In modern day diesel engines, measures are taken to minimize fuel consumption and harmful emissions. The emissions of diesel soot and NOx can be reduced in an engine aftertreatment system (EAS). Typical components of such an aftertreatment system may be a diesel particulate filter to capture soot, and an SCR (Selective Catalytic Reduction) catalyst that converts NOx into harmless products also known as the deNOx process. Aftertreatment systems may further have a diesel oxidation catalyst (DOC) and/or a diesel particulate filter (DPF), but also other configurations are possible such as sDPF, PNA, TWC, known to the skilled person etc. Typically the reactivity of aftertreatment systems increases when temperature of the catalyst material and the exhaust gas increases at least up to a certain temperature. In order to quickly reach a high conversion efficiency of the after treatment system after engine start, a heater may be used to heat the after treatment system to an operating temperature, which may be around 300-400° C. In normal operation, the aftertreatment can be heated by residual heat from the combustion engine. However, the temperature of the exhaust gas is often limited, especially during engine idle or other situations where the exhaust gas flow is relatively low. In these conditions the amount of enthalpy that can be added to the exhaust gas flow is also limited by a certain maximum exhaust gas temperature, in order not to damage the aftertreatment system. However, the catalyst material itself is still under the target temperature. In such conditions only a maximum amount of heat enthalpy can be transferred from the heater to the aftertreatment system, since the maximum temperature should not be exceeded, in view of chemicals and coatings present in the aftertreatment system. Thus, heating the aftertreatment system may require time longer than desirable, during which the system is not functioning optimally. It is an object of the invention to generate more enthalpy without exceeding the exhaust gas temperature limit, and therewith increasing the warm-up speed of the after treatment system.
It is an aspect of the present invention to alleviate, at least partially, the problems discussed above by an internal combustion engine comprising: an exhaust line configured to receive exhaust gas from the internal combustion engine and an intake line configured to supply pressurized air from an air intake to the internal combustion engine. A heater is disposed adjacent the exhaust line to generate heat that is transported via the exhaust line to an exhaust aftertreatment system. A bypass line controllably connects the intake line to the exhaust line to bypass the engine, the bypass line in fluid communication with the exhaust line through an inlet opening in the exhaust line upstream of the heater. An electric flow generator is arranged in the intake line and/or bypass line between the air intake and the inlet opening to supply intake air to the exhaust line. A control system is arranged to control the heater and selectively control the bypass line and the electric flow generator, to provide pressurized intake air from the electric flow generator, via the inlet opening to supply intake air to the exhaust line for transporting heat generated by the heater towards the aftertreatment system.
Accordingly air flow from the flow generator is used with the purpose of increasing the exhaust mass flow and therewith allowing the heater or heater to generate more enthalpy without exceeding the exhaust gas temperature limit, and therewith increasing the warm-up speed of the after treatment system.
The accompanying drawings, which are incorporated herein and form part of the specification, illustrate the present invention and, together with the description, further serve to explain the principles of the invention and to enable a person skilled in the relevant art(s) to make and use the invention.
Unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs as read in the context of the description and drawings. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein. In some instances, detailed descriptions of well-known devices and methods may be omitted so as not to obscure the description of the present systems and methods. The term “and/or” includes any and all combinations of one or more of the associated listed items. It will be further understood that the terms “comprises” and/or “comprising” specify the presence of stated features but do not preclude the presence or addition of one or more other features. All publications, patent applications, patents, and other references mentioned herein are incorporated by reference in their entirety. In case of conflict, the present specification, including definitions, will control.
