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Enhanced Low-Temperature NOx Conversion by High-Frequency Hydrocarbon Pulsing on a Dual Layer LNT-SCR Catalyst

机译:在双层LNT-SCR催化剂上通过高频烃脉冲增强的低温NOx转化

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Current NOx emission reduction systems, selective catalytic reduction (SCR) and NOx storage and reduction (NSR), function well after achieving their operation temperature (typically ca. 250℃) but have unsatisfactory NOx conversion at lower exhaust temperatures encountered during cold start and low load operation. The reduced exhaust temperature of advanced diesel engines with higher fuel efficiency challenges the low-T NOx reduction. We report here a new concept of high low-T deNOx efficiency of up to 80% at a feed temperature of ca. 200℃ at relevant space velocities (70k h~(-1)). It utilizes high-frequency hydrocarbon pulsing on a dual-layer LNT-SCR monolithic catalyst under lean conditions. This system has the potential to expand the operating temperature window of the conventional deNOx devices. Inspired by Toyota's Di-Air ("Diesel NO_x aftertreatment by Adsorbed Intermediate Reductants) process [1], the proposed dual-layer LNT-SCR operation utilizes rapid short-cycle injection of hydrocarbons to increase the NOx conversion at low temperatures (< 250℃). The new operation exploits the reported Di-Air mechanism which involves generation of short-lived intermediates in the LNT base layer that can be captured and utilized by a top layer SCR-zeolite catalyst for incremental NOx conversion. Our experiments consisted of rapid short cyclic injection of propene into a lean NOx stream fed to an aged LNT-SCR dual-layer catalyst. High frequency HC pulsing on the dual-layer reduced the light-off temperature by ca. 50℃ below that of an LNT catalyst subjected to conventional NSR cycling. The enhanced low-T performance can be attributed to both chemical and thermal effects. Under high frequency operation the deposited SCR layer enables utilization of intermediate species (C_xH_yO_z and C_xH_yO_zN_t) and appreciable storage of heat both generated from oxidation of the hydrocarbon by O_2/NOx in the underlying LNT layer. Under fast cycling the low-T NOx conversion of the dual-layer catalyst exceeds that of either the LNT alone or of LNT-SCR dual-brick catalysts. Increased PGM loading of the dual-layer catalyst to 120 g/ft~3 decreases the light-off temperature to a feed temperature of around 175℃.
机译:现有的NOx减排系统,选择性催化还原(SCR)和NOx储存与还原(NSR),在达到其工作温度(通常约为250℃)后即可正常运行,但在冷启动和低温下遇到较低的排气温度时,其NOx转化率不能令人满意。加载操作。具有更高燃油效率的先进柴油发动机的排气温度降低对低T NOx排放提出了挑战。我们在这里报告了一个新的概念,即在大约200℃的进料温度下,高低T脱硝效率高达80%。在相关空速(70k h〜(-1))下为200℃。它在稀薄条件下在双层LNT-SCR整体催化剂上利用高频烃脉冲。该系统具有扩大传统脱硝设备的工作温度范围的潜力。受丰田Di-Air(吸附式中间还原剂对柴油机NO_x后处理)工艺的启发[1],建议的双层LNT-SCR操作利用碳氢化合物的快速短周期注入来提高低温(<250℃)下的NOx转化率。 )。该新工艺利用了报道的Di-Air机理,该机理涉及在LNT基础层中生成短寿命的中间体,该中间体可以被顶层SCR沸石催化剂捕获并利用以进行增量NOx转化。将丙烯循环注入稀的NOx料流中,该稀NOx料流送入老化的LNT-SCR双层催化剂,双层上的高频率HC脉冲将起燃温度降低了约50℃,该温度比常规条件下的LNT催化剂低。 NSR循环。增强的低T性能可以归因于化学和热效应。在高频操作下,沉积的SCR层可以利用中间物种(C_xH_yO_z和C_xH_y O_zN_t)和热量的显着存储,它们都是由底层LNT层中O_2 / NOx氧化烃所产生的。在快速循环下,双层催化剂的低T NOx转化率超过了单独的LNT或LNT-SCR双砖催化剂的转化率。双层催化剂的PGM负载增加至120 g / ft〜3时,起燃温度降低至进料温度约175℃。

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