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Open AccessCCS ChemistryRESEARCH ARTICLES29 Nov 2024

鱼子酱是什么

    Exploring the intricate relationship between noble metal ensembles and supporting materials stands as a captivating frontier in chemistry and catalysis. However, the precise control of noble metal ensembles on inert support remains challenging. We present here a facile strategy to construct noble metal ensembles, ranging from single atom to clusters or nanoparticles, on inert pure-silica zeolites. Typically, the internal silanol nests of silicalite-1 (S-1) platelike zeolites are identified as anchoring sites for Pt ensembles. The dynamic interplay between silanol nests and Pt precursors in solution phase are monitored to reveal the formation and evolution of Pt ensembles. Various Pt ensembles on S-1 zeolites show distinct catalytic behaviors in the model reaction of benzonitrile hydro-conversion. Thereinto, Pt1/S-1 catalyst containing exclusive mononuclear ionic Ptδ+ sites shows remarkable performance in the hydro-conversion of benzonitrile to di-benzylamine, which can be extended to the synthesis of secondary amines from the hydro-conversion of nitriles or nitriles/amines mixtures. The methodology developed herein offers the precise control of noble metal ensembles on inert zeolite support towards selective catalysis.

    Introduction

    Noble metal-based catalysts hold significant importance in heterogeneous catalysis, showing broad applications in various fields such as fine chemical engineering, energy transformation, and environmental protection.1 Among supported noble metal catalysts, single-atom catalysts (SACs) have drawn special attention owing to their superior atomic utilization efficiency and unique electronic configuration, thereby facilitating a wide range of chemical transformations including dehydrogenation, C–H bond activation, Suzuki coupling, and so on.25 However, the inherent high surface energy of noble metal species commonly results in their aggregation during catalyst preparation and reaction processes, compromising catalytic activity or even leading to catalyst deactivation.68 In this context, the precise control of stable noble metal ensembles, from single-atom to clusters or nanoparticles, over a specific support remains a key challenging topic in catalysis.1,8,9

    Zeolites, characterized by adjustable framework composition, abundant acid-base sites, well-defined topology as well as distinctive local electronic field, stand out as versatile hosts for transition metal ensembles.10,11 Several strategies, including ligand-protect encapsulation,11,12 ion-exchange,13 and incipient wetness impregnation5 have been explored for constructing zeolite-supported SACs. Meanwhile, it has been reported that noble metal clusters can be confined in the structure of pure silica zeolites like silicalite-1 (S-1) via ligand-protect encapsulation followed by specific treatment, which show distinctive catalytic properties in several important reactions.1417 However, all these processes might confront problems of complex procedures or poor reproducibility,13 which are unfortunately not suitable for production in large scale. On the other hand, diverse target product orientations necessitate different active metal species, ranging from single-atom5 to dual single atoms18,19 and metal clusters,1416,20,21 or even multiple sites.22,23 A simple and general strategy to control stable noble metal ensembles over zeolite supports is highly desired to facilitate their catalytic applications with target product distributions.

    Herein, we develop a straightforward postsynthesis strategy for the construction of noble metal ensembles, ranging from isolated atoms to clusters or nanoparticles, on pure silica platelike zeolites (S-1) utilizing their unique hydroxyl nests. The evolution of noble metal ensembles on zeolites are monitored to reveal the essence and general applicability of this strategy. The as-prepared Pt1/S-1 (containing single-atom Pt), Pt1+c/S-1 (containing single-atom Pt and Pt clusters), and Ptn/S-1 (containing Pt nanoparticles) samples show distinct catalytic behaviors in the hydro-conversion of benzonitrile. Notably, Pt1/S-1 catalyst containing hydroxyl nest-stabilized mononuclear Ptδ+ species demonstrates remarkable performance in the synthesis of secondary amines from the cascade hydro-conversion of nitriles.

    Experimental Methods

    Various characterization methods were applied to confirm the structure of Ptx/S-1, including powder X-ray diffraction (XRD), temperature-programmed reduction, X-ray photoelectron spectroscopy (XPS), and X-ray absorption spectroscopy (XAS) shown in the Supporting Information. The catalytic performance was performed on a high-pressure autoclave. Subsequently, all the structures and simulation processes were performed based on the spin-polarized density functional theory (DFT) as implemented in the Vienna Ab initio Simulation Package.

    Results and Discussion

    Synthesis and characterization of Pt ensembles on S-1 zeolites

    S-1 platelike zeolites were obtained through hydrothermal synthesis involving a mixed gel comprising SiO2, tetrapropylammonium hydroxide, H2O, tetraethoxysilane, and H2SO4 and subsequently processed (detailed procedures in Supplementary Information).24 Then, various Pt ensembles, including Pt1, Pt1+c, and Ptn, were deposited on S-1 zeolites through wetness impregnation followed by evaporation and calcination in flowing air ( Supporting Information Table S1). XRD patterns reveal the characteristic Mobil Five (MFI) topological structure of all zeolite samples without any discernible diffraction peaks corresponding to Pt species ( Supporting Information Figure S1). The type I isotherms and the corresponding pore width distributions confirm the microporous structure of zeolites and hint to the homogeneous distribution of Pt species within zeolite microporous structure ( Supporting Information Figures S2 and S3 and Table S1). Transmission electron microscopy (TEM) images of S-1 sample show typical platelike morphology ( Supporting Information Figure S4), with an average thickness of ~40?nm ( Supporting Information Figure S5). Meanwhile, no obvious Pt aggregates could be observed in the images of Pt-containing zeolite samples, that is, Ptx/S-1.

    To reveal the distribution and configuration of Pt species within Ptx/S-1, aberration-corrected high-angle annular dark-field scanning transmission electron microscopy (AC-HAADF-STEM) analyses were conducted, capitalizing on distinct atomic contrasts (78Pt, 14Si, and 8O) in samples.25 As depicted in Figure?1a, the as-synthesized S-1 zeolites exhibit good crystallinity with well-defined crystal lattice, devoid of any discernible structural defects. The topologic structure of S-1 sample remains intact along the [010] orientation, as evidenced by the corresponding selected area electron diffraction pattern shown inset (Figure?1b,c). Particularly, the perspective along the [010] direction provides a clear view to distinguish the 5,6,10-membered rings, while the [001] and [100] orientations showcase the interlacing of various rings ( Supporting Information Figure S6).26,27 As shown in Figure?1d, Pt1/S-1 zeolite displays singular bright dots without any bright aggregates, indicative of atomically dispersed Pt atoms. The contrast is accentuated in the high-magnification AC-HAADF-STEM images along the [010] orientation (Figure?1e). The elemental mapping analysis of Pt1/S-1 zeolite further confirms the homogeneous distribution of Pt atoms throughout the crystal of S-1 zeolites (Figure?1f). In contrast, the Ptn/S-1 sample displays a series of regular aggregates with apparent sizes of ~2?nm (Figure?1gi), as labeled by blue squares. Expectedly, the Pt1+c/S-1 displays both single Pt atoms and aggregates of ~1?nm, the latter being denoted as Pt clusters immobilized within zeolite structure (Figure?1jl).28

