NO x conversion performance of a urea-selective catalytic reduction (SCR) system comprising V 2 O 5 /TiO 2 catalyst under steady state operating conditions of an 8-litre, common-rail turbo direct injection (TDI) diesel engine was investigated. It was shown that the urea-SCR system achieves 70–90 per cent NO x conversion under medium and high load conditions at 1440 r/min and that NO x conversion is low under low load conditions because of the low catalyst temperatures and the NO/NO 2 ratio being higher than unity. It was also shown that NO x conversion exceeds 90 per cent when the catalyst temperature is higher than 530 K. To investigate the details of the chemistry and thermofluid dynamics within the urea-SCR system, a computational fluid dynamics (CFD) code that incorporates detailed surface chemistry was developed based on the modified subroutines of CHEMKIN-II. The spatial variations of chemical species including NO and NH 3 in a thin catalyst channel was calculated using the model. The calculated result of NO conversion showed relatively good agreement with experimental results.
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Kusaka et al. (2005) studied this question.
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