SAE Technical Paper Series 2000
DOI: 10.4271/2000-01-0188
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An Integrated SCR and Continuously Regenerating Trap System to Meet Future NOx and PM Legislation

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Cited by 58 publications
(15 citation statements)
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“…The auxiliary oxidation catalyst in this system is used to increase the NO 2 concentration in the exhaust gases. Laboratory studies [Chandler et al 2000;Gieshoff 2001] have confirmed that the efficiency in NO X abatement increases with an elevated NO 2 concentration at the inlet of the main SCR catalyst. The optimum NO 2 /NO ratio was reported to be near 1:1 [Gieshoff 2000;Koebel et al 2002;Goo et al 2007] .…”
Section: Scr Technologymentioning
confidence: 92%
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“…The auxiliary oxidation catalyst in this system is used to increase the NO 2 concentration in the exhaust gases. Laboratory studies [Chandler et al 2000;Gieshoff 2001] have confirmed that the efficiency in NO X abatement increases with an elevated NO 2 concentration at the inlet of the main SCR catalyst. The optimum NO 2 /NO ratio was reported to be near 1:1 [Gieshoff 2000;Koebel et al 2002;Goo et al 2007] .…”
Section: Scr Technologymentioning
confidence: 92%
“…Studies have reported that the majority of the slipped ammonia (NH 3 ) undergoes complete oxidation to NO and NO 2 over the ASC [Havenith and Verbeek 1997]. NH 3 concentrations at the tailpipe, resulting from NH 3 slip [Chandler et al 2000] , have been found to be below 25 parts per million, the ambient ammonia ACGIH TWA/TLV (American Conference of Governmental Industrial Hygienists, time-weighted average / threshold limit value). Therefore, a possible NH 3 slip from an SCR system should not pose a problem and would not require additional ventilation air in underground work areas.…”
Section: Scr Technologymentioning
confidence: 99%
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“…Maintaining "fast-SCR" or optimum NO2/NOx ratios has further potential to increase the SCR performance, even at lower temperatures (Koebel et al, 2002). From a study performed by Chandler, shows that the control of SCR catalyst activity can be significantly varied by having NO2 in the exhaust gas, especially at low exhaust temperatures (Chandler et al, 2000). Figure 2, illustrates such catalyst activities where at lower temperature ranges (175 to 300°C), NOx conversion efficiency tends to remain above 90% when feeding NO2 as a feed gas than compared to not having any NO2 at all in the exhaust stream.…”
Section: Urea-scr Catalytic Reactionsmentioning
confidence: 99%
“…[13][14][15] SCR systems require the use of urea to generate ammonia on-board a vehicle to reduce NO x . 16 Urea fluid is not traditionally found on-board a vehicle.…”
Section: Introductionmentioning
confidence: 99%