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Article

Crotonaldehyde Adsorption on Cu-Pt Surface Alloys: A Quantum Mechanics Study

by
Ricardo Ruvalcaba
1,
Jonathan Guerrero-Sanchez
1,
Noboru Takeuchi
1 and
Francisco Zaera
2,*
1
Centro de Nanociencias y Nanotecnología, Universidad Nacional Autónoma de México, Ensenada 22860, Baja California, Mexico
2
Department of Chemistry and UCR Center for Catalysis, University of California Riverside, Riverside, CA 9252, USA
*
Author to whom correspondence should be addressed.
Chemistry 2023, 5(1), 463-478; https://doi.org/10.3390/chemistry5010034
Submission received: 27 January 2023 / Revised: 23 February 2023 / Accepted: 1 March 2023 / Published: 3 March 2023

Abstract

:
The adsorption of crotonaldehyde on Cu-Pt alloy surfaces was characterized by density functional theory (DFT). Two surfaces were considered: Cu2Pt/Cu(111) and Cu3Pt/Cu(111). It was determined that the presence of Pt on the surface, even when isolated as single atoms fully surrounded by Cu, provides additional stability for the adsorbates, increasing the magnitude of the adsorption energy by as much as 40 kJ/mol. The preferred bonding on both surfaces is via multiple coordination, with the most stable configuration being a cis arrangement with di-σ bonding of the C=O bond across a Cu–Cu bridge and an additional π bonding to a Pt atom. The fact that Pt significantly affects the adsorption of unsaturated aldehydes such as crotonaldehyde explains why the kinetics of their hydrogenation using single-atom alloy (SAA) catalysts vary with alloy composition, as we previously reported, and brings into question the simple model in which the role of Pt is only to promote the dissociation of H2.

Graphical Abstract

1. Introduction

Heterogeneous catalysis is at the center of a vast range of industrial processes, and many of the catalysts used in these are based on transition-metal nanoparticles (NPs) dispersed on high-surface-area supports [1,2,3]. It has long been recognized that the performance of pure metals is not always optimal and needs to be improved via the addition of other elements; alloys in particular afford the fine-tuning of the electronic properties of metals for this purpose [4,5,6]. Metal alloying has been a useful approach when designing selective hydrogenation catalysts, as it is often the case that platinum-group metals (Pt, Pd, and Rh in particular) are the most active promoters of hydrogenations of organic feedstocks with multiple unsaturations but are not particularly discriminating; the main product usually is the fully hydrogenated molecules [1,7,8,9].
In order to tame the activity of Pt, Pd, Rh, or Ir metals and to improve their selectivity, it has been customary to add a second metal as an additive [1,6,10]. Sn, for instance, has been used extensively to modify the performance of Pt-based catalysts in oil-refining processes [4,11,12,13,14,15]. More recently, this line of thought has been turned on its head, because when it comes to hydrogenation selectivity, it is quite possible that coinage metals may be the best choices [16,17,18]. Unfortunately, pure coinage metals are often not viable hydrogenation catalysts because they are not effective at promoting the required scission of the H–H bond in H2 [17,19,20]. For that, it may be a good solution to add a platinum metal (Pt, Pd) as an additive and a minority component. Accordingly, it may be that once hydrogen atoms are produced on the Pt or Pd sites and spilled over onto the coinage metal substrate, the rest of the hydrogenation steps can take place selectively. This is the premise underpinning the excitement over the new generation of so-called single-atom alloy (SAA) catalysts [21,22,23,24].
Much surface-science work with model systems [25,26], in conjunction with quantum mechanics calculations [27,28], has provided support for the viability of SAAs functioning according to the mechanism stated above. However, with realistic supported catalysts and in catalytic processes carried out under atmospheric conditions, a number of complications arise requiring further consideration [29]. For one, individual atoms within alloys can easily diffuse in and out of the surface of the bimetallic NPs, a process often facilitated by temperature and also by the presence of the reaction mixture [16,30,31,32,33,34,35]. It is therefore important to determine where the minority metal in SAAs is placed within the supported bimetallic NPs during the catalytic reaction. In addition, alloying one metal with another modifies its electronic properties, potentially changing its chemical behavior [36,37,38,39]. It has been recently argued that the d band of platinum-group and coinage metals display maximum density of states (DOS) at significantly different energies, a fact that minimizes any orbital mixing when alloying the two [27,28,39,40,41]; this would justify considering the minority metal (Pt, Pd) as isolated and unaffected by the surrounding majority component (Cu, Ag, Au). Nevertheless, some electron transfer is still likely to happen, and, in any case, if not the d orbitals, at least the sp band is fully delocalized across the whole bimetallic NP and can be affected by metal mixing [42]. Additional entropic factors may be introduced by the reaction mixture as well [43].
Lastly, many adsorbates require multiple-atom ensembles to bind to the surface, and new combinations of those become available in bimetallic NPs [44,45,46]. The added flexibility in creating new atom ensembles on the surface is in fact the basis for much catalysis design, to, for instance, minimize coke formation in reforming processes [47]. It is therefore important to understand how the addition of a second metal in SAAs may affect the adsorption energetics of the reactants [48,49]. This is the issue addressed in the present report. Our study focuses on the adsorption of crotonaldehyde, a prototypical unsaturated aldehyde, and on Cu surfaces modified by diluted Pt atoms. Cu-Pt SAAs have already been shown to improve the selectivity of several hydrocarbon conversions [33,50,51,52,53], including the hydrogenation of unsaturated aldehydes [16,54]. However, kinetic data acquired for those reactions as a function of alloy composition have suggested that the role of the added Pt is not only to promote H2 activation, that is, to help with the dissociation of the H–H bond, but to also affect the subsequent hydrogenation of the unsaturations of the reactant, the C=C and C=O bonds in the case of unsaturated aldehydes [54]. Here, we provide results from density functional theory (DFT) calculations indicating that, indeed, the addition of Pt atoms to Cu surfaces modifies the uptake of unsaturated aldehydes, changing their adsorption geometry to favor multiple coordinations and increasing their adsorption energy. It is argued that the role of the added Pt in these SAAs is more complex than previously appreciated.

2. Methods

The quantum mechanics study reported here relied on spin-unrestricted first-principles calculations based on periodic DFT, as implemented in the Vienna Ab initio Simulation Package (VASP) [55]. The calculations were performed using the Projector Augmented Wave (PAW) pseudopotentials [56,57]. The exchange-correlation energy was described using the generalized gradient approximation with the Perdew-Burke-Ernzerhof (PBE-GGA) parameterization [58]. The electronic states were expanded in plane waves with an energy cutoff of 400 eV. Forces on individual atoms were optimized up to 1 × 103 Ry/a.u. The Van der Waals interactions were modeled using the Grimme D3 method [59]. The Brillouin zone integrations were performed using 10 × 10 × 10 and 5 × 5 × 1 Monkhorst-Pack k-point grids [60] for the bulk and the surfaces, respectively, and a Methfessel-Paxton smearing [61] of the second order of the Fermi-Dirac distribution function was used, with a width of 0.2 eV. The lattice parameter used for bulk Cu, which was structurally optimized, was a = 0.36 nm. Using the supercell method, the surfaces were modeled by periodically repeating slabs with nine atomic planes along the [111] direction and with a vacuum larger than 10 Å. The bimetallic surfaces, the Cu3Pt/Cu(111) and Cu2Pt/Cu(111) systems, were constructed by adding Pt atoms in the periodic patterns shown in Figure 1a, but only on the topmost layer; all the other subsurface layers consisted of pure Cu. The structures of all these cells were optimized before exploring the adsorption of crotonaldehyde. It is worth pointing out that the size and shape of the unit cells are different in the two alloy cases, as the periodicity of the alloys is defined by their stoichiometry and fixes the characteristics of their repetitive pattern. The Hessian matrix and phonon frequencies were calculated using the finite differences method. The infrared absorption spectroscopy intensities were calculated using Density Functional Perturbation Theory (DFPT) [62] and processed using the program published by David Karhánek [63] based on linear response theory. The illustrations of the crystal structures and graphs presented in this paper were generated using the VESTA [64] and Matplotlib [65] codes, respectively.
On the basis of our quantum mechanical calculations, adsorption energies were calculated using the following equation:
Eads = Esurface crotonaldehyde − Esurface − Eisolated crotonaldeyde
where Esurface crotonaldehyde reflects the energy of every adsorption configuration considered in this study, Esurface is the energy of the clean surface in each case (for each alloy), and Eisolated crotonaldeyde is the energy of the isolated molecule in the gas phase. All Eads is reported in units of kJ/mol.

