Combustion engines may employ emission controls or systems that are configured to reduce the amount of nitrogen oxides (NOx) present in the engine's exhaust gas. One approach to controlling such emissions may include the use of a Selective Catalytic Reduction system (SCR). The SCR typically uses a catalyst and a reductant to convert NOx in the exhaust gas into at least nitrogen gas and water. The reductant may be a liquid or gas, such as, for example, urea, anhydrous ammonia, or aqueous ammonia, among others, that is injected into the stream of exhaust gas generated by the engine.
For example, in instances in which urea is injected into an exhaust gas stream having normal diesel exhaust gas temperatures, the urea undergoes a thermal decomposition and hydrolysis to produce ammonia. The ammonia may then react with NOx on an SCR catalyst substrate to produce nitrogen and water. As the NOx conversion efficiency of SCR catalysts may exceed 80% over a relatively wide range of exhaust gas temperatures, high engine-out NOx levels can be tolerated. Thus, in at least some applications in which an SCR is used with diesel engines, the diesel engines may be calibrated to run near optimum performance in terms of fuel consumption, as the SCR may be able to handle engine-out NOx levels of the order of several hundred parts-per-million (ppm), and may even tolerate NOx levels exceeding 1000 ppm.
However, the reductants employed by an SCR, such as urea fluid, are typically not naturally found on-board a vehicle. Thus, an SCR often requires that a vehicle include an on-board storage and delivery system for the reductant or for the solution used to provide the reductant. However, with such systems, it is typically the responsibility of the end-user to maintain a supply of reductant for the supply system. For example, the end-user is typically responsible for re-filling a depleted storage system with reductant, such as, for example, re-filling or replacing reductant depleted storage cartridges. However, placing such responsibility on the end-user to monitor and maintain the SCR in functioning condition may be problematic.
Another approach to controlling NOx emissions for a lean burn engine may include the use of a lean NOx trap (LNT). The LNT is typically a high surface area ceramic substrate coated with a washcoat which usually contains at least a NOx storage substance, such as barium oxide (BaO), and a precious metal. Under typical diesel oxygen rich exhaust conditions, NOx in the exhaust gas may be stored as solid nitrates on the LNT catalyst surface. The LNT catalyst however may become at least partially saturated with NOx over a relatively short time period, which may severely reduce the NOx storage capacity of the LNT catalyst due to a finite amount of NOx storage sites. Moreover, with traditional diesel combustion, typical engine-out NOx levels are relatively high, such as being on the order of hundreds of ppm, and consequently the LNT saturation process is relatively quick.
Accordingly, an LNT catalyst requires a NOx regeneration or desorption processes for the release and conversion of the stored nitrates to nitrogen. Regeneration may be achieved via a temporary fuel rich spike in the exhaust gas, which may be provided by the injection of fuel into the exhaust gas stream, or by calibration of the engine's fuel injection map to account for the need for LNT regeneration. Under fuel rich conditions, the solid nitrates are released from the catalyst surface of the LNT and reduced to nitrogen. At least some catalysts used with LNTs may convert up to over approximately 80% of the stored nitrates under optimal conditions. To prevent excessive NOx slip through the LNT, regeneration typically takes place before the LNT is fully saturated with nitrates, implying that a fuel rich spike is required every couple of minutes under traditional operation of a diesel engine, as illustrated by
According to certain embodiments, an engine system is provided for treating nitrogen oxides present in an exhaust gas generated by the combustion of fuel. The engine system includes a diesel engine configured to generate the exhaust gas by the combustion of a fuel. The diesel engine may be calibrated, through the use of in-cylinder NOx reduction strategies which may incur a minor fuel penalty, for the generated exhaust gas to have an engine-out nitrogen oxide level of less than around 100 parts-per-million. The engine system also includes a lean nitrogen oxide trap that is configured to store at least a portion of the nitrogen oxide in the exhaust gas when the lean nitrogen oxide trap operates in an absorption mode. The lean nitrogen oxide trap is also configured for the conversion of a plurality of nitrates stored by the lean nitrogen oxide trap during a regeneration event. According to certain embodiments, the ratio of a duration that the lean nitrogen oxide trap is in the absorption mode to a duration of the regeneration event may be approximately 6:1, however this ratio may vary for other embodiments.
Additionally, certain embodiments provide an engine system for treating nitrogen oxides present in an exhaust gas generated by the combustion of fuel by an engine. The engine system includes a primary exhaust gas recirculation system configured for at least a portion of the exhaust gas generated by the diesel engine to be circulated to an intake manifold of the engine. The engine system also includes at least one injector configured to inject a fuel into the exhaust gas as well as a plurality of lean nitrogen oxide traps. Additionally, the engine system includes a secondary exhaust gas recirculation system that is configured to recirculate at least a portion of the exhaust gas that exits one or more of the lean nitrogen oxide traps to a location upstream of the engine.
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 and associated particulate matter, such as soot, produced by or during the combustion event(s) may then flow out of the cylinders 32 and engine 34 through an exhaust port(s) and along an exhaust line 36.
