(734e) Investigating the Effect of Alloying Sn and Pd on Direct Synthesis of H2O2
H2O2 formation rates on Pd and Pd2Sn in a protic solvent (e.g., methanol) are significant, whereas those in aprotic solvents (e.g., acetonitrile) are immeasurable. These results are consistent with a proton-electron transfer (PET) mechanism on Pd in which the presence of a proton is necessary to facilitate DS.4 Steady state H2O2 and H2O formation rates over silica supported PdSnxÂ nanoparticles (7-15 nm in diameter) synthesized by colloidal methods depend on the number of oxidative and reductive treatments as well as the final treatment used prior to direct synthesis, however, Pd nanoparticles (~10 nm in diameter) do not. Activation enthalpiesÂ (âHÇ) were calculated from rates measured as a function of temperature (281-305 K) and show that PdSn2Â catalysts have greater âHÇÂ for H2O2 (9 kJ mol-1) and H2O (15 kJ mol-1) formation than do Pd nanoparticles (-6 kJ mol-1, 11 kJ mol-1). These differences in âHÇÂ values suggest that the addition of Sn raises the barriers of H2O2 formation much more than H2O formation, however, H2O2 selectivities on PdSn2 (45%, oxidized and reduced) exceed those on Pd (23%, reduced). Spectra of adsorbed CO on PdSnx obtained using Fourier transform infrared spectroscopy (FTIR) show that the ratio of the peak area for the bridge bound CO to that of the atop bound CO decreases from 17 on Pd to 2 on PdSn2, indicating that Sn disrupts the ensembles of surface Pd atoms that are proposed to be necessary for O-O bond rupture and subsequent H2O formation. Together, theÂ values and spectroscopic data suggest that the addition of Sn to Pd increases the selectivity towards H2O2 production predominantly through ensemble effects, which differs significantly from the electronic effects that are largely responsible for the high H2O2 selectivities observed on PdAux catalysts.3
Apart from alloying metals, factors such as the presence of additives in the reaction medium (i.e., acids, halides) and the type of reactor used (e.g., PFR vs. BSTR) also affect H2O2 selectivities and rates of DS.1 Such results indicate that the active form(s) of the catalyst may include soluble forms of Pd in addition to supported nanoparticles. Homogeneous Pd complexes may form by dissolution of Pd from surfaces and complexation with anionic species added to serve as âpromoters.â The contributions of both homogeneous and heterogeneous Pd can be distinguished by the further addition of specific titrants that render either heterogeneous or homogeneous catalysts inactive (e.g., Hg, CS2, C4H4S).5Â These results will show that comparisons between direct synthesis catalysts operating in continuous flow or batch modes require corrections to account for more than just the simple difference between the design equations of the systems.
(1) Wilson, N. M.; Bregante, D. T.; Priyadarshini, P.; Flaherty, D. W. In Catalysis; Spivey, J., Han, Y., Eds.; Royal Society of Chemistry: 2017; Vol. 29, p 122.
(2) Freakley, S. J.; He, Q.; Harrhy, J. H.; Lu, L.; Crole, D. A.; Morgan, D. J.; Ntainjua, E. N.; EDwards, J. K.; Carley, A. F.; Borisevich, A. Y.; Kiely, C. J.; Hutchings, G. J. Science 2016, 351, 965.
(3) Edwards, J. K.; Thomas, A.; Carley, A. F.; Herzing, A. A.; Kiely, C. J.; Hutchings, G. J. Green Chem. 2008, 10, 388.
(4) Wilson, N. M.; Flaherty, D. W. J Am Chem Soc 2016, 138, 574.
(5) Widegren, J. A.; Finke, R. G. J Mol Catal A: Chemical 2003, 198, 317.