J. Phys. Chem. B, 101 (33), 6420 -6428
jp971230b S1089-5647(97)01230-3
Copyright © 1997 American Chemical Society
Modeling of Adsorption Properties of Zeolites: Correlation with the Structure
A. Goursot,*V. Vasilyev, and
A. Arbuznikov![]()
Laboratoire de Matériaux Catalytiques et Catalyse
en Chimie Organique, UMR 5618 CNRS, Ecole Nationale Supérieure
de Chimie de Montpellier, 8 Rue de l'Ecole Normale, 34053 Montpellier
Cédex 1, France
Received: April 9, 1997
Abstract:
The adsorption of N2 and CO in Na X-zeolites has
been studied for different framework structures and extraframework
cation distributions. To this aim, the cation-molecule system
modeling one site has been embedded in a set of external point
charges which simulate the zeolite environment of the site and
has been treated quantum chemically, using a method based on density
functional theory. This procedure has been applied to the 64 cationic
sites accessible for adsorption in a crystal unit cell of an ideal
X-zeolite with a Si/Al ratio equal to 1. These calculations have
shown that only a few cations are favorable for initial adsorption
and that those cations are always of type III(III'). Their efficiency
depends both on the framework geometry and on their location in
the supercages. The analysis of the quantum chemical results in
terms of a classical description involving electrostatic and induction
interaction energies with the framework has led to the conclusion
that the direction of the electric field vector created by the
zeolite in the supercages is an important factor determining the
zeolite adsorption properties.
Zeolites are aluminosilicate materials that are widely used
for size and shape catalysis, hydrocarbon conversion, and sorbing
processes. Their physicochemical properties are based on the ability
of these open crystalline structures to enclose charged and neutral
species within cavities. Their properties are thus strongly related
to the structure of the framework and also to the distribution
among cages and channels of the cations that are associated with
the Al centers. Indeed, those extraframework cations are the active
sites for adsorption processes, whereas their neighboring oxygens
are involved in base catalysis. Adsorption and desorption studies
of small probe molecules like N2 and CO are used to provide information
about cations and basic sites. Those experiments show that the
adsorption of molecules within the cages varies with the number
and nature of occupied cationic sites.1-3
However, there is presently no real understanding of how adsorption properties of zeolites depend on the cation distribution. The major difficulty encountered in the study of such a correlation arises from the incomplete information provided by experimental structure determinations about cationic sites. First, very few structures are known for low-silica zeolites, i.e. for those including a large number of cations.4 Moreover, the studies concerned with zeolites containing a single type of cations are even more scarce, due to the difficulty of full cationic exchange. Crystal and powder structure determinations provide positions for the cations associated with the probabilities of occupying the various sites, which, very often, do not sum up to the total number of cations. Cation positions vary also with their chemical nature and with the extent of dehydration. Lithium cations are hardly detectable by X-ray diffraction, and sodium cations may not be well differentiated from water molecules. Finally, experimental conditions of preparation and dehydration may induce differences in the solids, leading to different structures and thus different adsorption properties.
For all these reasons, we think that modeling may be an appropriate
tool to analyze the relations between adsorption properties and
zeolite structures. Although a large variety of modeling techniques
have already been used for the prediction and analysis of zeolite
structures and properties, only a very few studies have been devoted
to systems including cations other than protons. During the last
decade, the main effort has been devoted to H-zeolites, mainly
due to their widespread applications in acid catalysis.5-7
For this purpose, three experimental structures of Na X-zeolites of very similar compositions were chosen in order to generate an ideal X-zeolite with a Si/Al ratio of 1, i.e. a composition Na96Al96Si96O384. These three structures differ by some geometrical parameters of their framework and also by the positions attributed to the site III cations. The impact of these differences on the adsorption of N2 and CO will be ascertained by our modeling study.
