초록 ▼

An NOx emission system for diesel powered vehicles has a "Y" exhaust system with an NOx adsorber catalyst in each leg and an oxidation catalyst in the combined leg. One bank of cylinders sends exhaust gases to one of the "Y" legs while a second bank of cylinders send exhaust gases to the other "Y" l

An NOx emission system for diesel powered vehicles has a "Y" exhaust system with an NOx adsorber catalyst in each leg and an oxidation catalyst in the combined leg. One bank of cylinders sends exhaust gases to one of the "Y" legs while a second bank of cylinders send exhaust gases to the other "Y" leg. Composition of the exhaust gases in each leg is independently controlled by the engine's ECU so that exhaust gases in one leg are rich for regenerating the NOx adsorber catalyst in that leg while exhaust gas composition in the other leg is lean so that the combined gas stream is always lean and reductant slip is oxidized in the oxidation catalyst.

대표청구항 ▼

The invention claimed is: 1. A system for treating exhaust gases emitted from a vehicle comprising: a) a multi-cylinder diesel engine having a first exhaust manifold in fluid communication with a first plurality of cylinders and a second exhaust manifold in fluid communication with a different seco

The invention claimed is: 1. A system for treating exhaust gases emitted from a vehicle comprising: a) a multi-cylinder diesel engine having a first exhaust manifold in fluid communication with a first plurality of cylinders and a second exhaust manifold in fluid communication with a different second plurality of cylinders; b) a first NOx adsorber catalyst in a first exhaust leg in fluid communication with said first manifold; c) a second NOx adsorber catalyst in a second exhaust leg in fluid communication with said second manifold; d) a common exhaust leg having an inlet in fluid communication with said first and second exhaust legs downstream of said first and second NOx catalysts, said common exhaust leg having an oxidation catalyst therein through which exhaust gases from said first and second legs pass after being combined in said common exhaust leg; and, e) ECU means controlling the composition of exhaust gases in said first exhaust manifold independently of the composition of exhaust gases in said second exhaust manifold in accordance with a programmed routine, to periodically produce rich gases in one exhaust manifold and lean gases in the other exhaust gas manifold and controlling the quantities of combustible gases present in said rich gas and the quantities of oxygen present in said lean gas to produce a combined gas stream in said common exhaust leg upstream of said oxidation catalyst to have a lambda of at least 1.0, and further including NOx sensors upstream and downstream of each NOx adsorber catalyst and lambda sensors upstream and downstream of each NOx adsorber catalyst, said ECU means sensing said NOx sensors to determine the start of said routine and sensing said lambda sensors to determine the end of said routine wherein said ECU means periodically switches the generation of said rich and lean gases from one exhaust manifold to the other. 2. The system of claim 1 wherein said ECU means periodically switches the gases after an NOx adsorber catalyst receiving said rich gas has been regenerated to a set value. 3. The system of claim 1 further including a catalyzed soot filter upstream of each NOx adsorber catalyst either as a separate catalyst or formed integrally with each NOx adsorber catalyst as an upstream bed thereof. 4. The system of claim 1 wherein said NOx adsorber catalyst includes one or more platinum group metals coated on an alkaline or alkaline earth metal oxide carrier support. 5. The system of claim 1 wherein said oxidation catalyst includes a catalyst material comprising bulk ceria and bulk aluminum with a precious metal. 6. The system of claim 1 wherein said NOx adsorber catalyst is a low temperature lean NOx catalyst including platinum and a zeolite. 7. The system of claim 1 wherein said NOx adsorber catalyst is a high temperature lean NOx catalyst including a base metal and a zeolite. 8. The system of claim 1 wherein each cylinder in said first and second plurality has a fuel injectors, said fuel injector in said first cylinder plurality in fluid communication with a first rail and said fuel injectors in said second cylinder plurality in fluid communication with separate second rail and said ECU means controlling the pressure and flow of fuel oil in said first and second rails independently whereby the A/F ratio in each cylinder plurality is independently controlled to produce desired rich or lean exhaust gases from each plurality of cylinders. 9. The system of claim 1 wherein the combined gas stream in said common exhaust leg upstream of said oxidation catalyst having a lambda not less than about 2.0. 