This is a non-provisional application claiming the benefit of International Application Number PCT/IB2011/001696 filed Jul. 18, 2011.
The proposed invention concerns the automotive industry and more particularly concerns a method for controlling a system intended to reduce the amount of NOx in motor vehicle exhaust gases.
Transport-related pollutant emissions have for nearly thirty years been at the forefront for prompting progress in the industry. Increasingly more severe emission limits for the four regulated pollutants (CO, HC, NOx, particles) have allowed a significant improvement in air quality, in particular in large cities.
The ever increasing use of motor vehicles requires continued efforts to further reduce these pollutant emissions. Therefore the reduction of nitrogen oxides (NOx) remains a complex problem within the context of more severe European thresholds expected in 2015 when the Euro 6 standard comes into force. To have available highly efficient depolluting technologies under all driving conditions remains a major challenge for the transport industry.
Secondly, fuel consumption directly linked with CO2 emissions has become a major concern. For example regulations will be introduced at European level on and after 2012 relating to passenger vehicle CO2 emissions. It is henceforth accepted that this limit will be regularly lowered over the coming decades. CO2 reduction has therefore become an obvious necessity for the entire transport industry.
This dual issue of reducing local pollution (NOx) and reducing fuel consumption (CO2) raises particular difficulties for diesel engines whose lean-burn combustion is accompanied by NOx emissions that are difficult to treat.
Devices already exist which allow a reduction in NOx quantities by means of a SCR catalyzer (Selective Catalytic Reduction) via ammonia stored in storage material of salt type e.g. alkaline-earth chlorides. The injection of ammonia into exhaust gases is controlled by means of a heating device used to heat the storage material to allow a reversible absorption/desorption reaction of ammonia, since this reaction is directly related to the temperature within the storage material.
It is the objective of the present invention to propose a method for limiting the energy consumption of the heating device whilst ensuring sufficiently high pressure within the storage material to allow a sufficient injection rate that is compatible with NOx emissions.
According to the invention, this objective is achieved by means of a method for controlling a system intended to reduce the quantity of NOx in the exhaust gases of a motor vehicle. The system, on-board a motor vehicle, comprises a storage chamber containing a pollutant-removing agent, a heating device arranged to control the temperature of the storage chamber, and a feed module arranged to inject the pollutant-removing agent into the exhaust gases. The feed module comprises a device for measuring the pressure or temperature inside the storage chamber and a device for proportioning the pollutant-removing agent. The method of the invention comprises the following steps:
To determine the set pressure or temperature in the storage chamber during the predetermined driving period, step a) preferably comprises the following operations:
According to one preferred embodiment of the invention, the mean driving criterion during the first operating period (T1) of the motor vehicle is compared with at least three and preferably five different thresholds so that it is possible respectively to determine at least three and preferably five types of driving. Also, according to this preferred embodiment, three driving patterns are determined for the second operating period (T2) of the motor vehicle respectively corresponding to urban, rural road and motorway driving. Optionally a so-called mixed pattern can be added when no type of driving is predominant during this second period (T2). Finally, the system is adapted so that the set pressure is able to vary, preferably between 1 and 15 bars, so as to cause the flow rate of ammonia to vary over a range of 0.5 mg/s to 50 mg/s.
The characteristics of the invention will become better apparent on reading the description of this preferred embodiment, given solely as an example which is in no way limiting with reference to the schematic Figures in which:
According to this preferred embodiment of the invention, the control method is adapted to a device for selective catalytic reduction (SCR) of NOx emitted by exhaust gases from a vehicle engine.
According to
More particularly according to
The ammonia 16 is injected by means of an injection module 3 into the exhaust downstream of the first pollutant-removing element 2 and is mixed with the exhaust gases. The ammonia/exhaust gas mixture 13 then passes through a SCR catalyzer 4 which allows the reduction of NOx via the ammonia. Various additional post-treatment elements 5 can be positioned after the SCR catalyzer such as a particle filter or oxidation catalyst. The depolluted exhaust gases 14 are then directed towards the exhaust outlet.
To ensure the feed and proportioning of ammonia 16, the ammonia storage chamber 8 contains a storage material 7 and is arranged so that its temperature can be controlled by the heating device 9 which may be in the form of an electric resistance or a heat exchanger supplied with a heat-exchange fluid such as the engine coolant. According to the present invention, the ammonia is preferably stored in a salt of alkaline-earth metal chloride type (MgCl2, SrCl2, CaCl2, BaCl2, etc.)
In the proposed system, the storage of ammonia is based on a reversible solid-gas reaction of the type:
With alkaline-earth chlorides, ammonia forms coordination complexes also called ammoniacates. This phenomenon is known and abundantly described in the literature.
For example, the reactions of ammonia with strontium chloride are:
The chemical absorption of the ammonia ligand by the absorbent SrCl2 and BaCl2 causes a transfer of electrons between the solid and the gas, which translates as chemical bonds between NH3 and the outer layer of the atoms of SrCl2 and BaCl2. The entry of the gas into the structure of the solid occurs within the entirety of its mass via a diffusion process. This reaction is fully reversible, absorption being exothermic and desorption endothermic.
During this reaction, the fixing of the gas by the solid is accompanied by an increase in volume, the octa-ammoniacate then occupying a much greater volume than the volume of the pure salt (up to a ratio of 4 to 5 times). The increase in the volume of the salt is due not only to expansion of its crystalline lattice but also to fractionating thereof thereby leaving free space between the microcrystals of Sr(NH3)8Cl2 and Ba(NH3)8Cl2.
