Article | Open | Published:

Selective ensembles in supported palladium sulfide nanoparticles for alkyne semi-hydrogenation

Nature Communicationsvolume 9, Article number: 2634 (2018) | Download Citation


Ensemble control has been intensively pursued for decades to identify sustainable alternatives to the Lindlar catalyst (PdPb/CaCO3) applied for the partial hydrogenation of alkynes in industrial organic synthesis. Although the geometric and electronic requirements are known, a literature survey illustrates the difficulty of transferring this knowledge into an efficient and robust catalyst. Here, we report a simple treatment of palladium nanoparticles supported on graphitic carbon nitride with aqueous sodium sulfide, which directs the formation of a nanostructured Pd3S phase with controlled crystallographic orientation, exhibiting unparalleled performance in the semi-hydrogenation of alkynes in the liquid phase. The exceptional behavior is linked to the multifunctional role of sulfur. Apart from defining a structure integrating spatially-isolated palladium trimers, the active ensembles, the modifier imparts a bifunctional mechanism and weak binding of the organic intermediates. Similar metal trimers are also identified in Pd4S, evidencing the pervasiveness of these selective ensembles in supported palladium sulfides.


The ultimate mission of researchers working in heterogeneous catalysis is the identification of active ensembles with a high density to enable efficient turnover while avoiding undesired intermolecular interactions, and exhibiting long-term stability to ensure a well-defined performance. Nevertheless, the fulfillment of all these requirements in one catalytic material has yet to be accomplished, even for well-established reactions like heterogeneously-catalyzed hydrogenations studied since the 1880’s by Wilde, Sabatier, and Senderens1,2.

The chemo- and stereoselective hydrogenation of functionalized alkynes is a key catalytic transformation applied industrially at different scales, ranging from the gas-phase multi-ton purification of olefin streams for polymer manufacture3 to the smaller three-phase batch preparation of high-added-value fine chemicals4,5. Examination of the rich scientific literature emphasizes the wide dominance of palladium-based catalysts, due to the ability to dissociate hydrogen, and the importance of preventing the undesired hydrogenation of competing functional groups through electronic poisoning with suitable modifiers (Fig. 1)6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21,22,23,24,25,26,27,28,29,30,31,32,33,34,35. Similarly, oligomerization paths (C–C couplings) must be suppressed by the strict control over the ensemble size. Thus, the synthesis of trimeric ensembles36,37,38,39, and the presence of electronic modifiers reducing the hydrogen uptake of Pd and the formation of subsurface hydrides, are key parameters for achieving high selectivity both in gas- and three-phase operations.

Fig. 1
Fig. 1

Survey of alkyne semi-hydrogenation catalysts. Chronological development for gas- and liquid-phase applications tracing from the pioneering works of Wilde1 and Sabatier2 to the more recent discoveries6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21,22,23,24,25,26,27,28,29,30,31,32,33,34,35. Six prominent catalyst families can be distinguished based on (i) supported metal nanoparticles, (ii) intermetallics, alloys, and Lindlar-type formulations where Pd is poisoned by a second metal, (iii) ligand-modified or hybrid materials featuring an organic surfactant that partially covers the surface of Pd nanoparticles, (iv) metal oxides, (v) supported single atoms, and (vi) Pd modified by p-block elements. The current industrially applied catalysts are indicated in bold. Surface structures of representative examples of each catalyst family are illustrated, highlighting the catalytic ensemble

Since 1952, the manufacture of building blocks for pharmaceuticals, vitamins, agrochemicals, and fragrances via alkyne semi-hydrogenation4,40,41 has been conducted over the well-known lead-poisoned palladium (5 wt.%) supported on calcium carbonate (Lindlar catalyst), despite drawbacks of poor metal utilization and toxicity42,43. However, the recent disruptive legislations restricting the use of hazardous compounds have steered the innovation and creativity of scientists towards the development of sustainable alternatives. This has enabled the incorporation of new families of hydrogenation catalysts based on: (i) alternative metals1,2,7,9,10,30, (ii) alloy and intermetallic compounds8,11,12,13,14,15,16,18,19,20,21, (iii) ligand-modified nanoparticles6,17,22,25, (iv) transition metal oxides26,27,34,35, and (v) supported single atoms24,31,32. While these share better ensemble definition than unmodified Pd, intrinsic drawbacks like instability against high pressure induced segregation for intermetallics44,45,46, accessibility constraints in ligand-modified and single atom catalysts31,47, and poor H2 activation on oxides48 have been identified.

In the search for new catalysts, very few works have studied the modification with p-block elements22,28,29,49. In particular, sulfur-modified Pd catalysts could be envisaged mimicking the strategy of ensemble and electronic density control in enzymes. In fact, transition metal sulfides are applied for hydrotreating in oil refineries due to their resistance to poisons and ability toward H2 activation50,51, and have also been studied for electrochemical hydrogen evolution52. Recently, a crystalline Pd4S phase was shown to exhibit promising performance in the high pressure gas-phase hydrogenation of simple alkynes impurities in petroleum-derived olefin streams, although no molecular-level understanding was gathered33,53,54. Since the Pd-S phase diagram shows full mixing in all compositions and a continuum of closely related stable phases55, it offers room to tailor the active phase with the most selective ensemble and amount of electronic poisoning at the atomic scale.

By introducing a facile and scalable procedure to prepare crystal phase and orientation controlled Pd3S nanoparticles supported on carbon nitride, this article demonstrates that sulfur can play a multifunctional role enabling unparalleled hydrogenation performance in the continuous-flow three-phase semi-hydrogenation of linear, internal, and bulky functionalized alkynes. This is linked to the presence of trimeric metal ensembles, which are also shown to be present in palladium sulfides of different stoichiometry by the preparation and detailed interrogation of the supported Pd4S phase. The superiority with respect to other major families of hydrogenation catalysts is established by determining the hierarchy of key descriptors for the performance.


Synthesis of supported palladium sulfides

Sulfided palladium phases (PdxSy) can be readily prepared by the post-synthetic modification of supported metal nanoparticles with sulfur-containing compounds such as H2S, Na2S, PdSO4, and Pd thiolates. Several works have examined the phase evolution on treatment of Pd/C with H2S56, which often leads to mixed crystal phases57, but this toxic and highly corrosive gas is synthetically unattractive. Here, aqueous sodium sulfide was applied as an alternative, less widely studied sulfidation agent and the phase selectivity was monitored at different temperatures (Fig. 2a). Mesoporous graphitic carbon nitrite (C3N4) was targeted as a carrier due to its well-known ability to stabilize palladium with high dispersion, including as single atoms (Pd@C3N4)31, which was expected to facilitate the sulfidation treatment. Interestingly, despite exhibiting high stability in oxidative and reductive environments at elevated temperatures, tests in the temperature range 373–423 K over Pd@C3N4 revealed that isolated palladium atoms were not stable against sulfidation treatments, transforming into nanoparticles, as evidenced by scanning transmission electron microscopy (STEM) (Supplementary Fig. 1a). For this reason, palladium was introduced via the wet deposition of palladium chloride coupled with an additional sodium borohydride reduction step to promote the formation of palladium nanoparticles (Pd/C3N4) with an average diameter of 1–2 nm and a very narrow size distribution.