    Figure 1

    Figure 1 | Electron microscopy analyses of Ptx/S-1 samples. (a–c) AC-HAADF-STEM images of S-1 zeolites along the orientation of [010] as well as the schematic models on the same projection. Insets: view of single S-1 zeolite crystal and selected area electron diffraction pattern; (d, e) AC-HAADF-STEM images of Pt1/S-1 zeolite, indicating the presence of Pt single atoms, as marked by red circles; (f)?Elemental mapping analysis of Pt1/S-1 zeolite; (g, h) AC-HAADF-STEM images of Ptn/S-1 zeolite, indicating the presence of Pt nanoparticles, as marked by blue squares; (i)?Elemental mapping analysis of Ptn/S-1 zeolite; (j, k) AC-HAADF-STEM images of Pt1+c/S-1 zeolite, indicating the co-existence of Pt clusters (~1?nm) and single atoms, as marked by blue squares and red circles; (l)?Elemental mapping analysis of Pt1+c/S-1 zeolite.

    Diffuse reflectance infrared spectroscopy (DRIFTS) of CO adsorption was conducted to identify the geometric configuration of various Pt sites in Ptx/S-1. As shown in Supporting Information Figure S7, Pt1/S-1 manifests a distinct peak at 2092?cm?1, attributed to di-carbonyl on atomically dispersed Ptδ+ species ( Supporting Information Table S2).2931 Ptn/S-1 containing nanosized Pt aggregates exhibits a distinctive peak at around 1850?cm?1, which can be attributed to bridge-bonded CO on Pt–Pt ensembles ( Supporting Information Figure S8).3234 While for Pt1+c/S-1, two major peaks at 2078 and 1934?cm?1 can be captured, corresponding to linearly adsorbed CO on atomically dispersed Ptδ+ species and Pt0 clusters, respectively ( Supporting Information Figure S9).30,33,35 The abovementioned results are consistent with STEM observations (Figure?1), together revealing the growth of Pt species from single atoms to clusters and nanoparticles on S-1 zeolites with increasing Pt loadings from 0.05% to 0.3% ( Supporting Information Table S1).

    On the premise of different configurations of Pt ensembles revealed by STEM and DRIFTS of CO adsorption, XAS was conducted to reveal the electronic structure and coordination environment of Pt species. As shown in the X-ray absorption near-edge structure (XANES) spectra (Figure?2a), the Pt L3-edge white-line intensities of Ptx/S-1 zeolites are located between reference PtO2 and Pt foil, following the order of PtO2 > Pt1/S-1 > Pt1+c/S-1 > Ptn/S-1 > Pt foil. That is, positively charged Pt species in Pt1/S-1 exhibit stronger electronic interaction with oxygen atoms than those in Pt1+c/S-1 and Ptn/S-1. The oxidation states of Pt species in Ptx/S-1 were investigated by XPS. As shown in Supporting Information Figure S10, cationic Pt species are detected in Pt1/S-1 and metallic Pt species are observed in Ptn/S-1, while a mixture of ionic and metallic Pt species are present in Pt1+c/S-1. Obviously, most deposited Pt species in Ptn/S-1 and partial Pt species in Pt1+c/S-1 undergo auto-reduction to metallic Pt species upon calcination in flowing air, accompanied by the formation of aggregates. These can be further confirmed by the experiments of dihydrogen temperature-programmed reduction (H2-TPR). As shown in Supporting Information Figure S11, a distinct dihydrogen consumption peak at ~710?K is observed for Pt1/S-1 zeolite corresponding to the reduction of ionic Pt species (H/Pt?=?1.9). In contrast, Ptn/S-1 shows a very small dihydrogen consumption peak at ~710?K (H/Pt?>?0.01) since most Pt species already exist in the metallic form that will not be reduced by dihydrogen. For Pt1+c/S-1 containing both ionic and metallic Pt species, a small dihydrogen consumption peak with H/Pt ratio of 0.12 can be observed. Fourier-transformed k2-weighted extended X-ray absorption fine structure (EXAFS) spectroscopy was conducted to provide detailed coordination information of Pt sites in Ptx/S-1 (Figure?2b,c and Supporting Information Table S3). For Pt1/S-1, a prominent signal assigned to the first Pt-O shell coordination (~1.6??, CN?≈?2.7) is observed without any Pt–Pt scattering, demonstrating the atomically dispersed ionic Pt species.36 For Pt1+c/S-1, two dominant peaks at 1.6 and 2.4??, assignable to Pt-O and Pt–Pt path, respectively, are observed. While for Ptn/S-1, the Pt–Pt scattering signal at ~2.4?? becomes the prominent one with an average coordination number of 5.6, indicating the presence of Pt aggregates rather than single Pt atoms.19 The EXAFS data were further processed by wavelet transformation (WT) analyses to reveal the fine structure of Pt species in both k and R space. As shown in Figure?2d, only one intensity maximum at ~6???1 is observed for Pt1/S-1 zeolite, confirming the presence of exclusive atomically-dispersed Pt sites and verifying the assignment of peak at 1.6?? to Pt-O path. In contrast, the WT contour plot of Ptn/S-1 zeolite shows a dominating maximum at ~10.7???1 associated with Pt–Pt scattering (Figure?2d), validating the presence of metallic Pt aggregates with high coordination number. In short, the characterization results from XAS, XPS, and H2-TPR reveal the evolution of atomically dispersed ionic Pt species to metallic Pt aggregates with increasing Pt loadings from 0.05% to 0.3% in Ptx/S-1.

    Figure 2

    Figure 2 | Pt L3-edge XAS analyses of Pt-containing zeolite samples. (a)?XANES spectra of PtO2, Pt foil, and Pt-containing zeolite samples; (b)?FT EXAFS spectra of PtO2, Pt foil, and Pt-containing zeolite samples; (c)?FT EXAFS fitting spectra of PtO2, Pt foil, and Pt-containing zeolite samples at R space; (d)?WT EXAFS of PtO2, Pt foil, and Pt-containing zeolite samples.

