Facile C-C bond formation is essential to the formation of long hydrocarbon chains in Fischer-Tropsch synthesis. Various chain growth mechanisms have been proposed previously, but spectroscopic identification of surface intermediates involved in C-C bond formation is scarce. We here show that the high CO coverage typical of Fischer-Tropsch synthesis affects the reaction pathways of C2Hx adsorbates on a Co(0001) model catalyst and promote C-C bond formation. In-situ high resolution x-ray photoelectron spectroscopy shows that a high CO coverage promotes transformation of C2Hx adsorbates into the ethylidyne form, which subsequently dimerizes to 2-butyne. The observed reaction sequence provides a mechanistic explanation for CO-induced ethylene dimerization on supported cobalt catalysts. For Fischer-Tropsch synthesis we propose that C-C bond formation on the close-packed terraces of a cobalt nanoparticle occurs via methylidyne (CH) insertion into long chain alkylidyne intermediates, the latter being stabilized by the high surface coverage under reaction conditions.
Supported cobalt catalysts find their most widespread application in low-temperature Fischer–Tropsch synthesis (FTS), a process in which C-C bond-forming reactions produce long-chain hydrocarbon products from synthesis gas, a mixture of CO and H21. In today’s fossil fuel-based economy, synthesis gas is predominantly manufactured from natural gas or coal, where FTS adds value by converting gaseous (gas-to-liquids) or solid (coal-to-liquids) reactants into more valuable products, such as food-grade wax, lubricants and sulfur-free transportation fuels. The FTS process will continue to play a role in future energy scenarios: synthesis gas can be derived from any carbon-containing source, e.g. biomass or even CO2 may be used2. These renewable carbon sources offer an alternative route to produce a ‘syncrude’ that can, to a large part, replace petroleum as the principal feedstock of chemicals and the liquid fuels that power transportation modes (airplanes, ships, heavy vehicles) that cannot be readily replaced by fully electric alternatives. Insight into the molecular mechanism by which long-chain hydrocarbon species grow on the surface of the cobalt catalyst particle is of direct relevance to better understand the molecular origin of selectivity in FTS and may ultimately drive rational design of catalysts.
A large variety of chain growth mechanisms can be found in the literature, summarized in, e.g. refs. 3,4,5. Growth intermediates of different chain length co-exist on the active surface, and steady-state isotopic transient kinetic analysis studies reveal that their concentration is low6,7. Furthermore, they are surrounded by much larger quantities of co-adsorbates such as C1Hxad species8,9,10, COad7,9,10, Had10 and long-chain products11. This complexity makes it impossible to distinguish those few active surface species from other adsorbates by, e.g. in situ infrared (IR) absorption spectroscopy12. We instead use a model approach to study CxHy reactivity on a cobalt catalyst under conditions relevant to FTS. As shown hereafter, it is important to study how co-adsorbed Had and CO affect CxHy reactivity, since both adsorbates will be present on the surface under reaction conditions.
Water is a major by-product of FTS, and the high conversion levels reached lead to a water partial pressure that amounts to several bars during industrial operation. However, since chain growth also occurs under low conversion conditions where the H2O partial pressure is low, the presence of H2O does not appear to be essential to the chain growth mechanism and therefore it was omitted from our study. Moreover, surface science studies show that water adsorbs much weaker on Co(0001) than on both CO and hydrogen13 and the H2O surface coverage under reaction conditions is expected to be low even when the H2O partial pressure is comparable to that of CO and H2. An in situ X-ray absorption study of cobalt supported on a carbon nanofiber support shows that neither bulk oxidation nor substantial surface oxidation occurs on cobalt during FTS14. Furthermore, cobalt single crystals were found to be active for FTS11,15,16,17,18, and the turnover frequencies reported are similar to those found for supported catalysts. This confirms that metallic cobalt is the active phase for chain growth and that insights from single crystal studies are of direct relevance for fundamental understanding of FTS.
We here use a Co(0001) model catalyst to study how C2Hxad species react to form a new C-C bond under FTS-like conditions, that is, in the presence of co-adsorbed hydrogen and COad. Using this approach, we find that C-C bond formation is promoted by CO spectators, which stabilize the alkylidyne intermediate needed for this reaction. This finding can rationalize why CO promotes alkene dimerization on cobalt catalysts and reveals the hidden role of CO as promoter of chain growth during FTS on supported cobalt catalysts.
C2H4 decomposition on Co(0001)
Synchrotron-based high-resolution X-ray photoemission spectroscopy (XPS) was used as the primary tool to determine both nature and concentration of the CxHy surface intermediates that form at various stages in our experiments. The C1s binding energy is sensitive to both chemical nature and binding site of the carbon atom, and excitation of the C-H stretch vibration along with the photoemission process gives rise to additional features at +350–400 meV (2800–3200 cm−1) from the main photoemission peak19,20, with an intensity that is proportional to the number of hydrogen atoms attached to the carbon atom that is photo-ionized19,20.
Figure 1a shows high-resolution C1s spectra of the different surface intermediates that form during heating of an ethylene-saturated surface in vacuum, previously discussed in detail elsewhere21. The two peaks at 283.9 and 283.4 eV in the spectrum at 100 K are attributed to the two carbon atoms of ethylene21,22. The changes seen around 180 K in the heat map of C1s spectra recorded during heating (Fig. 1b) are attributed to a combination of ethylene desorption and decomposition, the latter producing 0.12 monolayer (ML) acetylene (C2H2ad) + 0.24 ML Had. The C1s spectrum of adsorbed acetylene shows a peak at 283.3 eV, which accounts for both carbon atoms and is accompanied by two small shoulders at +0.37 and +0.74 eV due excitation (double excitation) of the C-H stretching vibration21,22,23. Acetylene remains stable up to 400 K where it dehydrogenates completely (see H2 desorption data reported below). Atomic carbon is the only adsorbate present after heating to 630 K, as evident from the C1s peak at 282.8 eV24.
