Modeling Transport Phenomena in Selective Catalytic Reductant Catalytic Converter with NH3 as Reductant for NO Degradation

E. Salehi, M. A. Moghaddam, N. Sahebjamee
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引用次数: 3

Abstract

In the current study, reduction of nitrogen oxide from exhaust gas in the presence of NH3 as reductant on selective catalytic reductant (SCR) impregnated catalytic converter was simulated using Comsol© software. Mass transfer (one-dimensional) and heat transfer (three-dimensional) governing equations were taken into account to model the unsteady state behavior of the catalytic converter. Modeling results of reaction rate indicated good agreement with the experimental data. Results showed that the cumulative conversion exceeded 98 percent for both NO and NH3 components in the outflow gas emitted from the converter. In addition, temperature distribution graphs showed that the exhaust gas temperature varied from 450 K at the converter inlet to 550 K at the outlet. According to the results, the temperature tolerance inside the converter was less than 20 °C. Moreover, radial temperature gradient was sharper than axial one because of lesser energy accumulation in the direction of the convective flow.
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选择性催化还原剂NH3催化转化器降解NO的输运现象建模
本研究采用Comsol©软件模拟了以NH3为还原剂在选择性催化还原剂(SCR)浸渍催化转化器上还原废气中氮氧化物的过程。采用一维传质控制方程和三维传热控制方程对催化转化器的非稳态行为进行了建模。反应速率的模拟结果与实验数据吻合较好。结果表明,转炉流出气中NO和NH3组分的累计转化率均超过98%。此外,温度分布图显示,排气温度从转炉进口450 K到出口550 K不等。结果表明,转炉内部的耐温小于20℃。此外,由于对流方向的能量积累较少,径向温度梯度比轴向温度梯度更大。
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CiteScore
3.10
自引率
0.00%
发文量
29
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