3. Results

3.1. Energetics and Structural Properties

Calculations were first carried out for the four rotational conformers of crotonaldehyde in the gas phase: E-(s)-trans, E-(s)-cis, Z-(s)-trans, and Z-(s)-cis (Figure 1b). E-(s)-trans was found to be the most stable conformer, and the other structures to exhibit higher energies by differences of 9.6, 11.8, and 16.0 kJ/mol, respectively. In the following study, only the adsorption of crotonaldehyde in its E-(s) configurations was considered, because those are the most stable.
The bonding of crotonaldehyde to the Cu2Pt/Cu(111) and Cu3Pt/Cu(111) surfaces was optimized for both the cis and trans isomers considering a variety of coordination modes, ranging from a single coordination via the oxygen atom (η1-O) to a fourfold coordination via bonding to all O, C1, C2, and C3 atoms (η4). The most stable structures obtained for each case are shown in Figure 2, and the corresponding energetics of adsorption reported in Figure 3. The adsorption energies for cis- and trans-crotonaldehydes on pure Cu(111) and Pt(111), reported before [66], were included in Figure 3 for reference. The key bond distances estimated for the adsorbed structures calculated for the cis and trans isomers are summarized in Table 1 and Table 2, respectively.
Some interesting trends are evident from the data in Figure 2 and Figure 3. In terms of bonding, it is seen that, in all cases, single coordination of crotonaldehyde to the surface is via the formation of a Cu–O bond. On pure Pt η1 bonding is also via the terminal oxygen atom, but in both alloy surfaces attachment to the Cu atoms is still preferred. On the other hand, the η2-OC1 and η2-C2C3 coordinations are the most stable if the carbon atom binds to an adjacent Pt center (the oxygen atom still binds to Cu); the latter is the most stable of the two in all four surfaces considered here. In terms of the relative behavior of the cis versus trans isomers, the former is always less stable than the latter in the low-coordination η1-O and η2-OC1 configurations, but that trend flips for the η2-C2C3 case (except on pure Cu(111)); the possibility of having the C3 atom interact with a surface Pt center provides a particularly large stabilizing effect. Then, for the η3-OC2C3 and η4 coordinations, the cis isomer is always the most stable of the two. This can be justified in terms of an increase in chain stress forced by the multiple coordination to the surface in the trans case, but it is also interesting to note that, in the structures shown in Figure 2, the C=C double bond coordinates to the surface of the alloys in a di-σ rehybridized form across a Cu–Pt bridge in the trans cases but it does so via π bonding to a single Pt atom with the cis isomer. Curiously, the same difference in bonding mode was seen on pure Cu(111) and Pt(111) surfaces [66]. It has been previously reported that the most stable form of adsorbed ethylene on both Cu(111) and Cu3Pt(111) is in the π geometry, on Cu3Pt(111) on a Pt atop site, and the vibrational spectrum of ethylene adsorbed on Cu(111) was found to be very different from that observed on Cu3Pt(111) [67]. It can be inferred that π bonding of C=C double bonds is favored over di-σ coordination, hence the stronger adsorption of the cis- (versus trans-) crotonaldehyde reported here.
Another observation deriving from the calculations reported in Figure 2 and Figure 3 is that, in general, higher coordination to the surface stabilizes the adsorbates. This trend is more clearly seen with the cis isomer but it often applies to the trans configuration as well, the exception being the η3-OC2C3 bonding mode, which appears to be destabilized by the strain put on the hydrocarbon chain. As a consequence, the most stable adsorbed species in almost all cases is the one with η4 coordination to the surface; only with the trans isomer does a η2-C2C3 coordination prevail over the η4 option on Cu(111) and Cu2Pt/Cu(111). It should be noted that higher coordination typically leads to a larger footprint of the adsorbates on the surface, which may be viable only at low coverages. As the coverage increases, more compressed layers form, thus destabilizing such multiple bonding. The end result is that, at times, the adsorption geometry may change to a less coordinated arrangement. In the case of acrolein on Cu(111), for instance, a switch from η4 to η3-OC2C3 was calculated when transitioning from a coverage of θ = 1/9 ML to θ = 1/4 [18].
Additional details on the nature of the bonds in the adsorbed crotonaldehyde can be extracted from the information on bond distances provided in Table 1 and Table 2. For one, it is interesting to note that, in spite of the fact that most of the configurations considered here involve some bonding through the oxygen atom in the carbonyl moiety, the C1=O bond only stretches marginally upon bonding to the surface, by less than 0.08 Å, and often by only ~0.02 Å in the η1-O coordination. Some rehybridization of the C=O bond would be expected in that case, but the final bond lengths seen here are quite far from those expected for C–O single bonds (1.43 Å in ethanol); the limited bond hybridization justifies the weak nature of the adsorption of the aldehyde on the Cu surfaces. Not surprisingly, larger C–O bond lengths are observed in the structures where the bond is oriented close to parallel to the surface plane (a di-σ rehybridized structure), as seen in some of the η2-OC1, η3-OC2C3, and η4 configurations. Similar arguments can be put forward for the C2=C3 double bond: its length is affected only when it interacts with the surface via di-σ bonding. On the other hand, the effect in the C=C bond is more pronounced than in the C=O case, as values as high as 1.46 Å can be seen (for the η3-OC2C3 configuration of the trans isomer in Cu3Pt/Cu(111)), an elongation more than half way toward the length of a C–C single bond (1.54 Å in ethane). It should be noted that the differences seen here between the cis and trans isomers are not too significant and cannot be used to fully explain the adsorption energy differences estimated for the two isomers. What may be relevant is that the C1–C2 bond distance is also affected by the adsorption, becoming shorter to different extents in the several cases considered; it appears that a degree of intramolecular rehybridization may take place. An extreme of this rehybridization can be seen for trans-crotonaldehyde adsorbed on C3Pt/Cu(111) in a η4 configuration: the C1–C2 and C2=C3 bond distances calculated for that adsorbate are 1.434 and 1.440 Å, respectively, suggestive of the formation of an allylic species with a delocalized double bond.
An important conclusion from these calculations is that the presence of Pt atoms on the surface appears to provide an additional stabilizing factor leading to stronger bonding of crotonaldehyde to the surface via multiple coordination. It is particularly notable that, whereas the adsorption energies of both cis and trans isomers of crotonaldehyde remain relatively unaffected by the extent of coordination on the Cu(111) surface, larger effects are seen on the other three surfaces. As indicated above, this is due to the additional bond that appears to form between the C3 atom and a Pt surface atom. The observed behavior is true regardless of the presence of Cu (in the alloys, compared to pure Pt(111)), or of the coordination mode of the C=C bond, di-σ with the trans isomer or π with the cis counterpart (although the effect is larger in the latter case). It can be said that, if Pt atoms are present on the surface of the Cu-Pt SAA catalysts, they are likely to affect the energetics of the hydrogenation steps during unsaturated aldehyde hydrogenation; the role of such Pt may therefore not just be that of activating the H–H bond in H2. Our previous kinetic studies on the catalytic hydrogenation of cinnamaldehyde promoted by CuPtx/SBA-15 catalysts had already provided indirect evidence for this additional contribution of Pt to the kinetics and thermodynamics of the hydrocarbon conversion steps [54].
One interesting quirk seen in the data in Figure 3 is that bonding of crotonaldehyde to Cu2Pt/Cu(111) is slightly weaker than to Cu3Pt/Cu(111), in spite of the fact that the former surface has a higher Pt coverage than the latter. However, this difference is small, and may be related to the different sizes of the unit cells used in each case (Figure 1a), which leads to slightly different surface coverages; the structure of all adsorbates, of both cis and isomers of crotonaldehyde in all η1-O to η4 configurations, are almost identical in the two alloyed surfaces (Figure 2).
To further understand the nature of the bonding of crotonaldehyde to the Cu-Pt alloys, the DOS of the various molecular orbitals were calculated for the more relevant adsorption configurations. The data for the Cu2Pt/Cu(111) surface are shown in Figure 4. Several observations are worth highlighting. For instance, the η1-O structure (Figure 4a) shows several peaks at negative energies from ~−3.0 eV to −4.5 eV related to the C2=C3 and C–H molecular bonds, as those do not interact with the surface. On the other hand, the peak at ~−1.5 eV is related to the C dangling bond that develops upon O attachment to the surface. Similar behavior is observed in the η2-OC1 configuration (Figure 4b), in which case the dangling bond associated with the C1 atom disappears because of its bonding to the surface. Notice that here the peaks at more negative energies, associated with the C2=C3 bond, remain. In the η2-C2C3 coordination (Figure 4c), the negative peaks from ~−3.0 eV to −4.5 eV are reduced because the C2=C3 bond rehybridizes and because the two carbons form two new single bonds with the surface. In exchange, a new peak consisting mainly of CH-sp and O-sp orbitals appears around the Fermi energy. A similar trend is observed in the η3-OC2C3 (Figure 4d) and η4 (Figure 4e) species: the molecular peaks for all double bonds disappear because the molecule is fully attached to the surface. A fact to point out here is that in the η3-OC2C3 case, there are no peaks related to C1 dangling bonds as in η1-O. This is probably because there is still some interaction between the C1 atom and the surface, a fact that confirms the high affinity of Cu-Pt alloys to form highly coordinated systems. Our DOS analysis shows that, in every adsorption geometry, there is a distinctive projected density of states that evidences the formation of bonds in the corresponding molecule-surface complex.