10. The system of claim 9 wherein said rich gas has a lambda less than 1.0 and said lean gas has a lambda greater than 1.0. 11. The system of claim 10 wherein said rich gas has a lambda not greater than about 1.0 and said lean gas has a lambda not less than about 2.0. 12. A process for controlling noxious emissions produced by a vehicle equipped with a multi-cylinder diesel engine having separate first and second exhaust manifolds through which discrete first and second pluralities of cylinders, respectively, exhaust their products of combustion as exhaust gases, said engine having a programmable ECU controlling the composition of said exhaust gases produced by said engine, said method comprising the steps of: a) providing a first NOx adsorber catalyst downstream of and in fluid communication with said first exhaust manifold through which a first steam of exhaust gases from said first exhaust manifold pass and a second NOx adsorber catalyst downstream of and in fluid communication with said second exhaust manifold through which a second stream of exhaust gases from said second exhaust manifold pass; b) combining the exhaust gas streams downstream of said first and second NOx adsorber catalysts into a common exhaust stream to produce a substantially mixed common stream of exhaust gases from said first and second exhaust streams; c) providing NOx sensors upstream and downstream of each NOx adsorber catalyst and lambda sensors upstream and downstream of each NOx adsorber catalyst: d) passing said combined stream of exhaust gases through an oxidation catalyst; e) controlling by said ECU with a programmed routine the composition of said exhaust gases in said first exhaust stream independently of the composition of said exhaust gases in said second stream to periodically produce a rich exhaust stream passing through one of said NOx adsorber catalysts and a lean exhaust stream passing through the other adsorber catalyst, and controlling the quantities of combustible gases present in said rich gas and the quantities of oxygen present in said lean gas to produce a combined gas stream in said common exhaust leg upstream of said oxidation catalyst having a lambda of at least 1.0, whereby the NOx catalyst exposed to said rich exhaust stream is regenerated; and, f) sensing with said ECU said NOx sensors to determine the start of said routine and sensing said lambda sensors to determine the end of said routine wherein said ECU periodically switches the generation of said rich and lean gases from one exhaust manifold to the other. 13. The process of claim 12 wherein sufficient oxygen exists in said combined stream to permit oxidation of HC and CO in said oxidation catalyst. 14. The process of claim 12 wherein lambda of said rich exhaust stream is 1.0 or less and lambda of said lean exhaust stream is 1. 0 or greater. 15. The process of claim 14 wherein lambda of said rich exhaust stream is less than 1.0 and lambda of said lean exhaust stream is at least 2.0 or greater. 16. The process of claim 12 further including the step of providing a catalyzed soot filter upstream of each NOx adsorber catalyst or integrated into said NOx adsorber catalyst and periodically changing the composition of the lean exhaust stream to cause the presence of combustibles in the lean exhaust stream sufficient to heat the exhaust gas passing through said catalyzed filter to higher temperatures and thereafter further changing the composition of said lean exhaust gas compositions to generate a pulse of set time duration causing a rich exhaust gas to pass over said NOx adsorber catalyst previously receiving said lean exhaust gas when the bed temperature of said NOx adsorber catalyst is at a temperature sufficient to release sulfur, said sulfur being reduced to H2S and subsequently oxidized in said oxidation catalyst. 17. The process of claim 16 wherein the temperature range at which said NOx adsorber catalyst is catalytically active to store and release NOx is about 150째 C. to about 550째 C. and the temperature range at which said NOx catalyst is catalytically active to release sulfur trapped therein is about 550EC or greater and lambda is less than 1. 18. The process of claim 12 further including the step of causing the composition of said first and second exhaust gases to reverse when one of said NOx adsorber catalysts has been regenerated. 19. The process of claim 18 wherein the lambda values of said first and second exhaust streams are set at values sufficient to assure that a net oxygen content of said combined gas stream is at least 2.0% or greater. 20. The process of claim 19 wherein the net oxygen content of said combined exhaust stream is at least 5.0% or greater. 