Oxidation Catalyst for a Lean Burn Internal Combustion Engine

Abstract

An apparatus is disclosed. The apparatus comprises a lean-burn internal combustion engine, engine management means and an exhaust system for treating exhaust gas of the engine. The exhaust system comprises a first oxidation catalyst disposed on a first honeycomb monolith substrate. The first oxidation catalyst comprises platinum supported on a first metal oxide support comprising at least one reducible oxide, and is substantially free of alkali metals and alkaline earth metals. The engine management means is arranged, when in use, intermittently to modulate the lambda composition of the exhaust gas entering the first oxidation catalyst to a rich lambda composition.

1 - 26 . (canceled) 
     
     
         27 . A method of recovering an oxidation activity of a first oxidation catalyst aged in an exhaust gas of a lean-burn internal combustion engine, which first oxidation catalyst comprising platinum supported on a first metal oxide support and disposed on a honeycomb substrate monolith, which method comprising the step of intermittently contacting the first oxidation catalyst with exhaust gas modulated to a rich lambda composition, wherein the first metal oxide support comprises at least one reducible oxide and wherein the first oxidation catalyst is substantially free of alkali metals and alkaline earth metals. 
     
     
         28 . The method according to  claim 27 , wherein the at least one reducible oxide is selected from the group consisting of oxides, composite oxides and mixed oxides of one or more metal selected from the group consisting of manganese, iron, tin, copper, cobalt and cerium, and stabilised homologues thereof. 
     
     
         29 . The method according to  claim 28 , wherein the at least one reducible oxide comprises at least one of MnO 2 , Mn 2 O 3 , Fe 2 O 3 , SnO 2 , CuO, CoO and CeO 2 . 
     
     
         30 . The method according to  claim 28 , wherein the stabilised homologue of CeO 2  comprises zirconia, at least one non-cerium rare earth oxide or both zirconia and at least one non-cerium rare earth oxide. 
     
     
         31 . The method according to  claim 28 , wherein the first metal oxide support consists essentially of bulk at least one reducible oxide or optionally stabilised homologues thereof. 
     
     
         32 . The method according to  claim 28 , wherein the at least one reducible oxide or optionally stabilised homologue thereof is supported on the first metal oxide support with the platinum. 
     
     
         33 . The method according to  claim 27 , wherein the first oxidation catalyst disposed on the monolith substrate has a platinum group metal loading of >10 g/ft 3 . 
     
     
         34 . The method according to  claim 27 , wherein the first oxidation catalyst comprises palladium supported on the first metal oxide support in combination with the platinum. 
     
     
         35 . The method according to  claim 27 , wherein the first oxidation catalyst comprises at least one molecular sieve. 
     
     
         36 . The method according to  claim 35 , wherein the at least one molecular sieve comprises at least one precious metal and either (i) copper, (ii) iron, or (iii) copper and iron. 
     
     
         37 . The method according to  claim 27 , wherein the first oxidation catalyst is combined with a second oxidation catalyst different from the first oxidation catalyst, which second oxidation catalyst comprises at least one precious metal supported on a second metal oxide support. 
     
     
         38 . The method according to  claim 27 , wherein the first honeycomb monolith substrate, and, where present, a second honeycomb monolith substrate, is disposed upstream of a catalysed filter for filtering particulate matter from the exhaust gas. 
     
     
         39 . The method according to  claim 27 , wherein the first honeycomb substrate monolith is disposed upstream of a monolith substrate comprising a catalyst for selectively reducing oxides of nitrogen using a nitrogenous reductant. 
     
     
         40 . The method according to  claim 39 , wherein the monolith substrate is a flow-through monolith substrate.