The influence of CO spectators on C2Hx reactivity
The mixed C2H2ad/Had layer produced by heating the ethylene-covered surface to 220 K was chosen as the starting point to investigate how CO spectators affect C2Hxad reactivity. A top view of the C1s spectra (Fig. 1c) shows that acetylene gets converted around 270 K when heated in the presence of 1 × 10−7 mbar CO. A second reaction step is seen around 310 K, while extensive dehydrogenation occurs above 350 K to produce a mixture of ‘polymeric’24 (284.4 eV) and atomic carbon (282.7 eV) at 630 K. This is different from the carbon layer found after heating in vacuum, which consisted exclusively of atomic carbon (Fig. 1a and Supplementary Note 1).
High-resolution C1s spectra reveal the identity of the intermediates formed at each stage. Figure 1d only shows the spectral features due to the dominant product to simplify the discussion, while a detailed discussion of the as-measured spectra is provided in Supplementary Note 2. The spectrum recorded after heating to 200 K shows the spectral shape of acetylene, and co-adsorption of CO causes only a slight broadening of the acetylene peak. We find that up to 0.30 ML CO can adsorb alongside the 0.12 ML acetylene (and 0.24 ML Had), with 0.14 ML COad residing on top sites (285.7 eV25) and 0.16 ML in threefold hollow sites (285.3 eV25).
Acetylene gets converted to ethylidyne between 220 and 270 K, as evident from two new peaks at 282.9 and 283.5 eV after heating to 285 K. The peak at 282.9 eV does not show any loss features related to the presence of C-H bonds, in line with the assignment to the surface-bound carbon atom of ethylidyne (≡C-CH3)21,26. The three hydrogen atoms in the methyl group of ethylidyne give rise to prominent vibrational signals at +0.4 and +0.8 eV relative to the main peak at 283.5 eV. The C1s binding energy of the methyl group is 0.5 eV lower than the typical value reported for methyl groups in a variety of other CxHyad adsorbates19,21,27. This can be attributed to the presence of COad: a similar downward shift of the methyl group binding energy of ethylidyne adsorbed on Rh(111) upon co-adsorption of CO was reported previously26, and our reference experiment (Supplementary Note 3) showed that co-adsorption of CO alongside adsorbed propyne causes a CO coverage-dependent shift of the methyl (H3C-C≡CH) binding energy, from 284 eV down to 283.5 eV for the highest CO coverage. The CO coverage at this point is 0.30 ML but now with 0.18 ML CO adsorbed on-top and 0.12 ML in hollow sites.
Two ethylidyne adsorbates couple around 310 K to form a 2-butyne product. This proposition is confirmed by the high-resolution spectrum recorded after heating to 335 K, which closely resembles the previously reported high-resolution spectrum of 2-butyne adsorbed on Ni(111)28. The CO coverage has dropped to 0.21 ML, and only the top sites are populated at this point. Reference experiments using propyne (Supplementary Note 3)21 show that COtop has only a minor influence on the methyl binding energy, and both methyl groups in 2-butyne, H3C-C≡C-CH3, therefore appear at 284.1 eV, the typical value for -CH319,21,27. The 283.4 eV peak is attributed to the two central carbon atoms of adsorbed 2-butyne, H3C-C≡C-CH3. Their binding energy value is identical to that of the central carbon atom of adsorbed propyne H3C-C≡CH, which is unsurprising since the adsorption site and immediate surroundings of the central carbon atoms in adsorbed propyne and 2-butyne are practically identical.
These results thus show that CO spectators cause acetylene to react with surface hydrogen to produce ethylidyne around 270 K. Two ethylidyne products subsequently couple around 310 K to produce adsorbed 2-butyne. Other experimental techniques corroborate these conclusions and reveal additional details. Temperature-programmed reaction spectroscopy (TRPS; Fig. 2a) shows that ~0.08 ML ethylene desorbs intact during heating of the ethylene-saturated surface in vacuum. Hydrogen desorbs in two steps, with a peak at 320 K due to recombination of the 0.24 ML Had produced by ethylene decomposition to acetylene and another peak around 400 K, which amounts to 0.24 ML H2 and is attributed to complete dehydrogenation of acetylene21,29. The presence of CO strongly affects the H2 TPRS trace as shown in Fig. 2b. The peak around 270 K is attributed to desorption of surface-bound hydrogen, shifted downward due to the presence of CO30,31,32. The peak area indicates that 0.12 ML Had desorbs around 270 K, only 50% of the 0.24 ML Had that was present prior to CO exposure. This is explained by acetylene hydrogenation to ethylidyne (HC≡CH + Had → ≡C-CH3), a reaction that consumes one Had for each acetylene adsorbate converted. The H2 desorption trace above 320 K has a close similarity to that of a reference experiment in which 0.05 ML 2-butyne was heated in the presence of CO. This supports the conclusion that adsorbed 2-butyne is produced by subsequent ethylidyne coupling (Supplementary Note 4). We attribute the pronounced peak at 370 K to dehydrogenation of the two methyl groups in 2-butyne21. The remaining hydrogen gradually leaves the surface between 380 and 600 K, characteristic of dehydrogenation of ‘polymeric’ surface carbon, the formation of which was also evident from XPS. The small H2 desorption peak around 320 K is attributed to a minor quantity of ethylidyne that did not find a coupling partner and instead dehydrogenate back to acetylene.
Figure 3a shows the top view of a series of reflection absorption infrared spectra (RAIRS), recorded during heating of an C2H2ad/2 Had-covered surface in CO. Individual high-quality spectra at the temperatures indicated are shown in Fig. 3b. The strong bands around 2000 and 1840 cm−1 are due to COtop and COhollow, respectively25. CO adsorbed alongside small CxHy adsorbates attenuates absorption bands in the C-H (~2800–3000 cm−1) and C-C (1000–1200 cm−1) stretching regions, a phenomenon that has been observed before for ethylidyne adsorbed alongside CO on, e.g. Ru(0001) and Pt(111)32,33,34. This leaves only the C-H bending region (1500–1300 cm−1) as our main source of information. The 1352 cm−1 band, which appears around 220 K and disappears again around 300 K, can be readily assigned to the symmetric bending mode (δs-CH3) of ethylidyne35. The band at 1767 cm−1 that appears and disappears together with the 1352 cm−1 band has been reported previously for COhollow co-adsorbed with ethylidyne on both Rh(111) and Ru(0001)34,36.