Most salts desorb ammonia in stages as a function of their coordination sites. With regard to Strontium chloride seven molecules of ammonia are initially desorbed, and a last ammonia molecule at a second stage. The ammonia absorption/desorption equilibrium curve of the salts is defined as a function of temperature and pressure via the Clausius-Clapeyron equation:
where ΔHr represents enthalpy and ΔSr the entropy of formation of the ammonia/salt complex for the stoichiometry under consideration.
The table below gives the enthalpy and entropy formation values taken from the scientific literature for the salts MgCl2, SrCl2 and BaCl2.
The equilibrium curves of ammonia absorption/desorption in these three salts are illustrated in
According to
According to
According to the invention, the ammonia proportioning device 6b is controlled in relation to a certain number of engine and vehicle parameters derived from the engine computer 11 which are used in combination with the data to allow optimized controlling of the heating device 9.
The term “system pressure” will be used to designate the pressure prevailing during operation inside the storage and feed system including the storage chamber 8, the connection interface 8a, the pressure sensor 6a and the ammonia proportioning device 6b. This system pressure is directly related to the temperature inside the storage chamber 8 via the Clausius-Clapeyron equation defined above.
The pressure of the system when in operation may vary as a function of the outer temperature and/or heating applied to the storage chamber over a pressure range of between 1 and 15 bar.
To limit the energy consumption of the heating device, it is sought to limit the system pressure as far as possible. On the other hand, the system pressure must be sufficiently high to allow a sufficient injection rate compatible with NOx emissions of the engine.
In the present invention, the set pressure is determined dynamically in relation to analysis of a certain number of engine and vehicle parameters such as the concentration of NOx emitted at any one time (magnitude able to be measured and/or modelled), the temperature of the engine lubricant, the temperature of the engine coolant, vehicle speed, engine speed, engine load or a combination of these parameters.
A preferred embodiment is described below for this analysis of present driving conditions (driving type criterion) and past driving conditions (driving pattern criterion) which allows a precise breakdown of the different life phases of a vehicle and offers extensive freedom for defining of the set pressure.
At a first stage a driving criterion is defined by the equation:
Driving criterion=vehicle speed×(1+K×CMI)
where CMI is the mean engine torque and K is the correction coefficient of engine torque allowing integration of the weight/power ratio, consideration of differences between vehicles having manual gearboxes or automatic gearboxes, and thereby best characterization of each type of driving (a parameter which can be calibrated for each application).
As illustrated in
The type of driving is then defined by comparing the filtered driving criterion with calibratable thresholds in the following manner:
The time spent on each type of driving condition during a second period T2 five times longer than period T1 is then calculated. This gives a vector of five values X1 to X5 whose sum is 100 (
On the basis of the distribution of the types of driving conditions at time t, a pattern is associated representing past driving conditions. The number of patterns is limited to 3 (urban, rural road and motorway) to which a “mixed” pattern is added when no type of driving is predominant. The rules for determining pattern are the following:
For reasons of coherency the following rules are applied:
The driving pattern is re-initialized as soon as the engine is stopped. There being no distribution of driving types during the first T2 seconds, the driving pattern is systematically initialized at 2 (rural road).
In the present invention, it is proposed to determine the set pressure as a function of this analysis of present and past driving conditions. Therefore, the set pressure is calculated by mapping such as illustrated in
The analysis of present and past driving conditions allows a precise breakdown of the different life phases of a vehicle and is well adapted to calculating ammonia pressure. For example, for a vehicle whose past and present conditions are severe urban, there is little advantage in ensuring a high system pressure, the flow rates of NH3 required for treating the NOx emitted under these driving conditions being relatively low. On the other hand, for a vehicle whose past is urban and present is rural road, it would appear to be of advantage to increase the system pressure so as to provide for the high NH3 flow rates required under these driving conditions.
It is to be noted that it is the calibration of calculation for criteria of driving type and driving pattern (T1, T2, X1, X2 . . . ) which allows optimized controlling of the set pressure over time i.e. sizing as accurately as possible the energy consumption related to heating of the system. It is to be noted that this calibration must also take into account the system's response time i.e. the response time between an increase in the set system pressure and the reaching of this system pressure.
In the present invention, ΔPeq defines the pressure difference between Pset, the set pressure determined using the above strategies, and Psystem the pressure measured by the pressure sensor 6a:
ΔPeq=Pset−Psystem
In the present invention, the power of the heating system is controlled via mapping dependent on the system pressure Psystem and the pressure difference ΔPeq. This mapping is to be calibrated for the system used and for the desired response time. In this manner mapping is determined of the “rise in temperature of the ammonia storage and feed system”.
It is to be noted that it is also possible to control the power of the device by means of Tsystem and ΔTeq mapping, these 2 magnitudes able to be calculated directly from the values of system pressure (Psystem) and pressure difference (ΔPeq) using the Clausius-Clapeyron equation.
Also to be noted is that this pressure (or temperature) mapping can be determined experimentally on the system used since it depends on a large number of parameters: heat loss in the system (advantage of insulating the storage chamber), heating system (electric, heat-exchange fluid), graphite/salt composite matrix (type of salt, binder density, conductivity and permeability, etc.).
Number | Date | Country | Kind |
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10007831 | Jul 2010 | EP | regional |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB2011/001696 | 7/18/2011 | WO | 00 | 5/8/2013 |
Publishing Document | Publishing Date | Country | Kind |
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WO2012/014037 | 2/2/2012 | WO | A |
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Number | Date | Country | |
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20130213011 A1 | Aug 2013 | US |