are required rather than the single site needed when a substance adsorbs in its molecular form. The probability of two vacant sites occurring adjacent to one another is proportional to the square of the concentration of vacant sites. These two observations mean that the rate of adsorption is proportional to the product of the hydrogen partial pressure and the square of the vacant site concentration,. |
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For desorption to occur, two occupied sites must be adjacent, meaning that the rate of desorption is proportional to the square of the occupied-site concentration, ()2. The net rate of adsorption can then be expressed as |
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(R10.10-8) |
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On this particular |
Figure R10.1-2 |
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Rate of |
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where |
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At equilibrium, r AD = 0, and |
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or |
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(R10.1-9) |
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From Equation (R10.1-1), |
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This value may be substituted into Equation (R10.1-9) to give an expression that can be solved for. The resulting isotherm equation is |
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Langmuir isotherm for adsorption as atomic hydrogen |
(R10.1-10) |
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Taking the inverse of both sides of the equation, and then multiplying through by, yields |
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(R10.1-11) |
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This equation is the linearized Langmuir isotherm for dissociative adsorption. It says that if the hydrogen is dissociatively adsorbed on the copper, a straight line should result whenis plotted as a function of. |
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The dissociative |
The data in Figure R10.1-1 are replotted in Figure R10.1-3 in the form suggested by Equation (R10.1-11). An excellent straight line is obtained, giving support to the postulate of hydrogen being dissociatively adsorbed on the copper powder. A comparison of the results of the models indicates that hydrogen is adsorbed on the copper as atoms rather than as molecules. Hydrogen-deuterium tracer studies have confirmed this interpretation. Some comments seem deserved here. The data presented seemed very precise. If they had not been so, and there had been significant scatter, it would have been impossible to distinguish between the two models. The curvature in Figure R10.1-2 is slight, so the difference between the two plots is somewhat subtle. A discerning eye is necessary to distinguish between the two mechanisms in this situation. This subtle difference is one reason why this type of agreement between a model and the behavior of experimental data usually requires supporting spectroscopic and tracer experiments.
Figure R10.1-3 |