The ethylidyne product forms an ordered adsorbate overlayer together with CO, as evident from the c(4 × 2) diffraction pattern that was found between 270 and 305 K by low-energy electron diffraction (LEED) (Fig. 3c). The ordered ethylidyne/COhollow overlayer that causes this pattern is known from earlier studies on Rh(111)26,36. The local ethylidyne coverage in the c(4 × 2) structure is 0.25 ML. However, the overall C2Hxad coverage in our experiment is only 0.12 ML. This means that the c(4 × 2) pattern is caused by islands of ethylidyne/COhollow that cover only 40–50% of the surface, leaving the other half covered by a disordered layer, which contains CO as well as minor quantities of unreacted acetylene and Had. A more detailed analysis of this structure is provided in Supplementary Note 5. The c(4 × 2) pattern disappears above 300 K, and the IR absorption spectrum after heating to 335 K shows a weak band at 1365 cm−1. This is attributed to the δs-CH3 mode of adsorbed 2-butyne, an assignment that is supported by reference spectra using 2-butyne (Supplementary Note 4).
XPS at near-ambient pressure (NAP)
The reactivity of acetylene under high-coverage conditions was further explored using the HIPPIE beamline of MAX IV, which allows XPS measurements at near-ambient pressures. Figure 4 shows a series of C1s spectra recorded during an isothermal experiment at 313 K in which a 0.08 ML acetylene-covered Co(0001) surface (prepared by dosing ethylene at 313 K) was exposed to an increasingly high H2 pressure. A H2 pressure of ~10−5 mbar would be sufficient to create a high hydrogen coverage at 313 K31,37, but the spectrum shape shows that co-adsorbed hydrogen did not cause the acetylene to react.
A CO contamination in the gas led to the appearance of COad when the hydrogen pressure was increased to 1 × 10−2 mbar. The appearance of COad coincides with the conversion of acetylene to ethylidyne, the temporary formation of the latter being evident from the transient peaks at 282.9 and 283.8 eV. The COhollow peak (285.2 eV) comes and goes together with the ethylidyne-related peaks, consistent with the RAIRS results which show that COhollow is associated with ethylidyne. Ethylidyne reacts further to produce 2-butyne, evident from a peak at 283.4 eV due to the two central carbon atoms and at 284.1 eV due to the two methyl groups. Acetylene conversion reached completion after 400 s in 1 × 10−2 mbar H2, and a pressure increase to 1 × 10−1 mbar H2 did not affect 2-butyne at all. Interestingly, this pressure increase triggers the desorption of COad. We attribute this to the same repulsive interactions that cause the decreased H2 desorption temperature when Had is heated in CO (Fig. 2b). With an overwhelming majority of hydrogen in the NAP experiment, Had-induced destabilization of COad causes it to desorb at 313 K, significantly below its ‘normal’ desorption temperature of 350–400 K25.
The invariance of the C1s spectral shape during subsequent heating in 1 × 10−1 mbar H2 (Fig. 5) indicates that 2-butyne remains intact during heating. The decrease of the signal intensity >370 K is attributed to loss of 2-butyne from the surface. Since computed alkyne adsorption energies are in excess of 200 kJ mol−1, the possibility that 2-butyne simply desorbs can be excluded38. We instead propose that 2-butyne is hydrogenated to 2-butene, which desorbs upon formation. A simple kinetic analysis (Supplementary Note 6) yields an apparent activation energy of 106 ± 12 kJ mol−1 for 2-butyne hydrogenation.
The results presented here provide uniquely detailed information on the mechanism by which C-C bonds are formed between two CxHy species adsorbed on a Co(0001) model catalyst in the presence of co-adsorbed CO and Had. After discussing the barriers for ethylidyne formation and ethylidyne dimerization and the possible origins of the driving force of these reactions, we continue with a discussion of how these findings relate to C-C bond formation reactions catalysed by metallic cobalt in the presence of CO.
Quantitative analysis of the TP-XPS data (Supplementary Note 5) yields the coverage of all C-containing adsorbates during the CO-induced reaction while θH can be deduced from the H2 desorption trace. Figure 6 shows the adsorbate coverages together with the output of a simple mean field microkinetic model (Supplementary Note 6) used to estimate reaction barriers for acetylene hydrogenation and ethylidyne dimerization. The conversion of acetylene to ethylidyne requires the addition of two hydrogen atoms to one end of the molecule and abstraction of a hydrogen atom from the other end. Our analysis yields an overall barrier height of only 60 ± 6 kJ mol−1, far below the computed barriers >100 kJ mol−1 as predicted by density functional theory starting with either acetylene hydrogenation or acetylene dehydrogenation as a first step39,40,41. This indicates that the high CO coverage may also lower the reaction barriers involved in the conversion of acetylene.
Acetylene is the most stable C2Hx adsorbate in the absence of CO21,38,39,40,41, and it is therefore the sole product of ethene decomposition around 180 K. The experiments show that CO causes conversion of acetylene to ethylidyne, and the driving force for this must be that ethylidyne becomes more stable than acetylene when CO is present on the surface32,40. Two experimental observations give more insight into why ethylidyne is preferred when CO is present: (i) repulsive interactions between Had and COad destabilize Had (Fig. 2b), thereby destabilizing one of the reactants. (ii) The formation of ordered COhollow/ethylidyne layer islands with a local high coverage is driven by attractive interactions, indicating that the ethylidyne reaction product is stabilized by COad (Fig. 3c). Mate et al.42 attributed the ordering of mixed ethylidyne/CO layers on Rh(111) to favourable dipole–dipole interactions due to the oppositely oriented dipoles of CO and ethylidyne. A third contributing factor is that a high surface coverage favours species that occupy less space on the surface21. This makes acetylene hydrogenation to ethylidyne favourable, first because it incorporates a surface hydrogen into the CxHy adsorbate, and second, the footprint of ethylidyne is expected to be lower than that of acetylene since the former adsorbs through only one carbon atom.
