Method for the Cleaning of Exhaust Gas from a Compression Ignition Engine

Abstract

A method for the cleaning of exhaust gas from a compression ignition engine, comprising the steps of injecting a first amount of an aqueous urea solution into the gas; in a first mode of operation and at an exhaust gas temperature of between 150 and 220° C. hydrolysing the first amount of urea to ammonia reducing agent in presence of a first catalyst comprising vanadium oxide supported on titania and subsequently removing part of nitrogen oxides contained in the exhaust gas by contacting the gas mixed with the ammonia reducing agent through a second catalyst comprising platinum on titania and/or alumina; and in a second mode of operation and at an exhaust gas temperature above 220° C. removing a part of the nitrogen oxides in presence of the first catalyst and the ammonia reducing agent and subsequently oxidising hydrocarbons, carbon monoxide and remaining amount of the ammonia reducing agent further contained in the exhaust gas by passing the gas through the second catalyst.

1 - 8 . (canceled) 
     
     
         9 . A system for cleaning an exhaust gas from a compression ignition engine, comprising
 a first catalyst, which is a selective catalytic reduction (SCR) catalyst comprising vanadium oxide supported on titania,   a second catalyst, which is a diesel oxidation (DOC) catalyst comprising platinum on titania and/or alumina, close coupled with the first catalyst, and   a urea injector arranged upstream of the first catalyst,   wherein the first catalyst is arranged close to the compression ignition engine such that exhaust gas therefrom heats the first catalyst to a first temperature resulting in catalytic hydrolysis of aqueous urea into ammonia and then heats the second catalyst to a second temperature resulting in catalytic reduction of NOx,   said system is capable of operating in a first mode and a second mode, wherein   in the first mode of operation the exhaust gas comprising the aqueous urea solution reaches an exhaust gas temperature of between 150 and 220° C. and (a) the aqueous urea solution is catalytically hydrolysed to an ammonia reducing agent by contacting with the first catalyst and (b) a part of the nitrogen oxides contained in the exhaust gas are subsequently removed in the exhaust gas mixed with the ammonia reducing agent by contacting with the second catalyst arranged downstream of the first catalyst; and   in the second mode of operation the exhaust gas comprising the aqueous urea solution reaches an exhaust gas temperature above 220° C. and (a) the aqueous urea solution is decomposed to the ammonia reducing agent and a part of the nitrogen oxides contained in the exhaust gas is removed by reacting the part of the nitrogen oxides with the ammonia reducing agent in presence of the first catalyst and (b) subsequently oxidising hydrocarbons, carbon monoxide, and ammonia in the exhaust gas leaving the first catalyst by contacting the exhaust gas with the second catalyst.   
     
     
         10 . The system of  claim 9 , wherein the first catalyst further comprises tungsten oxide. 
     
     
         11 . The system of  claim 9 , wherein the second catalyst further comprises palladium. 
     
     
         12 . The system of  claim 9 , wherein an ammonia oxidation catalyst is layered on at least part of the second catalyst. 
     
     
         13 . The system of  claim 12 , wherein the ammonia oxidation catalyst comprises platinum and zeolites promoted with iron and/or copper. 
     
     
         14 . The system of  claim 9 , wherein the first catalyst further comprises a zeolite SCR catalyst. 
     
     
         15 . The system of  claim 14 , wherein the zeolite SCR catalyst comprises at least one of Y-zeolite, beta-zeolite, SAPO-zeolites and chabazites. 
     
     
         16 . The system of  claim 9 , wherein the first catalyst and second catalyst are arranged in a single catalyst unit.