3.2. Vibrational Properties

The vibrational modes of the most stable adsorption configurations of crotonaldehyde were also calculated; they are reported in Figure 5 and in Table 3. For the Cu3Pt/Cu(111) surface, results are provided for the η4-cis, η3-OC2C3-cis, η2-C2C3-cis, and η4-trans configurations, whereas for the Cu2Pt surface only the data for the η4-cis configuration are presented. The assignments of the modes were aided by information provided in the literature for the vibrational spectra of pure crotonaldehyde [68] as well as for crotonaldehyde adsorbed on Pt(111) [69] and on the surface of a Cu polished disk [66]. Unfortunately, there are no experimental data available in the literature for the vibrational spectra of crotonaldehyde adsorbed on Cu-Pt alloys: the IR spectra reported in our past publication with CuPtx/SBA-15 catalysts is likely to be dominated by adsorption on the silica support (blank experiments were performed to check that; data not shown) [16], and we have not yet succeeded in preparing Pt/Cu surfaces under UHV stable enough to be useful to test the adsorption of molecules on them (as mentioned in the Introduction, us and others have determined that the Pt atoms tend to diffuse into the bulk at relatively low temperatures [16,30,31,32,33,34,35]). There are, however, high-resolution electron-loss spectroscopy data for acrolein adsorbed on Pt–Cu–Pt(111) and Cu–Pt–Pt(111) substrates (with a Cu layer in the subsurface or surface regions, respectively) [70], which can be used to extract general trends. Given the clearly distinct IR spectra obtained for crotonaldehyde on Pt(111) [69] versus polycrystalline Cu [66], the new calculations on the CuxPt/Cu(111) can provide some clues on what to expect in the new systems as well.
One important distinctive vibrational mode in these adsorbates is the C=O stretching mode, because it appears around 1670–1710 cm−1, in a range quite separate from the rest of the spectra. That mode is quite prominent in the traces for Pt(111) [69], but barely seen on Cu [66]. With acrolein, the peak is quite intense on Pt(111) (~1700 cm−1) [71], but not detectable on Cu(111) [72], Cu–Pt–Pt(111), or Cu–Pt–Pt(111) [70]. Here, no peaks are seen in the spectra for adsorbed crotonaldehyde in any of the configurations for which the data were calculated. As it has been discussed before, the suggestion is that the C=O bond may be oriented in a direction close to the plane of the surface, in which case the surface selection rule that apply to IR spectra on metals predicts no peak intensity at all [73,74]. What can be seen in the vibrational data for η2-C2C3-cis crotonaldehyde on Cu3Pt/Cu(111) is a feature at 1594 cm−1 associated with its C=C stretching mode. This is also a signature peak in the experimental data for crotonaldehyde on pure Cu (1650 cm−1) [66] and for acrolein on Pt–Cu–Pt (111) (1644 cm−1), but such peak is not seen with Cu–Pt–Pt(111) [70]. Overall, the relative intensities of the C=O and C=C stretching peaks can provide insightful information on the configuration adopted by unsaturated aldehydes upon adsorption; our calculations suggest that in the Cu-Pt bimetallic surfaces, they may be dominated by the features due to bonding to Cu.
The other telling region of the infrared spectra of these adsorbed species worth discussing is that between approximately 1300 and 1500 cm−1, since there is where most C–H deformation modes become visible. The asymmetric deformation of the terminal methyl group in crotonaldehyde is noticeable in most spectra, on all Pt(111), Cu(111), and the mixed Pt–Cu–Pt(111) and Cu–Pt–Pt(111) surfaces; it appears at about 1450–1470 cm−1 [66,70]. On the other hand, the symmetric deformation (or umbrella) mode of the methyl moiety, typically located between 1330 and 1370 cm−1, has not been seen in any of those surfaces. In our calculations for crotonaldehyde on CuxPt/Cu(111) surfaces, several adsorption configurations do result in a detectable vibration for that mode. This is particularly noticeable for the Cu2Pt-η4-cis case (1358 cm−1), and to a lesser extent for the Cu3Pt-η3-OC2C3-cis (1356 cm−1) and Cu3Pt-η2-C2C3-cis (1356 cm−1) species. This pair of peaks, for the symmetric and asymmetric methyl deformation modes, can also be used to test the predictions of adsorption geometries for unsaturated aldehydes (with such methyl groups) once the experimental data become available.

