Modelling the ammonia adsorption-desorption process over an Fe-zeolite catalyst for SCR automotive applications

被引:49
作者
Colombo, Massimo [1 ,2 ]
Koltsakis, Grigorios [2 ]
Nova, Isabella [1 ]
Tronconi, Enrico [1 ]
机构
[1] Politecn Milan, Dipartimento Energia, Lab Catalysis & Catalyt Proc, I-20133 Milan, Italy
[2] Aristotle Univ Thessaloniki, Lab Appl Thermodynam, Thessaloniki 54124, Greece
关键词
Urea SCR; Diesel exhausts after-treatment; Ammonia storage; Converter modelling; TEMPERATURE-PROGRAMMED DESORPTION; ACIDIC PROPERTIES; DIESEL EXHAUST; BETA ZEOLITE; REDUCTION; NH3-SCR; NOX; TPD; H-ZSM-5; NH3;
D O I
10.1016/j.cattod.2011.09.002
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The accurate description of NH3 adsorption/desorption from the catalyst surface is the basis for the correct description of the NH3-SCR catalytic chemistry. Currently, Temkin-type kinetics are widely and successfully used to describe the NH3 adsorption/desorption process over V-based and metal-promoted zeolite catalysts in the 200-600 degrees C T-window: in this approach the heterogeneity of the catalytic surface is taken into account considering the activation energy of the desorption process as a linear function of the adsorbed species surface coverage. In the present work, carried out over a commercial Fe-zeolite SCR catalytic system, we show that this modelling approach fails when extended to lower temperatures (T <= 150 degrees C) and in the presence of water, conditions of growing interest for Diesel exhaust after-treatment systems. Based on literature evidence, an improved, physically consistent dual-site modelling approach is implemented, resulting in an accurate description of the ammonia adsorption/desorption process in the extended 50-550 degrees C temperature window. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:42 / 52
页数:11
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