The amount of nitrogen oxides (NOx) exhausted from a diesel engine is typically dependent on the air-to-fuel ratio used to run the engine, along with several other factors, including, for example, combustion temperatures and the amount of oxygen present in the cylinder(s) during combustion events. Engines that operate solely under steady-state conditions are typically run using a lean burn mixture having a high air-to-fuel ratio. Desired torque, fuel economy and containable NOx emissions can be achieved through combustion optimization. However, during transient events, such as sudden changes in the load on the engine, achieving NOx containment through combustion optimization becomes challenging.
An aspect of an illustrated embodiment is an exhaust system for the treatment of an exhaust gas generated during the operation of a diesel engine. The exhaust system includes an upstream treatment housing having a dual functionality catalyst comprising a three way catalyst and a diesel oxidation catalyst. The three way catalyst of the dual functionality catalyst has a formulation configured for the reduction of nitrogen oxides in the exhaust gas when the diesel engine is operating in stoichiometric or rich exhaust conditions. The diesel oxidation catalyst of the dual functionality catalyst is configured to oxidize hydrocarbons and carbon monoxide in the exhaust gas when the diesel engine is operating under lean exhaust conditions. The system also includes a main exhaust gas treatment system positioned downstream of the upstream treatment housing. The main exhaust gas treatment system has at least one of the following: (1) a diesel oxidation catalyst configured for the oxidation of hydrocarbons in the exhaust gas; and/or (2) a three-way catalyst formulation for the reduction of nitrogen oxides in the exhaust gas.
Another aspect of an illustrated embodiment is an exhaust system for the treatment of an exhaust gas generated during the operation of a diesel engine that includes an upstream treatment housing that has a dual functionality catalyst comprising a three-way catalyst and a diesel oxidation catalyst. The three way catalyst has a formulation configured for the reduction of nitrogen oxides in the exhaust gas when the diesel engine is operating in stoichiometric or rich exhaust conditions. The diesel oxidation catalyst of the dual functionality catalyst is configured to oxidize hydrocarbons and carbon monoxide in the exhaust gas when the diesel engine is operating under lean exhaust conditions. The exhaust system also includes a main exhaust gas treatment system positioned downstream of the upstream treatment housing. The main exhaust gas treatment system has a second dual functionality catalyst comprising: (1) a diesel oxidation catalyst configured for the oxidation of hydrocarbons and carbon monoxide present in the exhaust gas when the engine is operating under lean exhaust conditions; and (2) a three-way catalyst formulation configured for the reduction of nitrogen oxides when the diesel engine is operating in stoichiometric or rich exhaust conditions.
Another aspect of an illustrated embodiment is an exhaust system for the treatment of an exhaust gas generated during the operation of a diesel engine that includes a turbine having an inlet and an outlet, the exhaust gas exiting the outlet at a first temperature. The exhaust system also includes an upstream treatment housing operably connected to the outlet of the turbine. The upstream treatment housing has a first dual functionality catalyst comprising a first three way catalyst and a first diesel oxidation catalyst. The first three way catalyst having a formulation configured for the reduction of nitrogen oxides in the exhaust gas. The first diesel oxidation catalyst is configured to oxidize hydrocarbons and carbon monoxide in the exhaust gas. The upstream treatment housing is positioned in the exhaust system to receive exhaust gas at a second temperature that is within at least approximately 5 degrees Celsius of the first temperature. The exhaust gas treatment system also includes a main exhaust gas treatment system positioned downstream of the upstream treatment housing. The main exhaust gas treatment system has a second dual functionality catalyst comprising: (1) a second diesel oxidation catalyst configured to oxidize hydrocarbons and carbon monoxide in the exhaust gas; and (2) a second three-way catalyst formulation configured for the reduction of nitrogen oxides in the exhaust gas.
The air may flow through the intake manifold 30 and to cylinders 32 of the engine 34, where the air may be used in a combustion event(s) that is used to displace the pistons of the engine 34, thereby transmitting the force of the combustion event(s) into mechanical power that is used to drive the drivetrain of the associate vehicle. The resulting hot exhaust gas produced by the combustion event(s) may flow out of the cylinders 32 and engine 34 through an exhaust port(s) and along an exhaust line 36.