Earlier studies have shown that methylidyne dimerizes around 250 K on both Ni(111) and Co(0001) to form acetylene31,43,44. We here show that ethylidyne, the methyl-substituted analogue of methylidyne, reacts in a similar way to produce 2-butyne. We attribute the comparatively higher temperature (310 vs 250 K) to increased steric hindrance in the transition state for coupling when hydrogen is replaced by a bulky methyl group. Ethylidyne reactivity in the absence of CO was studied by intentionally maximizing beam-induced ethylene decomposition (Supplementary Note 7). Instead of dimerization, we find that ethylidyne dehydrogenates to acetylene around 280 K during heating in vacuum21. Since dimerization of CHad does not require CO to be present, we propose that COad is not needed for the C-C bond formation reaction itself. Instead, CO facilitates the C-C bond-forming reaction indirectly: it stabilizes ethylidyne so that it still exists at 310 K in our temperature-programmed experiment, the temperature required to overcome the barrier of 75 ± 7 kJ mol−1 associated with ethylidyne dimerization.
The work of Eidus et al.45 shows that traces of CO during ethylene hydrogenation on a supported cobalt catalyst changes the product selectivity, from ethane to C4 products. Cant et al.46 reproduced these early studies and reported cis-2-butene as the main C4 product of ethylene hydrogenation at 393 K in presence of CO. CO-induced stabilization of ethylidyne is key to understand why CO promotes ethylene dimerization on cobalt. Figure 7 shows the proposed catalytic cycle for this reaction, with activation energies derived from direct observation of the respective reactions on our single-crystal model catalyst. Ethylene decomposition initially produces acetylene, which is quickly hydrogenated to ethylidyne under the influence of CO spectators. Alternatively, a more direct pathway may exist from ethylene to ethylidyne: our previous work shows that ethylidyne can also form directly as a minor product of ethylene decomposition around 180 K, but only when the surface is highly covered by CxHyad and/or Had21. The C-C bond is then formed via coupling of two ethylidynes. Hydrogenation of the alkyne coupling product is the slowest step, and the 2-butyne concentration under reaction conditions is therefore expected to be rather high. This facilitates the formation of carbonaceous deposits via side reactions such as 2-butyne dehydrogenation and alkyne cyclo-trimerization38,47, and explains the fast catalyst deactivation which was attributed to carbon deposition by Cant et al.46.
The surface composition during CO-promoted ethylene dimerization is similar to the situation during FTS, as in both cases hydrocarbon surface intermediates react to form new C-C bonds on a cobalt surface covered with CO and surface hydrogen. For FTS, Bezemer et al.14 report a CO turnover frequency of only 2.3 × 10−2 s−1 for their most active cobalt catalyst (tested at 483 K and 35 bar). This translates to a production rate of only 40 monomers per second on each cobalt crystallite (hemispherical, average diameter 8.5 nm). So even in the unlikely case that all monomers insert into a single chain, it still takes ~0.25 s to grow a one C10 product molecule per particle (C10 being the average chain length when α = 0.94). Such slow growth on the second time scale can only involve very stable growth intermediates that have difficulty leaving the surface. Our work shows that alkynes and alkylidynes are indeed very stable, and the NAP-XPS experiment (Fig. 5) confirms that alkyne hydrogenation is a slow reaction that only proceeds at a significant rate above 370 K. Their high stability and long lifetimes thus make alkynes and alkylidynes feasible intermediates for chain growth under FTS conditions.
Our experiments moreover show that CO spectators stabilize alkylidyne over all other forms of CxHyad and that alkylidynes are highly reactive in C-C bond-forming reactions. These findings provide compelling support for the previously proposed alkylidyne chain growth mechanism4,38, schematically depicted in Fig. 8. New chains are initiated by coupling of two methylidyne (CH) monomers, the most stable form of CHxad, both without31,48,49 and with CO co-adsorbed41. Subsequent, CO-promoted hydrogenation of acetylene produces the ethylidyne needed for further growth. With the C1Hx concentration being much higher than that of growing chains under FTS conditions6,8, methylidyne insertion (producing adsorbed propyne) prevails over coupling with ethylidyne that we find in our model experiments. In analogy to the acetylene–ethylidyne reaction, CO also promotes conversion of the propyne coupling product to the propylidyne form32 needed for further growth. Chain termination requires hydrogenation and is comparatively slow, as illustrated by the difficulty to hydrogenate 2-butyne in our experiments. The mechanism observed in our experiments is of the carbide type, and although CO is promoting chain growth by stabilizing the intermediates in the correct form, it does not participate in the C-C bond-forming reaction. A detailed analysis of the O1s spectra provided in Supplementary Note 8 shows that the formation of oxygen-containing intermediates during the experiments can be excluded.
The experimentally observed surface reactions presented here show that C-C bond formation via alkylidyne coupling is favourable on the close-packed terraces that constitute ~60% of the surface of an (fcc-)Co nanoparticle4,41. The methylidyne monomers required for chain growth during FTS can either be supplied via H-assisted routes on the terrace or via spill-over from adjacent step sites that are active for CO dissociation18,50 and surround the nm-sized close-packed terrace exposed by an fcc-Co nanoparticle4. An fcc-Co nanoparticle also exposes (100) facets as well as step and kink sites51, and the role of the different structural elements remains a topic of debate52. Given that our experiments only speak about CxHy reactivity on close-packed terraces, we can only provide a qualitative consideration about chain growth on other sites. Since the relative stabilities of CxHy adsorbates depends on the surface structure, chain growth may proceed via a different pathway on other parts of the catalyst surface. In fact, experiments on stepped Ni(111) show that step sites favour C-C bond scission rather than C-C bond formation53,54, and C-C bond scission was reported on Ni(100) at temperatures below 300 K55. This is in line with computational work on cobalt, which shows that 2 C1Hx adsorbates are more stable than C2Hx adsorbates on both Co(100) and stepped Co(211), while acetylene and ethylidyne are instead significantly more stable than 2 CH species on Co(111)41. In other words, C-C bond scission is favoured on steps and (100) facets, whereas C-C bond formation is favoured on terrace sites. This means that growth of long chains at step edges can only occur when exothermic C-C bond breaking is strongly suppressed, e.g. by a local high coverage at the step site. The concentration of carbon is indeed expected to be high on step sites due to their high affinity for carbon41,56. Chain growth requires growing chains to physically meet with a monomer, and since the growing chain concentration is expected to be small6, the nearest monomer is most probably generated at some distance from the growth intermediate. A high local coverage at step edges poses a significant barrier for CxHy diffusion along the one-dimensional step edge, making it difficult for a monomer to reach a growing chain that is located a few sites away. Thus, owing to the limited mobility along the highly covered step sites, only those monomers formed at a small ensemble of step sites will contribute to a single chain, whereas monomers produced at step sites far away may not be able to reach the growing chain and make methane instead. Instead, spill-over of monomers to the adjacent (two-dimensional) terrace circumvents blockages of strongly adsorbed species at step sites so that monomers and growing chains can more easily diffuse over a larger distance and monomers produced by different active sites located at the edges of a single terrace can all be incorporated into the same product chain.
