“…Reaction yields could be increased by af actor of 3, and the conversion extended to further internal olefins such as 4-octene,b y increasing the reaction temperature to 413 K, in this case with comparatively lower product regioselectivities,y et in excess of 80 %( entries 14 and 15). This catalytic system proved also efficient to selectively convert complex mixtures of terminal and internal olefins into terminal organosilanes.Amixture of 8-bromooctene isomers,generated by isomerization of the corresponding a-olefin (8-bromo-1-octene) with 1.0 Ru/CeO 2 ,w as converted with 91 %s electivity to the terminal 1,1,1-triethyl-8bromooctylsilane.S imilarly high regioselectivities were also achieved from industrially relevant olefin mixtures,representative for output streams from mild-temperature paraffin dehydrogenation processes, [4] and olefin oligomerization/ metathesis operations,a si nt he commercial Shell Higher Olefin Process . [10,23] In all cases,the cooperation of Ru/CeO 2 and Rh/CeO 2 single-atom catalysts in tandem led to ahighly selective (> 95 %) production of terminal organosilanes ( Table 2, entries 18 and 19).…”