    Formation and evolution of Pt ensembles on S-1 zeolites

    To reveal the formation and evolution of Pt ensembles, it is extremely important to know the anchoring sites in zeolite support and their interaction with Pt species. There are no anchoring sites in perfect S-1 zeolite crystals and the only possible anchoring sites should come from the crystal defects, namely silanols. As shown in Figure?3a, S-1 and Ptx/S-1 samples demonstrate two distinctive signatures between 3800–3600?cm?1 and 3600–3400?cm?1 in the DRIFT spectra, corresponding to external free silanols (non-H-bonded) and internal silanol nests (H-bonded), respectively.3739 The intensity of internal silanol nests in Pt1/S-1 shows a significant decline in comparison with that in S-1, indicating the consumption of internal silanol nests upon interaction with atomically dispersed Pt species. It is interesting to note that the intensity of H-bonded silanol nests recovers with increasing Pt loadings from 0.05% to 0.3% (Figure?3b), which might be due to the formation of metallic Pt aggregates and the corresponding reduction in the demand of silanol nest anchoring sites (vide infra). Two dimensional 1H-1H single-quantum/double-quantum magic angle spinning (SQ/DQ MAS NMR) experiments were further conducted to reveal the nature of silanols in S-1 zeolite support and their interaction with Pt species. As shown in Figure?3c, strong autocorrelation peaks at (2, 4) and (3, 6) ppm, corresponding to external free silanols and internal silanol nests, respectively, are observed for S-1 platelike zeolites.40 Upon the introduction of Pt ensembles, a significant consumption of internal silanol nests can be observed (Figure?3d and Supporting Information Figure S12), revealing that the internal silanol nests act as the preferred anchoring sites for Pt ensembles. That is actually very easy to understand since the silanol nests can provide stronger interaction and better stabilizing effect for guest metal species than the free silanols. On the other hand, it is strange to see that less silanol nests are required to stabilize more Pt ensembles (Figure?3b and Supporting Information Figure S12). For Pt1/S-1, the atomically dispersed Ptδ+ species are exclusively stabilized by the silanol nests with the formation of Si-O-Ptδ+ linkages. While for Pt1+c/S-1 and Ptn/S-1, the interplay between silanol nests and Pt ensembles/precursors are much more complicated, ultimately controlling the configuration of Pt ensembles.

    Figure 3

    Figure 3 | Characterization of anchoring sites in S-1 zeolites for Pt ensembles. (a)?DRIFT spectra of S-1 and Ptx/S-1 zeolites; (b)?Relative intensity of internal silanol nests in S-1 and Ptx/S-1 zeolites; 1H-1H SQ/DQ MAS NMR spectra of S-1 (c)?and Pt1/S-1 (d)?zeolites.

    The dynamic interplay between silanol nest anchoring sites and Pt ensembles/precursors (PtL, L: ligand) is proposed, as shown in Scheme?1. With an abundance of internal hydroxyl nests as the anchoring sites (Figure?3), the concentration of Pt precursor emerges as a pivotal factor driving significant alterations in the configurations of obtained Pt ensembles (Scheme?1). Typically, the preferential formation of [Si-O]x-Pt1 linkages (Pt1/S-1) occurs when the rate constant associated with the amalgamation of Pt precursor and internal hydroxyl nests is much greater than that of the spontaneous collision among Pt precursor, namely k1?k2. This is kinetically facile at low Pt precursor concentrations. In contrast, at higher Pt precursor concentrations, Pt clusters or nanoparticles will be formed with accelerated collision rate among Pt precursors (k2, k3?k1), which are then stabilized through bonding with silanol nests (k4, k5).

    Scheme 1

    Scheme 1 | Formation of Pt ensembles ranging from single atom to aggregates on S-1 zeolites.

    Extension of noble metal ensembles on plate-like S-1 zeolites

    Harnessing the distinctive interplay between the metal precursor and the hydroxyl nest anchoring sites, a series of noble metal ensembles on S-1 zeolite support, including Rh1/S-1, Rh1+c/S-1, Rhn/S-1, Pd1/S-1, Pd1+c/S-1, and Pdn/S-1 can be engineered. As shown in Figure?4a,d, isolated noble metal atoms, marked by red circles, on platelike S-1 zeolites can be clearly illustrated for Rh1/S-1 and Pd1/S-1 through the AC-HAADF-STEM images. In contrast, Rhn/S-1 and Pdn/S-1 present uniform noble metal clusters of ~2?nm, as labeled by blue squares (Figure?4c,f). As for Rh1+c/S-1 and Pd1+c/S-1, both single atoms as well as tiny clusters can be observed (Figure?4b,e). These observations strongly confirm the generality of this facile strategy for the construction of controlled noble metal ensembles on platelike S-1 zeolites. Subsequently, Fourier transform infrared spectroscopy of CO adsorption was employed to identify the configurations of noble metal sites on zeolite support. As shown in Figure?4g, two infrared (IR) bands at 2095 and 2020?cm?1 attributed to the symmetric and asymmetric stretch of CO from the positively charged Rh(CO)2 species can be observed in Rh1/S-1 ( Supporting Information Table S2).12 As for Rhn/S-1 catalyst, two IR bands at 2050 and 1920?cm?1 ascribed to linearly adsorbed CO and bridge-CO on Rh clusters are captured. Meanwhile, several IR bands at 2090, 2055, and 2015?cm?1 are observed with Rh1+c/S-1, indicating the co-existence of isolated Rh ions and Rh clusters.41,42 Similarly, Pd1/S-1 shows a typical band at 2050?cm?1 corresponding to linearly bonded CO on positively charged Pd species, while Pdn/S-1 shows an IR band at 1855?cm?1 ascribed to three-fold bridge bonded CO species (Figure?4h and Supporting Information Table S2).43 Expectedly, Pd1+c/S-1 containing both isolated Pd ions and clusters show IR bands at 2050 and 1930?cm?1, in line with AC-STEM observations. Overall, noble metal (Pt, Rh, and Pd) ensembles ranging from single atom to clusters or nanoparticles, on inert S-1 zeolites can be rationally constructed through the facile strategy developed in this study, offering versatile candidates for selective catalysis.

    Figure 4

    Figure 4 | Characterization of noble metal species on S-1 zeolites. AC-HAADF-STEM images of Rh1/S-1 (a), Pd1/S-1 (d), Rh1+c/S-1 (b), Pd1+c/S-1 (e), Rhn/S-1 (c), and Pdn/S-1 (f), with topologic structure inset in (a)?and (d), scale bar?=?2?nm; DRIFT spectra of CO adsorption on Rhx/S-1 (g)?and Pdx/S-1 (h)?(x?=?1, 1+c and n).

    Figure 5

    Figure 5 | Catalytic behaviors of Pt1/S-1 (left), Pt1+c/S-1 (middle), and Ptn/S-1 (right) in the hydro-conversion of benzonitrile. Reaction conditions: catalyst?=?100?mg, BN?=?1?mmol, isopropanol?=?5?mL, temperature?=?413?K (left), 393?K (middle and right), tetradecane?=?40?μL, H2?=?1?MPa, stirring speed?=?1000?rpm.