In summary, our detailed investigation of the reactivity of C2Hxad species on Co(0001), both at low and near-ambient reactant pressures, reveals that a high coverage of COad spectators profoundly influences the reactivity of hydrocarbon adsorbates. CO-induced hydrogenation of adsorbed acetylene-producing ethylidyne (≡C-CH3) is a facile reaction that occurs around 270 K. The driving force for the reaction is provided by a combination of CO-induced destabilization of the Had reactant and stabilization of the ethylidyne product. Formation of 2-butyne (H3C-C≡C-CH3) occurs around 310 K via ethylidyne dimerization and highlights the high reactivity of alkylidynes (≡C-CH2R) for C-C bond formation on the close-packed surface of cobalt. The finding that COad stabilizes CxHyad adsorbates in the alkylidyne form, which readily forms a new C-C bond with other alkylidynes, rationalizes why CO promotes ethylene dimerization on cobalt catalysts. For FTS, we propose that C-C bonds form on the close-packed facets via coupling of a long-chain alkylidyne with a methylidyne monomer to form a 1-alkyne adsorbate. CO spectators promote chain growth by stabilizing the growing chain in the alkylidyne form needed for C-C bond formation. NAP-XPS shows that 2-butyne hydrogenation is slow. This suggest that the alkyne and alkylidyne adsorbates terminate only slowly, an essential requirement for the growth of long chains5.
Sample description and sample cleaning
The disc-shaped (d = 8 mm) Co(0001) single crystal (Surface Preparation Laboratory) was cleaned by cycles of ~10 min sputtering (1 kV Ar+) at 650 K followed by ~10 min annealing at the same temperature21,32. Residual carbon was most efficiently removed by dosing ~1 × 10−7 mbar O2 at 650 K for a few minutes. The excess surface oxygen can be removed by a short sputtering step or by exposure to H2 (10−6−10−5 mbar) at 650 K. In this way, the carbon concentration could be reduced to below the sensitivity of synchrotron XPS.
Synchrotron XPS at ultra-high vacuum (UHV) condition
The synchrotron XPS measurements under UHV conditions reported here were performed at the SuperESCA beamline of ELETTRA, the European synchrotron light source located in Trieste, Italy57. For these experiments, the sample was spotwelded to a Ta rod, which was in direct thermal contact with a liquid nitrogen reservoir such that a sample temperature of 80 K could be reached. The sample was heated by the radiation of three tungsten filaments located close to its backside. Sample temperatures were measured using a K-type thermocouple, spotwelded to the side of the sample. Binding energies are reported relative to the Fermi edge, which was remeasured after each change of the photon energy. CO (SIAD, 99.95%), propene (Messer, 99.5%) and ethylene (SIAD, 99.995%) were used without further purification during the experiments at the SuperESCA beamline. XPS did not show any indication of contaminations introduced by dosing these gases. The ordered layer formed by CO after adsorption at room temperature, with a coverage of 0.33 ML and a (√3 × √3)R30° in LEED, was used as a reference point for both C1s and O1s quantification21,25. C1s and O1s spectra were recorded with 800 and 1100 eV for this known structure, where the higher photon energies were chosen to minimize the impact of photoelectron diffraction effects (Supplementary Note 2) on the signal intensity. The concentration of CxHy species derived from XPS was found to be in good agreement with the values derived from TPRS, as discussed hereafter.
Synchrotron XPS at near-ambient conditions
The NAP XPS measurements were performed at the HIPPIE beamline of MAX IV, Lund, Sweden. The system consists of multiple chambers separated by gate valves. For the results presented here, only the preparation chamber, the transfer chamber (both with a base pressure of ~5 × 10−10 mbar) and the analysis chamber (base pressure ~5 × 10−9 mbar) were used. Several sputter–anneal cycles (1 keV Ar+) at 650 K combined with oxygen treatments (pO2 ~ 1 × 10−7 mbar, 5 min at 650 K) were performed in the preparation chamber, where the sample can be heated by radiative or e-beam heating using a W filament in close proximity to the backside of the sample plate. Sample heating in the analysis chamber is performed by irradiating the backside of the sample plate with a fibre-coupled infrared laser. After transfer to the analysis chamber (via the transfer chamber), the sample cleanliness was checked at a sample temperature of 650 K. Residual carbon was removed by dosing O2 (p ≤ 1 × 10−7 mbar) at 650 K until the C1s region showed a carbon-free surface. Excess Oad was then removed by dosing H2 (p ≤ 1 × 10−5 mbar) at 650 K. Both UHV and NAP XPS can be performed in the analysis chamber. During measurements, the sample surface is ~0.3 mm away from the entrance of the differentially pumped Scienta HIPP3 electron energy analyser. After preparation in UHV conditions, the NAP cell, with a volume of ~500 mL, can be closed and local pressures up to 30 mbar can be introduced while the pressure in the main chamber remains <5 × 10−5 mbar.
Two stainless steel strips were used to clamp the sample onto a stainless steel flag-style sample holder. The sample temperature was measured using a K-type thermocouple, spotwelded to the sample plate below the Co(0001) sample. A photon energy of 420 eV was used to record C1s spectra during H2 exposure and heating in H2. Owing to the extremely high photon flux generated by MAX IV, acquisition of a single C1s spectrum, in the presence of H2 (g), takes around 30 s. Spectra recorded with 800 eV of a CO-covered surface serve as a quantitative reference to determine the coverages of CxHy and COad.