According to certain embodiments, at least a portion of the hot exhaust gas from the engine 34 may be diverted from the exhaust line 36 and to a primary exhaust gas recirculation (EGR) system 38. The primary EGR system 38 is configured to recirculate the diverted exhaust gas back to the intake manifold 30. However, before the primary 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. By recirculating cooled exhaust gas back into the intake manifold, cooled exhaust gas may occupy a portion of the cylinder(s) 32 that may otherwise be occupied by a gas with a relatively high concentration of oxygen, such as fresh air, which may result in a reduction in the temperatures attained in the cylinder 32 during a combustion event. Because NOx forms primarily when a mixture of nitrogen and oxygen is subjected to high temperature, lowering the temperature of the combustion event in the cylinder 32 through the use of the cooled exhaust gas re-circulated by the primary EGR system 38 may reduce the quantity of NOx generated as a result of the combustion event.
According to certain embodiments, exhaust gas that is not diverted to the primary 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 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 LNT 46 may operate as a long-breathing LNT, in which engine 34 operating parameters allow for the extension of the duration in which the LNT 46 may absorb and/or store NOx between regeneration events. Moreover, the LNT 46 may be a long-breathing LNT through a reduction in the NOx levels in the exhaust gas exiting the engine 34 (or engine-out NOx levels). For example, the engine-out NOx levels may be reduced to around or below 100 ppm by the presence of cooled exhaust gases in the cylinder(s) 32, such as exhaust gas that has been cooled and circulated back to the intake manifold by the primary EGR system 38, as discussed above.
With reduced engine-out NOx levels, the NOx absorption or saturation process of the LNT 46 is slowed down. Accordingly, as the absorption process is slowed down, regenerations of the long breathing LNT 46 may be required less frequently when compared to the conventional operation of an LNT. For example,
As shown in at least
With a secondary EGR system 52, at least a portion of the NOx slipping from the LNT 46, such as, for example, half of the NOx slip, during the regeneration event may be sent back upstream of the LNT 46. For example, referencing
During a regeneration event for the LNT 46, the engine system 10, 10′ may be calibrated for the engine 34 to operate at a low temperature combustion (LTC) mode, which, for example, may aim to reduce in-cylinder flame temperatures below approximately 1800 Kelvin, so as to limit the further formation of NOx during combustion events in the cylinders 32. More specifically, the secondary EGR line 56 may deliver a high temperature combustion (high NOx, meaning several hundreds of ppm of NOx) EGR gas from the LNT 46 to engine 34 that is operating in the LTC mode. By running the engine 34 in the LTC mode, a part of the NOx slipping through the LNT 46 during regeneration is re-routed to the LTC operating engine 34 and partially destroyed by the high total hydrocarbon and carbon monoxide levels typically present inside the cylinder(s) 32 of an engine 34 that is operating in the LTC mode.
For example,
Referencing
The use of multiple LNTs 46a, 46b, may allow for various operating scenarios during the course of engine 34 operation. For example, according to one scenario, the LNTs 46a, 46b may be operated in the same mode, such as, for example, all of the LNTs 46a, 46b operating in a absorption process where the LNT 46a, 46b is absorbing NOx, or all of the LNTs 46a, 46b undergoing a regeneration event. Alternatively, at least some of the LNTs 46a, 46b may be operating in different modes, such as at least one LNT 46a, 46b operating in an absorption process, while another LNTs is undergoing a regeneration event.
For example, referencing
Similarly, while the first LNT 46a is undergoing a regeneration event, the second LNT 46b may be operating under an absorption process in which NOx is being absorbed by the second LNT 46b. Accordingly, during the absorption process, the injector 62 may be configured or operated to not inject fuel into exhaust gas that is entering into the second LNT 46b, thereby allowing the second LNT 46b to continue operating under lean conditions. As the second LNT 46b is in the process of removing NOx from the exhaust gas, a switching valve 60b downstream of the second LNT 46b may be in an on position so that exhaust gas flowing out of the second LNT 46b is able to continue flowing along the exhaust line 36 and toward the DPF 48 and tailpipe 50. Additionally, as the exhaust gas exiting the second LNT 46b may have a relatively low level of NOx, a switch valve 60d that controls the flow of exhaust gas from the second LNT 46b into the secondary EGR system 52′ may be in an off, or closed, position so as to prevent exhaust gas that has exited the second LNT 46b from entering into the secondary EGR system 52′.
While the foregoing has been described with respect to first LNT 46a undergoing regeneration while the second LNT 46b undergoes NOx absorption, the general process is equally applicable when the second LNT 46b undergoes regeneration and the first LNT 46b undergoes the absorption process. Additionally, due to the relatively high ratio of the duration of absorption process to regeneration of the long breathing LNT 46, both the first and second LNTs 46a, 46b may typically both be simultaneously storing NOx for a significant portion of the period of time during which the engine 34 is operating. For example, according to certain embodiments, the absorption process to regeneration ratio for the long breathing LNT 46 may result in the first and second LNTs 46a, 46b operating in the absorption process during over 75% of the time that the engine 34 is operating. Accordingly, during simultaneous storage, NOx release out of the exhaust pipe 50 may be relatively very low, such as, for example, less than 50 ppm, as indicated in