    Selective catalysis by Pt ensembles on S-1 zeolites

    The hydro-conversion of benzonitrile (BN) (Scheme?2) was employed to clarify the ensemble effect of Ptx/S-1 catalysts. Generally, all Ptx/S-1 catalysts are active for the hydro-conversion of BN (full BN conversion achieved within 1.5–6?h) while various Pt ensembles manifest totally distinct product distributions. As shown in Figure?5, Pt1/S-1 shows high selectivity towards N-benzylidenebenzylamine (DBI) and di-benzylamine (DBA), accompanied by the formation of trace benzylamine (BA) as by-product. The selectivity towards DBA gradually increases to >95% with prolonged reaction time, in accordance with the hydrogenation of DBI to DBA under employed conditions ( Supporting Information Figure S13). That is, the atomically dispersed ionic Pt sites on S-1 zeolites facilitate the condensation deamination between BI and BA ( Pathway I in Scheme?2), thereby contributing to the subsequent hydrogenation of DBI towards DBA ( Pathway II).44 The high selectivity towards DBA and DBI is first roughly explained by temperature-programmed desorption experiments. A much higher desorption temperature of BN with larger adsorption capacity (desorption peak at 570?K) is observed on Pt1/S-1 than that of DBI (desorption peak at 455?K) and DBA (desorption peak at 480?K) ( Supporting Information Figure S14), indicating the facile desorption of DBI and DBA as products. In contrast, full BN conversion is achieved with Ptn/S-1 containing tiny Pt nanoparticles, mainly producing BA and toluene (TOL) (Figure?5) due to the successive hydrogenation and hydro-deamination process ( Pathway III in Scheme?2). While for Pt1+c/S-1 containing both atomically dispersed ionic Pt sites and metallic Pt clusters, various products DBA, DBI, BA, and TOL are expected from parallel reaction pathways and indeed detected at full BN conversion (Figure?5).

    Scheme 2

    Scheme 2 | Reaction pathways of benzonitrile hydro-conversion.

    Reaction mechanism of benzonitrile hydro-conversion over Pt ensembles on S-1 zeolites

    For insight into dihydrogen activation over Pt1/S-1 catalyst, hydrogen-deuterium pulse experiments were performed. As shown in Supporting Information Figure S15, H-D signal (m/z=3) emerges immediately upon the injection of D2 molecules into H2 stream over Pt1/S-1 no matter with BN preadsorption or not, indicating the cleavage of H2/D2 and the subsequent formation of HD. The facile dissociation of dihydrogen over Pt1/S-1 catalyst can be therefore illustrated, facilitating the subsequent hydro-conversion reactions. Then in situ DRIFT spectroscopy was employed to monitor the surface species during BN hydro-conversion over Pt1/S-1. As shown in Supporting Information Figure S16, Pt1/S-1 displays two distinctive IR bands at 3725 and 3460?cm?1, corresponding to residual terminal free silanol and internal silanol nests in S-1 zeolites, respectively. The introduction of dihydrogen does not induce any discernible changes in the silanol groups (Figure?6a). Upon the subsequent feeding of BN, notable IR bands appear at 3100–3000?cm?1, along with a series of IR bands at 2230, 1600, 1490, 1448, and 756?cm?1, attributable to the stretching vibrations of aryl C–H, C≡N, and C–C bonds of BN molecules ( Supporting Information Figures S17–S19 and Table S4).4552 The vibrational frequency of silanol nest exhibits a significant red shift from 3460 to 3400?cm?1 upon BN introduction, indicating the strong interaction between the –C≡N functional group and the silanol nest within Pt1/S-1 zeolite.53 This red shift intensifies with inverse feeding of reactants (first BN and then dihydrogen), demonstrating the preferential adsorption of BN in Pt1/S-1 (Figure?6b). These observations disclose that the hydro-conversion of BN over Pt1/S-1 catalyst is characterized by the preferential adsorption of BN followed by dihydrogen activation. To confirm the mode of dihydrogen activation, in situ DRIFT spectra of H2 and D2 activation were recorded. As shown in Figure?6c, a distinct IR band at 3743?cm?1, corresponding to free silanol group, can be captured on Pt1/S-1 only after the adsorption of BN molecules37 ( Supporting Information Figure S20). Compared to the results from hydrogen-deuterium pulse experiments ( Supporting Information Figure S15), the DRIFT spectra provide strong evidence of BN-assisted dihydrogen heterolytic activation mechanism. Although dihydrogen activation can proceed on bare Pt1/S-1, the formed Pt-H and O-H species are extremely unstable and hardly detectable. In contrast, the Pt-H and O-H species remain stable on Pt1/S-1 with preadsorbed BN molecules. It is therefore proposed that BN adsorption induces the heterolytic dissociation of dihydrogen via the associative mechanism and subsequently produces additional silanol groups (H bonded to framework oxygen). While in the DRIFT spectra of D2 activation (Figure?6d and Supporting Information Figure S21), BN can induce the heterolytic dissociation of D2 and the subsequent H-D isotope exchange with OH bonds (3743, 3725, and 3460?cm?1; Figure?3a), which will produce a series of O–D bonds (2761, 2685, and 2546?cm?1, νO?HO?D≈1.35)5457 ( Supporting Information Table S4).

    Figure 6

    Figure 6 | In situ spectroscopy of benzonitrile hydro-conversion over Pt1/S-1 catalyst. (a)?In situ DRIFT spectra of Pt1/S-1 recorded after the successive feeding of H2 and BN at 403?K; (b)?In situ DRIFT spectra of Pt1/S-1 recorded after the successive feeding of BN and H2 at 403?K; (c)?In situ DRIFT spectra of H2 activation over Pt1/S-1 after saturation with BN at 403?K; and (d)?In situ DRIFT spectra of D2 activation over Pt1/S-1 after saturation with BN at 403?K.

    The reaction mechanism of BN hydro-conversion over distinct Pt ensembles was finally interpreted by DFT calculations. According to characterization results, Pt1/S-1 should feature mononuclear Pt motifs embedded into the internal silanol nests ([Si-O]3-Pt1···[Si-OH]), while Ptn/S-1 is simplified by Pt4 clusters positioned adjacent to silanol nests.58 As shown in Figure?7a, the adsorption of BN molecules on mononuclear Ptδ+ proceeds smoothly, highly exothermic by 1.85?eV ( M1) ( Supporting Information Figure S22 and Table S5). Subsequently, the heterolytic dissociation of dihydrogen occurs rapidly over the Pt-O linkage with adsorbed BN molecule, generating Pt-H and O-H species, respectively. The heterolytic dissociation of adsorbed dihydrogen encounters an energy barrier of 1.67?eV ( TS1) and is slightly exothermic by 0.01?eV. Accordingly, a new O–H bond is formed accompanied by the cleavage of Pt-O linkage ( M3). It aligns well with the observations in the DRIFT spectra of dihydrogen activation, wherein a distinctive signal associated with –OH bond appears upon the successive feeding of BN and dihydrogen (Figure?6c). Subsequently, the hydrogenation of BN to BI proceeds with PhC≡N*+Pt-H* and PhC=NH*+O-H* steps, overcoming the energy barriers of 1.55 ( TS2) and 0.10?eV ( TS3), respectively. The second dihydrogen molecule undergoes similar heterolytic dissociation with an energy barrier of 1.10?eV ( TS4). The further hydrogenation of BI to BA proceeds with PhCH=NH*+Pt-H* ( TS5) and PhCH-NH2*+O-H* ( TS6) steps, involving the energy barriers of 1.10 and 1.59?eV, respectively. DBI can be formed through the condensation reaction of BI and BA, including the formation and facile desorption of ammonia. Importantly, the effective barrier of condensation ( TS7, 1.50?eV) is found to be relatively lower than that of hydrogenation process ( TS1, 1.67?eV and TS6, 1.59?eV), indicating the kinetic feasibility of condensation between BI and BA. That is, the BI intermediate, once generated, prefers to attack BA to form DBI product. Dihydrogen can undergo heterolytic dissociation via the Pt···N linkage ( M16) for the further hydrogenation of DBA, exothermic by 0.93?eV. The lower energy barrier of DBA formation ( TS11, 1.09?eV) compared to that of DBI ( TS7, 1.50?eV) demonstrates the facile hydrogenation of DBI to DBA, consistent with the observed time-dependent product distribution (Figure?5). DBA might also be formed via a direct hydrogenation pathway without going through the DBI intermediate ( Supporting Information Figure S23 and Table S6). However, the higher energy barrier ( TS12′, 2.04?eV) associated with this route suggests its infeasibility, providing strong evidence for the indispensability of Pathway I (Scheme?2).