Fig. 2
Fig. 2

Synthetic approach and microscopy images of the palladium sulfide catalysts. a Graphical depiction of the sulfidation of palladium nanoparticles supported on graphitic carbon nitride. The average particle size increased from 1.2 to 1.8 nm upon treatment with Na2S (see Supplementary Note 1), consistent with the distortion of the palladium lattice expected upon introduction of sulfur atoms. Scale bars: 30 nm. b HAADF-STEM image with the particle size distribution (inset) of Pd3S/C3N4-423 fresh (left) and after 50 h on stream (right) excluding the occurrence of sintering. Scale bars: 2 nm. c HRTEM image of Pd3S/C3N4-423 fresh (left) and after 50 h on stream (right) confirming the preserved crystalline structure. d HAADF-STEM image (left) and the derived Pd particle size distribution (inset), and HRTEM (right) image of Pd4S/CNF. Scale bars: 30 and 2 nm, respectively

Analysis of the bulk properties of Pd/C3N4 and the sulfided analogs (Pd3S/C3N4-T, where Pd3S was the only crystalline phase identified and T = 373–473 K) confirmed the uptake of sulfur, absence of metal leaching, the negligible incorporation of sodium (< 2 ppm), and structural integrity of the carrier upon sulfidation treatment (Table 1). The latter was verified by equivalent treatment of the metal-free C3N4 establishing the preserved crystallinity and negligible sulfur uptake (Supplementary Fig. 2). Consistent with the low content and high dispersion of palladium, no metal-containing phases were detected by X-ray diffraction (XRD) in any of the catalysts supported on C3N4. To determine whether the treatment resulted in the formation of one or more PdxSy phases or sulfur doping localized at the surface, high-resolution transmission electron microscopy (HRTEM) analyses were undertaken. Examination of the HRTEM images revealed the formation of crystalline Pd3S nanoparticles, characterized by an interplanar distance of 0.25 nm corresponding to the (202) facet56, in all of the sulfided samples on C3N4 (Fig. 2c and Supplementary Fig. 3). Elemental mapping by energy-dispersive X-ray spectroscopy (EDX) further confirmed the close proximity of palladium and sulfur and absence of any sulfidation of the carrier (Supplementary Fig. 4).

Table 1 Properties of the catalysts studied

To gain insight into the thermodynamically preferred surface terminations of Pd3S, the stability of several stoichiometric low-index planes was considered by density functional theory (DFT). The simulations indicate that Pd3S has two low-energy crystal facets: (001) and (202), both exhibiting inequivalent palladium and sulfur atoms (Fig. 3 and Supplementary Fig. 14). The Pd3S(001) surface displays Pd atoms arranged in chains and surrounded by S atoms, where rectangular patterns resembling those of the (110) surface of an fcc structure are found between the surface Pd neighbors. On the Pd3S(202) surface, each Pd is surrounded by four Pd atoms and one S. Therefore, both surfaces show triangular Pd ensembles with an area of 7.09 Å2 separated by S atoms. While on Pd3S(202), the triangular ensembles belong to the topmost layer, on Pd3S(001) they are formed by two surface and one subsurface Pd atoms. The surface energy (γs) of these terminations differs by 0.15 J m−2 with the (001) facet slightly favored (Supplementary Table 4).

Fig. 3
Fig. 3

Structural resemblance of Pd3S and Pd4S to pristine Pd surfaces. Top views of the low-energy terminations. The structural correspondence of the sulfide surfaces with the most closely related palladium surface Pd(111) or Pd(110) is highlighted with an orange hexagon or rectangle. The Pd atoms on the Pd3S and Pd4S surfaces belonging to the ensemble are connected with a white triangle. Inequivalent palladium and sulfur atoms are identified with different colors (for more details see Supplementary Note 3). Color code: Pd(1)surf (purple), Pd(2)surf (blue), Pdbulk (light blue), S(1)surf (yellow), S(2)surf (orange)

Comparative inspection of the Pd3S(202) and Pd(111) surfaces sheds light on the observed preferential development of the former, identifying their close geometrical relationship, maintaining the same pseudo-hexagonal arrangement of the surface Pd(111) atoms in the fcc structure typically adopted by this metal. In contrast, the Pd3S(001) surface displays a closer resemblance to the rectangular pattern of Pd(110). Therefore, starting from the metallic Pd nanoparticles the mild sulfidation treatment can be seen as a lattice distortion to incorporate S anions, leading to a kinetically-controlled process where the formation of the (202) surface implies the lowest number of distortions. This agrees with earlier results identifying the preferential development of Pd3S(202) surface terminations upon sulfidation of carbon-supported palladium nanoparticles with hydrogen sulfide56.

The chemical state of Pd at the surface of the sulfided catalysts was probed by X-ray photoelectron spectroscopy (XPS) (Supplementary Fig. 5). All the samples display Pd 3d5/3 peaks at 335.5 and 337.9 eV assigned to Pd0 and Pd2+ species, respectively53. Evaluation of the spectra shows that the relative ratio of Pd0/Pd2+ increases upon sulfidation, pointing to the formation of sulfided Pd species with an average oxidation state close to 0. Note that there is still a debate on the XPS signals attributed to PdxSy species; some works reporting the presence of cationic Pd species58 and other observing a ‘metallic’ nature. The latter were attributed to the possible formation of a solid solution between Pd and S. To address this point and discern the bonding character, the difference charge density of Pd3S crystal and the charge transfer from Pd to S have been evaluated by the Bader charge analysis (Supplementary Note 3). The results point to a high degree of covalency, with a polar Pd–S bond and negligible electron transfer, which is in agreement with the experimentally observed tendency towards Pd0. In addition to charge effects, XPS shifts could also arise due to the finite size of the small nanoparticles in the catalyst that can also lead to deviations from the bulk values. To further explore the effect of sulfur poisoning on the catalysts electronic properties, projected d-band densities of states were calculated for all of the systems studied (Supplementary Fig. 15). Consistent with the XPS observations, down-shifts to –1.80 and –1.90 eV are evidenced for Pd3S(202) and Pd3S(001), respectively, compared to the reference value of –1.39 eV for Pd(111).

For reference purposes, a supported Pd4S catalyst was prepared via thermal decomposition in H2 flow of PdSO4 on carbon nanofibers (CNF)33. This procedure is less attractive since for every mole of Pd4S produced it evolves three moles of toxic gaseous SO2 or even H2S. Furthermore, as previously reported, it lacks of a precise control over the particle size distribution (1–20 nm). Characterization by XRD confirms the formation of the Pd4S phase (Supplementary Fig. 2a), and contrarily to Pd3S/C3N4, the resulting crystals mainly expose the lowest-energy (200) facet (Fig. 2d). Interestingly, a similar theoretical analysis of the Pd4S(200) surface reveals that it also features Pd trimers spaced by S atoms as well as a small fraction of Pd-square arrangements (Fig. 3). Consistent with the lower amount of sulfur, analysis by XPS evidences the closely metallic nature of surface palladium (peak at 335.5 eV, Supplementary Fig. 5) and a downshift of the Pd d-band to −1.70 eV, a slightly less poisoned state than Pd3S.

Performance in alkyne semi-hydrogenation

The sulfided palladium catalysts were evaluated in the continuous-flow three-phase semi-hydrogenation of 2-methyl-3-butyn-2-ol, an important building block in the synthesis of vitamin E, at various temperatures and pressures (Fig. 4a, b and Supplementary Fig. 7) and benchmarked against state-of-the-art materials (Lindlar-type PdPb/CaCO3, ligand-modified Pd-HHDMA, Pd@C3N4 the properties of which are provided in Table 1 and Supplementary Table 1). Compared to the Lindlar catalyst, which achieves ~90% selectivity to 2-methyl-3-buten-2-ol and the remaining 10% to 2-methyl-2-butanol, Pd3S/C3N4-423 is fully selective to the alkene and shows almost a 3.5-fold higher reaction rate (0.3 and 1.0 × 103 h–1, respectively, at 303 K and 1 bar). Under the same conditions, Pd-HHDMA and Pd@C3N4 catalysts are slightly less active (0.6 and 0.2 × 103 h–1, respectively) although they display excellent selectivity (100%). Pd4S/CNF displays similar selectivity to Pd3S/C3N4-423 under all conditions applied, but with slightly inferior reaction rates, for instance at 303 K and 1 bar the rate is 30% lower (0.7 compared to 1.0 × 103 h–1 than on Pd3S/C3N4-423). Interestingly, Pd/C3N4 presents lower selectivity to the alkene (90%), but similar activity to Pd3S/C3N4-423, likely due to the higher dispersion of palladium in the untreated sample (Table 1).