At least a portion of the hot exhaust gas from the engine 34 may be diverted from the exhaust line 36 and to an exhaust gas recirculation (EGR) system 38. The EGR system 38 is configured to recirculate the diverted exhaust gas back to the intake manifold 30. However, before the EGR system 38 recirculates exhaust gas, the exhaust gas is typically cooled by an EGR cooler 40 or heat exchanger. A coolant, such as antifreeze mixtures or non-aqueous solutions, among others, typically circulates through the EGR cooler 40. According to some designs, the coolant and/or the heated exhaust gases flow through tubes, a jacket, or other forms of conduits in the EGR cooler 40. The EGR cooler 40 may be configured so that heated exhaust gases flow around and/or over tubes containing flowing coolant, or vice versa, causing heat from the exhaust gas to be transferred to the coolant. The EGR cooler 40 may also include fins that assist with the transfer of heat from the exhaust gas to the coolant. After exiting the EGR cooler 40, the cooled exhaust gas is delivered to the intake manifold 30, thereby allowing the cooled exhaust gas to enter into the cylinders 32 with the air that was delivered to the intake manifold 30 through the intake line 20.
Exhaust gas that is not diverted to the EGR system 38 may continue to flow along the exhaust line 36 and be delivered to a high pressure turbine 42. The exhaust gas, and the heat entrained therein, may then at least assist in driving the high pressure turbine 42. Power generated by the high pressure turbine 42 may at least in part be used to power or drive the high pressure compressor 26.
Exhaust gas exiting the high pressure turbine 42 may then flow along the exhaust line 36 to an inlet 45 of a low pressure turbine 44. The low pressure turbine 44 may also be configured to be driven by the exhaust gas, and the heat entrained therein. Additionally, operation of the low pressure turbine 44 may be used to power or drive the low pressure air compressor 22. Although
According to the embodiment shown in
The upstream treatment housing 12 includes a TWC formulation that is used to reduce the quantity of NOx in the exhaust gas. Such a TWC formulation may include chemical elements such as, for example, platinum, palladium, and/or rhodium, and various alkali, alkaline earth, and/or rare earth oxides. According to certain embodiments, the upstream treatment housing 12 may be coated with a dual functionality catalyst that includes the TWC formulation as part of a diesel oxidation catalyst (DOC). Thus, a single formulation in the upstream housing, namely the formulation of the dual functionality catalyst, may provide the benefits of both a TWC and/or DOC, depending on the operating conditions of the engine, and, more specifically, the conditions of the exhaust gas. According to such embodiments, during normal lean conditions, the dual functionality catalyst in the upstream treatment housing 12 may serve as an oxidation catalyst for oxidizing hydrocarbons and carbon monoxide to water and carbon dioxide. Operation of the engine during lean exhaust conditions may occur when, for example, the engine is operating under a traditional mode where there may be excess of O2 present in the exhaust, such as relatively high air-to-fuel ratios. Such operations would include when the engine is operating under cruise control or operation, decelerations, or small rates of increase in high power demand. During engine usage, with the exception of occasional transient events, the engine usually is operating at under lean exhaust conditions, which facilitate the dual functionality catalyst to operate at as a DOC. The DOC of the dual functionality catalyst is configured for chemically converting pollutants in the exhaust stream under lean exhaust conditions. For example, the DOC of the dual functionality catalyst may contain palladium and platinum which serve as catalysts to oxidize hydrocarbons and carbon monoxide into carbon dioxide and water in the following reactions:
CO+½O2→CO2; and
[HC]+O2→CO2+H2O.
According to certain embodiments, the dual functionality catalyst may require the possible addition of an oxygen storage component (OSC) and Rhodium. The dual functionality catalyst may also include components commonly found in DOC formulations, such as, for example, platinum (Pt) and/or palladium (Pd) on a high surface area alumina and catalyst stabilizers, such as, for example, BaSO4, that may minimize PGM sintering at high temperatures (>500° C.).
