Abstract
The supported catalysts were prepared by coimpregnation with aqueous solutions of ruthenium and tin salt and characterized by temperature-programmed reduction (TPR), X-ray photoelectron spectroscopy (XPS), carbon monoxide (CO) and oxygen (O 2) chemisorption measurements. The surface of the reduced Al 2O 3-based bimetallic catalysts would be composed of metallic ruthenium and Sn(II) species. No evidence for substantial amounts of Sn(0) is found on reduced catalysts by XPS measurement. Based on the available evidence from the various techniques, the authors suggested that the high selectivity of the bimetallic Ru-Sn/Al 2O 3 catalyst for production of 1,4-cyclohexanedimethanol would be due to the action not only of the promoter (Sn) but also of the support (alumina). Catalytic hydrogenation of 1,4-cyclohexanedicarboxylic acid to 1,4-cyclohexanedimethanol over Ru-Sn supported catalysts was studied as functions of catalyst composition as well as various catalyst preparation parameters. Hydrogenation activity was affected by the kind of tin compounds and supports used for the preparation of the Ru-Sn catalyst. Stannous chloride and alumina were found to be the appropriate materials for the hydrogenation of C O group over the Ru-Sn catalysts. The yield for the 1,4-cyclohexanedimethanol on Ru-Sn/Al 2O 3 catalyst increased with Sn/Ru atomic ratio, reaching a maximum at a value of Sn/Ru = 1:1, which suggested a promotion of the C O bond hydrogenation by particular bimetallic Ru-Sn ensembles. The Ru-Sn/Al 2O 3 catalysts without any calcination activated in a hydrogen stream at 550 °C were effective for the hydrogenation of 1,4-cyclohexanedicarboxylic acid. Finally, we verified the durability of our catalyst by carrying out a catalyst-recycling test over five cycles.
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