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Kinetic analysis of N2O decomposition over calcined hydrotalcites

机译:煅烧水滑石上N2O分解的动力学分析

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Kinetics of N2O decomposition over catalyst prepared by calcination of Co-Mn hydrotalcite was examined in integral fixed-bed reactor (V/w = 12-961g(cat)(-1) h(-1)) at various N2O and O-2 initial partial pressure at temperature range of 330-450 degrees C. Kinetic data were evaluated by linear and non-linear regression method, 15 kinetic expressions were tested. Based on the obtained results a redox model of NO decomposition was proposed. At low pressures of O-2, adsorbed oxygen is formed by the N2O decomposition; the N2O chemisorption is considered as the rate-determining step. On the contrary, at high O-2 pressure it could be assumed that adsorbed oxygen species appear as a result of O-2 adsorption and the Eley-Rideal mechanism is the rate determining. N2O decomposition is well described by the 1 st rate law at N2O and O-2 concentrations typical for waste gases. (c) 2006 Elsevier B.V. All rights reserved.
机译:在整体固定床反应器中(V / w = 12-961g(cat)(-1)h(-1))在各种N2O和O-2下检查了通过Co-Mn水滑石煅烧制备的催化剂上N2O分解的动力学。初始分压在330-450摄氏度的温度范围内。通过线性和非线性回归方法评估动力学数据,测试了15个动力学表达式。基于获得的结果,提出了NO分解的氧化还原模型。在O-2的低压下,由于N2O分解而形成吸附的氧。 N2O化学吸附被认为是决定速率的步骤。相反,在高O-2压力下,可以假定由于O-2吸附而出现吸附的氧,而Eley-Rideal机制是决定速率的原因。一级速率定律很好地描述了废气中典型的N2O和O-2浓度下的N2O分解。 (c)2006 Elsevier B.V.保留所有权利。

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