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The effects of regeneration-phase CO and/or H2, and their amounts as a function of temperature on the trapping and reduction of NOX over a model and a commercial NOX storage/reduction catalyst have been evaluated. Overall, for both catalysts, their NOX removal performance improved with each incremental increase in H2 concentration. For the commercial sample, using CO at 200 °C, beyond a small amount added, was found to decrease performance. The addition of H2 to the CO-containing mixtures resulted in improved performance at 200 °C, but the presence of the CO still resulted in decreased performance in comparison to activity when just H2 was used. With the model sample, the presence of CO resulted in very poor performance at 200 °C, even with H2. The data suggest that CO poisons Pt sites, including Pt-catalyzed nitrate decomposition. At 300 °C, H2, CO, and mixtures of the two were comparable for trapping and reduction of NOX, although with the model sample H2 did prove consistently better. With the commercial sample, H2 and CO were again comparable at 500 °C, but mixtures of the two led to slightly improved performance, while yet again H2 and H2-containing mixtures proved better than CO when testing the model sample. NH3 formation was observed under most test conditions used. At 200 °C, NH3 formation increased with each increase in H2, while at 500 °C, the amount of NH3 formed when using the mixtures was higher than that when using either H2 or CO. This coincides with the improved performance observed with the mixtures when testing the commercial.  相似文献   
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Food Science and Biotechnology - The present study was performed to assess anti-obesity effects of raw pineapple juice in high fat diet (HFD)-induced fatness. Based on food type, rats were divided...  相似文献   
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The effects of using NO or NO2 as the NO X source on the performance of a NO X storage/reduction catalyst were investigated from 200 to 500 °C. The evaluation included comparison with constant cycling times and trapping the same amount of NO X during the lean phase. With NO2 as the NO X source, better trapping and reduction performance was attained in comparison to NO, at all operating temperatures except 300 °C. This exception, under the conditions tested, was likely due to high NO oxidation activity and rapid trapping of NO2, although it is expected that extending the trapping time would lead to consistent differences. Several reasons for the observed improvements at 200, 400 and 500 °C with NO2 relative to NO are discussed. One that can explain the data, for both trapping and release improvement, is treating the monolith as an integral reactor. With NO2, more NO X is trapped at the very inlet of the catalyst, whereas with NO, the maximum in trapping during cycling occurs slightly downstream. Thus more of the catalyst can be used for trapping with NO2 as the NO X source. The decreased release during catalyst regeneration is similarly explained; with more being released at the very inlet, there is more residence time and therefore contact with downstream Pt sites, but more importantly more interaction between reductant and stored NO X . NH3 and N2O measurements support this conclusion.  相似文献   
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