www.sciencemag.org/cgi/content/full/320/5872/86/DC1 Supporting Online Material for The Roles of Subsurface Carbon and Hydrogen in Palladium-Catalyzed Alkyne Hydrogenation Detre Teschner,* János Borsodi, Attila Wootsch, Zsolt Révay, Michael Hävecker, Axel Knop-Gericke, S. David Jackson, Robert Schlögl *To whom correspondence should be addressed. E-mail: [email protected] Published 4 April 2008, Science 320, 86 (2008) DOI: 10.1126/science.1155200 This PDF file includes: Materials and Methods Figs. S1 to S5 References Supporting Online Material for The roles of Subsurface Carbon and Hydrogen in Palladium-Catalyzed Alkyne Hydrogenation Detre Teschner*, János Borsodi, Attila Wootsch, Zsolt Révay, Michael Hävecker, Axel Knop-Gericke, S. David Jackson, Robert Schlögl *To whom correspondence should be addressed, E-mail: [email protected] Materials and Methods In situ (high-pressure) x-ray photoelectron spectroscopy (XPS) experiments were performed at beamlines U49/2-PGM1 and PGM2 at BESSY, Berlin, with a setup schematically shown in Figure S5. Samples were transferred from a pre-chamber and were mounted inside the reaction cell, 2 mm away from an aperture that is the entrance to the differentially pumped stages of the lens system of the hemispherical analyzer. The application of differential pumping allows minimization of the travel path of photoelectrons in the gas phase. The sample can be heated from the back side using an infrared laser system. Gas flows into the reaction cell were regulated by leak valves and mass flow controllers. The gas phase composition, to monitor the catalytic activity, can be recorded on-line by a mass spectrometer connected directly to the outlet of the reaction chamber. The undulator beamline provides a high intensity synchrotron light, essential for us to allow recording spectra under high mbar pressure conditions. Since the aim of these experiments was to record Pd 3d spectra at pressures as high as possible, we have used pure palladium samples: Pd foil (Goodfellow) and Pd black (Goodfellow, BET surface area 2.06 m2g-1). The samples were cleaned with oxygen and hydrogen treatments prior to experiments, in situ. Pd 3d core levels were recorded at normal emission with 720 eV excitation, corresponding to an inelastic mean free path of approximately 9 Å (SR1). The metallic Pd 3d spectra were fitted using Gauss-Lorentz functions with an exponential tail, while the PdC component was approximated by a simple Gauss-Lorentz function as indicated by the symmetric character of the peak. In situ Prompt Gamma Activation Analysis (PGAA) was carried out at the cold neutron beam of the Budapest Neutron Centre, Budapest, Hungary. The characteristic prompt gamma radiation was collected by a Compton-suppressed High-Purity Germanium detector; the spectra were acquired using a multi-channel analyzer. For the in situ PGAA experiments we placed a continuous flow reactor (Al2O3 ceramic tube with inner diameter of 2 mm) into the neutron beam, which was almost perfectly transparent to the cold neutrons. Gas flow was supplied by mass flow controllers (Bronkhorst) and the reaction was monitored by an online micro gas chromatograph (Varian CP-4900, CP-Sil 5 CB). 1Pentyne (1.6 cm3min-1) was introduced into the hydrogen stream (flow rate 2–64 cm3min-1) via N2 flow going through a saturator held at 273 K. For the study here, 7 mg Pd black (Goodfellow) was mixed with 100 mg of SiC and loaded into the reactor. Hydrogenation was carried out adiabatically at near room temperature, without any regenerative treatment 1 between catalytic runs. Since the typical timescale for recording a spectrum (0-12000 keV) is 1-2 hours, measurements were done after allowing an equilibration period of 20-30 min prior to acquisition. Molar ratios (H/Pd) were determined from the characteristic peak areas corrected by the detector efficiency and the nuclear data of the observed elements (SR2, SR3). Since the spectrum of hydrogen contains extra contribution from gas phase hydrogen in the feed and moisture in the “viewing angle” of the detector, reference experiments were carried out without Pd in the reactor but otherwise with identical conditions as during hydrogenation. This background hydrogen was subtracted from the hydrogen content of palladium during data evaluation. The uncertainty values (shown in Table 1 of the