Abstract

Abstract The direct addition of acetic acid to ethylene to form ethyl acetate over H 4 SiW 12 O 40 /SiO 2 using SiO 2 with various surface areas and mesopore sizes was studied. H 4 SiW 12 O 40 /SiO 2 was superior in activity to conventional solid acids including H 3 PO 4 /SiO 2 , Nafion–SiO 2 , WO 3 –ZrO 2 , and unsupported H 4 SiW 12 O 40 . While the selectivity for ethyl acetate was more than 98% regardless of the catalyst, the activities were significantly different. Maximum activity was obtained when SiO 2 having a high surface area and moderate pore size (ave. 6 nm) was utilized. The temperature-programmed desorption of benzonitrile technique and XRD both confirmed that this catalyst had a large amount of acid sites located on the outermost surface due to the high dispersion of H 4 SiW 12 O 40 . In contrast, H 4 SiW 12 O 40 /SiO 2 , with SiO 2 of very small mesopores (3 nm) showed a very low activity, despite having the largest amount of acid sites located on the outermost surfaces. On this catalyst, diffusion of the reactant and product were slow due to the very small-sized mesopores. This limited diffusion rate results in its low activity.

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