Ethylene (AGA, 99.95) and O2 (AGA, 99.999%) were only dosed at UHV pressures and used without further purification. The H2 (AGA 99.998%) first passed over a Pall GLPSIPVMM4 filter followed by a cold trap held at liquid nitrogen temperature prior to entering the NAP cell via a mass flow controller (MKS GF120). The experiments described in the main text reveal a small contamination with CO. This could be due to a residual contamination in the gas or instead from (H2-induced) desorption from the walls of the gas dosing system or those of the vacuum chamber. A trace amount of sulfur was detected by XPS after prolonged exposure to H2.
TPRS, LEED and RAIRS in UHV
The TPRS, LEED and RAIRS experiments were performed in a separate UHV set-up with a base pressure of ~5 × 10−10 mbar. Here the sample was clamped between the two legs of a 0.5-mm-thick U-shaped tungsten wire that is in thermal contact with a liquid nitrogen reservoir so that a sample temperature of ~95 K can be reached. The sample was heated by passing a direct current through the W support wire, and the temperature was measured using a K-type thermocouple, spotwelded to the backside of the sample. During the TPRS experiments, the sample is placed ~5 mm away from the 5-mm-wide aperture of the (separately pumped) mass spectrometer compartment. This arrangement effectively eliminates peaks due desorption from other parts of the sample holder during heating. The known 0.5 ML Had-covered surface30,37,58 was used to determine the quantity of H2 produced during CxHy decomposition. Using the known C/H ratio in the precursor molecule, this can be translated to ML coverages of CxHy. A mass balance was used to quantify molecular desorption of ethene: H2 desorption shows that 0.12 ML decomposes during heating in vacuum. Decomposition is suppressed down to 0.02 ML when the same C2H4 layer is heated in CO. The difference between C2H4 desorption in vacuum and in CO must therefore be equal to 0.1 ML, and with this reference point other coverages could be determined.
Infrared absorption spectra were recorded using a Perkin Elmer Frontier spectrometer. After leaving the spectrometer, the (p-polarized) light travels through a compartment with custom-made optics that focus the beam onto the 8 mm disc-shaped sample. The light enters the vacuum chamber through a KBr window and is reflected off the sample surface. The angle of incidence is 15° with respect to the surface plane. After reflection, the light leaves the vacuum chamber through another KBr window after which it is focused onto a liquid nitrogen-cooled MCT detector. All parts of the beam path that are at atmospheric pressure are flushed with dry N2 to eliminate signals from CO2 (g) and H2O (g) from the spectra. The spectrum obtained by reflection from a clean Co(0001) sample was subtracted from all spectra shown here, and in addition to this, a spline background was used to eliminate changes of the background resulting from sample heating. All spectra were measured with a resolution of 4 cm−1 and a step size of 0.5 cm−1. Thirty scans were averaged for each point in the TP-RAIRS experiments (Fig. 3a). The high-quality spectra shown in Fig. 3b are the result of averaging 512 individual scans, recorded at 95 K to minimize thermal broadening. By removing the CO pressure at the annealing temperature ensures that the CO coverage and site occupation for the high-quality spectra is identical to the coverage at the annealing temperature. We found that the intensity of the absorption peak due to the symmetric C-H bending mode of -CH3 in adsorbed 2-butyne, at 1365 cm−1, is very low. Since it appeared that cooling in CO led to a somewhat higher intensity of this band, we show the spectrum after cooling in CO in Fig. 2b instead of the cooling in vacuum spectrum where the 1365 cm−1 band is more difficult to distinguish from the noise.
A liquid nitrogen trap was used to further purify the CO (CK Specialty Gases Ltd., 99.97%) and H2 (CK Specialty Gases Ltd., 99.999%) used during the TPRS, LEED and RAIRS experiments. Ethylene (Messer, 99.95%) was used without further purification. 2-Butyne (Sigma-Aldrich, 99%) used in reference experiments was degassed by several pump–freeze–thaw cycles prior to use.
The data that support the findings of this study are available within the paper and its Supplementary Information, and all data are available from the authors on reasonable request.
van de Loosdrecht, J. et al. in Comprehensive Inorganic Chemistry II: From Elements to Applications (eds Reedijk, J. & Poeppelmeier, K.) 525–557 (Elsevier Ltd., 2013).
Schlögl, R. Chemistry’s role in regenerative energy. Angew. Chem. Int. 50, 6424–6426 (2011).
Claeys, M. & van Steen, E. Basic studies. Stud. Surf. Sci. Catal. 152, 601–680 (2004).
Weststrate, C. J., van Helden, P. & Niemantsverdriet, J. W. Reflections on the Fischer-Tropsch synthesis: mechanistic issues from a surface science perspective. Catal. Today 275, 100–110 (2016).
Van Santen, R. A., Ciobîcâ, I. M., Van Steen, E. & Ghouri, M. M. Mechanistic issues in Fischer-Tropsch. Catal. Adv. Catal. 54, 127–187 (2011).
Mims, C. A., Krajewski, J. J., Rose, K. D. & Melchior, M. T. Residence times and coverage by surface intermediates. Catal. Lett. 7, 119–125 (1990).
Mims, C. A. & McCandlish, L. E. Evidence for rapid chain growth. J. Phys. Chem. 91, 929–937 (1987).
Bertole, C. J., Kiss, G. & Mims, C. A. The effect of surface-active carbon on hydrocarbon selectivity in the cobalt-catalyzed Fischer-Tropsch synthesis. J. Catal. 223, 309–318 (2004).
Chen, W., Filot, I. A. W., Pestman, R. & Hensen, E. J. M. Mechanism of cobalt-catalyzed CO hydrogenation: 2. Fischer–Tropsch synthesis. ACS Catal. 7, 8061–8071 (2017).
Den Breejen, J. P. et al. On the origin of the cobalt particle size effects in Fischer-Tropsch catalysis. J. Am. Chem. Soc. 131, 7197–7203 (2009).
Navarro, V., van Spronsen, M. A. & Frenken, J. W. M. In situ observation of self-assembled hydrocarbon Fischer–Tropsch products on a cobalt catalyst. Nat. Chem. 8, 929 (2016).
Paredes-Nunez, A. et al. Nature and reactivity of the surface species observed over a supported cobalt catalyst under CO/H2 mixtures. Catal. Today 242, 178–183 (2015).