Fig. 4
Fig. 4

Evaluation of the alkyne semi-hydrogenation performance of the catalysts. a The contour plots map the effect of temperature and pressure on the rate (in 103 h–1) and b selectivity to 2-methyl-3-buten-2-ol (in %) of Pd3S/C3N4-423 compared to Pd4S/CNF, PdPb/CaCO3, Pd-HHDMA, and Pd@C3N4. Conditions: Wcat = 0.1 g, T = 303 K, FL(alkyne + toluene) = 1 cm3 min–1, FG(H2) = 36 cm3 min–1

To provide a broader comparison among all state-of-the-art systems and extrapolate these conclusions, the reaction temperature and pressure were varied to study the influence on the rate and selectivity in the semi-hydrogenation of 1-hexyne, a widely studied model alkyne, where the reaction can be accompanied by the cis-trans isomerization of the alkene product (Supplementary Fig. 8). The contour maps clearly show the superiority of using p-block elements for modifying Pd-based catalysts. Note that the only side product formed over the palladium sulfides was n-hexane (<5%). Unlike in the cases of Pd-HHDMA, PdPb/CaCO3, and Pd@C3N4, no traces of isomers like cis and trans 2-hexene were produced on PdxS catalysts. Furthermore, the similarly high selectivity observed below 343 K and 5 bar, points to the resistance of Pd3S/C3N4-423 towards the formation of β-hydrides. Consistently, analysis by the temperature-programmed reduction in H2 did not evidence any peak due to β-hydrides5. The DFT results indicate that the adsorption of H atoms in subsurface positions is endothermic by 0.14 eV. Since it was not possible to reach higher alkyne conversions in our continuous-flow set up, additional batch tests were conducted to evaluate the selective performance under more challenging conditions. An impressive 95% selectivity to 2-methyl-3-buten-2-ol was preserved even at 80% conversion over the Pd3S and Pd4S phases, whereas much more significant losses were evidenced for the PdPb/CaCO3 (80%) and Pd-HHDMA (85%) catalysts.

To gain insight into the comparative reaction mechanisms over Pd and PdxS surfaces, DFT calculations were performed (details in Supplementary Note 4). Acetylene was chosen as a model alkyne to obtain robust answers to the challenging reaction networks. The validity of using this surrogate was verified by the parallel adsorption and reaction profiles observed for acetylene and 2-methyl-3-butyn-2-ol over the Pd3S catalysts (Supplementary Fig. 17). Although the adsorption of 2-methyl-3-butyn-2-ol is slightly more exothermic, due to the hydrogen bond between the alcohol group of the alkynol and the surface sulfur atom, this interaction does not change the reaction profile as is present for all intermediates and products. Also, under liquid-phase operations the reaction environment has a limited effect on the state of the catalyst59. Alkyne hydrogenation follows a Horiuti-Polanyi mechanism59,60 (Fig. 5, Supplementary Tables 57). The first step of the reaction is the dissociation of molecular hydrogen that occurs homolytically at surface Pd sites over Pd(111), Pd4S(110), Pd4S(200), and Pd3S(001), while the alternative heterolytic path61 features low energy only on the Pd3S(202) surface. This results in the storage of hydrogen atoms in the form of thiol groups (SH) on the Pd3S(202) surface. C2H2 adsorption is exothermic on Pd(111), Pd3S(202), and Pd4S(200) surfaces (–2.51, –0.48, and –0.24 eV, respectively). Note that on Pd both the alkyne and H2 compete for the same site, while on Pd3S this is not the case because H atoms bind to surface sulfur atoms and the organic reactant at the Pd-ensembles. This bifunctional mechanism, where fragments are stored at different sites of the catalyst surface, ensures higher activity of PdxS than the reference Pd/Al2O3 (Supplementary Note 2). The first addition of H to the activated alkyne leads to a vinyl moiety (HCCH2), whereas the second can result in either ethene (H2CCH2) or ethylidene (HCCH3) formation. Notably, the difference in energy barrier between H2CCH2 and HCCH3 formation on Pd3S(202) is greater than on Pd(111) and on Pd4S(200). At this stage, the desired semi-hydrogenation product (H2CCH2) could desorb or undergo over-hydrogenation via an ethyl intermediate (H2CCH3) to form ethane. Ethene desorption from the Pd3S(202) and Pd4S(200) surfaces (0.08 and 0.22 eV, respectively) is energetically preferred over its further hydrogenation (0.79 and 0.55 eV, respectively), even when the zero point vibrational energy corrections are included (Supplementary Table 6), which is completely opposite to the behavior encountered on Pd(111) where the over-hydrogenation barrier 0.45 eV is much lower than that of the alkene desorption (0.85 eV). This ultimately explains the low selectivity to ethene on Pd. The second potential side reaction investigated is oligomer formation, which was studied by modeling ethyne-ethyne coupling (Fig. 5c) and alkyne-vinyl paths providing similar insights due to scaling relations62 (Supplementary Fig. 19, 21). The barrier for oligomerization is 1.34 eV on the Pd(111) surface, and 1.64 eV on Pd3S(202), which indicates that the surface anisotropy hinders the diffusion of the alkyne on the latter surface, consistent with the expected site isolation. This explains why almost no oligomer formation is observed over the sulfided catalyst. Complementary analysis of the reaction profiles on the Pd3S(001) and Pd4S(110) surfaces are provided in Supplementary Note 4.

Fig. 5
Fig. 5

Density functional theory reaction analysis. ac Energy profiles for the semi-hydrogenation (a), over-hydrogenation (b), and oligomerization (c) of acetylene on Pd3S(202), Pd4S(200), and Pd(111). The asterisks denote adsorbed species, the color of the profile matches that of the possible intermediate, and the bars relate to the energy differences for Pd3S(202) presented in e: HCCH adsorption (black bars), H2CCH2 desorption (gray bars), and the difference in activation energy between H2CCH2 (ethene) and HCCH3 (ethylidene) formation (red bars), H2CCH2 desorption and H2CCH3 formation (orange bars), and for oligomerization (blue bars). d Top view of the DFT-optimized adsorption configuration of the reaction intermediates and transition states (TS) on the surfaces. The elementary steps are shown in Supplementary Table 5. Color code as in Fig. 3, carbon (black), hydrogen (white)

Long-term tests conducted to verify the stability of the Pd3S/C3N4-423 and Pd4S/CNF catalysts, evidenced no signs of deactivation after 50 and 25 h on stream, respectively (Fig. 6a). Unfortunately, a longer test on the Pd4S/CNF sample was not possible due to the development of substantial pressure drop in the reactor, which resulted from the mechanical instability of the CNF. Analysis post-reaction by HRTEM, STEM, and XPS confirmed the similar composition and absence of nanoparticle sintering or phase segregation with respect to the fresh catalyst for Pd3S/C3N4-423 (Fig. 2, Supplementary Fig. 5). This is an important advantage with respect to intermetallic compounds, where segregation effects have been reported to limit the ensemble control on the surface20,44,46,63,64. To shed light on the intrinsic stability of the system, detailed simulations were conducted to assess the likelihood of vacancy formation, sulfur incorporation to the reacting alkyne, and segregation effects. The energy penalty for forming a vacancy and releasing H2S on the (202) and (001) surfaces was calculated to be 0.56 and 1.58 eV, respectively, pointing to the stability under liquid-phase processes, while the formation energy of H2C = CHSH on the (202) and (001) surfaces is 1.13 and 2.60 eV, highlighting the impossibility of transferring sulfur to the substrate. Also, the segregation of a Pd atom from the bulk towards the surface requires 2.90, 4.30, and 2.96 eV for Pd3S(001), Pd3S(202), and Pd4S(200), respectively, meaning that even in the presence of high amounts of atomic H on the surface no preferential Pd or S segregation occurs44. Similarly, the formation of islands is not favored as the energy to exchange a Pd by a surface S atom is 3.12, 2.20, and 1.43 eV, respectively.