4. Discussion

The main purpose of this investigation has been to assess the effect that the minority metal may play in the performance of SAA catalysts for hydrocarbon conversions. The specific case of the addition of Pt to Cu to improve on the performance of the hydrogenation of unsaturated aldehydes (crotonaldehyde) was tested by using quantum mechanics (DFT) calculations. It is often assumed that the role of Pt is only to activate molecular hydrogen and to form hydrogen atoms, which then spill over onto the Cu surface where the hydrocarbon hydrogenation steps are expected to take place [22]. However, the adsorption of hydrocarbons often involves sites composed of ensembles of surface atom, and if single Pt atoms are present on the surface, they are likely to participate in such hydrocarbon bonding; the interaction of hydrocarbons with Pt is in general much stronger than with Cu. Our calculations, reported above, corroborate this hypothesis for the case of crotonaldehyde.
What was found in this study is that the initial bonding of unsaturated aldehydes on Cu-Pt bimetallic surfaces takes place via the carbonyl oxygen atom (Figure 2). Moreover, in a η1-O configuration, the molecule binds preferentially to Cu atop sites; this was previously determined to be the case on pure Cu surfaces [66], and was shown here to be true for the Cu2Pt/Cu(111) and Cu3Pt/Cu(111) surfaces as well. Similar results were also reported previously for acrolein [16,18] and for cinnamaldehyde [75]. It is somewhat surprising that on the alloys the initial bonding happens on Cu centers given that bonding to Pt is stronger, at least for the cis isomer: Eads1-O-cis, Pt(111)) = −67.4 kJ/mol versus Eads1-O-cis, Cu(111)) = −53.0 kJ/mol (Figure 3). The adsorption of the trans isomer is approximately equally strong on both metals (Eads1-O-trans, Pt(111)) = Eads1-O-trans, Cu(111)) = −72.5 kJ/mol), but perhaps the main reason for the preferential bonding to Cu relates to potential additional interactions of other parts of the molecule with the adjacent metal atoms present on these surfaces.
Indeed, what we found is that the presence of Pt atoms leads to a preference for multiple coordination of crotonaldehyde to the surface. On pure Cu, the adsorption energy is not very sensitive to additional interactions between any of the carbon atoms of crotonaldehyde and the surface [66], but on pure Pt, multiple coordination leads to much stronger binding [66,69], and the data reported here indicate that the same is true with the Cu-Pt alloys. For one, in all η2-OC1 and η2-C2C3 configurations, the carbonyl and C=C groups of crotonaldehyde (respectively) both bind across a Cu–Pt bridge, with the O atoms placed on the Cu atoms and the C bonded to the Pt in the first case (Figure 2). Moreover, and more significantly, the more extensively coordinated η3-OC2C3 and η4 adsorptions show binding with both carbonyl and C=C groups, which make those species significantly more stable: the carbonyl group still binds with the O atom attached to Cu, but the C=C bond is π-bonded to a single Pt in the case of the more stable cis isomers (the trans isomer, with its weaker adsorption energies relative to the cis form, binds in a di-σ mode across a Cu–Pt bridge instead). The bottom line is that, if Pt is present on the surface of the alloy, even in single-atom form, that atom is likely to participate in the binding of the reactant, crotonaldehyde in this case. It must be concluded that, in addition to aiding in the activation of molecular hydrogen, the addition of Pt to Cu surfaces is likely to also affect the hydrocarbon hydrogenation steps. An indirect kinetic evidence for this conclusion was already obtained by us before for the case of cinnamaldehyde: both the equilibrium constants for the adsorption of the reactant and products and the reaction constants for the hydrogen incorporation steps were seen to vary with alloy composition in the CuPtx/SBA-15 catalysts, some by up to three orders of magnitude [54].
The fact that single Pt atoms on Cu surfaces affect the adsorption energies of crotonaldehyde is not surprising, and is expected to be a general effect. Even with individual atoms, significant differences in adsorption energies have been calculated on ensemble sites in Cu surfaces that include one Pt atom (compared to pure-Cu ensemble sites): for instance, the addition of Pt to Cu(111) has been calculated to cause decreases in the adsorption energy of carbon, oxygen, and nitrogen atoms by approximately 14, 15, and 18 kJ/mol, respectively [28]. A possible reason for this is the small electronic contribution that the nearest Cu atoms receive from the Pt d orbitals, leading to a depletion of the Cu 3d DOS. Similar effects have also been reported with other SAA metal combinations; the adsorption energy estimated for acrolein, for instance, have been shown to change upon the addition of a second dopant metal to Pt, Pd, Ni, Au, and Ag surfaces [76] On Cu–Pt–Pt(111), where Cu is added to a Pt surface, acrolein adsorption in a η4 configuration was estimated to be stabilized by an additional 1.3 kJ/mol, but in the case of Pt–Cu–Pt(111), where the Cu atoms are placed on the subsurface, the adsorption is destabilized by as much as 65 kJ/mol instead [70,77]. None of these reported systems simulate SAA surfaces directly, but nevertheless point to the clear effect exerted by the addition of a second metal on adsorption energies even if they are quite diluted.
The last point to be made here is that, in these calculations, it was assumed that the minority metal, Pt, is present (in diluted form) on the surface of the SAAs. The placement of such atoms within the bimetallic nanoparticles of SAA catalysts under reaction conditions has not, however, been fully established to date. As mentioned in the introduction, both temperature and gaseous or liquid chemicals in contact with the surface of these bimetallics can induce the preferential segregation of one of the elements to the surface or its diffusion back deep into the bulk [16,30,31,32,34,35]. For the case of Pt added to Cu, it has been repeatedly observed that Pt often disappears from the surface, typically upon exposures to atmospheric environments but even under controlled ultrahigh vacuum (UHV) conditions. These changes are often reversible [34], which means that post-mortem analysis of the surfaces after catalysis may not reflect the nature of the active catalytic surface. It could be thought that the reactants in hydrocarbon hydrogenation reactions may in fact drive the Pt atoms to the surface, as that metal binds the reactants more strongly than Cu, but experiments with CO have shown the opposite behavior [16,34]. Clearly, our calculations here only address the situation where the Pt atoms are present on the surface; the conclusion that Pt affects the adsorption energies of the reactants and products and therefore the kinetics of the catalysis may not apply if those atoms diffuse into the bulk during reaction. Additional studies would need to be carried out to evaluate those circumstances, as Pt may still exert a remote electronic effect in those cases.

5. Conclusions

Quantum mechanics (DFT) calculations were performed to assess the details of the adsorption of crotonaldehyde on two Cu-Pt alloy surfaces, namely, on ordered Cu2Pt/Cu(111) and Cu3Pt/Cu(111) structures, where Pt was added only to the top-most (exposed) surface, and compared with similar estimates previously carried out by us on pure Cu(111) and pure Pt(111) [66]. Different coordination modes were considered, from single bonds, which were found to be the most stable between the O atom in the carbonyl moiety of the unsaturated aldehyde and a Cu atom in an atop position, to η4 configurations involving the O atom together with its three nearest C atoms in the hydrocarbon chain. Both cis and trans isomers of crotonaldehyde were considered as well. From an energetics point of view, it was determined that the addition of Pt atoms to the surface, even in dilute form, increases the magnitude of the adsorption energy. Two possible η2 binding forms were tested, via the carbonyl (OC1) and via the C=C (C2C3) double bonds, and the latter was found to be the more favorable of the two in all cases. Regardless, bonding in all those structures was determined to occur in di-σ fashion, across a Cu–Pt bridge. Coordination in η3-OC2C3 mode provides additional stability for the cis isomer but not for the trans counterpart, presumably because of the chain strain required to accommodate the multiple bonding in the latter case. Finally, η4-OC1C2C3 is the preferred coordination in most cases, except for the trans isomer on pure Cu(111) and on Cu2Pt/Cu(111), for which the η2-C2C3 binding is slightly preferred. Ultimately, the cis isomer is more stable than the trans counterpart on all surface, in the case of the η4 configuration apparently because the C=C double bond π coordinates to a single Pt atom (it rehybridizes to a di-σ configuration across a Cu–Pt bridge with the trans isomer). Additionally, the addition of Pt to the surface increases the magnitude of the adsorption energy of the most stable configurations by approximately 20 to 40 kJ/mol.
The stabilization of the adsorption of crotonaldehyde on the Cu-Pt alloy surfaces is also evidenced by the changes in bond distances between relevant atoms. Such changes are minor in the case of the η1-O coordination, where even the C1=O bond often stretches by less than 0.02 Å, but become more noticeable when multiple coordination is involved, especially if rehybridization to di-σ bonding occurs. In fact, with trans-crotonaldehyde, η4 adsorption on C3Pt/Cu(111) leads to the formation of an allylic species where the C1–C2 and C2–C3 bonds have approximately the same length. Further evidence of the stabilizing effect of Pt toward crotonaldehyde adsorption was obtained from calculations of vibrational frequencies. Although no experimental data are available yet to make full use of those results, some key pointers were nevertheless identified highlighting what to expect. On the whole, the main conclusion from our study is that, if Pt atoms are present on the surface as it has been proposed for Cu-Pt SAA catalysts, they are likely to not only help with the activation of H2, to start hydrogenation reactions, but also affect the energetics of the subsequent H-incorporation steps into the unsaturated aldehyde hydrogenation. Past results from in situ characterization of Cu-Pt catalysts under catalytic conditions have suggested that the Pt atoms may in fact diffuse into the bulk of the bimetallic nanoparticles, in which case the results reported here would not be directly applicable, but even in that case there may be a remote electronic effect in play. This may be worth further investigation.