A detailed analysis of the structures published for Y- and
X-zeolites, including various cations,4,15-21
|
Figure 1 Faujasite-type structure with cationic sites: "ideal" site III (a), monocoordinated site III (b), and bicoordinated site III (c). |
In dehydrated Y-zeolites (Si/Al > 1.5), the cations are essentially distributed among sites I(I') and II(II'), with a maximum of 32 site II cations available for adsorbing molecules, and very few or no cations at site III(III'), which are also located in the supercages.4 In contrast, dehydrated X-zeolites (Si/Al < 1.5) are known to contain cations occupying those extra sites in the supercages. There are 48 possible sites III, also called "ideal" sites, coordinated to two O4 oxygens, whereas 96 additional III' positions are coordinated to O1 and O4 oxygens (192 if Al and Si are differentiated) (Figure 1). In fact, there are still other possibilities for such type III cations, for example coordination with three oxygens (O1, O1, O4 or O1, O2, O4) or with only one oxygen (O1 or O4). If we assume a full occupancy of 64 cations in sites I(I') and II(II'), then 32 cations have to be accommodated in the type III sites of the supercages for an ideal X-zeolite with a Si/Al ratio equal to 1. This explains the difficulty of the experimental determination of the positions of site III cations, as well as their interest, since X-zeolites are the most efficient systems for adsorption.
For the present study, we have chosen to compare three recent
experimental structures referred to as OLS,21 ALA,16
and SMO.15 They contain only sodium cations and correspond
to very comparable compositions with 88, 86, and 92 cations for
OLS, ALA, and SMO, respectively. Examination of Table 1,
which collects the site occupancies for these three X-zeolites,
leads to several remarks: (i) there are very few cations in sites
I and none in sites II', (ii) the OLS and ALA determinations lead
to five extra cations, whereas 21 are missing in the SMO structure,
and (iii) the ALA structure contains more cations of type III
and less site II cations than the two other structures.
In addition to the above differences between cation distributions, these structures differ also by the location of type III cations in the supercages and by some geometric characteristics of the aluminosilicate framework.
Figure 2 illustrates the different type III sites reported
for the OLS (a-c), ALA (e,f), and SMO (d) structures. In the OLS
structure, the sodium cations are essentially bicoordinated to
O1, O4 oxygens with Al or Si as the T atom
and there are also 11 cations coordinated to O4. The
10 site III cations reported in the SMO structure are also singly
coordinated to O4. The ALA structure contains 23 "ideal"
bicoordinated cations (on the corresponding four-membered rings)
and 24 cations coordinated to only O4.
|
Figure 2 Experimental site III positions: OLS structure (a, b, and c), ALA structure (e and f), and SMO structure (d). |
In parallel with these different site III locations, the framework
bond lengths and angles show some differences that are more pronounced
for the ALA structure with respect to the others. In particular,
the O4-O4 distance is much larger, whereas
the O1-O1 and O1-O4
distances are smaller, in this structure (Table 2).![]()
In order to compare the adsorption energies of N2 and CO in these three structures, we have chosen to model them as idealized Na96(AlO2)96(SiO2)96 structures with 32 cations in sites I', II, and III, all framework characteristics being reproduced from the corresponding X-ray data. The 32 type III cations in the OLS structure were distributed as described above, i.e. 11 monocoordinated and 21 bicoordinated. Examination of the geometry around the singly coordinated type III site of the ALA structure has revealed some unrealistic features: (i) a symmetrical arrangement around O4, whereas it should be nonsymmetrical; (ii) a quite long O4-Na bond length, which also corresponds to a hydrogen bond length, as O4-(HOH); (iii) the large number (47) of type III cations, which does not look reasonable, since this large concentration of cations in the supercages leads to a repulsion energy between cations that is twice as large as the repulsion energy when all sites II are populated and only 32 cations are distributed in sites III.
We have thus chosen to model 32 "ideal" type III cations in this ALA structure, instead of the 23 ones in the published structure, and to occupy the 32 available sites II.
In the same spirit, 32 type III cations were distributed among the monocoordinated sites proposed for the SMO structure.
In the three cases, the 32 type III cations were distributed among the corresponding possible locations through the minimization of their mutual Coulomb repulsion, all other cations in sites I' and II being kept fixed. It is worth noting that this minimization can lead to several distributions of type III cations that have comparable stabilities. In the case of the OLS structure, which has the largest number of possible type III sites (240), we have compared the N2 adsorption energies calculated for three distributions of type III cations that were energetically comparable. The largest difference between the calculated adsorption energies obtained with these three distributions was about 1 kcal/mol, which indicates the largest error related to this procedure. For the ALA and SMO structures, this error is much smaller, due to the much smaller number of possible sites III (48 and 96, respectively).