Fig. 6
Fig. 6

Stability and substrate scope of the palladium sulfide catalysts. a Both Pd3S/C3N4 (blue circles) and Pd4S/CNF (red triangles) display a stable performance on stream in the selective hydrogenation of 2-methyl-3-butyn-2-ol. b The impact of the adsorption length (Lads) of functionalized alkynes of different sizes over Pd3S/C3N4-423 (blue circles) and Pd-HHDMA (green circles). Conditions: Wcat = 0.1 g, T = 303 K, P = 1 (a) or 3 (b) bar, FL(alkyne + toluene) = 1 cm3 min–1, FG(H2) = 36 cm3 min−1

Most of the relevant alkynes for the pharmaceutical and fine chemical industries are highly branched compounds with internal triple bonds and additional functionalities. To explore the scope of supported Pd3S systems, the performance of Pd3S/C3N4-423 has been compared with that of the commercial ligand-modified Pd-HHDMA catalyst in the hydrogenation of alkynes of varying size and functionality, namely, 1-hexyne, 3-hexyne, 1-dodecyne, and 1,1-diphenyl-2-propyn-1-ol (Fig. 6b). With adsorption lengths (defined by the size of the activated alkyne) shorter than 8 Å, similar rates were observed over both catalysts. However, while Pd-HHDMA becomes significantly less active at longer adsorption lengths, the performance of Pd3S/C3N4-423 is independent of the size and functionality of the substrate. This effect can be rationalized by the fact that the architecture of active ensembles in Pd3S is two dimensional as in the Lindlar system, whereas the HHDMA-modified catalyst shows a three dimensional structure featuring hydrophobic pores that provide access to the alkynes only if they are terminal and not too bulky47. Thus, we can conclude that the Pd3S/C3N4-423 catalyst matches and even exceeds the performance of Pd-HHDMA, illustrating the effectiveness of the sulfur modification for preparing superior catalysts with clear practical scope.


To overcome the intrinsic limitations of palladium nanoparticles (i.e., uncontrolled ensemble size and strong adsorption of the alkene product), researchers have mainly targeted the integration of confined ensembles (no more than 3 atoms) and tailored electronic properties (Fig. 1). To compare those strategies with PdxS catalysts, we first evaluated the alkyne semi-hydrogenation performance using the differential adsorption energies, Eads(C2H2) – Eads(C2H4), as a unified descriptor accounting for the intrinsic thermodynamic selectivity (Fig. 7a). Notice that other previously reported criteria for gas-phase hydrogenation screening such as the energy of methyl group adsorption38 or the difference between the hydrogen barrier and the adsorption energy of the alkene65 do not provide a satisfactory description. The former parameter does not consider the effects of van der Waals contributions, while the latter parameter is not suitable for catalysts in which hydrogen dissociation is rate determining (e.g., oxides). Even though all the modified materials display favorable values with respect to bare palladium (becoming more positive), correlation with the observed rates of 2-methyl-3-buten-2-ol formation reveals a wide variation in the productivity depending on the catalyst family. Thus, a framework and hierarchy of property-performance relationships were identified to account not only for selectivity, but also activity and stability (Fig. 7b).

Fig. 7
Fig. 7

Catalytic descriptors for alkyne semi-hydrogenation. a Rate of alkene formation at T = 303 K and P = 1 bar versus the differential adsorption energy of acetylene and ethene for all classes of catalysts. b Radar plot charting the relation of the rate with key theoretical indicators for the activity: the adsorption energy of the alkyne (Eads(C2H2)) and the activation energy for H2 dissociation (Ea(H2)), selectivity: the alkene adsorption energy (Eads(C2H4)), and the ensemble area (Aensemble), and the stability: the segregation energy (Eseg). Values closest to the perimeter lead to enhanced properties. The blue shaded area connects the optimal values to date found for the Pd3S system

Selectivity depends on (i) the adsorption energy of the alkene (Eads(C2H4)) which shows an optimal value close to 0 or positive, and (ii) the ensemble area whose improved value (ca. 8 Å2) is shared by all catalysts. Activity is driven by two criterion with different relative weight: the adsorption of the alkyne (described by the negative Eads(C2H2)) is favorable over all catalysts, while most importantly the hydrogen activation energy (Ea(H2)) discriminates between materials able of readily split molecular hydrogen and catalysts requiring harsh reaction conditions. Consideration of these factors clearly emphasizes the superiority of Pd-based systems, exhibiting the lowest barriers for H2 dissociation and strong alkyne adsorption energies. Finally, stability could be assessed by several potential phenomena and scenarios, but for the sake of simplicity the segregation energy (Eseg), which is the differential energy between the ground state (i.e., an alloyed metallic surface) and the system after segregating one atom towards the surface, is taken as a measure for the robustness of the catalyst.

Compared to the archetypal Lindlar catalyst, sulfur in PdxS systems would embed both the functions of acting as a molecular modulator on the ensemble mimicking the cooperative lead-quinoline role, and the electronic poisoning effect of lead42. However, sulfur poisoning is much more effective as very small nanoparticles with a high surface/volume ratio can be used instead of the large nanoparticles required for the PdPb catalyst. The need for facile hydrogen activation limits the practical relevance of oxides and other metals (Ag, Au)19,26,34,35,66. This is not the case in PdxS, intermetallics, ligand-modified nanoparticles, and single-atom catalysts due to the intrinsic ability of Pd to activate H2. The excellent site isolation in well-defined ensembles featured by intermetallics, ligand-modified nanoparticles, and single-atom catalysts lead to quite selective catalysts16,23,25,31. However, the preferential hydrogen adsorption on Pd in alloys and intermetallics induces severe segregation effects spoiling the control of surface ensembles achieved via the precise synthesis45,46. Note that induced segregation issues are much more relevant in gas-phase applications due to the high temperature, pressure, and absence of an organic solvent (Supplementary Table 8). Remarkably, Pd segregation or islanding by substituting a palladium atom with sulfur is not favorable due to the polarization of the Pd-S bond enhancing the robustness of Pd3S. This is even more enhanced in Pd3S(001) and Pd4S(110) as both display vacancy formation energy higher than Pd3S(202), making Pd4S more suited to high-pressure gas-phase operation. That is the reason why among all catalysts the Eseg (accounting for the energy needed to enlarge the surface ensemble by one Pd atom from the bulk) of Pd3S and Pd4S are the highest ones (5.0 and 3.0 eV, respectively), while in PdPb this requires 0.7 eV. When considering ligand-modified systems like Pd-HHDMA, the three dimensional structure of such catalysts imposes accessibility constraints limiting their applicability for the conversion of bulky and internal alkynes, important intermediates in the fine chemical industry. This limitation is not present in the PdxS catalyst as a two dimensional structure ensures the conversion of complex sterically hindered substrates. Single atoms display distinct geometric and electronic properties compared to catalysts based on nanoparticles, while the scaffold can also contribute to H2 activation and stabilization of the reactants31. Sulfur atoms in PdxS also share some of these features. The adsorbed H atoms are stored at the S centers in the form of thiols leaving the Pd site free for alkyne adsorption. This means that there is no competition between the alkyne and hydrogen for site availability and the mechanism is similar to that of a dual site, which is again a consequence of the Pd–S bond polarity. The bifunctionality is more effective as no competition between the alkyne and hydrogen for the active sites occurs, this is reflected in the different reaction orders with respect to the alkyne, which is negative for Pd and close to zero for Pd3S (Supplementary Note 2). This explains the higher activity of Pd3S/C3N4 than the reference Pd/Al2O3. Therefore, the combination of crystal phase and orientation control observed in the sulfidation process to form the Pd3S/C3N4 catalyst ensures that the best values for the set of descriptors are achieved in an elegant, yet efficient manner constituting a revolutionary step in catalyst design.