    Figure 7

    Figure 7 | Reaction pathways of benzonitrile hydro-conversion over (a)?mononuclear ionic Pt1 and (b)?metallic Pt4 clusters stabilized by the internal hydroxyl nests of S-1 zeolites at 0?K with optimized structures shown inset.

    Dihydrogen molecule can undergo facile dissociation over metallic Pt4 cluster ( TS1, 0.1?eV), followed by hydrogen transfer ( TS2, 0.31?eV) after the co-adsorption of BN (Figure?7b, Supporting Information Figure S24 and Table S7). The hydrogenation of BN to BI proceeds with the PhC≡N*+Pt-H* and PhC=NH*+Pt-H* step, overcoming the energy barriers of 1.90 ( TS3) and 0.55?eV ( TS5), respectively. Subsequently, the second dihydrogen molecule undergoes similar homolytic dissociation ( TS6, 0.12?eV) and hydrogen transfer ( TS7, 0.26?eV) with the coadsorption of BI. Importantly, the dissociation of the second dihydrogen molecule involves a continuous exothermic process, thereby promoting the further hydrogenation of BI intermediate to BA through PhCH=NH*+Pt-H* ( TS8) and PhCH-NH2*+Pt-H* ( TS9) steps, overcoming energy barriers of 1.76 and 1.60?eV, respectively. It should be noted that the energy barrier of dihydrogen activation over metallic Pt4 clusters (homolytic dissociation) is significantly lower than that over mononuclear ionic Pt sites (heterolytic dissociation), rationally leading to distinct products from hydro-conversion. The hydro-deamination of BA to TOL is also calculated, which suffers from a high energy barrier of 2.14?eV ( TS10). That is, the conversion of BA to TOL may occur on zeolite-stabilized Pt clusters but with some difficulty, in accordance with observed relatively low TOL selectivity (Figure?5). According to the calculations results, various Pt ensembles, namely mononuclear ionic Pt sites and metallic Pt clusters, on zeolites, show distinct intrinsic catalytic behaviors in the hydro-conversion of BN, leading to distinct product distributions. Pt1/S-1 containing mononuclear ionic Pt motifs embedded into the internal silanol nests of S-1 zeolites, are proved to be a robust catalyst for the synthesis of DBA from BN hydro-conversion.

    Synthesis of secondary amines over Pt1/S-1 catalyst

    Inspired by the unique catalytic behaviors of Pt1/S-1 in the hydro-conversion of BN, Pt1/S-1 was also tested for the synthesis of secondary amines from a wide array of both aromatic and aliphatic nitriles. As shown in Table?1, Pt1/S-1 exhibits good tolerance to electron-withdrawing groups ( Entry 1–3) or electron-donating groups ( Entry 4–7) in the benzene ring, manifesting high selectivity to the corresponding secondary amines with good product yields of 91%–95% (from the hydro-conversion of aromatic nitriles). The hydro-conversion of aliphatic nitriles proceeds a bit more smoothly on Pt1/S-1 catalyst, giving secondary amine product yields of 95%–97% ( Entry 8–10). According to the reaction network, it should be possible to synthesize secondary amines from the successive condensation deamination (between imines and amines) and hydrogenation process (Scheme?2). Herein, a series of nitriles and amines were tested for the synthesis of secondary amines over Pt1/S-1 catalyst following the cascade reaction pathways of (1) nitriles selective hydrogenation to imines, (2) condensation deamination between imines and amines to produce coupled imines, and (3) coupled imines selective hydrogenation to secondary amines.59 Remarkably, good yields of secondary amines (>90%) can be obtained from the hydro-conversion of aromatic nitriles and aliphatic amines or aliphatic nitriles and aromatic amines ( Entry 11–16). With the newly developed Pt1/S-1 catalyst, the efficient synthesis of valuable amines can be achieved from the simple one-pot cascade reactions.

    Table 1 | Hydro-Conversion of Substituted Nitriles or Nitriles/Amines over Pt1/S-1 Catalysta

    Entry Substrate Product Conversion (%) Selectivity to Secondary Amines (%)
    1 if1.eps if2.eps >99 95
    2 if3.eps if4.eps >99 94
    3 if5.eps if6.eps >99 91
    4 if7.eps if8.eps >99 92
    5 if9.eps if10.eps >99 93
    6 if11.eps if12.eps >99 92
    7 if13.eps if14.eps >99 92
    8 if15.eps if16.eps >99 95
    9 if17.eps if18.eps >99 97
    10 if19.eps if20.eps >99 96
    11 if21.eps if22.eps >99 91
    12 if23.eps if24.eps >99 93
    13 if25.eps if26.eps >99 92
    14 if27.eps if28.eps >99 96
    15 if29.eps if30.eps >99 95
    16 if31.eps if32.eps >99 94

    aReaction conditions: Nitrile (amine)?=?1?mmol, catalyst?=?100?mg, tetradecane?=?40?μL, isopropanol?=?5?mL, temperature?=?393–413?K, time?=?6–12?h.

    Conclusion

    We develop herein a facile strategy for the construction of various noble metal ensembles ranging from single atom to clusters or nanoparticles on pure silica zeolites. Typically, the internal silanol nests of S-1 zeolites are established as efficient anchoring sites for Pt ensembles. The dynamic interplay between silanol nest anchoring sites and Pt precursors in solution phase ultimately control the Pt ensembles on S-1 zeolites. This synthesis strategy is applicable to the large-scale production of various noble metal ensemble on pure silica zeolites containing internal silanol nests.

    The ensemble effect of Pt catalysts in the hydro-conversion of benzonitrile is disclosed. Various Pt ensembles show quite different catalytic properties in these two reactions. Pt1/S-1 containing atomically dispersed ionic Pt sites stabilized by hydroxyl nests can efficiently catalyze the hydro-conversion of benzonitrile to DBA, following the cascade steps of selective hydrogenation, condensation deamination and selective hydrogenation. The substrate-assisted heterolytic dissociation of dihydrogen on Pt1/S-1 is identified as a key factor in the reaction. Pt1/S-1 is proved to be a versatile catalyst for the synthesis of various amines from the hydro-conversion of nitriles or nitriles/amines mixtures with good yields of >90%. Our work provides an example of controlling noble metal ensembles on pure silica zeolite support for the large-scale production of SACs toward complex chemical transformations.

