“…Supported boron oxide catalysts can provide abundant "BO" sites on the surface, and exhibit high activity in ODHP. 17,18,25 It has been reported that B 2 O 3 impregnation on conventional three-dimensional porous supports, 9,26,27 such as TiO 2 , SiO 2 and Al 2 O 3 , could enhance the abundance of "BO" sites on the catalyst surface for the oxidative dehydrogenation reaction. However, under the higher reaction temperature (mostly >450 °C) normally used for the oxidative dehydrogenation of propane, the above catalysts may suffer from insufficient stability due to the low melting point of boron oxide (∼450 °C), 12,22 easily causing its liquefaction on the catalyst surface, weakening the interaction force between boron oxide and the carrier and even leading to the loss of boron.…”