The strategy adopted for these calculations is to model the adsorption of one nitrogen or carbon monoxide molecule in turn at each cationic site available in the eight supercages of one crystal unit cell, i.e. at all 32 sites II and 32 sites III, for the three structures defined above. In each case, the Na+-N2 and Na+-CO systems are treated quantum chemically, including their interaction with 18 143 external point charges, which represent all the atoms of a central unit cell where the adsorption occurs (except the concerned Na+ cation) and, in addition, all the atoms of 26 surrounding neutral unit cells. We have verified that this network of charges is sufficient by calculating more extended networks. The error of convergence on the electrostatic potential in the central unit cell is 0.5 kcal/mol only (0.4%), whereas the error on the electric field is 0.0002 au (0.4%).
The interaction of Na+-N2 (Na+-CO) with the zeolite ionic environment includes the Coulomb terms as well as the modifications of the electron density induced by the nonuniform electric field generated by the zeolite (induction terms). Dispersive interactions between the adsorbed molecule and the framework ions are negligible in this case, since their distance is always larger than 9 bohrs. The sodium cations have been fixed at their experimental positions in dehydrated zeolites, which implies that the cation-framework distance is unchanged upon N2 (CO) adsorption. There is no experimental evidence for any displacement of cations during adsorption of these molecules at room temperature, in contrast with their observed mobility when solvated with water molecules. As shown in previous calculations12,13 and through the electrostatic potential values reported below, the binding energy of the cation with the framework is more than an order of magnitude larger than its binding energy to CO and N2. Moreover, this assumption allows an easier comparison of the effect of the structure on the relative adsorption strengths at different sites and in different frameworks.
As in our previous study of adsorption modeling,13,14
the calculations have been carried out in the framework of density
functional theory, using the deMon-KS program.22-24
quality have been adopted for N, C, and O,27,28
Since a linear Na+-molecule geometry is the most favorable in the gaseous state,13 the incoming molecules were approached to site II cations along the pseudo C3 axis of the six-membered ring, yielding the optimum distances to Na+, the N-N and C-O bond lengths being kept fixed at their equilibrium values optimized for isolated Na+-N2 and Na+-CO (1.095 and 1.127 Å, respectively).
For the bicoordinated sites III, the molecules approached along the bisector of the ONaO angle, whereas they were collinear with the O-Na direction for the monocoordinated site III cations.
In the case of nonideal sites III (OLS and SMO structures),
other type III cations may prevent a linear approach. The orientation
of the incoming molecule has thus been adjusted, minimizing the
van der Waals repulsion with the neighboring atoms. In a simplified
treatment, N2 or CO was assumed to be a sphere centered
at the middle of the bond, and its repulsion energy with all nonbonded
atoms has been evaluated as
(Aj/Rj12),
where Rj is its distance to atom j and
Aj is the van der Waals parameter, calculated
as Aj = (asaj)1/2.
The parameters a (as, aj)
are defined classically by a = 4![]()
12. The values 0.02957 (
)
and 7.5133 kcal mol-1 (
) for
this sphere were found to be sufficient to keep the adsorbate
from interacting strongly with the other cations (represented
by point charges). The corresponding parameters for the other
atoms were taken from ref 30.
The charges used for these calculations were -1.2 for O, 1.4 for Al, 2.4 for Si, and 1.0 for Na.30 It is worth mentioning that the validity of the conclusions that will be drawn from this study are not dependent on the precise values of these atomic charges. Indeed, test calculations have been performed in order to check the effect of the charge values on the calculated adsorption energies. These calculations have shown that the use of another set of charges (derived from MNDO calculations on zeolite models, i.e. -1.0355 for O, 1.245 for Al, 1.897 for Si, and 1.0 for Na) induce a uniform shift of less than 1 kcal/mol for the calculated adsorption energies, leaving unchanged their differences between sites and structures.
4.1. Adsorption Energies. The adsorption energies of N2 and CO at the 64 accessible sites II and III are presented in Figures 3, 4, and 5, for the OLS, ALA, and SMO structures, respectively. They have been evaluated using the expression
where E(Z-Na+-molecule) is the total energy of the embedded system at one specific site, E(Z-Na+) is the total energy of the embedded cation at this site, and E(molecule) is the total energy for a gaseous N2 or CO molecule.
