cette régénération thermique s'effectue après quelques centaines de kilomètres environ. Cependant, si les températurestempératures`températuresà ce niveau de la ligne d'´ echappement augmentent l'efficacité du catalyseur (température d'activation du catalyseur atteinte plus rapidement), l'exotherme engendré par la régénération provoque des fuites importantes d'ammoniac, composé fortement odorant ,
excédent de NH 3 issu du premier catalyseur SCR-FAP etéviteretéviter leur rejet dans l'environnement. Une conséquence non négligeable est que l'on pourra de cette façon, réduiré egalement l'excédent de NO x non traité par le premierélémentpremierélément catalytique et améliorer l'efficacité globale de l'architecture. Cette architecture nécessite donc un moyen de contrôle spécifique permettant d'´ eviter les fuites en ammoniac issue des catalyseurs mais aussi d'en optimiser le fonctionnement globaì a travers la gestion des ,
Une stratégie de contrôle du catalyseur SCR-FAP (seul dans l'architecture) est proposée Elle consiste simplement en la diminution voire l'arrêt de l'injection d'urée dans la ligne d'´ echappement avant et pendant les phases de régénération permettant de prévenir d'´ eventuelles fuites d'ammoniac. Un système de mesure de résistance fluidique (cf ,
Nous pouvons faire le constat suivant : cette méthode a pour inconvénient d'´ eviter lesémissions lesémissions polluantes (en diminuant l'apport en NH 3 ) en dépit desémissionsdesémissions de NO x . En effet, pendant les phases de régénération o` u l'on réduit l'apport en ammoniac, l'efficacité du catalyseur est détériorée, et on ne traite plus les NO x de façon efficace ,
Nous proposons de tirer profit du catalyseur en aval de l'architecture décrite en Figure 5.3 afin de contrôler au mieux et de façon continue, les NO x et le NH 3 , en adaptant la stratégie d'injection d'urée suivant les plages de température d'entrée dans lesquelles on se trouve. Cette procédure s'effectue en régulant demanì ere précise chacun des stocks de NH 3 des catalyseurs SCR-FAP et SCR de la ligne d'´ echappement. Cela permet d'´ eviter la pollution en NH 3 tout en préservant l'efficacité de traitement des NO x . Dans cette application, p.84 ,
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