Author Contributions

R.R. and J.G.-S. carried out the calculations and performed the initial data analysis and interpretation. N.T. supervised the theoretical work, acquired funding for it, contributed with further data analysis, and helped with manuscript preparation. F.Z. conceived the project, acquire funding for it, directed the research, carried out the final complete data analysis, and wrote the manuscript. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the U.S. National Science Foundation, Division of Chemistry (NSF-CHE1953843; F.Z.) and DGAPA-UNAM (projects IN105722, IA100920), and Conacyt (A1-S-9070; R.R., J.G.-S., N.T.). Calculations were performed in the DGCTIC-UNAM Supercomputing Center, projects LANCAD-UNAM-DGTIC-051, and LANCAD-UNAM-DGTIC-368.

Data Availability Statement

Original data may be provided upon request to the authors.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Bond, G.C. Metal-Catalysed Reactions of Hydrocarbons; Springer: New York, NY, USA, 2005. [Google Scholar]
  2. Sanfilippo, D.; Rylander, P.N. Hydrogenation and Dehydrogenation. In Ullmann’s Encyclopedia of Industrial Chemistry; Wiley-VCH Verlag GmbH & Co. KGaA: Weinheim, Germany, 2012; Volume 18, pp. 451–471. [Google Scholar]
  3. Ma, Z.; Zaera, F. Heterogeneous Catalysis by Metals. In Encyclopedia of Inorganic and Bioinorganic Chemistry; Scott, R.A., Ed.; John Wiley & Sons, Ltd.: Chichester, UK, 2014; p. eibc0079. [Google Scholar]
  4. Sinfelt, J.H. Bimetallic Catalysts: Discoveries, Concepts and Applications; John Wiley and Sons: New York, NY, USA, 1983; p. 164. [Google Scholar]
  5. Ferrando, R.; Jellinek, J.; Johnston, R.L. Nanoalloys:  From Theory to Applications of Alloy Clusters and Nanoparticles. Chem. Rev. 2008, 108, 845–910. [Google Scholar] [CrossRef]
  6. Yu, W.; Porosoff, M.D.; Chen, J.G. Review of Pt-Based Bimetallic Catalysis: From Model Surfaces to Supported Catalysts. Chem. Rev. 2012, 112, 5780–5817. [Google Scholar] [CrossRef]
  7. Meemken, F.; Baiker, A. Recent Progress in Heterogeneous Asymmetric Hydrogenation of C═O and C═C Bonds on Supported Noble Metal Catalysts. Chem. Rev. 2017, 117, 11522–11569. [Google Scholar] [CrossRef]
  8. Zaera, F. The Surface Chemistry of Metal-Based Hydrogenation Catalysis. ACS Catal. 2017, 7, 4947–4967. [Google Scholar] [CrossRef]
  9. Zhang, L.; Zhou, M.; Wang, A.; Zhang, T. Selective Hydrogenation over Supported Metal Catalysts: From Nanoparticles to Single Atoms. Chem. Rev. 2020, 120, 683–733. [Google Scholar] [CrossRef]
  10. Vilé, G.; Albani, D.; Almora-Barrios, N.; López, N.; Pérez-Ramírez, J. Advances in the Design of Nanostructured Catalysts for Selective Hydrogenation. ChemCatChem 2016, 8, 21–33. [Google Scholar] [CrossRef]
  11. Burch, R.; Garla, L.C. Platinum-tin reforming catalysts: II. Activity and selectivity in hydrocarbon reactions. J. Catal. 1981, 71, 360–372. [Google Scholar] [CrossRef]
  12. Joyner, R.W.; Shpiro, E.S. Alloying in platinum-based catalysts for gasoline reforming: A general structural proposal. Catal. Lett. 1991, 9, 239–243. [Google Scholar] [CrossRef]
  13. Delbecq, F.; Sautet, P. Influence of Sn additives on the selectivity of hydrogenation of α-β-unsaturated aldehydes with Pt catalysts: A density functional study of molecular adsorption. J. Catal. 2003, 220, 115–126. [Google Scholar] [CrossRef]
  14. Yang, X.; Koel, B.E. Adsorption and Reaction of Unsaturated Hydrocarbons on Sn/Pt Alloys. In Encyclopedia of Interfacial Chemistry; Wandelt, K., Ed.; Elsevier: Oxford, UK, 2018; pp. 1–10. [Google Scholar]
  15. Stassi, J.; Méndez, J.; Vilella, I.; de Miguel, S.; Zgolicz, P. Synthesis of PtSn nanoparticles on carbon materials by different preparation methods for selective catalytic hydrogenation of citral. Chem. Eng. Commun. 2020, 207, 1074–1091. [Google Scholar] [CrossRef]
  16. Cao, Y.; Chen, B.; Guerrero-Sánchez, J.; Lee, I.; Zhou, X.; Takeuchi, N.; Zaera, F. Controlling Selectivity in Unsaturated Aldehyde Hydrogenation Using Single-Site Alloy Catalysts. ACS Catal. 2019, 9, 9150–9157. [Google Scholar] [CrossRef]
  17. Chen, B.; Zaera, F. Hydrogenation of Cinnamaldehyde on Cu(110) Single-Crystal Surfaces. J. Phys. Chem. C 2021, 125, 14709–14717. [Google Scholar] [CrossRef]
  18. Nayakasinghe, M.T.; Ponce Perez, R.; Chen, B.; Takeuchi, N.; Zaera, F. Adsorption, thermal conversion, and catalytic hydrogenation of acrolein on Cu surfaces. J. Catal. 2022, 414, 257–266. [Google Scholar] [CrossRef]
  19. Johansson, M.; Lytken, O.; Chorkendorff, I. The sticking probability for H2 on some transition metals at a hydrogen pressure of 1 bar. J. Chem. Phys. 2008, 128, 034706. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  20. Álvarez-Falcón, L.; Viñes, F.; Notario-Estévez, A.; Illas, F. On the hydrogen adsorption and dissociation on Cu surfaces and nanorows. Surf. Sci. 2016, 646, 221–229. [Google Scholar] [CrossRef]
  21. Han, J.; Lu, J.; Wang, M.; Wang, Y.; Wang, F. Single Atom Alloy Preparation and Applications in Heterogeneous Catalysis. Chin. J. Chem. 2019, 37, 977–988. [Google Scholar] [CrossRef]
  22. Hannagan, R.T.; Giannakakis, G.; Flytzani-Stephanopoulos, M.; Sykes, E.C.H. Single-Atom Alloy Catalysis. Chem. Rev. 2020, 120, 12044–12088. [Google Scholar] [CrossRef]
  23. Zaera, F. Molecular approaches to heterogeneous catalysis. Coord. Chem. Rev. 2021, 448, 214179. [Google Scholar] [CrossRef]
  24. Zaera, F. Designing Sites in Heterogeneous Catalysis: Are We Reaching Selectivities Competitive with Those of Homogeneous Catalysts? Chem. Rev. 2022, 122, 8594–8757. [Google Scholar] [CrossRef]
  25. Luneau, M.; Lim, J.S.; Patel, D.A.; Sykes, E.C.H.; Friend, C.M.; Sautet, P. Guidelines to Achieving High Selectivity for the Hydrogenation of α,β-Unsaturated Aldehydes with Bimetallic and Dilute Alloy Catalysts: A Review. Chem. Rev. 2020, 120, 12834–12872. [Google Scholar] [CrossRef]
  26. Sykes, E.C.H.; Christopher, P. Recent advances in single-atom catalysts and single-atom alloys: Opportunities for exploring the uncharted phase space in-between. Curr. Opin. Chem. Eng. 2020, 29, 67–73. [Google Scholar] [CrossRef]
  27. Thirumalai, H.; Kitchin, J.R. Investigating the Reactivity of Single Atom Alloys Using Density Functional Theory. Top. Catal. 2018, 61, 462–474. [Google Scholar] [CrossRef]