In conclusion, supported palladium sulfides have been shown to possess unique ensembles with face- and phase-dependent geometric and electronic characteristics and high stability, demonstrating exciting potential as catalysts for the selective hydrogenation of alkynes. A mild sulfidation treatment over supported metallic Pd nanoparticles led to the incorporation of sulfur into the palladium lattice, which drives the formation of a nanostructured Pd3S phase preferentially exposing the (202) crystal facets. This surface displays isolated Pd3 ensembles surrounded by sulfur atoms featuring the right ensemble and electronic poisoning to allow the selective hydrogenation of linear, branched, and bulky functionalized alkynes. Ensembles of similar architecture and functionality were also evidenced in Pd4S/CNF. The PdxS catalysts outperformed all state-of-the-art catalysts in terms of alkene formation rate per mole of Pd, and evidenced high durability with no sign of segregation. A detailed comparison to the existing hydrogenation catalysts illustrated the hierarchy of key performance descriptors, demonstrating that the reported synthetic protocol produces a catalyst that synergistically combines the best characteristics of bond polarization, crystal phase and orientation control, while keeping a two-dimensional nature enabling the superior performance for a broad set of compounds. The present approach illustrates how the concept of ensemble control in kinetically-trapped crystal orientations can be employed in the precise design of evolved catalysts.


Catalyst preparation

The mesoporous graphitic carbon nitride carrier (C3N4) was prepared by controlled polymerization. Briefly, cyanamide (3.0 g, Sigma-Aldrich, 99%) and an aqueous dispersion of colloidal silica (12 g, 40 wt.% solids, 12 nm average diameter, Sigma-Aldrich) were mixed and stirred at 373 K for 6 h to completely evaporate the water. The resultant solids were ground and calcined at 823 K (2.3 K min–1 ramp) for 4 h under a nitrogen flow (15 cm3 min–1). The silica was removed by treating the solid in a 4 M aqueous solution of NH4HF2 (200 cm3, Acros Organics, 95%) for 48 h. The template free mesoporous carbon nitride was collected by filtration, washed thoroughly with distilled water and ethanol, and dried at 333 K overnight.

The incorporation of palladium nanoparticles was approached by wet deposition, targeting a metal loading of 0.5 wt.%. The carrier was dispersed in deionized water (0.01 gcarrier cm–3) under sonication for 1 h prior to the introduction of an aqueous solution (4.72 cm3 gcarrier–1) containing PdCl2 (0.01 M, ABCR Chemicals, 99%) and NaCl (0.04 M, Sigma-Aldrich, 99%). The resulting suspension was stirred at room temperature for 2 h in the dark. To promote metal nanoparticle formation, an aqueous solution (1.4 cm3 gcarrier–1) of NaBH4 (0.5 M, Sigma-Aldrich, 99%) was subsequently added dropwise and the mixture was stirred overnight. Finally, the solids (Pd/C3N4) were collected by filtration, washed thoroughly with distilled water and ethanol and subsequently dried at 333 K overnight. The atomic dispersion of palladium on C3N4 (Pd@C3N4) was achieved by microwave-assisted-deposition. An aqueous solution of Pd(NH3)4(NO3)2 (0.05 cm3, 5 wt.% Pd, ABCR Chemicals) was added to a suspension (20 cm3) of the dispersed C3N4 (0.5 g) and stirred overnight in the dark. The resulting suspension was treated in a microwave reactor (CEM Discover SP), applying a cyclic program of 15 s irradiation and 3 min cooling with 20 repetitions using a power of 100 W. The resulting powder was collected, washed, and dried as described for the nanoparticle-based system.

The catalyst was added to a Teflon-lined autoclave containing an aqueous solution of Na2S·9H2O (Sigma-Aldrich, 99%) using a molar S/Pd ratio of 10. The autoclave was then heated to the desired temperatures (373, 398, or 423 K) for 3 h. The solid was collected by filtration, extensively washed with deionized water and ethanol, and dried overnight at 333 K.

In an alternative route, a supported Pd4S catalyst was prepared by incipient wetness impregnation of PdSO4 (ABCR-Chemicals, 99.99%) on CNFs (Aldrich). After drying the resulting material was treated under 10 vol.% H2/He at 523 K for 1 h.

Reference PdPb/CaCO3 (Alfa Aesar, ref: 043172) and Pd-HHDMA, where HHDMA stays for hexadecyl(2-hydroxyethyl)dimethylammonium dihydrogen phosphate (NanoSelect LF 200TM, Strem Chemicals, ref.46-1711) catalysts were used as received. No quinoline was added to the PdPb/CaCO3 catalyst during testing.

Characterization methods

The Pd and Na contents in the catalyst were determined by inductively coupled plasma-optical emission spectrometry (ICP-OES) using a Horiba Ultra 2 instrument equipped with a photomultiplier tube detector. The samples were dissolved in piranha solution under sonication until the absence of visible solids. The S content was determined by infrared spectroscopy using a LECO CHN-900 combustion furnace. Nitrogen isotherms were obtained at 77 K using a Micrometrics Tristar instrument, after evacuation of the samples at 423 K for 3 h. The Brunauer–Emmett–Teller (BET) method was applied to calculate the total surface area (SBET). High-resolution transmission electron microscopy (HRTEM), high-angle annular dark field STEM (HAADF-STEM), and elemental mapping with EDX spectroscopy were conducted on a FEI Talos microscope operated at 200 kV. Samples were prepared by dusting respective powders onto lacey-carbon coated nickel grids. The particle size distribution was assessed by counting more than 100 individual Pd nanoparticles. CO chemisorption was performed using a Micromeritics Autochem II 2920 chemisorption analyzed coupled with a MKS Cirrus 2 quadrupole mass spectrometer. The sample was pretreated in situ at 393 K under He flow (20 cm3 min–1) for 60 min, and reduced at 348 K under flowing 5 vol.% H2/N2 (20 cm3 min–1) for 30 min. Thus, 0.491 cm3 of 1 vol.% CO/He was pulsed over the catalyst bed at 308 K every 4 min. The palladium dispersion was calculated from the amount of chemisorbed CO, considering an atomic surface density of 1.26 × 1019 atoms m–2 and an adsorption stoichiometry Pd/CO = 2. Powder XRD was measured using a PANalytical X’Pert PRO-MPD diffractometer and Cu-Kα radiation (λ = 0.154 nm). The data was recorded in the 10–70° 2θ range with an angular step size of 0.017 and a counting time of 0.26 s per step. XPS was conducted with a Physical Electronics Instruments Quantum 2000 spectrometer using monochromatic Al Kα radiation generated from an electron beam operated at 15 kV and 32.3 W. The spectra were recorded under ultra-high vacuum conditions (residual pressure = 5 × 10−8 Pa) at a pass energy of 50 eV. In order to compensate for charging effects, all binding energies were referenced to the C 1 s at 288.2 eV. 13C solid-state cross-polarization/magic angle spinning nuclear magnetic resonance (CP/MAS NMR) spectra were recorded on a Bruker AVANCE III HD NMR spectrometer at a magnetic field of 16.4 T corresponding to a 1H Larmor frequency of 700.13 MHz. A 4 mm double resonance probe head at a spinning speed of 10 kHz was used for all experiments. The 13C spectra were acquired using a cross polarization experiment with a contact time of 2 ms and a recycle delay of 1 s. A total of 64 × 103 scans were added for each sample. 13C experiments used high-power 1H decoupling during acquisition using a SPINAL-64 sequence.

