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首页> 外文期刊>Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications >Dynamics of N-2 and N2O peaks during and after the regeneration of lean NOx trap
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Dynamics of N-2 and N2O peaks during and after the regeneration of lean NOx trap

机译:稀薄NOx捕集阱再生期间和之后N-2和N2O峰值的动态

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摘要

The dynamics and selectivity of N-2 and N2O formation during and after the regeneration of a commercial NOx storage catalyst containing Pt, Pd, Rh, Ba on Ce/Zr, Mg/AI and Al oxides was studied with high-speed FTIR and SpaciMS analyzers. The lean/rich cycling experiments (60s/5 s and 60 s/3 s) were performed in the temperature range 200-400 degrees C, using Hy, CO, and C3H6 individually for the reduction of adsorbed NOx. Isotopically labeled (NO)-N-15 was employed in combination with Ar carrier gas in order to quantify the N-2 product by mass spectrometry. N-2 and N2O products were formed concurrently. The primary peaks appeared immediately after the rich-phase inception, and tailed off with breakthrough of the reductant front (accompanied by NH3 product). Secondary N-2 and N2O peaks appeared at the rich-to-lean transition as a result of reactions between surface-deposited reductants/intermediates (CO, HC, NH3, -NCO) and residual stored NOx. At 200-300 degrees C, up to 30% of N-2 and 50% of N2O products originated from the secondary peaks. The N2O/N-2 selectivity ratio as well as the magnitude of secondary peaks decreased with temperature and duration of the rich phase. Among the three reductants, propene generated secondary N-2 peak up to the highest temperature. The primary N-2 peak exhibited a broadened shoulder aligned with movement of reduction front from the zone where both NOx, and oxygen were stored to the NOx-free zone where only oxygen storage capacity was saturated. N-2 formed in the NOx-free zone originated from reaction of NH3 with stored oxygen, while N2O formation in this zone was very low. (C) 2014 Elsevier B.V. All rights reserved.
机译:利用高速FTIR和SpaciMS研究了在Ce / Zr,Mg / Al和Al氧化物上含Pt,Pd,Rh,Ba的商用NOx储存催化剂再生期间和再生后N-2和N2O形成的动力学和选择性。分析仪。在200-400摄氏度的温度范围内进行稀薄/浓循环实验(60s / 5 s和60 s / 3 s),分别使用Hy,CO和C3H6减少吸附的NOx。同位素标记的(NO)-N-15与Ar载气结合使用,以便通过质谱定量N-2产物。 N-2和N2O产物同时形成。富集相开始后,主峰立即出现,并随着还原剂前沿(伴随NH3产物)的突破而逐渐消失。由于表面沉积的还原剂/中间体(CO,HC,NH3,-NCO)与残留的NOx发生反应,在浓淡过渡过程中出现了次要的N-2和N2O峰。在200-300摄氏度下,高达30%的N-2和50%的N2O产物源自次级峰。 N2O / N-2选择性比以及次级峰的幅度随温度和富相持续时间而降低。在这三种还原剂中,丙烯生成的次级N-2达到最高温度。主要的N-2峰表现出与从NOx和氧气都储存的区域到只有NO储存容量饱和的NOx的还原前锋移动一致的宽肩。在无NOx区域中形成的N-2源自NH3与存储的氧气的反应,而在该区域中N2O的形成非常低。 (C)2014 Elsevier B.V.保留所有权利。

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