摘要
Background Compared to propane dehydrogenation (PDH) technology, propane oxidative dehydrogenation (ODHP) technology represents an effective approach to overcoming thermodynamic limitations. Supported boron oxide catalysts demonstrate promising potential by co-producing high-value ethylene while enhancing olefin selectivity. However, the critical challenge impeding the development of boron-based catalysts lies in the evaporation-induced loss of active components (boron oxide) under calcination process. Methods BO x −M ( M = SnO 2 , SiO 2 , MgO, CaO, MgSO 4 , CaSO 4 ) catalysts with 10 wt% boron trioxide loading were prepared by simple co-impregnation method using different supports. Significant findings Compared with other catalysts, the BO x -SnO 2 , BO x -CaSO 4 , and BO x −MgSO 4 systems featuring covalent oxygen-containing supports demonstrated superior catalytic performance, achieving propane conversions of 50.1 %, 49.4 %, and 48.9 %, respectively. Analysis revealed that the covalently bonded oxygen in the support forms covalent bridges with the active BO 3 species, thereby enhancing the stable interactions between the support and active components. This effectively mitigates the loss of active species during calcination and improves the catalytic activity. These findings provide a feasible pathway for developing high-performance catalytic systems for ODHP.
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