  28. Schumann, J.; Bao, Y.; Hannagan, R.T.; Sykes, E.C.H.; Stamatakis, M.; Michaelides, A. Periodic Trends in Adsorption Energies around Single-Atom Alloy Active Sites. J. Phys. Chem. Lett. 2021, 12, 10060–10067. [Google Scholar] [CrossRef] [PubMed]
  29. Zaera, F. In-Situ and Operando Spectroscopies for the Characterization of Catalysts and of Mechanisms of Catalytic Reactions. J. Catal. 2021, 404, 900–910. [Google Scholar] [CrossRef]
  30. Zafeiratos, S.; Piccinin, S.; Teschner, D. Alloys in catalysis: Phase separation and surface segregation phenomena in response to the reactive environment. Catal. Sci. Technol. 2012, 2, 1787–1801. [Google Scholar] [CrossRef] [Green Version]
  31. Gumuslu, G.; Kondratyuk, P.; Boes, J.R.; Morreale, B.; Miller, J.B.; Kitchin, J.R.; Gellman, A.J. Correlation of Electronic Structure with Catalytic Activity: H2–D2 Exchange across CuxPd1–x Composition Space. ACS Catal. 2015, 5, 3137–3147. [Google Scholar] [CrossRef]
  32. Simonovis, J.P.; Hunt, A.; Palomino, R.M.; Senanayake, S.D.; Waluyo, I. Enhanced Stability of Pt-Cu Single-Atom Alloy Catalysts: In Situ Characterization of the Pt/Cu(111) Surface in an Ambient Pressure of CO. J. Phys. Chem. C 2018, 122, 4488–4495. [Google Scholar] [CrossRef]
  33. Yang, K.; Yang, B. Identification of the Active and Selective Sites over a Single Pt Atom-Alloyed Cu Catalyst for the Hydrogenation of 1,3-Butadiene: A Combined DFT and Microkinetic Modeling Study. J. Phys. Chem. C 2018, 122, 10883–10891. [Google Scholar] [CrossRef]
  34. Han, T.; Li, Y.; Cao, Y.; Lee, I.; Zhou, X.; Frenkel, A.I.; Zaera, F. In situ identification of surface sites in Cu–Pt bimetallic catalysts: Gas-induced metal segregation. J. Chem. Phys. 2022, 157, 234706. [Google Scholar] [CrossRef]
  35. Finzel, J.; Christopher, P. Dynamic Pt Coordination in Dilute AgPt Alloy Nanoparticle Catalysts Under Reactive Environments. Top. Catal. 2022, 65, 1587–1603. [Google Scholar] [CrossRef]
  36. Rodriguez, J.A. Physical and Chemical Properties of Bimetallic Surfaces. Surf. Sci. Rep. 1996, 24, 223–287. [Google Scholar] [CrossRef]
  37. Wang, Y.; Balbuena, P.B. Design of Oxygen Reduction Bimetallic Catalysts:  Ab-Initio-Derived Thermodynamic Guidelines. J. Phys. Chem. B 2005, 109, 18902–18906. [Google Scholar] [CrossRef]
  38. Medford, A.J.; Vojvodic, A.; Hummelshøj, J.S.; Voss, J.; Abild-Pedersen, F.; Studt, F.; Bligaard, T.; Nilsson, A.; Nørskov, J.K. From the Sabatier principle to a predictive theory of transition-metal heterogeneous catalysis. J. Catal. 2015, 328, 36–42. [Google Scholar] [CrossRef] [Green Version]
  39. Greiner, M.T.; Jones, T.E.; Beeg, S.; Zwiener, L.; Scherzer, M.; Girgsdies, F.; Piccinin, S.; Armbrüster, M.; Knop-Gericke, A.; Schlögl, R. Free-atom-like d states in single-atom alloy catalysts. Nat. Chem. 2018, 10, 1008–1015. [Google Scholar] [CrossRef]
  40. Duchesne, P.N.; Li, Z.Y.; Deming, C.P.; Fung, V.; Zhao, X.; Yuan, J.; Regier, T.; Aldalbahi, A.; Almarhoon, Z.; Chen, S.; et al. Golden single-atomic-site platinum electrocatalysts. Nat. Mater. 2018, 17, 1033–1039. [Google Scholar] [CrossRef] [Green Version]
  41. Hopper, N.; Thuening, T.; Manzi, S.; Weinert, M.; Tysoe, W.T. Binding of Oxygen on Single-Atom Sites on Au/Pd(100) Alloys with High Gold Coverages. J. Phys. Chem. C 2021, 125, 9715–9729. [Google Scholar] [CrossRef]
  42. Xin, H.; Vojvodic, A.; Voss, J.; Nørskov, J.K.; Abild-Pedersen, F. Effects of d-band shape on the surface reactivity of transition-metal alloys. Phys. Rev. B 2014, 89, 115114. [Google Scholar] [CrossRef]
  43. Han, T.; Lee, I.; Cao, Y.; Zhou, X.; Zaera, F. Thermodynamics of Carbon Monoxide Adsorption on Cu/SBA-15 Catalysts: Under Vacuum versus under Atmospheric Pressures. J. Phys. Chem. C 2022, 126, 3078–3086. [Google Scholar] [CrossRef]
  44. Ponec, V. Alloy catalysts: The concepts. Appl. Catal. A 2001, 222, 31–45. [Google Scholar] [CrossRef]
  45. Liu, P.; Nørskov, J.K. Ligand and ensemble effects in adsorption on alloy surfaces. Phys. Chem. Chem. Phys. 2001, 3, 3814–3818. [Google Scholar] [CrossRef]
  46. Gao, F.; Goodman, D.W. Pd-Au bimetallic catalysts: Understanding alloy effects from planar models and (supported) nanoparticles. Chem. Soc. Rev. 2012, 41, 8009–8020. [Google Scholar] [CrossRef] [PubMed]
  47. Trimm, D.L. Coke Formation and Minimisation During Steam Reforming Reactions. Catal. Today 1997, 37, 233–238. [Google Scholar] [CrossRef]
  48. Marcella, N.; Lim, J.S.; Płonka, A.M.; Yan, G.; Owen, C.J.; van der Hoeven, J.E.S.; Foucher, A.C.; Ngan, H.T.; Torrisi, S.B.; Marinkovic, N.S.; et al. Decoding reactive structures in dilute alloy catalysts. Nat. Commun. 2022, 13, 832. [Google Scholar] [CrossRef]
  49. Mancera, L.A.; Diemant, T.; Groß, A.; Behm, R.J. Molecular and Dissociative Hydrogen Adsorption on Bimetallic PdAg/Pd(111) Surface Alloys: A Combined Experimental and Theoretical Study. J. Phys. Chem. C 2022, 126, 3060–3077. [Google Scholar] [CrossRef]
  50. Lucci, F.R.; Liu, J.; Marcinkowski, M.D.; Yang, M.; Allard, L.F.; Flytzani-Stephanopoulos, M.; Sykes, E.C.H. Selective hydrogenation of 1,3-butadiene on platinum–copper alloys at the single-atom limit. Nat. Commun. 2015, 6, 8550. [Google Scholar] [CrossRef] [Green Version]
  51. Humbert, M.P.; Chen, J.G. Correlating hydrogenation activity with binding energies of hydrogen and cyclohexene on M/Pt(111) (M = Fe, Co, Ni, Cu) bimetallic surfaces. J. Catal. 2008, 257, 297–306. [Google Scholar] [CrossRef]
  52. Lv, C.-Q.; Liu, J.-H.; Guo, Y.; Wang, G.-C. Selective hydrogenation of 1,3-butadiene over single Pt1/Cu(111) model catalysts: A DFT study. Appl. Surf. Sci. 2019, 466, 946–955. [Google Scholar] [CrossRef]
  53. Liu, D.; Chen, H.Y.; Zhang, J.Y.; Huang, J.Y.; Li, Y.M.; Peng, Q.M. Theoretical investigation of selective hydrogenation of 1,3-butadiene on Pt doping Cu nanoparticles. Appl. Surf. Sci. 2018, 456, 59–68. [Google Scholar] [CrossRef]
  54. Cao, Y.; Guerrero-Sańchez, J.; Lee, I.; Zhou, X.; Takeuchi, N.; Zaera, F. Kinetic Study of the Hydrogenation of Unsaturated Aldehydes Promoted by CuPtx/SBA-15 Single-Atom Alloy (SAA) Catalysts. ACS Catal. 2020, 10, 3431–3443. [Google Scholar] [CrossRef]
  55. Kresse, G.; Furthmüller, J. Efficient iterative schemes for ab initio total-energy calculations using a plane-wave basis set. Phys. Rev. B 1996, 54, 11169–11186. [Google Scholar] [CrossRef]
