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TWC+LNT/SCR Systems for Satisfying Tier 2, Bin 2 Emission Standards on Lean-Burn Gasoline Engines

机译:TWC + LNT / SCR系统,用于满足Tier 2,Bin 2瘦燃烧汽油发动机的排放标准

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A laboratory study was performed to assess the potential capability of TWC+LNT/SCR systems to satisfy the Tier 2, Bin 2 emission standards for lean-burn gasoline applications. It was assumed that the exhaust system would need a close-coupled (CC) TWC, an underbody (U/B) TWC, and a third U/B LNT/SCR converter to satisfy the emission standards on the FTP and US06 tests while allowing lean operation for improved fuel economy during select driving conditions. Target levels for HC, CO, and NO_x during lean/rich cycling were established. Sizing studies were performed to determine the minimum LNT/SCR volume needed to satisfy the NO_x target. The ability of the TWC to oxidize the HC during rich operation through steam reforming was crucial for satisfying the HC target. Temperature studies indicated that the CC TWC needed to operate at a minimum of 500°C to provide good steam reforming activity, while the LNT/SCR needed to operate between 300 and 350°C to satisfy the NO_x slip target while minimizing the slip of NH_3, N_2O, and HC during the purges. Sulfur poisoning increased the HC slip by degrading the steam reforming reaction, and the sulfur increased the NO_x slip by decreasing the NO_x storage capacity of the LNT. Both the TWC and LNT/SCR could be desulfated with rich exhaust at 700°C. However, it was projected that the ability to obtain 700°C at the underbody LNT/SCR location would be difficult without additional exhaust hardware, such as fuel injectors or air pumps. Consequently, development of the LNT/SCR system was terminated in favor of a passive TWC+SCR approach because of its superior sulfur tolerance. Investigations into the passive TWC+SCR approach are discussed in a companion SAE paper.
机译:进行实验室研究以评估TWC + LNT / SCR系统的潜在能力,以满足瘦燃烧汽油应用的第2层,BIN 2排放标准。假设排气系统需要紧密耦合(CC)TWC,底部(U / B)和第三U / B LNT / SCR转换器,以满足FTP和US06测试的排放标准,同时允许精益运行在选择驾驶条件下改善燃油经济性。建立了HC,CO和NO_X的目标水平,建立了精益/富循环期间。进行尺寸研究以确定满足NO_X目标所需的最小LNT / SCR体积。通过蒸汽重整在富含蒸汽重整过程中氧化HC的能力对于满足HC靶标至关重要。温度研究表明,CC TWC需要至少500℃,以提供良好的蒸汽重整活性,而LNT / SCR需要在300到350°C之间运行以满足NO_X滑动目标,同时最小化NH_3的滑动净化过程中的N_2O和HC。硫中毒通过降解蒸汽重整反应来增加HC滑移,通过降低LNT的NO_X储存容量,硫增加NO_X滑动。 TWC和LNT / SCR都可以在700℃下用浓排气脱硫。然而,预计将在没有额外的排气硬件(例如燃料喷射器或空气泵)的情况下难以提供700°C的能力。因此,由于其优异的硫耐受性,终止了LNT / SCR系统的开发支持被动TWC + SCR方法。在伴侣SAE论文中讨论了进入被动TWC + SCR方法的调查。

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