Catalytic testing

The hydrogenation of 2-methyl-3-butyn-2-ol (Acros Organics, 99.9%), 1-hexyne (Acros Organics, 98%), 3-hexyne (Acros Organics, 99%), 1-dodecyne (Acros Organics, 98%), 4-octyne (Acros Organics, 98%), and 1,1-diphenyl-2-propyn-1-ol (Sigma-Aldrich, 99 %) was carried out in a fully-automated flooded-bed reactor (ThalesNano H-Cube ProTM), in which the gaseous hydrogen, produced in situ by the electrolysis of Millipore water, and the liquid feed flow concurrently upward through a cartridge of approximately 3.5 mm internal diameter. The latter contains a fixed bed which is composed of the catalyst (0.10 g) well mixed with silicon carbide as diluent (0.12 g, Aldrich, 99.8%), both with particle size of 0.2–0.4 mm. The potential role of heat- and mass-transfer limitations was excluded using the Koros-Nowak diagnostic test (Supplementary Note 2). The liquid feed contained 5 wt.% of substrate, 3 wt.% of benzene (Merck, 99%) as internal standard, and toluene (Fischer Chemicals, 99.95%). The reactions were conducted at various temperatures (303–363 K) and total pressures (1–8 bar), keeping constant liquid (1 cm3 min–1) and H2 (36 cm3 min−1) flow rates. The reaction orders were obtained as a function of the gas-phase H2 pressure and the 2-methyl-3-butyn-2-ol concentration. Blank alkyne semi-hydrogenation experiments over the range of conditions investigated, excluded the competitive hydrogenation of benzene or toluene. The stability test was carried out at T = 303 K and P = 1 bar. The products were collected after 20 min of steady-state operation. The batch hydrogenation was carried out in a CEM Discover SP microwave reactor with a pressure-controlled vessel under continuous stirring. In a typical reaction, the liquid feed (1.5 cm3) was heated in the presence of the catalyst (0.01–0.02 g) at 323 K. The initial H2 pressure was 3 bar. In all cases, the products were analyzed offline using a gas chromatograph (HP-6890) equipped with a HP-5 capillary column and a flame ionization detector. The conversion (X) of the substrate was determined as the amount of reacted substrate divided by the initial amount of substrate. The reaction rate (r) was expressed as the number of moles of 2-methyl-3-buten-2-ol produced per hour and total moles of Pd. The selectivity (S) to each product was quantified as the amount of the particular product divided by the amount of reacted substrate. The carbon balance exceeded 98% in all cases, excluding the formation of oligomers. Consistently, negligible differences were observed between the thermogravimetric profiles of both the fresh and used catalyst.

Computational details

The reaction network for hydrogenation on Pd and PdxS surfaces was investigated by means of DFT calculations with periodic boundary conditions67 within the RPBE approach with a plane wave cut-off energy of 450 eV (for more details see Supplementary Method 1 and Note 4) and dispersion contributions with D2 parameters68,69 complemented with our reparametrized values for metals70. The models for the Pd3S and Pd4S surfaces were constructed with six S-Pd-S trilayers where the two topmost S-Pd-S trilayers were fully relaxed, whereas the four bottommost layers were fixed to their bulk positions. The bare Pd(111) surface was modeled as a periodically repeated p(3 × 2) slab consisting of five atomic layers, where the three at the bottom were fixed and the two on the top were fully relaxed. Due to the operation in liquid phase and the low binding energies found for the reactants, no significant deviation from the original stoichiometry is observed, which differs from gas-phase operation59. The climbing image-modified nudged elastic band (CI-NEB) method71,72 was employed to locate the transition states. To date, the solvent contributions to the evaluation of Gibbs energies is still under debate, thus, the energy profiles are presented in terms of the potential energies. The contributions of zero-point vibrational energy (Supplementary Table 6) and vibrational entropies to competing steps are similar for bifurcation steps, thus their differences are small enough to be safely neglected. The computed structures can be retrieved from the ioChem BD database73 via the link (

Data availability

The authors declare that the data supporting the findings of this study are available within the article and its Supplementary Information file. All other relevant source data are available from the corresponding author upon reasonable request.

Additional information

Publisher's note: Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.


  1. 1.

    Wilde, M. Pv vermischte mittheilungen. Ber. Dtsch. Chem. Ges. 7, 352 (1874).

  2. 2.

    Sabatier, P. & Senderens, J. B. Action of hydrogen on acetylene in presence of nickel. C. R. Chim. 128, 1173 (1899).

  3. 3.

    Borodziński, A. & Bond, G. C. Selective hydrogenation of ethyne in ethene‐rich streams on palladium catalysts. Part 1. Effect of changes to the catalyst during reaction. Catal. Rev. 48, 91–144 (2006).

  4. 4.

    Eggersdorfer, M. et al. One hundred years of vitamins - a success story of the natural sciences. Angew. Chem. Int. Ed. 51, 12960–12990 (2012).

  5. 5.

    McCue, A. J. & Anderson, J. A. Recent advances in selective acetylene hydrogenation using palladium containing catalysts. Front. Chem. Sci. Eng. 9, 142–153 (2015).

  6. 6.

    Paal, C. & Hohenegger, C. Über katalytische Wirkungen kolloidaler Metalle der Platingruppe. XII. Die stufenweise Reduktion des Acetylens. Ber. Dtsch. Chem. Ges. 48, 275–287 (1915).

  7. 7.

    Bolton, E. K. & Downing, F. B. Process of preparing butadiene. US patent 1,777,600 (1930).

  8. 8.

    Campbell, K. N. & O’Connor, M. J. The hydrogenation of substituted acetylenes with Raney nickel. J. Am. Chem. Soc. 61, 2897–2900 (1939).

  9. 9.

    Sauerwein, K. Production of ethylene from acetylene. US patent 1,860,624 (1932).

  10. 10.

    Soday, F. J. Process for refining unsatuated hydrocarbon material with an alkali or alkaline earth metal. US patent 2,413,254 (1946).

  11. 11.

    Lindlar, H. Ein neuer Katalysator für selektive Hydrierungen. Helv. Chim. Acta 35, 446–450 (1952).

  12. 12.

    Frevel, L. K. & Kressley, L. J. Selective hydrogenation of acetylene in ethylene and catalyst therefor. US patent 2,802,889 (1957).

  13. 13.

    Leeds, M. W. & Tedeschi, R. J. Process for the production of olefinic carbinols. US patent 2,989,567 (1961).

  14. 14.

    Jean, B. G. Palladium-tin catalysts. US patent 3,192,168 (1965).

  15. 15.