Xu, L. et al. Water adsorption on a Co (0001) surface. J. Phys. Chem. C 114, 17023–17029 (2010).
Bezemer, G. L. et al. Cobalt particle size effects in the Fischer-Tropsch reaction studied with carbon nanofiber supported catalysts. J. Am. Chem. Soc. 128, 3956–3964 (2006).
Geerlings, J. J. C., Zonnevylle, M. C. & de Groot, C. P. M. Studies of the Fischer-Tropsch reaction on Co(0001). Surf. Sci. 241, 302–314 (1991).
Geerlings, J. J. C., Zonnevylle, M. C. & de Groot, C. P. M. Structure sensitivity of the Fischer-Tropsch reaction on cobalt single crystals. Surf. Sci. 241, 315–324 (1991).
Ehrensperger, M. & Wintterlin, J. In situ scanning tunneling microscopy of the poisoning of a Co(0001) Fischer–Tropsch model catalyst by sulfur. J. Catal. 329, 49–56 (2015).
Böller, B., Durner, K. M. & Wintterlin, J. The active sites of a working Fischer–Tropsch catalyst revealed by operando scanning tunnelling microscopy. Nat. Catal. https://doi.org/10.1038/s41929-019-0360-1 (2019).
Andersen, J. N. et al. Vibrational fine structure in the C 1s core level photoemission of chemisorbed molecules: ethylene and ethylidyne on Rh(111). Chem. Phys. Lett. 269, 371–377 (1997).
Steinrück, H. P., Fuhrmann, T., Papp, C., Tränkenschuh, B. & Denecke, R. A detailed analysis of vibrational excitations in x-ray photoelectron spectra of adsorbed small hydrocarbons. J. Chem. Phys. 125, 204706 (2006).
Weststrate, C. J., Ciobîcă, I. M., van de Loosdrecht, J. & Niemantsverdriet, J. W. Adsorption and decomposition of ethene and propene on Co(0001): the surface chemistry of Fischer–Tropsch chain growth intermediates. J. Phys. Chem. C 120, 29210–29224 (2016).
Lorenz, M. P. et al. Ethene adsorption and dehydrogenation on clean and oxygen precovered Ni(111) studied by high resolution x-ray photoelectron spectroscopy. J. Chem. Phys. 133, 11–16 (2010).
Borg, A. et al. Acetylene chemisorption and decomposition on the Co(11-20) single crystal surface. Surf. Sci. 499, 183–192 (2002).
Weststrate, C. J. et al. Atomic and polymeric carbon on Co(0001): surface reconstruction, graphene formation, and catalyst poisoning. J. Phys. Chem. C 116, 11575–11583 (2012).
Weststrate, C. J., van de Loosdrecht, J. & Niemantsverdriet, J. W. Spectroscopic insights into cobalt-catalyzed Fischer-Tropsch synthesis: a review of the carbon monoxide interaction with single crystalline surfaces of cobalt. J. Catal. 342, 1–16 (2016).
Wiklund, M., Beutler, A., Nyholm, R. & Andersen, J. N. Vibrational analysis of the C 1s photoemission spectra from pure ethylidyne and ethylidyne coadsorbed with carbon monoxide on Rh(111). Surf. Sci. 461, 107–117 (2000).
Weststrate, C. J. et al. Ethanol decomposition on Co(0001): C-O bond scission on a close-packed cobalt surface. J. Phys. Chem. Lett. 1, 1767–1770 (2010).
Hirschmugl, C. J., Paolucci, G., Esch, F., Lizzit, S. & Schindler, K.-M. Vibrational fine structure on C 1s core-level photoemission: Ni(111)-ethyne and Ni(111)-butyne. Surf. Sci. 488, 43–51 (2001).
Vaari, J., Lahtinen, J. & Hautojärvi, P. The adsorption and decomposition of acetylene on clean and K-covered Co(0001). Catal. Lett. 44, 43–49 (1997).
Habermehl-Ćwirzeń, K. M. E., Kauraala, K. & Lahtinen, J. Hydrogen on cobalt: the effects of carbon monoxide and sulphur additives on the D2/Co(0001) system. Phys. Scr. T108, 28–32 (2004).
Weststrate, C. J. & Niemantsverdriet, J. W. Understanding FTS selectivity: the crucial role of surface hydrogen. Faraday Discuss. 197, 101–116 (2016).
Weststrate, C. J. & Niemantsverdriet, J. W. CO as a promoting spectator species of CxHy conversions relevant for Fischer-Tropsch chain growth on cobalt: evidence from temperature-programmed reaction and reflection absorption infrared spectroscopy. ACS Catal. 8, 10826–10835 (2018).
McCoustra, M. R. S., Ainsworth, M. K., De La Cruz, C., Chesters, M. A. & Sheppard, N. An infrared study of ethene and CO coadsorption on Pt(111) and a Pt/SiO2 catalyst: ambiguities in the interpretation of difference spectra. Surf. Sci. 437, 9–17 (2002).
Mims, C. A., Weisel, M. D., Hoffmann, F. M., Sinfelt, J. H. & White, J. M. Site blocking effects in ethylidyne decomposition kinetics on Ru(001): in-situ study with infrared reflection absorption spectroscopy at elevated pressure. J. Phys. Chem. 97, 12656–12659 (1993).
Zaera, F. An organometallic guide to the chemistry of hydrocarbon moieties on transition metal surfaces. Chem. Rev. 95, 2651–2693 (1995).
Blackman, G. S. et al. LEED and HREELS studies of the coadsorbed CO + ethylidyne and NO + ethylidyne systems on the Rh(111) crystal surface. Surf. Sci. 207, 66–88 (1988).
van Helden, P., van den Berg, J.-A. & Weststrate, C. J. Hydrogen adsorption on Co surfaces: a density functional theory and temperature programmed desorption study. ACS Catal. 2, 1097–1107 (2012).
Weststrate, C. J., Ciobîcă, I. M., Saib, A. M., Moodley, D. J. & Niemantsverdriet, J. W. Fundamental issues on practical Fischer–Tropsch catalysts: how surface science can help. Catal. Today 228, 106–112 (2014).