    Supporting Information

    Supporting Information is available and includes experimental details, material and method, characterization results including XRD, scanning electron microscopy, TEM, XPS, XAS, more catalytic data, and theoretical calculations.

    Conflict of Interest

    There is no conflict of interest to report.

    Funding Information

    This work was supported by the National Natural Science Fund of China (grant nos. 22025203 and 22302099), China Postdoctoral Science Fund (grant nos. 2023M731797 and 2024T170438), and the Fundamental Research Funds for the Central Universities (Nankai University).

    References

    • 1. Guo Y.; Wang M.; Zhu Q.; Xiao D.; Ma D.Ensemble Effect for Single-Atom, Small Cluster and Nanoparticle Catalysts.Nat. Catal.2022, 5, 766–776. Google Scholar
    • 2. Chen Z.; Vorobyeva E.; Mitchell S.; Fako E.; Ortu?o M. A.; López N.; Collins S. M.; Midgley P. A.; Richard S.; Vilé G.; Pérez-Ramírez J.A Heterogeneous Single-Atom Palladium Catalyst Surpassing Homogeneous Systems for Suzuki Coupling.Nat. Nanotechnol.2018, 13, 702–707. Google Scholar
    • 3. Zeng L.; Cheng K.; Sun F.; Fan Q.; Li L.; Zhang Q.; Wei Y.; Zhou W.; Kang J.; Zhang Q.; Chen M.; Liu Q.; Zhang L.; Huang J.; Cheng J.; Jiang Z.; Fu G.; Wang Y.Stable Anchoring of Single Rhodium Atoms by Indium in Zeolite Alkane Dehydrogenation Catalysts.Science2024, 1004, 998–1004. Google Scholar
    • 4. Qiao B.; Wang A.; Yang X.; Allard L. F.; Jiang Z.; Cui Y.; Liu J.; Li J.; Zhang T.Single-Atom Catalysis of CO Oxidation Using Pt1/FeOx.Nat. Chem.2011, 3, 634–641. Google Scholar
    • 5. Shan J.; Li M.; Allard L. F.; Lee S.; Flytzani-Stephanopoulos M.Mild Oxidation of Methane to Methanol or Acetic Acid on Supported Isolated Rhodium Catalysts.Nature2017, 551, 605–608. Google Scholar
    • 6. Jeong H.; Kwon O.; Kim B.; Bae J.; Shin S.; Kim H.; Kim J.; Lee H.Highly Durable Metal Ensemble Catalysts with Full Dispersion for Automotive Applications Beyond Single-Atom Catalysts.Nat. Catal.2020, 3, 368–375. Google Scholar
    • 7. Liang X.; Fu N.; Yao S.; Li Z.; Li Y.The Progress and Outlook of Metal Single-Atom-Site Catalysis.J.?Am. Chem. Soc.2022, 144, 18155–18174. Google Scholar
    • 8. Vogt C.; Weckhuysen B. M.The Concept of Active Site in Heterogeneous Catalysis.Nat. Rev. Chem.2022, 6, 89–111. Google Scholar
    • 9. Ha M.; Baxter E. T.; Cass A. C.; Anderson S. L.; Alexandrova A. N.Boron Switch for Selectivity of Catalytic Dehydrogenation on Size-Selected Pt Clusters on Al2O3.J.?Am. Chem. Soc.2017, 139, 11568–11575. Google Scholar
    • 10. Li Y.; Yu J.Emerging Applications of Zeolites in Catalysis, Separation and Host–Guest Assembly.Nat. Rev. Mater.2021, 6, 1156–1174. Crossref,?Google Scholar
    • 11. Li W.; Chai Y.; Wu G.; Li L.Stable and Uniform Extraframework Cations in Faujasite Zeolites.J.?Phys. Chem. Lett.2022, 13, 11419–11429. Crossref,?Google Scholar
    • 12. Sun Q.; Wang N.; Zhang T.; Bai R.; Mayoral A.; Zhang P.; Zhang Q.; Terasaki O.; Yu J.Zeolite-Encaged Single-Atom Rhodium Catalysts: Highly-Efficient Hydrogen Generation and Shape-Selective Tandem Hydrogenation of Nitroarenes.Angew. Chem. Int. Ed.2019, 58, 18570–18576. Google Scholar
    • 13. Deng X.; Yang D.; Li W.; Chai Y.; Wu G.; Li L.Chemistry of Coordinatively Unsaturated Centers in Zeolites.Trends Chem.2023, 5, 892–905. Crossref,?Google Scholar
    • 14. Liu L.; Lopez-Haro M.; Lopes C. W.; Li C.; Concepcion P.; Simonelli L.; Calvino J. J.; Corma A.Regioselective Generation and Reactivity Control of Subnanometric Platinum Clusters in Zeolites for High-Temperature Catalysis.Nat. Mater.2019, 18, 866–873. Google Scholar
    • 15. Wang N.; Sun Q.; Bai R.; Li X.; Guo G.; Yu J.In Situ Confinement of Ultrasmall Pd Clusters Within Nanosized Silicalite-1 Zeolite for Highly Efficient Catalysis of Hydrogen Generation.J.?Am. Chem. Soc.2016, 138, 7484–7487. Google Scholar
    • 16. Wang N.; Sun Q.; Zhang T.; Mayoral A.; Li L.; Zhou X.; Xu J.; Zhang P.; Yu J.Impregnating Subnanometer Metallic Nanocatalysts into Self-Pillared Zeolite Nanosheets.J.?Am. Chem. Soc.2021, 143, 6905–6914. Google Scholar
    • 17. Choi M.; Na K.; Kim J.; Sakamoto Y.; Terasaki O.; Ryoo R.Stable Single-Unit-Cell Nanosheets of Zeolite MFI as Active and Long-Lived Catalysts.Nature2009, 461, 246–249. Google Scholar
    • 18. Yu B.; Cheng L.; Dai S.; Jiang Y.; Yang B.; Li H.; Zhao Y.; Xu J.; Zhang Y.; Pan C.; Cao X. M.; Zhu Y.; Lou Y.Silver and Copper Dual Single Atoms Boosting Direct Oxidation of Methane to Methanol via Synergistic Catalysis.Adv. Sci.2023, 10, 2302143. Google Scholar
    • 19. Tian S.; Wang B.; Gong W.; He Z.; Xu Q.; Chen W.; Zhang Q.; Zhu Y.; Yang J.; Fu Q.; Chen C.; Bu Y.; Gu L.; Sun X.; Zhao H.; Wang D.; Li Y.Dual-Atom Pt Heterogeneous Catalyst with Excellent Catalytic Performances for the Selective Hydrogenation and Epoxidation.Nat. Commun.2021, 12, 3181. Google Scholar