Examination of these curves leads to two remarks. First, the most striking result is the very large dispersion of Eads values. Indeed, the calculated values spread over 6 (SMO) or 7 (OLS, ALA) kcal mol-1 for N2 and 7 (SMO) or 10 (OLS, ALA) kcal mol-1 for CO. This large range of energies reveals that the local adsorption on a sodium cation, which amounts to -8.15 and -11.4 kcal mol-1 for N2 and CO, respectively, without embedding (gaseous state), is strongly perturbed by the environment of the site and that, also, this perturbation is very asymmetric. It is worth noting that the N2 or CO adsorption energies without embedding are included within the Eads values for OLS and ALA structures but remain more stable than the values obtained for the SMO structure. This indicates that, for the former structures, the zeolite environment can weaken or enhance the binding energies of isolated cation-molecule systems, whereas, for the latter structure, there is a weakening effect only.
The second remark concerns the relative adsorption energies for N2 and CO in the three structures: CO adsorbs more strongly than N2 on the Na+ cations and the difference between their adsorption energies increases with the strength of the binding. The fact that CO binds more strongly to Na+ is due to the additional dipole-cation interaction and is indeed obtained in the gaseous state, where their binding energy difference amounts to 3.25 kcal mol-1. For the OLS and ALA structures, this difference is decreased at sites with low adsorption energies and increased at sites with large ones. For the SMO structure, the same trend is followed, but the differences between CO and N2 binding energies always remain smaller than without embedding.
As a first conclusion, we can say that the embedding generates a large diversity among the accessible sites and may weaken or enhance adsorption properties.
Let us now turn to a more comparative analysis of the adsorption
energies on sites II and sites III, which are presented for N2
in Figures 6, 7, and 8, for OLS, ALA, and SMO structures, respectively.
CO adsorption curves are not presented here because they reproduce
all the detailed features of Figures 6-8, but with more stable
Eads values. The ordering of the cationic sites,
adopted in these figures, corresponds to that of increasing values
for the electrostatic potential (ESP) created by the framework
at the cationic sites. The ESP values will be discussed in the
next paragraph.
As visible from these figures, the dispersion of Eads values for sites II is roughly half this dispersion for sites III, and this is true for all three structures. Moreover, for sites III, the ALA structure shows a significantly smaller dispersion than the two other structures. Those facts correlate with a greater local symmetry around sites II, whichever is the structure, and also for "ideal" sites III (ALA structure).
The second interesting result is that the largest adsorption
energies (most stable systems) always correspond to site III cations,
for N2 and CO. Moreover, as shown in the figures, the
largest adsorption energies are characteristics of only a few
sites of type III. There are also a small number of sites II and
sites III which display comparable Eads values.
However, if the adsorption energies are averaged for sites II
and sites III, in order to delineate a trend, the (Eads)av
values obtained are significantly different for these two types.
The average values, presented in Table 3,
allow one to delineate several trends: (i) N2 and CO
adsorption are favored at sites III, (ii) the ALA structure is
the most efficient for adsorption, whereas the SMO structure is
the least efficient, and (iii) the difference between N2
and CO is larger at sites III than at sites II.
The equilibrium distance between the sodium cations and an incoming molecule does not depend much on the type of site nor on the structure, except for site III adsorption in the ALA structure. The average equilibrium distances are calculated at 2.55 Å (Na+-N) and 2.63 Å (Na+-C), for all sites of the OLS and SMO structures, as well as for sites II of the ALA structure. These distances were reduced to 2.35 and 2.45 Å, respectively, for sites III in the ALA structure. However, it is worthwhile to point out that, in the embedded systems, the binding energy curve is very flat around the equilibrium distance (change of 0.1-0.2 kcal mol-1 for 0.05 Å). In spite of this imprecision, we can say that, except at sites III in the ALA structure, the zeolite induces some elongation of the Na+-N and Na+-C distances. For all sites and all structures, the molecule-cation charge transfer is very small, since the Mulliken net charge on the sodium cation ranges from 0.958 to 0.973 for Na+-N2 and from 0.930 to 0.990 for Na+-CO. These values are very comparable to the gas phase sodium net charge (0.95 and 0.92 for Na+-N2 and Na+-CO, respectively).
Optimization of the N-N and C-O distances has been performed at several sites of the ALA and OLS structures. The vibrational frequencies have also been evaluated. The cation-molecule distances were not changed and the optimized N-N and C-O bond distances were 1.100 ± 0.003 and 1.125 ± 0.003 Å, respectively, which shows no important variation with respect to the equivalent isolated systems. The effect of this optimization on the calculated adsorption energies was less than 0.2 kcal/mol. These results show that although the embedding charges have a large effect on the adsorption energies, the extra perturbation on the geometries induced by the zeolite in the adsorbed molecules is very small.