manuscript) involve all deviation in calculating H/Pd ratios (e.g. the uncertainty in determining the PGAA peak areas; uncertainty due to background correction) and not only the deviation of H/Pd values during averaging the individual experiments; hence the law of propagation of errors was applied. Since the agreement of H/Pd in the fresh sample to the measured phase diagram is much better than estimated by the error bars, we are confident that the uncertainty of the relative changes between experiments are an order of magnitude lower than indicated by the error bars. Pressure dependent catalytic experiments were carried out in a closed-loop apparatus (71 cm3) equipped with GC analytic (50-m CP-Sil capillary column, FID). This setup permits to investigate reactions in the “low-mbar” to “sub-atmospheric” pressure range. The catalytic samples (Pd black, as above; 1% Pd/Al2O3, Johnson Matthey) were allowed at each condition to come to steady state by repeated experiments without regeneration. The applied partial pressure and temperature conditions are detailed at each corresponding Figure. Supporting Figures Figure S1. A, 1-pentyne hydrogenation experiments over 1% Pd/Al2O3 with 10 Torr 1-pentyne and 100 Torr H2 at 305 K in the closed-loop reactor. The catalyst was treated in hydrogen at 358 K prior to the first experiment. The reaction mixture was analyzed after 5 minutes circulation through the catalyst bed. The figure shows repeated experiments indicating an activation period, and stabilization only after 3-5 experiments (15-25 minutes on stream). B, 1-pentyne hydrogenation experiments over Pd black at atmospheric condition using 4 cm3ml-1 H2, 1.6 cm3ml-1 1-pentyne (in 8 2 cm3ml-1 N2) at 292 K, during in situ PGAA experiments. The catalyst was pretreated in hydrogen before hydrogenation. Figure S2. 1-pentyne hydrogenation experiments over 1% Pd/Al2O3 with (A) 10 Torr and (B) 0.33 Torr 1-pentyne as a function of H2 partial pressure (Torr). The reaction rate is expressed as moles of 1-pentyne converted pro surface Pd (in moles). Experiments were carried out at 305 K in the closedloop reactor; sampling time 5 minutes. At both “low mbar” and “sub-atmospheric” conditions hydrogenation is characterized by two distinct regimes: one with first order for hydrogen (and zeroth or slightly negative order for 1-pentyne; not shown here), and the other with 0th order for hydrogen (and 1st order for pentyne). Hydrogenation is generally selective in the regime of 1st order for hydrogen, yielding 1-pentene. A similar dependence was observed for Pd black, as well. Figure S3. The effect of reaction temperature on the formation of PdC. The in situ Pd 3d spectra clearly indicate that at ~ 7 mbar, above the decomposition temperature of β-hydride, formation of PdC was significantly enhanced. 3 Figure S4. 1-pentyne conversion (A, C) and corresponding H/Pd (B, D) values during in situ PGAA experiments. Experiments 1-4 were carried out using 4 cm3min-1 hydrogen and Exp. 5,6 with 6 cm3min-1 hydrogen. 1-Pentyne flow was kept constant at 1.6 cm3min-1. Experiments marked by 1-4 have not been performed directly after each other; therefore the prehistory of the sample was always different. The same holds for Experiments 5 and 6, as well, at which both the initial and the final (after ~2 h time on stream) activities are included. The increasing conversion was due to the activation effect and partly due to slow temperature rise of the adiabatic catalyst bed. During all these experiments hydrogenation was selective toward 1-pentene. The comparison clearly indicates that there is absolutely no correlation between activity in the regime of selective hydrogenation and the amount of dissolved hydrogen in palladium. Since the reaction rate is limited by hydrogen (see Figure S2), the equilibrium of hydrogen between bulk and surface should be necessarily disturbed. Figure S5. Schematic representation of the in situ XPS setup 4 Supporting References SR1, S. Tanuma, C. J. Powell, D. R. Penn, Surf. Interface Anal. 17, 911 (1991). SR2, Zs. Révay, T. Belgya, Zs. Kasztovszky, J. L. Weil, G. L. Molnár, Nucl. Instrum. and Meth. B 213 385 (2004). SR3, G.L. Molnár (Ed.) Handbook of Prompt Gamma Activation Analysis with Neutron Beams, Kluwer Academic Publishers, Dordrecht/London/Boston, 2004. 5
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