    Dubuis, R. & Lindlar, H. Process for selective hydrogenation. US patent 3,715,404 (1973).

  16. 16.

    Sarkany, A., Zsoldos, Z., Furlong, B., Hightower, J. W. & Guczi, L. Hydrogenation of 1-butene and 1,3-butadiene mixtures over Pd/ZnO catalysts. J. Catal. 141, 566–582 (1993).

  17. 17.

    Mastalir, Á. & Király, Z. Pd nanoparticles in hydrotalcite: mild and highly selective catalysts for alkyne semihydrogenation. J. Catal. 220, 372–381 (2003).

  18. 18.

    Choudhary, T. V., Sivadinarayana, C., Datye, A. K., Kumar, D. & Goodman, D. W. Acetylene hydrogenation on Au-based catalysts. Catal. Lett. 86, 1–8 (2003).

  19. 19.

    Bridier, B. & Pérez-Ramírez, J. Cooperative effects in ternary Cu-Ni-Fe catalysts lead to enhanced alkene selectivity in alkyne hydrogenation. J. Am. Chem. Soc. 132, 4321–4327 (2010).

  20. 20.

    Osswald, J. et al. Palladium-gallium intermetallic compounds for the selective hydrogenation of acetylene. J. Catal. 258, 210–218 (2008).

  21. 21.

    Semagina, N., Grasemann, M., Xanthopoulos, N., Renken, A. & Kiwi-Minsker, L. Structured catalyst of Pd/ZnO on sintered metal fibers for 2-methyl-3-butyn-2-ol selective hydrogenation. J. Catal. 251, 213–222 (2007).

  22. 22.

    McKenna, F.-M. & Anderson, J. A. Selectivity enhancement in acetylene hydrogenation over diphenyl sulphide-modified Pd/TiO2 catalysts. J. Catal. 281, 231–240 (2011).

  23. 23.

    Armbrüster, M. et al. Al13Fe4 as a low-cost alternative for palladium in heterogeneous hydrogenation. Nat. Mater. 11, 690–693 (2012).

  24. 24.

    Kyriakou, G. et al. Isolated metal atom geometries as a strategy for selective heterogeneous hydrogenations. Science 335, 1209–1212 (2012).

  25. 25.

    Witte, P. T. et al. BASF NanoSelect™ technology: innovative supported Pd- and Pt-based catalysts for selective hydrogenation reactions. Top. Catal. 55, 505–511 (2012).

  26. 26.

    Vilé, G., Bridier, B., Wichert, J. & Pérez-Ramírez, J. Ceria in hydrogenation catalysis: high selectivity in the conversion of alkynes to olefins. Angew. Chem. Int. Ed. 51, 8620–8623 (2012).

  27. 27.

    Vilé, G. et al. Stereo- and chemoselective character of supported CeO2 catalysts for continuous-flow three-phase alkyne hydrogenation. ChemCatChem 6, 1928–1934 (2014).

  28. 28.

    Chan, C. W. A. et al. Interstitial modification of palladium nanoparticles with boron atoms as a green catalyst for selective hydrogenation. Nat. Commun. 5, 5787 (2014).

  29. 29.

    Yang, B., Burch, R., Hardacre, C., Hu, P. & Hughes, P. Selective hydrogenation of acetylene over Pd–boron catalysts: a density functional theory study. J. Phys. Chem. C 118, 3664–3671 (2014).

  30. 30.

    Vilé, G. & Pérez-Ramírez, J. Beyond the use of modifiers in selective alkyne hydrogenation: silver and gold nanocatalysts in flow mode for sustainable alkene production. Nanoscale 6, 13476–13482 (2014).

  31. 31.

    Vilé, G. et al. A stable single-site palladium catalyst for hydrogenations. Angew. Chem. Int. Ed. 54, 11265–11269 (2015).

  32. 32.

    Chen, Z. et al. Merging single-atom-dispersed silver and carbon nitride to a joint electronic system via copolymerization with silver tricyanomethanide. ACS Nano 10, 3166–3175 (2016).

  33. 33.

    McCue, A. J., Guerrero-Ruiz, A., Rodríguez-Ramos, I. & Anderson, J. A. Palladium sulphide - a highly selective catalyst for the gas phase hydrogenation of alkynes to alkenes. J. Catal. 340, 10–16 (2016).

  34. 34.

    Tejeda-Serrano, M. et al. Synthesis of supported planar iron oxide nanoparticles and their chemo- and stereoselectivity for hydrogenation of alkynes. ACS Catal. 7, 3721–3729 (2017).

  35. 35.

    Albani, D. et al. Semihydrogenation of acetylene on indium oxide: proposed single-ensemble catalysis. Angew. Chem. Int. Ed. 56, 10755–10760 (2017).

  36. 36.

    Bridier, B., López, N. & Pérez-Ramírez, J. Molecular understanding of alkyne hydrogenation for the design of selective catalysts. Dalton. Trans. 39, 8412–8419 (2010).

  37. 37.

    Crespo-Quesada, M., Cárdenas-Lizana, F., Dessimoz, A.-L. & Kiwi-Minsker, L. Modern trends in catalyst and process design for alkyne hydrogenations. ACS Catal. 2, 1773–1786 (2012).

  38. 38.

    Studt, F. et al. Identification of non-precious metal alloy catalysts for selective hydrogenation of acetylene. Science 320, 1320–1322 (2008).

  39. 39.

    Vilé, G., Albani, D., Almora-Barrios, N., López, N. & Pérez-Ramírez, J. Advances in the design of nanostructured catalysts for selective hydrogenation. ChemCatChem 8, 21–33 (2016).

  40. 40.

    Cybulski, A., Moulijn, J. A., Sharma, M. M. & Sheldon, R. A. (eds) in Fine Chemicals Manufacture 59–124 (Elsevier Science B.V., Amsterdam, 2001).

  41. 41.

    Pollak, P. (ed.) in Fine Chemicals: The Industry and the Business, 8–25 (John Wiley & Sons, Inc., Hoboken, 2011).

  42. 42.

    García-Mota, M. et al. A density functional theory study of the ‘mythic’ Lindlar hydrogenation catalyst. Theor. Chem. Acc. 128, 663–673 (2011).

  43. 43.

    Sheldon, R. A. & van Bekkum, H. (eds) in Fine Chemicals through Heterogeneous Catalysis 351–471 (Wiley-VCH Verlag GmbH, Weinheim, 2007).

  44. 44.

    López, N. & Vargas-Fuentes, C. Promoters in the hydrogenation of alkynes in mixtures: insights from density functional theory. Chem. Commun. 48, 1379–1391 (2012).

  45. 45.

    Sankar, M. et al. Designing bimetallic catalysts for a green and sustainable future. Chem. Soc. Rev. 41, 8099–8139 (2012).

  46. 46.

    Rameshan, C. et al. In situ XPS study of methanol reforming on PdGa near-surface intermetallic phases. J. Catal. 290, 126–137 (2012).

  47. 47.

    Vilé, G., Almora-Barrios, N., Mitchell, S., López, N. & Pérez-Ramírez, J. From the Lindlar catalyst to supported ligand-modified palladium nanoparticles: selectivity patterns and accessibility constraints in the continuous-flow three-phase hydrogenation of acetylenic compounds. Chem. Eur. J. 20, 5926–5937 (2014).

  48. 48.

    García-Melchor, M., Bellarosa, L. & López, N. Unique reaction path in heterogeneous catalysis: the concerted semi-hydrogenation of propyne to propene on CeO2. ACS Catal. 4, 4015–4020 (2014).

  49. 49.