Zhang, M., Huang, H. & Yu, Y. Insight into the mechanism of ethylene decomposition over Co(0001) surface: formation of carbon species. Catal. Lett. 149, 744–752 (2019).
Zhuo, M., Borgna, A. & Saeys, M. Effect of the CO coverage on the Fischer-Tropsch synthesis mechanism on cobalt catalysts. J. Catal. 297, 217–226 (2013).
van Helden, P. et al. Computational investigation of the kinetics and mechanism of the initial steps of the Fischer–Tropsch synthesis on cobalt. Faraday Discuss. 197, 117–151 (2017).
Mate, C. M., Kao, C.-T. & Somorjai, G. A. Carbon monoxide induced ordering of adsorbates on the Rh(111) crystal surface: Importance of surface dipole moments. Surf. Sci. 206, 145–168 (1988).
Yang, Q. Y., Maynard, K. J., Johnson, A. D. & Ceyer, S. T. The structure and chemistry of CH3 and CH radicals adsorbed on Ni(111). J. Chem. Phys. 102, 7734–7749 (1995).
Denecke, R. Surface chemistry studied by in situ X-ray photoelectron spectroscopy. Appl. Phys. A 80, 977–986 (2005).
Eidus, Y. T., Ershov, N. I., Zueva, T. V. & Piroshkov, S. D. Accelerating effect of carbon monoxide as a function of its concentration and the reaction temperature during hydropolymerization of lower olefins. Bull. Acad. Sci. USSR Div. Chem. Sci. 23, 2758–2760 (1974).
Cant, N. W., Liu, I. O. Y. & Scott, J. A. Ethylene oligomerisation over Co/SiO2 in the presence of trace carbon monoxide: the Eidus reaction revisited. Catal. Today 215, 267–275 (2013).
Ormerod, R. M. & Lambert, R. M. Critical ensemble required for acetylene cyclization on Pd(111): a study of steric inhibition of coadsorbed oxygen. J. Phys. Chem. 16, 8111–8116 (1992).
Cheng, J. et al. A DFT study of the chain growth probability in Fischer-Tropsch synthesis. J. Catal. 257, 221–228 (2008).
Liu, J. X., Su, H. Y. & Li, W. X. Structure sensitivity of CO methanation on Co (0001), (10-12) and (11-20) surfaces: density functional theory calculations. Catal. Today 215, 36–42 (2013).
Weststrate, C. J., van Helden, P., van de Loosdrecht, J. & Niemantsverdriet, J. W. Elementary steps in Fischer–Tropsch synthesis: CO bond scission, CO oxidation and surface carbiding on Co(0001). Surf. Sci. 648, 60–66 (2016).
van Helden, P., Ciobîcă, I. M. & Coetzer, R. L. J. The size-dependent site composition of FCC cobalt nanocrystals. Catal. Today 261, 48–59 (2016).
Pestman, R., Chen, W. & Hensen, E. Insight into the rate-determining step and active sites in the Fischer–Tropsch reaction over cobalt catalysts. ACS Catal. 9, 4189–4195 (2019).
Vang, R. T. et al. Controlling the catalytic bond-breaking selectivity of Ni surfaces by step blocking. Nat. Mater. 4, 160–162 (2005).
Vang, R. T. et al. Ethylene dissociation on flat and stepped Ni(111): a combined STM and DFT study. Surf. Sci. 600, 66–77 (2006).
Neubauer, R., Whelan, C. M., Denecke, R. & Steinrück, H. P. The thermal chemistry of saturated layers of acetylene and ethylene on Ni(100) studied by in situ synchrotron x-ray photoelectron spectroscopy. J. Chem. Phys. 119, 1710–1718 (2003).
Zijlstra, B., Broos, R. J. P., Chen, W., Filot, I. A. W. & Hensen, E. J. M. First-principles based microkinetic modeling of transient kinetics of CO hydrogenation on cobalt catalysts. Catal. Today 342, 131–141 (2019).
Baraldi, A. et al. Time resolved core level photoemission experiments with synchrotron radiation. J. Electron Spectrosc. Relat. Phenom. 76, 145–149 (1995).
Huesges, Z. & Christmann, K. Interaction of hydrogen with a cobalt(0001) surface. Z. Phys. Chem. 227, 881–899 (2013).
This work has been carried out as part of the SynCat@DIFFER programme between the Dutch Institute for Fundamental Energy Research (DIFFER), Eindhoven university of Technology (TU/e) and Syngaschem BV and is funded jointly by the Netherlands Organization for Scientific Research (NWO) and Syngaschem BV (project number 731.016.301). We acknowledge ELETTRA, the European Synchrotron light source in Trieste, Italy (proposal 20180250), and MAX IV, the Swedish National Laboratory for research using X-rays, Lund, Sweden (proposal 20180237) for provision of beamtime. The staff at the SuperESCA (ELETTRA) and HIPPIE (MAX IV) beamlines are acknowledged for their excellent support. We acknowledge the technical support from the technical support staff at the DIFFER Institute. Professor Dr. M.C.M. van de Sanden (DIFFER) is acknowledged for commenting on the manuscript and providing valuable suggestions. Syngaschem BV gratefully acknowledges substantial funding from Synfuels China Technology Co. Ltd.
The authors declare no competing interests.
Peer review information Nature Communications thanks the anonymous reviewers for their contribution to the peer review of this work. Peer reviewer reports are available.
Publisher’s note Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
About this article
Cite this article
Weststrate, C.J.(J., Sharma, D., Garcia Rodriguez, D. et al. Mechanistic insight into carbon-carbon bond formation on cobalt under simulated Fischer-Tropsch synthesis conditions. Nat Commun 11, 750 (2020). https://doi.org/10.1038/s41467-020-14613-5
This article is cited by
Selective synthesis of butane from carbon monoxide using cascade electrolysis and thermocatalysis at ambient conditions
Nature Catalysis (2023)
CO2 Reforming of CH4 on Mesoporous Alumina-Supported Cobalt Catalyst: Optimization of Lanthana Promoter Loading
Topics in Catalysis (2021)
Reactivity of C3Hx Adsorbates in Presence of Co-adsorbed CO and Hydrogen: Testing Fischer–Tropsch Chain Growth Mechanisms
Topics in Catalysis (2020)