The route of the added air mass flow can have several embodiments, as the figures below show, and may depend on the type of flow generator that is used. For example, the air can be added upstream or downstream of the turbine, if applicable. Furthermore, the air might be fed from upstream or downstream of a compressor, if applicable. In case of the flow generator being an EGR pump, it might reverse normal flow direction to feed air mass flow to the exhaust. A flow generator, e.g. an e-turbo may be added to increase the bulk exhaust gas mass flow. This secondary device can be an electrical compressor, an e-turbo, an EGR pump, or a turbocharger mechanically coupled to the crankshaft, e.g. a SuperTurbo or supercharger
Catalyst (DOC), a Diesel Particulate Filter (DPF), a Urea dosing unit, a Selective Catalytic Reduction catalyst (SCR), an Ammonia Slip Catalyst (ASC) and a Control Module (CM) placed downstream in the exhaust line 13 of the ICE 10 typically including a turbo compressor. This setup is conventional, in the sense that the system elements are known to the skilled person. EAS control 50 in
The control system 50 may increase the air flow from the e-compressor or e-turbo and direct it directly into the exhaust line 13. The amount of air can thus be increased so that the heater/heater can be operated e.g. at a maximum capacity, without risking damage risks to the EAS 30 in view of a high temperatures, and thereby control the heater 20 as a function of a maximum heater capacity. The control system 50 controls the amount of flow, generated by the electric flow generator 40 guided towards the exhaust line 13 as function of the amount of mass flow required by the engine 10, the capability of the heater 20 and the capability of the flow generator 40, e.g. an e-turbo. It is noted that this type of air supply through an inlet opening in the exhaust line 13 is unlike feeding a heater with fresh air to increase the heater performance, e.g. by atomizing fuel in the heater and therewith increase the robustness of the flame, or supply air to realize a proper air/fuel ratio for proper combustion in the heater. In such cases the amount of air for such an application is very limited (−3-50 g/s, depending on the heater power), and there is no direct supply of intake air to the exhaust line which will not lead to a significant increase of enthalpy in situations where the heater heat power is limited by the temperature limit. In addition, a simple increase of fresh air mass flow in such systems will lead to improper fuel/air mixture leading to non-functioning of the heater. Furthermore, in such applications, fresh air is generated by electric flow generators typically not arranged in the intake line, that are not suitable for boosting the intake pressure of the engine 10. An important aspect of the invention is utilizing flow generator systems by systems, such a turbo compressor (i.e. an electric pre stage compressor or an e-turbo) already present in the engine system. A further important aspect is that the electric flow generator is not or only partly dependent on the mechanical power take of a turbine arranged in the exhaust channel, since the application has specific advantages at low exhaust flow speeds, when the turbine cannot render sufficient pumping energy for generating a sufficient fresh air mass flow. The electric flow generator 40, by its at least in part electrical powering is thus not fully dependent on power that can only be supplied at significant exhaust flows produced at relatively high load of ICE 10.
Advantageously the invention naturally uses the overcapacity, at low-load conditions of the engine, such as idling, of a flow generator to increase the mass flow in the exhaust, so that the heating power of the heater 20 is no longer limited by the temperature limit. By physical law :
Since the temperature downstream of the heater/heater is often limited to ˜500 degC in order to prevent too high thermal stress of the EAS 30, the equation shows that the amount of heat enthalpy can be increased by increasing the exhaust mass flow. As a non limiting example, e.g. during engine idling the exhaust mass flow is normally limited to −20-50 g/s, which is lower than e.g. a desired 100 g/s. in such cases also, the exhaust gas temperature upstream of a heater/heater can be in the range of 100-150 degC, or even colder in the case of a cold-start event. In such a condition taking into account the maximum temperature downstream of the heater/heater, the maximum heat enthalpy may be limited to about 5 kW, which is far below a typical capacity of a heater, which could be in the order of 15-40 kW, e.g. 30 kW. To be able to deliver the heat power while keeping the temperature in acceptable limits, the exhaust flow may be increased, by supplying intake air, via the bypass line into the exhaust line at a rate higher than e.g. 50 g/s that is, where the electric flow generator is arranged to supply intake air to the exhaust line in excess of 50 or even 100 g/s.
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If the query results in a ‘yes’; a further query mode Q2 is executed wherein it is decided whether the enthalpy transfer is limited by exhaust gas temperature limit. That is, if the burner already has a maximum allowable temperature, no further temperature increase is allowed and in state S1 fresh air flow is increased and routed towards exhaust directly via the bypass mode. In case the burner does not have a maximum temperature, in state S2, the temperature is increased while maintaining normal operation of the flow generator and re-routing valve, as in the normal condition.
Number | Date | Country | Kind |
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2023547 | Jul 2019 | NL | national |
Filing Document | Filing Date | Country | Kind |
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PCT/NL2020/050476 | 7/21/2020 | WO |