汽车工程
汽車工程
기차공정
AUTOMOTIVE ENGINEERING
2014年
10期
1193-1196
,共4页
唐韬%张俊%帅石金%曹东晓
唐韜%張俊%帥石金%曹東曉
당도%장준%수석금%조동효
柴油机%后处理系统%一氧化二氮%排放特性
柴油機%後處理繫統%一氧化二氮%排放特性
시유궤%후처리계통%일양화이담%배방특성
diesel engine%aftertreatment system%N2 O%emission characteristics
对一台重型柴油机的后处理系统进行台架试验,研究其N2 O生成特性,包括在颗粒捕集器( DPF)主动再生、选择性催化还原( SCR)反应和泄漏氨气在氨气氧化催化器( ASC)的氧化过程中一氧化二氮( N2 O)的生成规律。结果表明,DPF主动再生时,喷入排气管的柴油与排气中的氮氧化物在催化剂表面发生副反应生成N2 O,其生成量随DOC出口温度的升高呈现先增后减的趋势。在SCR反应中,Cu沸石催化剂生成的N2 O最多,Cu/Fe复合催化剂次之,而其它催化剂生成的N2 O很少;对于前两种催化剂,随着温度的升高,N2 O生成量呈先增后减再增的趋势。从SCR催化器泄漏的氨气在ASC中被氧化生成N2 O,温度在200~250益时N2 O生成量较大。
對一檯重型柴油機的後處理繫統進行檯架試驗,研究其N2 O生成特性,包括在顆粒捕集器( DPF)主動再生、選擇性催化還原( SCR)反應和洩漏氨氣在氨氣氧化催化器( ASC)的氧化過程中一氧化二氮( N2 O)的生成規律。結果錶明,DPF主動再生時,噴入排氣管的柴油與排氣中的氮氧化物在催化劑錶麵髮生副反應生成N2 O,其生成量隨DOC齣口溫度的升高呈現先增後減的趨勢。在SCR反應中,Cu沸石催化劑生成的N2 O最多,Cu/Fe複閤催化劑次之,而其它催化劑生成的N2 O很少;對于前兩種催化劑,隨著溫度的升高,N2 O生成量呈先增後減再增的趨勢。從SCR催化器洩漏的氨氣在ASC中被氧化生成N2 O,溫度在200~250益時N2 O生成量較大。
대일태중형시유궤적후처리계통진행태가시험,연구기N2 O생성특성,포괄재과립포집기( DPF)주동재생、선택성최화환원( SCR)반응화설루안기재안기양화최화기( ASC)적양화과정중일양화이담( N2 O)적생성규률。결과표명,DPF주동재생시,분입배기관적시유여배기중적담양화물재최화제표면발생부반응생성N2 O,기생성량수DOC출구온도적승고정현선증후감적추세。재SCR반응중,Cu비석최화제생성적N2 O최다,Cu/Fe복합최화제차지,이기타최화제생성적N2 O흔소;대우전량충최화제,수착온도적승고,N2 O생성량정선증후감재증적추세。종SCR최화기설루적안기재ASC중피양화생성N2 O,온도재200~250익시N2 O생성량교대。
A bench test is conducted on the after-treatment system of a heavy-duty diesel engine to study its N2 O formation characteristics, including the N2 O formation rule in the processes of active regeneration in diesel par-ticulate filter ( DPF) , the reaction in selective catalytic reduction ( SCR) system and the oxidation in ammonia slip catalyst ( ASC) . The results show that in active regeneration of DPF, N2 O is formed in a by-action occurring on cat-alyst surface and between diesel fuel injected into exhaust pipe and nitrogen oxides in exhaust gas. With the increase in the temperature of diesel oxidation catalyst exit, the quantity of N2 O produced shows a tendency of rise first and then fall. In the reaction of SCR system, the most N2 O is formed with Cu-zeolite catalyst, the less with Cu/Fe com-pound catalyst and very few with other catalysts, and for former two catalysts, the quantity of N2 O produced shows a tendency of "rise then fall and rise again" when the temperature of SCR catalyst increases. The ammonia escaped from SCR also produces N2 O due to its oxidation in ASC with a rather large quantity of N2 O formed at a temperature range of 200~250℃.