首页> 外文会议>SAE World congress;Diesel exhaust emission control session >The Effects of Sulfur Poisoning and Desulfation Temperature on the NOx Conversion of LNT+SCR Systems for Diesel Applications
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The Effects of Sulfur Poisoning and Desulfation Temperature on the NOx Conversion of LNT+SCR Systems for Diesel Applications

机译:硫中毒和脱硫温度对柴油应用LNT + SCR系统NOx转化的影响

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A laboratory study was performed to assess the effects of sulfur poisoning and desulfation temperature on the NO_x conversion of a LNT+(Cu/SCR) in-situ system. Four LNT+ (Cu/SCR) systems were aged for 4.5 hours without sulfur at 600, 700, 750, and 800°C using A/F ratio modulations to represent 23K miles of desulfations at different temperatures. NO_x conversion tests were performed on the LNT alone and on the LNT+SCR system using a 60 s lean/5 s rich cycle. The catalysts were then sulfur poisoned at 400°C and desulfated four times and re-evaluated on the 60/5 tests. This test sequence was repeated 3 more times to represent 100K miles of desulfations. After simulating 23K miles of desulfations, the Cu-based SCR catalysts improved the NO_x conversion of the LNT at low temperatures (e.g., 300°C), although the benefit decreased as the desulfation temperature increased from 600°C to 800°C. During the poisonings and desulfations, the SCR catalyst was effective at converting H_2S and COS produced by the LNT back into SO_2. After simulating 47K miles of desulfations, the benefit of the SCR catalyst for NO_x conversion on the 60/5 test was minimal, regardless of the aging temperature. However, the rich purge time was increased to 6 seconds after simulating 73K and 100K miles, and the benefit of the SCR catalyst for low temperature NO_x conversion was observed again for all four desulfation temperatures. These results suggested that, as the LNT+SCR system ages on a vehicle, the rich purge time may need to be increased to maintain the benefit of the SCR catalyst for low temperature NO_x conversion. This can be attributed to a decrease in the purge kinetics of the LNT with thermal aging. The optimal desulfation temperature for this LNT+SCR system was 750°C, as lower temperatures resulted in incomplete desulfations and consequently lower NO_x conversions at high temperatures, while 800°C desulfations resulted in thermal degradation.
机译:进行了一项实验室研究,以评估硫中毒和脱硫温度对LNT +(Cu / SCR)原位系统NO_x转化的影响。使用A / F比率调制将四个LNT +(Cu / SCR)系统在600、700、750和800°C下无硫老化4.5小时,以表示在不同温度下的23K英里脱硫。 NO_x转换测试仅在LNT和LNT + SCR系统上使用60 s稀薄/ 5 s浓循环进行。然后将催化剂在400°C的温度下进行硫中毒,并进行四次脱硫,并根据60/5的测试结果进行重新评估。将该测试序列再重复3次,以代表100K英里的脱硫。在模拟了23K英里的脱硫之后,Cu基SCR催化剂在低温(例如300°C)下提高了LNT的NO_x转化率,尽管随着脱硫温度从600°C升高到800°C而降低了收益。在中毒和脱硫过程中,SCR催化剂可有效地将LNT产生的H_2S和COS转化回SO_2。在模拟了47K英里的脱硫之后,无论老化温度如何,SCR催化剂在60/5测试中对NO_x转化的益处都是最小的。但是,在模拟73K和100K英里后,浓吹扫时间增加到6秒,并且在所有四个脱硫温度下都再次观察到SCR催化剂对低温NO_x转化的好处。这些结果表明,随着LNT + SCR系统在车辆上老化,可能需要增加浓吹扫时间以保持SCR催化剂在低温NO_x转化中的优势。这可以归因于LNT的吹扫动力学随热老化而降低。该LNT + SCR系统的最佳脱硫温度为750°C,因为较低的温度会导致脱硫不完全,从而导致高温下的NO_x转化率降低,而800°C的脱硫则会导致热降解。

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