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The Role of Activated Carbon Supported CeO_x and VO_x Phases during Oxidative Dehydrogenation of Propane to Propylene Using CO2 As a Soft Oxidant

机译:活性炭支持的作用支持CeO_x和Vo_x相期间丙烷氧化脱氢在丙烷与丙烯的丙烯作为软氧化剂

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Two parallel and independent reaction pathways occur: propane CO2-ODH which is related to participation of lattice oxygen, and propane cracking to methane, H2 and carbon. Ethylene is formed only in trace amounts suggesting fast C=C bond cleavage. Activation of propane is associated with lattice oxygen abstraction and catalyst reduction. Based on the C3H8-TPR and CO2-TPO results we can postulate that that bulk CeVO4 formation contains negligible activity for propane and CO2 activation. The ability of bulk crystalline V2O5 catalyst to activate CO2 is very limited leading to a progressive decline of its CO2-ODH activity. Bulk CeO2 acts favorably towards catalyst re-oxidation with CO2 already at 450°C. Presence of vanadium species strongly changes the redox and catalytic performance of CeO2, hindering its CO2 activation ability. Finely dispersed, non-crystalline VO_x species appear as the ones mainly responsible for propane activation, leading to propylene formation.
机译:发生两种平行和独立的反应途径:丙烷CO2-ODH,与晶格氧的参与有关,以及丙烷裂化至甲烷,H 2和碳。乙烯仅在痕量的含量表明快速C = C键切割中形成。丙烷的激活与晶格氧气抽象和催化剂还原相关。基于C3H8-TPR和CO2-TPO结果,我们可以假设散装Cevo4的形成含有可忽略的丙烷和CO2活化的活动。将块状晶体V2O5催化剂活化CO 2的能力非常有限,导致其CO 2-ODH活性的进行性下降。 Bulk CeO2在450℃下用CO 2致催化剂重新氧化。钒物种的存在强烈改变CeO2的氧化还原和催化性能,阻碍了其CO 2活化能力。精细分散的非结晶VO_X物种显示为主要负责丙烷活化的那些,导致丙烯形成。

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