21. The process of claim 20 wherein the next oxygen content of said combined exhaust stream is at least 8.0% or greater. 22. The process of claim 12 wherein said rich exhaust stream flowing through one of said NOx adsorber catalysts is caused to occur when said one NOx adsorber catalyst has at least 50% or more of its NOx storage sites occupied but saturation of the NOx storage site has not occurred. 23. The process of claim 22 further including the step of ascertaining that the NOx adsorber catalyst bed temperature is within the NOx catalytically active temperature range of the NOx adsorber catalyst before causing said rich exhaust gas composition to be produced. 24. The process of claim 23 further including the step of changing the rich exhaust gas composition to a lean exhaust gas composition when the engine is at a set load. 25. The process of claim 24 further including the step of changing the rich gas composition to a lean gas composition when the NOx adsorber catalyst has been purged of a trapped NOx so that 50% or more of the NOx actuation sites are available for adsorbing NOx. 26. In a process for controlling NOx emissions generated by a vehicular light duty diesel engine using a NOx adsorber catalyst, the improvement comprising the steps of: a) providing a first exhaust manifold in fluid communication only with a first bank of engine cylinders and a first NOx catalyst in fluid communication with said first exhaust manifold; b) providing a second exhaust manifold in fluid communication only with a second bank of different cylinders and a second NOx adsorber catalyst in fluid communication with said second exhaust manifold; c) providing NOx sensors upstream and downstream of each NOx adsorber catalyst and lambda sensors upstream and downstream of each NOx adsorber catalyst; d) sequentially regenerating said NOx adsorber catalysts by first causing said first bank of cylinders to generate a rich exhaust gas stream which passes through said first NOx adsorber catalyst while said second bank of cylinders generate a lean exhaust gas stream which passes through said second NOx adsorber catalyst until said first NOx adsorber catalyst is regenerated and then causing said second bank of cylinders to generate a rich exhaust gas passing through said second NOx adsorber catalyst while said first bank of cylinders generate a lean exhaust gas passing through said first NOx adsorber catalyst; e) combining the exhaust gas streams downstream of said first and second NOx adsorber catalysts into a common exhaust stream to produce a substantially mixed common stream of exhaust gases from said first and second exhaust streams; f) controlling with an ECU programmed routine the quantities of combustible gases present in said rich gas and the quantities of oxygen present in said lean gas to produce a combined gas stream having a lambda of at least 1.0; and, g) sensing with said ECU said NOx sensors to determine the start of said routine and sensing said lambda sensors to determine the end of said routine wherein said ECU periodically switches the generation of said rich and lean gases from one exhaust manifold to the other. 27. The improved process of claim 26 wherein said rich and lean exhaust gas streams in said exhaust manifolds are produced by independently varying the A/F ratio in each cylinder bank to produce said exhaust gas compositions, said process further including the step of providing separate first and second hydraulic rails in fluid communication with fuel injectors in said first and second cylinder banks, respectively, and independently controlling the pressure and flow of fuel oil in each rail to assure a desired A/F ratio in each bank of cylinders. 28. The improved process of claim 26 further including the steps of combining passing said combined gas stream through an oxidation catalyst to minimize emission slip. 29. The improved process of claim 28 further including the step of providing a catalyzed soot filter upstream of and adjacent to each NOx adsorber catalyst and when the temperature of said NOx adsorber catalyst through which a lean exhaust gas is flowing reaches a set temperature, momentarily changing the lean exhaust gas composition to a rich exhaust gas composition for releasing sulfur trapped in said NOx adsorber catalyst. 30. The improved process of claim 28 further including the step of setting the richness of said rich exhaust gases and the leanness of said lean exhaust gases to lambda values which produce said combined exhaust gas stream having a next oxygen content of 2.0% or more. 31. The improved process of claim 30 wherein the net oxygen content of said combined exhaust stream must be at least 5.0% or more. 32. The improved process of claim 31 wherein the net oxygen content of said combined exhaust stream must be at least 8.0% or more.