    Pinna, F. et al. Consecutive hydrogenation of benzaldehyde over Pd catalysts: influence of supports and sulfur poisoning. Appl. Catal. A 219, 195–200 (2001).

  50. 50.

    Chianelli, R. R. et al. Catalytic properties of single layers of transition metal sulfide catalytic materials. Catal. Rev. 48, 1–41 (2006).

  51. 51.

    McCue, A. J. & Anderson, J. A. Sulfur as a catalyst promoter or selectivity modifier in heterogeneous catalysis. Catal. Sci. Technol. 4, 272–294 (2014).

  52. 52.

    Hinnemann, B. et al. Biomimetic hydrogen evolution: MoS2 nanoparticles as catalyst for hydrogen evolution. J. Am. Chem. Soc. 127, 5308–5309 (2005).

  53. 53.

    Bachiller-Baeza, B. et al. Detecting the genesis of a high-performance carbon-supported Pd sulfide nanophase and its evolution in the hydrogenation of butadiene. ACS Catal. 5, 5235–5241 (2015).

  54. 54.

    McCue, A. J., Guerrero-Ruiz, A., Ramirez-Barria, C., Rodríguez-Ramos, I. & Anderson, J. A. Selective hydrogenation of mixed alkyne/alkene streams at elevated pressure over a palladium sulfide catalyst. J. Catal. 355, 40–52 (2017).

  55. 55.

    Zubkov, A., Fujino, T., Sato, N. & Yamada, K. Enthalpies of formation of the palladium sulphides. J. Chem. Thermodyn. 30, 571–581 (1998).

  56. 56.

    Xu, W. et al. Tailoring supported palladium sulfide catalysts through H2-assisted sulfidation with H2S. J. Mater. Chem. A 1, 12811–12817 (2013).

  57. 57.

    Vázquez-Zavala, A., Fuentes, S. & Pedraza, F. The influence of sulfidation on the crystalline structure of palladium, rhodium and ruthenium catalysts supported on silica. Appl. Surf. Sci. 78, 211–218 (1994).

  58. 58.

    Singh, V. V., Kumar, U., Tripathi, S. N. & Singh, A. K. Shape dependent catalytic activity of nanoflowers and nanospheres of Pd4S generated via one pot synthesis and grafted on graphene oxide for Suzuki coupling. Dalton Trans. 43, 12555–12563 (2014).

  59. 59.

    García-Mota, M., Bridier, B., Pérez-Ramírez, J. & López, N. Interplay between carbon monoxide, hydrides, and carbides in selective alkyne hydrogenation on palladium. J. Catal. 273, 92–102 (2010).

  60. 60.

    Horiuti, I. & Polanyi, M. Exchange reactions of hydrogen on metallic catalysts. Trans. Faraday Soc. 30, 1164–1172 (1934).

  61. 61.

    García-Melchor, M. & López, N. Homolytic products from heterolytic paths in H2 dissociation on metal oxides: the example of CeO2. J. Phys. Chem. C 118, 10921–10926 (2014).

  62. 62.

    Vignola, E. et al. Evaluating the risk of C–C bond formation during selective hydrogenation of acetylene on palladium. ACS Catal. 8, 1662–1671 (2018).

  63. 63.

    Coq, B. & Figueras, F. Bimetallic palladium catalysts: influence of the co-metal on the catalyst performance. J. Mol. Catal. A Chem. 173, 117–134 (2001).

  64. 64.

    Wowsnick, G. et al. Surface dynamics of the intermetallic catalyst Pd2Ga, Part II - Reactivity and stability in liquid-phase hydrogenation of phenylacetylene. J. Catal. 309, 221–230 (2014).

  65. 65.

    Yang, B., Burch, R., Hardacre, C., Headdock, G. & Hu, P. Origin of the increase of activity and selectivity of nickel doped by Au, Ag, and Cu for acetylene hydrogenation. ACS Catal. 2, 1027–1032 (2012).

  66. 66.

    Hammer, B. & Nørskov, J. K. Why gold is the noblest of all the metals. Nature 376, 238–240 (2009).

  67. 67.

    Makov, G. & Payne, M. C. Periodic boundary conditions in ab initio calculations. Phys. Rev. B 51, 4014–4022 (1995).

  68. 68.

    Grimme, S. Semiempirical GGA-type density functional constructed with a long-range dispersion correction. J. Comput. Chem. 27, 1787–1799 (2006).

  69. 69.

    Bučko, T., Hafner, J., Lebègue, S. & Ángyán, J. G. Improved description of the structure of molecular and layered crystals: ab initio DFT calculations with van der Waals corrections. J. Phys. Chem. A 114, 11814–11824 (2010).

  70. 70.

    Almora-Barrios, N., Carchini, G., Błoński, P. & López, N. Costless derivation of dispersion coefficients for metal surfaces. J. Chem. Theory Comput. 10, 5002–5009 (2014).

  71. 71.

    Henkelman, G., Uberuaga, B. P. & Jónsson, H. A climbing image nudged elastic band method for finding saddle points and minimum energy paths. J. Chem. Phys. 113, 9901–9904 (2000).

  72. 72.

    Henkelman, G. & Jónsson, H. Improved tangent estimate in the nudged elastic band method for finding minimum energy paths and saddle points. J. Chem. Phys. 113, 9978–9985 (2000).

  73. 73.

    Álvarez-Moreno, M. et al. Managing the computational chemistry big data problem: the ioChem-BD platform. J. Chem. Inf. Model. 55, 99–103 (2015).

Download references


Financial support from ETH Zurich, the Swiss National Science Foundation (Grant No. 200021-169679), and MINECO (grant number CTQ2015-68770-R). The Barcelona Supercomputing Centre (BSC-RES) and ScopeM of ETH Zurich are thanked for access to their facilities. Dr René Verel is thanked for help with the MAS NMR measurements. M.S. thanks the COFUND program and MINECO for support through Severo Ochoa Excellence Accreditation 2014-2018 (SEV-2013-0319).

Author information

Author notes

  1. These authors contributed equally: Davide Albani, Masoud Shahrokhi.


  1. Institute for Chemical and Bioengineering, Department of Chemistry and Applied Biosciences, ETH Zürich, Vladimir-Prelog-Weg 1, 8093, Zürich, Switzerland

    • Davide Albani
    • , Zupeng Chen
    • , Sharon Mitchell
    •  & Javier Pérez-Ramírez
  2. Institute of Chemical Research of Catalonia (ICIQ), and The Barcelona Institute of Technology Av., Països Catalans 16, 43007, Tarragona, Spain

    • Masoud Shahrokhi
    •  & Núria López
  3. EMPA, Swiss Federal Laboratories for Materials Science and Technology, Uberlandstrasse129, 8600, Dübendorf, Switzerland

    • Roland Hauert


  1. Search for Davide Albani in:

  2. Search for Masoud Shahrokhi in:

  3. Search for Zupeng Chen in:

  4. Search for Sharon Mitchell in:

  5. Search for Roland Hauert in:

  6. Search for Núria López in:

  7. Search for Javier Pérez-Ramírez in:


J.P.-R. and N.L. conceived and coordinated all stages of this research. D.A. and Z.C. prepared and characterized the samples. D.A. performed the catalytic tests. S.M. acquired the microscopy images. R.H. undertook the XPS analyses. M.S. conducted the DFT simulations. All authors contributed to writing the manuscript.

Competing interests

The authors declare no competing interests.

Corresponding authors

Correspondence to Núria López or Javier Pérez-Ramírez.

Electronic supplementary material

About this article

Publication history






By submitting a comment you agree to abide by our Terms and Community Guidelines. If you find something abusive or that does not comply with our terms or guidelines please flag it as inappropriate.