A more realistic description of the adsorption process is given by a statistical evaluation of the site occupancies at 298 K, which are calculated as
where Pi is the Boltzmann factor (Pi
= exp(-Eads(i)/kT), which represents
the relative weight of site i in the statistical adsorption
energy <Eads>, Ptot
is the sum of the 64 Pi values, and Eads(i)
is the adsorption energy at site i. The statistical adsorption
energy <Eads> is then evaluated as
(piEads(i)).
The results (Table 4)
show
that, indeed, few sites contribute with substantial efficiencies,
and, as expected from the above, these sites are all of type III.
There are only three to five sites, according to the structure,
which contribute with a probability larger than 5%. The trends
deduced from the analysis of the average Eads
values for sites III (Table 3) are still valid when the <Eads>
energies are considered.
From these results, we can already conclude that, whichever is the type of position for site III cations, i.e. "ideal" (ALA), mainly bicoordinated (OLS), or monocoordinated (SMO), they are the most probable sites for initial adsorption. We can thus propose that this is the reason why X-zeolites are more efficient for N2 and CO adsorption than Y-zeolites, where essentially sites II are populated. This conclusion is in agreement with several experimental results that compare adsorption properties of X- and Y-zeolites.1,2,31
As already precised, the purpose of this work is to analyze the incidence of the framework geometry and cation distribution on the adsorption properties of Na X-zeolites, without predicting accurate adsorption energies. We are indeed aware that the choice of external charge values and the necessary distribution of cations among all possible sites III are two sources of errors of the absolute values of adsorption energies. Moreover, different structures produce different calculated adsorption energies. However, keeping these restrictions in mind, we find it interesting to check if the values calculated with the embedded cluster model are in a reasonable range with respect to experimental values.
The <Eads> values are obtained directly from differences of electronic total energies for the isolated compounds and the complex. In order to compare with experimental enthalpies of adsorption, we have assumed that ideal gas conditions apply. The change in internal energy due to adsorption has been determined by subtracting the sum of the internal energies of the isolated species (Z-Na+, molecule) from the internal energy of the adsorbed model. For the latter, there are no rotational and translational degrees of freedom, whereas their contribution is (5/2)RT for the gaseous molecules. The zero point energy contributions have been evaluated using the vibrational frequencies calculated in each structure for the site with the largest adsorption energy. The corrections were 1.05, 0.77, 0.75 kcal/mol for N2 and 1.19, 0.76, 0.74 kcal/mol for CO, in the ALA, OLS, and SMO structures, respectively. The contributions due to the effect of temperature on vibrational populations were 0.92, 1.09, 1.00 kcal/mol for N2 and 0.87, 1.16, 0.97 kcal/mol for CO, respectively. The energy changes were converted to enthalpy by adding RT. For a temperature of 298 K, the evaluated adsorption enthalpies are thus within -6.5 to -8.7 kcal/mol for N2 and -9.0 to -13.7 kcal/mol for CO. These values should represent the upper limit for adsorption energies since our models correspond to the largest Al (and thus cationic) content. The agreement with experimental isosteric heats of adsorption is very reasonable. Indeed, values of 6.3 for N232 and 7.8 kcal/mole for CO33 have been proposed for initial heats of adsorption in dehydrated Na X-zeolites.
The adsorption energies obtained with the three structures spread over a range of 3 and 5 kcal/mol for N2 and CO, respectively. In spite of the errors related to our calculations (see sections 2 and 3), we think that these differences are not meaningless. The SMO and ALA structures, which have the lowest and the highest efficiency for adsorption, display significant differences in their framework geometries and in their site III positions. In contrast, the OLS and SMO structures have very similar framework geometries and differ essentially by 22 bicoordinated (OLS) or monocoordinated (SMO) site III cations. Although the error bar on adsorption energies is larger for the OLS structure, because of the large number of possibilities in distributing the 32 cations among sites III, we think that this structure is indeed more efficient than the SMO one, and the reason must be their difference in site III positions. Hence, both the framework geometries and the locations of site III cations play a role in the adsorption capacity of a zeolite, and it is, presently, hardly possible to delineate their relative influence.