    • 20. Liu L.; Lopez-Haro M.; Lopes C. W.; Rojas-Buzo S.; Concepcion P.; Manzorro R.; Simonelli L.; Sattler A.; Serna P.; Calvino J. J.; Corma A.Structural Modulation and Direct Measurement of Subnanometric Bimetallic PtSn Clusters Confined in Zeolites.Nat. Catal.2020, 3, 628–638. Google Scholar
    • 21. Peng M.; Dong C.; Gao R.; Xiao D.; Liu H.; Ma D.Fully Exposed Cluster Catalyst (FECC): Toward Rich Surface Sites and Full Atom Utilization Efficiency.ACS Cent. Sci.2021, 7, 262–273. Google Scholar
    • 22. An Z.; Zhang Z.; Huang Z.; Han H.; Song B.; Zhang J.; Ping Q.; Zhu Y.; Song H.; Wang B.; Zheng L.; He J.Pt1 Enhanced C-H Activation Synergistic with Ptn Catalysis for Glycerol Cascade Oxidation to Glyceric Acid.Nat. Commun.2022, 13, 5467. Google Scholar
    • 23. Wang C.; Yang B.; Gu Q.; Han Y.; Tian M.; Su Y.; Pan X.; Kang Y.; Huang C.; Liu H.; Liu X.; Li L.; Wang X.Near 100% Ethene Selectivity Achieved by Tailoring Dual Active Sites to Isolate Dehydrogenation and Oxidation.Nat. Commun.2021, 12, 5447. Google Scholar
    • 24. Tai W.; Dai W.; Wu G.; Li L.A Simple Strategy for Synthesis of b-Axis-Oriented MFI Zeolite Macro-Nanosheets.Chem. Synth.2023, 3, 38. Google Scholar
    • 25. Zhang Q.; Mayoral A.; Li J.; Ruan J.; Alfredsson V.; Ma Y.; Yu J.; Terasaki O.Electron Microscopy Studies of Local Structural Modulations in Zeolite Crystals.Angew. Chem. Int. Ed.2020, 59, 19403–19413. Google Scholar
    • 26. Zhang Q.; Li J.; Wang X.; He G.; Li L.; Xu J.; Mei D.; Terasaki O.; Yu J.Silanol-Engineered Nonclassical Growth of Zeolite Nanosheets from Oriented Attachment of Amorphous Protozeolite Nanoparticles.J.?Am. Chem. Soc.2023, 145, 21231–21241. Google Scholar
    • 27. Díaz I.; Kokkoli E.; Terasaki O.; Tsapatsis M.Surface Structure of Zeolite (MFI) Crystals.Chem. Mater.2004, 16, 5226–5232. Google Scholar
    • 28. Zhang X.; Yan T.; Hou H.; Yin J.; Wan H.; Sun X.; Zhang Q.; Sun F.; Wei Y.; Dong M.; Fan W.; Wang J.; Sun Y.; Zhou X.; Wu K.; Yang Y.; Li Y.; Cao Z.Regioselective Hydroformylation of Propene Catalyzed by Rhodium-Zeolite.Nature2024, 629, 597–602. Google Scholar
    • 29. Tshabalala T. E.; Coville N. J.; Anderson J. A.; Scurrell M. S.Dehydroaromatization of Methane over Sn-Pt Modified Mo/H-ZSM-5 Zeolite Catalysts: Effect of Preparation Method.Appl. Catal. A Gen.2015, 503, 218–226. Google Scholar
    • 30. Stakheev A. Y.; Shpiro E. S.; Tkachenko O. P.; Jaeger N. I.; Schulz-Ekloff G.Evidence for Monatomic Platinum Species in H-ZSM-5 from FTIR Spectroscopy of Chemisorbed CO.J.?Catal.1997, 169, 382–388. Google Scholar
    • 31. Chakarova K.; Mihaylov M.; Hadjiivanov K.Polycarbonyl Species in Pt/H-ZSM-5: FTIR Spectroscopic Study of 12CO-13CO Co-Adsorption.Catal. Commun.2005, 6, 466–471. Google Scholar
    • 32. Tkachenko O. P.; Shpiro E. S.; Jaeger N. I.; Lamber R.; Schulz-Ekloff G.; Landmesser H.Strong Modification of Pt-CO Interaction Caused by Alloying with Chromium in Pt-Cr/HZSM-5 Catalysts.Catal. Lett.1994, 23, 251–262. Google Scholar
    • 33. Nesterenko N. S.; Avdey A. V.; Ermilov A. Y.FTIR Study of the CO Adsorption over Pt/MFI Catalysts: Ab Initio Interpretation.Int. J. Quantum Chem.2006, 106, 2281–2289. Google Scholar
    • 34. Barshad Y.; Zhou X.; Gulari E.Carbon Monoxide Oxidation Under Transient Conditions: A Fourier-Transform Infrared Transmission Spectroscopy Study.J.?Catal.1985, 94, 128–141. Google Scholar
    • 35. Vazhnova T.; Rigby S. P.; Lukyanov D. B.Benzene Alkylation with Ethane in Ethylbenzene over a PtH-MFI Catalyst: Kinetic and IR Investigation of the Catalyst Deactivation.J.?Catal.2013, 301, 125–133. Google Scholar
    • 36. Deng Y.; Guo Y.; Jia Z.; Liu J. C.; Guo J.; Cai X.; Dong C.; Wang M.; Li C.; Diao J.; Jiang Z.; Xie J.; Wang N.; Xiao H.; Xu B.; Zhang H.; Liu H.; Li J.; Ma D.Few-Atom Pt Ensembles Enable Efficient Catalytic Cyclohexane Dehydrogenation for Hydrogen Production.J.?Am. Chem. Soc.2022, 144, 3535–3542. Google Scholar
    • 37. Barbera K.; Bonino F.; Bordiga S.; Janssens T. V. W.; Beato P.Structure-Deactivation Relationship for ZSM-5 Catalysts Governed by Framework Defects.J.?Catal.2011, 280, 196–205. Google Scholar
    • 38. Medeiros-Costa I. C.; Dib E.; Dubray F.; Moldovan S.; Gilson J. P.; Dath J. P.; Nesterenko N.; Aleksandrov H. A.; Vayssilov G. N.; Mintova S.Unraveling the Effect of Silanol Defects on the Insertion of Single-Site Mo in the MFI Zeolite Framework.Inorg. Chem.2022, 61, 1418–1425. Google Scholar
    • 39. Wang C.; Xu N.; Huang K.; Liu B.; Zhang P.; Yang G.; Guo H.; Bai P.; Mintova S.Emerging Co-Synthesis of Dimethyl Oxalate and Dimethyl Carbonate Using Pd/Silicalite-1 Catalyst with Synergistic Interactions of Pd and Silanols.Chem. Eng. J.2023, 466, 143136. Google Scholar
    • 40. Liu Y.; Liu Z.; Hui Y.; Wang L.; Zhang J.; Yi X.; Chen W.; Wang C.; Wang H.; Qin Y.; Song L.; Zheng A.; Xiao F. S.Rhodium Nanoparticles Supported on Silanol-Rich Zeolites Beyond the Homogeneous Wilkinson’s Catalyst for Hydroformylation of Olefins.Nat. Commun.2023, 14, 2531. Google Scholar