  56. Blöchl, P.E. Projector augmented-wave method. Phys. Rev. B 1994, 50, 17953–17979. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  57. Kresse, G.; Joubert, D. From ultrasoft pseudopotentials to the projector augmented-wave method. Phys. Rev. B 1999, 59, 1758–1775. [Google Scholar] [CrossRef]
  58. Perdew, J.P.; Burke, K.; Ernzerhof, M. Generalized Gradient Approximation Made Simple. Phys. Rev. Lett. 1996, 77, 3865–3868. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  59. Grimme, S.; Antony, J.; Ehrlich, S.; Krieg, H. A consistent and accurate ab initio parametrization of density functional dispersion correction (DFT-D) for the 94 elements H-Pu. J. Chem. Phys. 2010, 132, 154104. [Google Scholar] [CrossRef] [Green Version]
  60. Monkhorst, H.J.; Pack, J.D. Special points for Brillouin-zone integrations. Phys. Rev. B 1976, 13, 5188–5192. [Google Scholar] [CrossRef]
  61. Methfessel, M.; Paxton, A.T. High-precision sampling for Brillouin-zone integration in metals. Phys. Rev. B 1989, 40, 3616–3621. [Google Scholar] [CrossRef] [Green Version]
  62. Wu, X.; Vanderbilt, D.; Hamann, D.R. Systematic treatment of displacements, strains, and electric fields in density-functional perturbation theory. Phys. Rev. B 2005, 72, 035105. [Google Scholar] [CrossRef] [Green Version]
  63. Karhánek, D. Dakarhanek/Vasp-Infrared-Intensities: Vasp-Infrared-Intensities; (Version v1.0); Zenodo, 2020; Available online: https://zenodo.org/record/3930989#.ZAF24R9ByUk (accessed on 26 January 2023).
  64. Momma, K.; Izumi, F. VESTA 3 for three-dimensional visualization of crystal, volumetric and morphology data. J. Appl. Crystallogr. 2011, 44, 1272–1276. [Google Scholar] [CrossRef]
  65. Hunter, J.D. Matplotlib: A 2D Graphics Environment. Comput. Sci. Eng. 2007, 9, 90–95. [Google Scholar] [CrossRef]
  66. Nayakasinghe, M.T.; Guerrero-Sánchez, J.; Takeuchi, N.; Zaera, F. Adsorption of crotonaldehyde on metal surfaces: Cu vs Pt. J. Chem. Phys. 2021, 154, 104701. [Google Scholar] [CrossRef]
  67. Haubrich, J.; Becker, C.; Wandelt, K. Adsorption and interaction energy of π ethene on Pt(111) and Pt alloys: A detailed analysis of vibrational, energetic and electronic properties. Surf. Sci. 2009, 603, 1476–1485. [Google Scholar] [CrossRef]
  68. Lindenmaier, R.; Williams, S.D.; Sams, R.L.; Johnson, T.J. Quantitative Infrared Absorption Spectra and Vibrational Assignments of Crotonaldehyde and Methyl Vinyl Ketone Using Gas-Phase Mid-Infrared, Far-Infrared, and Liquid Raman Spectra: S-cis vs s-trans Composition Confirmed via Temperature Studies and ab Initio Methods. J. Phys. Chem. A 2017, 121, 1195–1212. [Google Scholar] [CrossRef]
  69. de Jesús, J.C.; Zaera, F. Adsorption and Thermal Chemistry of Acrolein and Crotonaldehyde on Pt(111) Surfaces. Surf. Sci. 1999, 430, 99–115. [Google Scholar] [CrossRef]
  70. Murillo, L.E.; Menning, C.A.; Chen, J.G. Trend in the CC and CO bond hydrogenation of acrolein on Pt–M (M = Ni, Co, Cu) bimetallic surfaces. J. Catal. 2009, 268, 335–342. [Google Scholar] [CrossRef]
  71. de Jesús, J.C.; Zaera, F. Double-Bond Activation in Unsaturated Aldehydes: Conversion of Acrolein to Propene and Ketene on Pt(111) Surfaces. J. Mol. Catal. A Chem. 1999, 138, 237–240. [Google Scholar] [CrossRef]
  72. Islam, A.; Molina, D.L.; Trenary, M. Adsorption of acrolein and its hydrogenation products on Cu(111). Phys. Chem. Chem. Phys. 2022, 24, 24383–24393. [Google Scholar] [CrossRef] [PubMed]
  73. Greenler, R.G. Infrared Study of Adsorbed Molecules on Metal Surfaces by Reflection Techniques. J. Chem. Phys. 1966, 44, 310–315. [Google Scholar] [CrossRef]
  74. Zaera, F. New advances in the use of infrared absorption spectroscopy for the characterization of heterogeneous catalytic reactions. Chem. Soc. Rev. 2014, 43, 7624–7663. [Google Scholar] [CrossRef]
  75. Chen, B.; Ponce, R.; Guerrero-Sánchez, J.; Takeuchi, N.; Zaera, F. Cinnamaldehyde adsorption and thermal decomposition on copper surfaces. J. Vac. Sci. Technol. A 2021, 39, 053205. [Google Scholar] [CrossRef]
  76. Lucci, F.R.; Darby, M.T.; Mattera, M.F.G.; Ivimey, C.J.; Therrien, A.J.; Michaelides, A.; Stamatakis, M.; Sykes, E.C.H. Controlling Hydrogen Activation, Spillover, and Desorption with Pd–Au Single-Atom Alloys. J. Phys. Chem. Lett. 2016, 7, 480–485. [Google Scholar] [CrossRef]
  77. Fan, T.; Sun, M.; Ji, Y. First-principles study on the selective hydrogenation of the C=O and C=C bonds of acrolein on Pt–M–Pt (M = Pt, Cu, Ni, Co) surfaces. Phys. Chem. Chem. Phys. 2020, 22, 14645–14650. [Google Scholar] [CrossRef] [PubMed]
Figure 1. (a) Side (left) and top (right) views of the pristine Cu(111) and of the simulated Cu3Pt/Cu(111) and Cu2Pt/Cu(111) alloy surfaces used in this study. The corresponding (3 × 3), (2√3 × 2√3)R30°, and (3 × 3) supercells are shown in the top views. (b) Optimized structures for the different configurations of crotonaldehyde in the gas phase.
Figure 1. (a) Side (left) and top (right) views of the pristine Cu(111) and of the simulated Cu3Pt/Cu(111) and Cu2Pt/Cu(111) alloy surfaces used in this study. The corresponding (3 × 3), (2√3 × 2√3)R30°, and (3 × 3) supercells are shown in the top views. (b) Optimized structures for the different configurations of crotonaldehyde in the gas phase.
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Figure 2. Optimized structures calculated for the cis and trans configurations of crotonaldehyde adsorbed on Cu2Pt/Cu(111) and Cu3Pt(111) surfaces, as a function of coordination mode. Atom color code: blue = Cu, grey = Pt, red = O, brown = C, and white (small) = H.
Figure 2. Optimized structures calculated for the cis and trans configurations of crotonaldehyde adsorbed on Cu2Pt/Cu(111) and Cu3Pt(111) surfaces, as a function of coordination mode. Atom color code: blue = Cu, grey = Pt, red = O, brown = C, and white (small) = H.
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Figure 3. Energies of adsorption for the cis (left panel) and trans (right) configurations of crotonaldehyde on Cu (red circles), Cu3Pt (pink downward-pointing triangles), Cu2Pt (blue upward-pointing triangles), and Pt (green squares) as a function of coordination mode to the surface, for the structures shown in Figure 2.