4.2. Electrostatic Potential (ESP). It is well-known that ESPs give a more realistic description of electron donor properties of a system than atomic net charges. In previous work on zeolites, the electron density of the framework was described with a QM method and the positions of the ESP wells were used as approximate cation locations, before geometry optimization.12,34 The ESP minima were shown to be good approximations for the optimized cation positions, whereas their relative depths gave a valuable estimate of their relative binding energies to the framework.
In this paper, the ESP values are calculated from the set of point charges that constitutes the embedding of each cationic site. This is a very crude description of the electron density of the zeolite, but it is worth mentioning that these charge values have themselves been evaluated through a fitting of ESP values obtained from QM calculations. We will thus consider the ESP values calculated at each cationic site (types II and III) as a measure of the local bond strength between the framework and the cation (represented by a +1 charge).
Examination of Figures 6-8 shows that there is a clear trend concerning the electrostatic potential at the cation position and the cation-molecule interaction energy, which distinguishes sites II and sites III. There is no individual correlation between Eads and ESP values, in the sense that two cations may have comparable ESP values, whichever is the type of site, but correspond to very different adsorption energies. However, there is a general trend for the three structures concerning the behavior of ESP values: they are smaller for sites III than for sites II (Table 3), leading to the proposal that larger adsorption energies are related with smaller ESPs. In fact, this trend seems very reasonable in the sense that if a cation is more strongly bonded to a more basic framework (large ESP), its electron deficiency is decreased, leading to a smaller interaction energy with N2 or CO. This decrease of the electrophilic character of the cation is not obtained through a full quantum treatment of the whole zeolite, i.e. involving charge transfer and exchange-correlation effects. It is indeed modeled by the action of an external negative potential in the QM treatment of the cation (alone and in the complex system), which screens its adsorption capacity. This screening changes with the cation location in the framework and also with the framework geometry itself.
This result correlates very well with the existence of an intrinsic framework basicity which has been proposed as being able to enhance basic properties of some zeolites with respect to what would be expected from their Al content.35 We can say that the framework structure around sites II has, in general, a larger aptitude to attract the cation, screening more than at sites III its electrophilic character.
However, the correlation between the ESP value at a cationic site and the adsorption energy at this site cannot be more than a general trend since the external potential created by the embedding interacts not only with the cation but also with the whole electron density of the complex cation-molecule. The action of the embedding provides then electrostatic energy terms involving all permanent multipole moments of this system.36 As for the ESP term (related to the monopole), these contributions vary with the cationic site and with the structure.
Besides these electrostatic terms, the embedded model includes also the interaction of the surrounding with the electric dipole moments it has induced in the cation-molecule complex. The induced dipoles result from the distortion of the electronic distributions of Na+-N2 and Na+-CO in response to the electric field created by the embedding. It is thus interesting to analyze in some detail the electric field values and directions that are produced in the different structures.
4.3. Electric Field. The action of a uniform
electric field F on a system provides a contribution to
its total energy, which, limited to the second order in F,
is approximated by -
F -(1/2)
:F2,
where
is the permanent dipole moment of the system and
its polarizability tensor.
Classically, the first term contributes to the electrostatic energy, wheras the second one is the so-called induction energy. In fact, the electric field in the supercages is nonuniform, varying in modulus and direction, going from the cations to the middle of the supercages and also from one cationic site to another. The nonuniformity of the field involves energy terms proportional to the electric field gradient, the quadrupole moment, and the quadrupole polarizability of the system.
In order to delineate the role of the electric field generated by the zeolite embedding on the N2 and CO adsorption energies, we have applied a uniform electric field of 0.02 au to Na+- N2 and Na+-CO, and the new binding energies of N2 and CO have been estimated, in a way similar to the above Eads values:
where the superscript F indicates that the energy is calculated in the presence of the electric field.