    • 41. Lang R.; Li T.; Matsumura D.; Miao S.; Ren Y.; Cui Y. T.; Tan Y.; Qiao B.; Li L.; Wang A.; Wang X.; Zhang T.Hydroformylation of Olefins by a Rhodium Single-Atom Catalyst with Activity Comparable to RhCl(PPh3)3.Angew. Chem. Int. Ed.2016, 55, 16054–16058. Google Scholar
    • 42. Li A.; Zhang Y.; Heard C. J.; Go??bek K.; Ju X.; ?ejka J.; Mazur M.Encapsulating Metal Nanoparticles into a Layered Zeolite Precursor with Surface Silanol Nests Enhances Sintering Resistance.Angew. Chem. Int. Ed.2023, 62, e202213361. Google Scholar
    • 43. Chai Y.; Liu S.; Zhao Z. J.; Gong J.; Dai W.; Wu G.; Guan N.; Li L.Selectivity Modulation of Encapsulated Palladium Nanoparticles by Zeolite Microenvironment for Biomass Catalytic Upgrading.ACS Catal.2018, 8, 8578–8589. Google Scholar
    • 44. Liu Z.; Huang F.; Peng M.; Chen Y.; Cai X.; Wang L.; Hu Z.; Wen X.; Wang N.; Xiao D.; Jiang H.; Sun H.; Liu H.; Ma D.Tuning the Selectivity of Catalytic Nitriles Hydrogenation by Structure Regulation in Atomically Dispersed Pd Catalysts.Nat. Commun.2021, 12, 6194. Google Scholar
    • 45. Hema ; Bhatt T.; Arya P.; Dhondiyal C. C.; Tiwari H.; Devlal K.Structural and Vibrational Study of Molecular Interaction in a Ternary Liquid Mixture of Benzylamine, Ethanol and Benzene.Struct. Chem.2022, 33, 207–218. Google Scholar
    • 46. Pretsch E.; Bühlmann P.; Badertscher M.IR Spectroscopy. In Structure Determination of Organic Compounds: Tables of Spectral Data; Springer: Berlin, Heidelberg, 2009; pp 1–67. Google Scholar
    • 47. Zou S.; Williams C. T.; Chen E. K. Y.; Weaver M. J.Surface-Enhanced Raman Scattering as a Ubiquitous Vibrational Probe of Transition-Metal Interfaces: Benzene and Related Chemisorbates on Palladium and Rhodium in Aqueous Solution.J.?Phys. Chem. B1998, 102, 9039–9049. Google Scholar
    • 48. Mrozek M. F.; Wasileski S. A.; Weaver M. J.Periodic Trends in Electrode-Chemisorbate Bonding: Benzonitrile on Platinum-Group and Other Noble Metals as Probed by Surface-Enhanced Raman Spectroscopy Combined with Density Functional Theory.J.?Am. Chem. Soc.2001, 123, 12817–12825. Google Scholar
    • 49. Khoma R. E.; Ennan A. A.; Gelmboldt V. O.; Shishkin O. V.; Baumer V. N.; Mazepa A. V.; Brusilovskii Y. E.Preparation and Some Physicochemical Properties of Benzylammonium Sulfates.Russ. J. Gen. Chem.2014, 84, 637–641. Google Scholar
    • 50. Korányi T. I.; Mihály J.; Pfeifer é.; Németh C.; Yuzhakova T.; Mink J.Infrared Emission and Theoretical Study of Carbon Monoxide Adsorbed on Alumina-Supported Rh, Ir, and Pt Catalysts.J.?Phys. Chem. A2006, 110, 1817–1823. Google Scholar
    • 51. Gellini C.; Moroni L.; Muniz-Miranda M.High Overtones of the C–H Stretching Vibrations in Anisole and Thioanisole.J.?Phys. Chem. A2002, 106, 10999–11007. Google Scholar
    • 52. McAllister M. I.; Boulho C.; Gilpin L. F.; McMillan L.; Brennan C.; Lennon D.Hydrogenation of Benzonitrile over Supported Pd Catalysts: Kinetic and Mechanistic Insight.Org. Process Res. Dev.2019, 23, 977–989. Google Scholar
    • 53. Zecchina A.; Geobaldo F.; Spoto G.; Bordiga S.; Ricchiardi G.; Buzzoni R.; Petrini G.FTIR Investigation of the Formation of Neutral and Ionic Hydrogen-Bonded Complexes by Interaction of H-ZSM-5 and H-Mordenite with CH3CN and H2O: Comparison with the H-NAFION Superacidic System.J.?Phys. Chem.1996, 100, 16584–16599. Google Scholar
    • 54. Deng X.; Qin B.; Liu R.; Qin X.; Dai W.; Wu G.; Guan N.; Ma D.; Li L.Zeolite-Encaged Isolated Platinum Ions Enable Heterolytic Dihydrogen Activation and Selective Hydrogenations.J.?Am. Chem. Soc.2021, 143, 20898–20906. Crossref,?Google Scholar
    • 55. Chakarova K.; Drenchev N.; Mihaylov M.; Nikolov P.; Hadjiivanov K.OH/OD Isotopic Shift Factors of Isolated and H-Bonded Surface Silanol Groups.J.?Phys. Chem. C2013, 117, 5242–5248. Google Scholar
    • 56. Bulánek R.; Vaculík J.; Vesely O.; P?ech J.; Kub? M.; Rube? M.; Bludsky O.Reactivity of Internal vs. External Br?nsted Acid Sites in Nanosponge MFI: H/D Exchange Kinetic Study.Micropor. Mesopor. Mater.2022, 332, 111717. Google Scholar
    • 57. Ma B.; Pan H.; Yang F.; Liu X.; Guo Y.; Wang Y.Efficient CO2 Catalytic Hydrogenation over CuOx-ZnO/Silicalite-1 with Stable Cu+ Species.Catal. Sci. Technol.2022, 12, 5850–5860. Google Scholar
    • 58. Felvey N.; Guo J.; Rana R.; Xu L.; Bare S. R.; Gates B. C.; Katz A.; Kulkarni A. R.; Runnebaum R. C.; Kronawitter C. X.Interconversion of Atomically Dispersed Platinum Cations and Platinum Clusters in Zeolite ZSM-5 and Formation of Platinum gem-Dicarbonyls.J.?Am. Chem. Soc.2022, 144, 13874–13887. Google Scholar
    • 59. Chandrashekhar V. G.; Baumann W.; Beller M.; Jagadeesh R. V.Nickel-Catalyzed Hydrogenative Coupling of Nitriles and Amines for General Amine Synthesis.Science2022, 376, 1433–1441. Google Scholar
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