Figure 3. Energies of adsorption for the cis (left panel) and trans (right) configurations of crotonaldehyde on Cu (red circles), Cu3Pt (pink downward-pointing triangles), Cu2Pt (blue upward-pointing triangles), and Pt (green squares) as a function of coordination mode to the surface, for the structures shown in Figure 2.
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Figure 4. Projected DOS of the E-(s)-cis isomer of crotonaldehyde when adsorbed on the Cu2Pt/Cu(111) surface in the (a) η1-O, (b) η2-OC1, (c) η2-C2C3, (d) η3-OC2C3, and (e) η4 adsorption configurations.
Figure 4. Projected DOS of the E-(s)-cis isomer of crotonaldehyde when adsorbed on the Cu2Pt/Cu(111) surface in the (a) η1-O, (b) η2-OC1, (c) η2-C2C3, (d) η3-OC2C3, and (e) η4 adsorption configurations.
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Figure 5. Calculated vibrational spectra of crotonaldehyde adsorbed on the indicated surfaces and configurations, namely, on (from top to bottom): (b) Cu3Pt-η4-cis, (c) Cu3Pt-η3-OC2C3-cis, (d) Cu3Pt-η2-C2C3-cis, (e) Cu3Pt-η4-trans, and (f) Cu2Pt-η4-cis; these are the most stable adsorption structures calculated in this study. The sum of all the spectra is shown at the very top (a) as well.
Figure 5. Calculated vibrational spectra of crotonaldehyde adsorbed on the indicated surfaces and configurations, namely, on (from top to bottom): (b) Cu3Pt-η4-cis, (c) Cu3Pt-η3-OC2C3-cis, (d) Cu3Pt-η2-C2C3-cis, (e) Cu3Pt-η4-trans, and (f) Cu2Pt-η4-cis; these are the most stable adsorption structures calculated in this study. The sum of all the spectra is shown at the very top (a) as well.
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Table 1. Calculated bond lengths for the E-(s)-cis crotonaldehyde in the different configurations considered in this work. Values for bonding to either Cu or Pt are indicated by the color of the numbers, blue for Cu and grey for Pt.
Table 1. Calculated bond lengths for the E-(s)-cis crotonaldehyde in the different configurations considered in this work. Values for bonding to either Cu or Pt are indicated by the color of the numbers, blue for Cu and grey for Pt.
GeometryGas PhaseCu2Pt/Cu(111)Cu3Pt/Cu(111)
E-(s)-cisη1-Oη2-OC1η2-C2C3η3-OC2C3η4-OC1C2C3η1-Oη2-OC1η2-C2C3η3-OC2C3η4-OC1C2C3
Supercell-3 × 33 × 33 × 33 × 33 × 32√3 × 2√32√3 × 2√32√3 × 2√32√3 × 2√32√3 × 2√3
Eab (kJ/mol)-−49.7−69.57−85.0−85.7−94.8−53.3−78.6−92.850−99.8−110.5
d(C1=O)1.2271.2471.2871.2401.2701.2521.2501.3071.2361.2781.273
d(C1–C2)1.4741.4551.4611.4611.4341.4621.4531.4651.4701.4251.443
d(C2=C3)1.3461.3481.3551.4281.4451.4181.3521.3591.4501.4571.431
d(C3–C4)1.4861.4821.4851.5121.5121.5021.4831.4851.5141.5141.509
d(O–Cu/Pt)2.3042.1012.2852.5382.2362.0322.1492.258
d(C1Cu/Pt)2.4302.6452.2992.6552.435
d(C2Cu/Pt)2.4162.2772.2772.2262.2122.456
d(C3Cu/Pt)2.2292.2012.2422.1802.1882.182
Table 2. Calculated bond lengths for the E-(s)-trans crotonaldehyde in the different configurations considered in this work. Values for bonding to either Cu or Pt are indicated by the color of the numbers, blue for Cu and grey for Pt.
Table 2. Calculated bond lengths for the E-(s)-trans crotonaldehyde in the different configurations considered in this work. Values for bonding to either Cu or Pt are indicated by the color of the numbers, blue for Cu and grey for Pt.
GeometryGas PhaseCu2Pt/Cu(111)Cu3Pt/Cu(111)
E-(s)-transη1-Oη2-OC1η2-C2C3η3-OC2C3η4-OC1C2C3η1-Oη2-OC1η2-C2C3η3-OC2C3η4-OC1C2C3
Supercell-3 × 33 × 33 × 33 × 33 × 32√3 × 2√32√3 × 2√32√3 × 2√32√3 × 2√32√3 × 2√3
Eab (kJ/mol)-−68.7−75.5−84.2−43.0−72.8−73.1−81.2−88.3−62.2−97.7
d(C1=O)1.2261.2471.2621.2401.2701.2521.2421.2961.2371.2431.275
d(C1–C2)1.4631.4551.4571.4611.4341.4621.4441.4641.4631.4741.434
d(C2=C3)1.3461.3481.3531.4281.4451.4181.3491.3591.4461.4661.440
d(C3–C4)1.4881.4821.4861.5121.5121.5021.4841.4831.5161.5121.511
d(O–Cu/Pt)2.4272.2802.3233.0872.1982.0692.2342.148
d(C1Cu/Pt)2.6042.8982.3302.550
d(C2Cu/Pt)2.3402.1452.8152.2472.1422.428
d(C3Cu/Pt)2.2332.2172.9782.1912.1612.178
Table 3. Calculated vibrational frequencies (in cm−1) for the E isomers of crotonaldehyde and for the five most stable adsorption configurations *.
Table 3. Calculated vibrational frequencies (in cm−1) for the E isomers of crotonaldehyde and for the five most stable adsorption configurations *.
GeometryGas phaseCu3Pt/Cu(111)Cu2Pt/Cu(111)
E-(s)-transE-(s)-cisη2-C2C3-cisη3-OC2C3-cisη4-OC1C2C3-cisη4-OC1C2C3-transη4-OC1C2C3-cis
Supercell--2√3 × 2√32√3 × 2√32√3 × 2√32√3 × 2√33 × 3
ν(C–H) range3110-27533095–28283037–28763045–28803043–28883022–28593089–2863
ν(C1=O)17011708
ν(C2=C3)164816221594 1537
δa(CH3) 1457147314561462
δ(CHx)1431, 14271423, 14291432, 14411423, 14351428, 14431427, 14401422, 1435
δip(CH)ald 1393140014131396
δs(CH3)1355, 13651351, 13761348, 13561356136313581334, 1358
δip(CH)vinyl1234, 12931271, 128812651245, 12831266, 13081223, 12931201, 1268
ν(C1–C2)113611191148114511821128, 11661110
ν(C3–C4)1073 10801049, 108010921066
10301005, 1036101599910051003998, 1025
ρ(CH3), τC2H2)973, 996972, 989985 947 963
δoop(CH)ald 926, 934884, 904823, 894899, 920913
* ν: stretching; δ: deformation; τ: twist; ip: in-plane; oop: out-of-plane; a: asymmetric; s: symmetric; ald: aldehyde.
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Ruvalcaba, R.; Guerrero-Sanchez, J.; Takeuchi, N.; Zaera, F. Crotonaldehyde Adsorption on Cu-Pt Surface Alloys: A Quantum Mechanics Study. Chemistry 2023, 5, 463-478. https://doi.org/10.3390/chemistry5010034

AMA Style

Ruvalcaba R, Guerrero-Sanchez J, Takeuchi N, Zaera F. Crotonaldehyde Adsorption on Cu-Pt Surface Alloys: A Quantum Mechanics Study. Chemistry. 2023; 5(1):463-478. https://doi.org/10.3390/chemistry5010034

Chicago/Turabian Style

Ruvalcaba, Ricardo, Jonathan Guerrero-Sanchez, Noboru Takeuchi, and Francisco Zaera. 2023. "Crotonaldehyde Adsorption on Cu-Pt Surface Alloys: A Quantum Mechanics Study" Chemistry 5, no. 1: 463-478. https://doi.org/10.3390/chemistry5010034

APA Style

Ruvalcaba, R., Guerrero-Sanchez, J., Takeuchi, N., & Zaera, F. (2023). Crotonaldehyde Adsorption on Cu-Pt Surface Alloys: A Quantum Mechanics Study. Chemistry, 5(1), 463-478. https://doi.org/10.3390/chemistry5010034

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