A value of 0.02 au has been chosen for the absolute value of
the electric field because it is included in the range 0.01-0.035
of the field values generated by the surroundings within a distance
of 2.6 Å from the cations. The action of the field vector
has been studied as a function of its direction, with the angle
= 0
when the vector is directed from the molecule
toward the cation. The results, presented in Figure 9, show that
the binding energies of N2 and CO to Na+
are very sensitive to the direction of the field, which is understandable,
due to the large polarizability of these systems (Table 5). As
could be expected, a field directed from the cation to the molecule
is very favorable for adsorption, due to the induced electric
dipole moment which pulls the electron density in the direction
opposite to the field. In that case, both the ![]()
![]()
·
F
cos
and induction terms contribute to stabilize the
Na+-molecule system.
|
Figure 9 Variation of Na+N2 (circles) and
Na+CO (triangles) adsorption energies with the direction |
The curves obtained for Na+-N2 and Na+-CO
also show that the binding energy difference between the two systems
is the smallest for
= 0
and the largest
for
= 180
, due to the permanent dipole
contribution, with the largest
value for Na+-CO.
Examination of the Mulliken atomic charges (Table 5)
confirms that, indeed, the field direction that is the least favorable
for adsorption (
= 0
) corresponds to the largest
positive charge on Na+, i.e. the smallest charge transfer
from the molecule to the cation, with the opposite behavior for
= 180
.
|
Figure 10 N2 adsorption energies as a function of the electric field direction at sites III in the OLS structure. |
In order to appreciate to what extent the adsorption energies
are correlated to the electric field direction in the zeolite,
we have reported in Figures 10-12 the variation of N2
adsorption energies at sites III for the three structures, together
with the field direction (indicated by the
angle
defined above), at the Na+, first and second nitrogen
positions.
From these figures, it is clear that the OLS and SMO structures
have comparable field directions, although OLS curves for N1
and N2 are slightly shifted toward larger
values. The features are different for the ALA structure, with
a smoother variation of Eads values with the
electric field direction at N1 and N2 and,
essentially, a constant
value of 180
at the sodium positions.
Moreover, for the three structures, there is a clear trend
of decreasing adsorption energies with a decreasing
value from 90
to 0
at the nitrogen positions.
The statistical <Eads> values are all
related to
values very close to 90
. The largest difference
between the ALA structure and the two others corresponds to a
more favorable field direction at the sodium position (
= 180
),
which favors its electron acceptor character in the direction
of the incoming molecule. This favorable
value
at the cation position for the ALA structure implies also that
the electric field gradient is larger than that for the OLS and
SMO structures, in this region of space (cation-molecule). Since
the quadrupole electrostatic term involves the electric field
gradient, this trend also favors the enhancement of the N2
and CO adsorption energy in the ALA structure.
Finally, if we go back to Figures 3-5 and compare with Figure
9, we can now explain the variation of the energy difference between
CO and N2 curves in the embedded model: the small difference
of energy corresponds to sites II, where the adsorption energy
is the smallest, whereas the largest difference corresponds to
the most efficient sites III, where the adsorption energy is the
largest. This variation correlates with the direction of the electric
field for the corresponding sites:
values smaller
than 10
for the least efficient sites II and
values
of around 90
for the most efficient sites III. Moreover, the
action of a favorable direction of the electric field explains
why the ALA structure, which is already the most favorable for
N2 adsorption, still enhances the CO adsorption energy,
through the existence of the permanent dipole-field interaction.
The electric field direction is thus indeed one governing factor of the largest efficiency of some site III cations.
The theoretical model we have used for this study provides a quantum mechanical treatment of the cation-molecule system, perturbed by different external potentials, modeling the different sites. Hence, it allows the accurate evaluation of the effect of these different perturbations on the binding energies with N2 and CO molecules. Since the embedding charges are at sufficiently large distances, the QM results can be rationalized using the classical decomposition of the long-range interaction energy between two systems, where one system is reduced to a set of point charges. Among the energy terms, only the electrostatic and induction contributions have been considered.
This analysis has allowed one to delineate how the zeolite structure can modulate the adsorption capacity of the cations, as well as the binding ability of the incoming molecules.
Our calculations have shown that the zeolite structure induces a strong dissymmetry among the different available cations. This dissymmetry, as well as the influence of the electric field direction cannot be reproduced using a small cluster modeling the zeolite. Indeed, in contrast with a previous proposal based on a cluster study,13 the present embedded model shows that the role of the zeolite cannot be reduced to a screening of the cation's electrophilic character. The long-range electrostatic terms can also enhance the Na+-N2 and Na+-CO binding energies. This is what happens, at some favored sites, where the adsorption energies are larger than for an isolated cation.
The analysis of the results obtained with the three structures
of faujasite-type chosen for this study has demonstrated that
favored cationic sites for adsorption are always of type III.