The TWC, on the other hand, operates optimally at or near lambda=1. At these conditions, the TWC oxidizes hydrocarbons and carbon monoxide while simultaneously reducing NOx to nitrogen. The reaction occurs via dissociative adsorption of NO onto the metal surface to create adsorbed N and O atoms ([N]ads and [O]ads). The adsorbed N atom will combine with another nitrogen atom on the surface and form nitrogen gas. The adsorbed O atom reacts with hydrocarbons, carbon monoxide and/or hydrogen to form carbon dioxide and water and regenerate the metal surface where NO can adsorb.
NO→[N]ads+[O]ads
2[N]ads→N2
CO+[O]ads→CO2; and
[HC]+[O]ads→CO2+H2O.
The presence of the TWC formulation as part of the DOC of the dual functionality catalyst in the upstream treatment housing 12 allows for both the treatment of hydrocarbon and carbon monoxide by the DOC while a diesel engine 34 runs primarily lean of stoichiometry as well as NOx reduction by the TWC during rich excursions along with the potential for accompanying NH3 formation. Rich or stoichiometric exhaust conditions may occur when the diesel engine is required to output high power over a short period of time, such as events including, for example, rapid acceleration. The addition of the upstream treatment housing 12, and the TWC contained therein, upstream of the main exhaust treatment system 14 also provides for additional catalyst volume (up to 15% of the main catalyst volume) with minimal packaging issues observed with a main or full-sized catalyst, such as the DOC or TWC housings 16, 46 of the main exhaust treatment system 14.
Additionally, according to certain embodiments, the upstream treatment housing 12 is in relative close proximity, such as, for example, between 6 to 12 inches, to the low pressure turbine 14 so as to prevent or minimize a decrease in the temperature of the exhaust gas, such as, for example, a temperature loss no greater than around 5° Celsius, as the exhaust gas passes from the low pressure turbine 44 to the upstream treatment housing 12. Thus, the temperature of the exhaust gas entering the upstream treatment housing 12 may be approximately the same as the temperature of the exhaust gas exiting the low pressure turbine 44. By generally maintaining the of temperature exhaust gas, the exhaust gas may arrive at the upstream treatment housing 12 at a temperature necessary for the TWC in the upstream treatment housing 12 to convert/reduce appreciable quantities of NOx in the exhaust gas. Further, by preventing or minimizing a drop in the temperature of the exhaust gas between the low pressure turbine 44 and the upstream treatment housing 12, the exhaust gas in the upstream treatment housing 12 may have a sufficiently high temperature for the conversion/reduction of NOx under cold engine or cold surrounding ambient conditions. Moreover, the temperature of the exhaust gas entering the upstream treatment housing 12 may be sufficient for the conversion/reduction of NOx during transient drive cycles despite the temperature of main exhaust gas treatment system 14, such as the DOC 16, being too low to exhibit appreciable conversion/reduction of NOx.
Further, the presence of the DOC in the upstream treatment housing 12 may also assist during active filter regenerations by serving as a mixing device to homogenize fuel that has been injected into the exhaust gas. Moreover, the DOC in the upstream treatment housing 12 may be used to create an exothermic reaction across components of the main exhaust treatment system 14, such as the DOC and/or TWC housings 16, 46, for burning stored soot on a filter in the main exhaust gas treatment system, such as soot on a diesel particulate filter (DPF) 18.
The exhaust gas exiting the upstream treatment housing 12 may then flow to the main exhaust treatment system 14. For example, according to certain embodiments, the exhaust gas exiting the upstream treatment housing 12 may flow through approximately at least 2 feet of a portion of the exhaust line 36 before reaching the main exhaust treatment system. The length of the exhaust line 36 between the upstream treatment housing 12 and the main exhaust treatment system 14 however may vary, and may be greater than or less than 2 feet. The main exhaust treatment system 14 may include a number of different components. For example, referencing
As shown in