This conclusion correlates very well with the upfield displacements
of the 129Xe NMR chemical shifts in X-zeolites with
respect to Y-zeolites.37,38
The zeolite structure has thus a substantial effect on N2 and CO adsorption energies since different structures may lead to quite different adsorption energies. From the present results, it is hardly possible to ascertain whether it is the cation distribution or the framework geometry which is the most important factor. Further calculations are in progress in order to reach a more detailed understanding of the correlation between the zeolite structure and its adsorption properties.
A.A. and V.V. thank Elf Aquitaine for a post-doctoral fellowship.
The authors thank Dr. F. Fajula for very fruitful discussions
and the Centre Universitaire Sud de Calcul de Montpellier for
the provision of computational resources.
* In papers with more than one author, the asterisk indicates
the name of the author to whom inquiries about the paper should
be addressed.
Abstract published in Advance ACS Abstracts,
July 1, 1997.
Permanent address: Boreskov Institute of Catalysis,
Siberian Branch of the Russian Academy of Sciences, 630090 Novosibirsk,
Russia.
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structure
composition
site I
site I'
site II
site II'
site III-type
sum
OLS
Na88
3
29
32
30
93
ALA
Na86
3
21
20
47
91
SMO
Na92
3
26
32
10
71
structure
R(O4-O4)a
R(O1-O1)a
R(O1-O4)a near
Al
<O1AlO4a
R(O1-O4)a near
Si
OLS
3.813
3.827
2.796
109.9
2.610
ALA
4.501
3.655
2.682
99.4
2.682
SMO
3.846
3.846
2.783
109.0
2.581
a Distances are in angstroms, and angles
are in degrees.
| sites II | sites III | |||||
| structure | (Eads)avN2 | (Eads)avCO | ESPav | (Eads)avN2 | (Eads)avCO | ESPav |
| OLS | -2.8 | -3.9 | -219.6 | -4.8 | -6.6 | -147.8 |
| ALA | -5.1 | -7.3 | -256.0 | -8.2 | -11.7 | -141.0 |
| SMO | -2.7 | -3.7 | -217.5 | -4.7 | -6.4 | -168.9 |
a Energies in kcal/mol.
| structure | molecule | <Eads>a | number of sitesb | pi values |
| OLS | N2 | -8.6 | 3 | 0.67, 0.23, 0.07 |
| CO | -11.2 | 3 | 0.73, 0.20, 0.06 | |
| ALA | N2 | -9.9 | 5 | 0.41, 0.12, 0.09, 0.09, 0.07 |
| CO | -14.9 | 4 | 0.67, 0.08, 0.08, 0.05 | |
| SMO | N2 | -7.4 | 4 | 0.55, 0.34, 0.08, 0.06 |
| CO | -9.8 | 4 | 0.55, 0.34, 0.05 |
a Energies in kcal/mol.b
Only sites with pi > 0.05 have been taken
into account.
| propertiesa |
|
|
|
|
|
|
|
N2 | -8.2 | -3.8 | -9.3 | -16.9 |
| CO | -11.4 | -5.8 | -12.8 | -21.4 | |
| qNa+ | N2 | 0.953 | 0.967 | 0.951 | 0.930 |
| CO | 0.924 | 0.947 | 0.920 | 0.885 | |
| qN1 | 0.013 | 0.020 | 0.015 | 0.000 | |
| qc | 0.098 | 0.150 | 0.100 | 0.057 | |
| qN2 | 0.034 | 0.013 | 0.034 | 0.070 | |
| q0 | -0.022 | -0.097 | -0.020 | 0.058 | |
|
|
N2 | 1.32 | 0.49 | 1.41 | 2.19 |
| CO | 1.60 | 0.74 | 1.72 | 2.56 | |
|
|
N2 | 16.5 | |||
| CO | 16.8 | ||||
|
|
N2 | 9.7 | |||
| CO | 11.6 |
a
E is the adsorption
energy in kcal/mol, qNa+, qN1,
qN2, qc, and q0
are the Mulliken atomic net charges in electron;
is the
dipole moment in D; ![]()
and ![]()
are the parallel and perpendicular polarizabilities
in au.b The electric field
F
is in au;
= 0 corresponds to the electric
field vector colinear with N2-N1-Na+
(O-C-Na+) and pointing toward Na+.