• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention concerns an exhaust gas aftertreatment system (2) adapted so as to reduce the amount of N2O that is produced in a selective catalytic reduction catalytic converter (SCR catalytic converter) (6) and/or in an ammonia slip catalyst (ASC catalyst) (4) disposed in the exhaust gas flow from a combustion engine (3), which exhaust gas aftertreatment system (2) comprises an SCR catalytic converter (6) arranged in an exhaust gas line (8) upstream of an optional ASC catalyst (4) and the exhaust gases from the combustion engine (3) pass through the SCR catalytic converter (6) and any ASC catalyst (4) before they are released into the surroundings via the exhaust gas outlet (10), and which exhaust gas aftertreatment system (2) further comprises an injection device (12) adapted so as to inject a reducing agent into the exhaust gases in the exhaust gas line (8) upstream of the SCR catalytic converter (6) at a dosing frequency F. The exhaust gas aftertreatment system further comprises a control unit (14) adapted so as to generate a control signal (16) intended to adjust the dosing frequency F so that the amount of N2O that is produced in the SCR catalytic converter (6) and/or in the ASC catalyst (4) is minimized while maintaining the amount of reducing agent added. The invention also concerns a method for an exhaust gas aftertreatment system.
    公开号:SE1350535A1
    申请号:SE1350535
    申请日:2013-05-02
    公开日:2013-11-04
    发明作者:Ola Stenlaaaas
    申请人:Scania Cv Ab；
    IPC主号:
    专利说明:

    2 depending on the storage level. In order to maintain a high conversion efficiency under different operating conditions, the NH 3 layer must be maintained. However, as the temperature of the SCR catalyst increases, the NH 3 level must be reduced to avoid NH 2 emissions (ie, excess NH 2 is emitted from the SCR catalyst), which may reduce the conversion efficiency of the catalyst.
    In summary, in order to meet stricter environmental requirements, all your vehicle manufacturers use SCR catalyst systems to purify diesel exhaust gases from nitrogen oxides (NOX). This is done by injecting ammonia solution into an SCR catalyst that helps convert NOX particles into nitrogen and water. The exhaust gas purification strategy should take into account that sufficient NOX is converted while not wanting to inject too much ammonia, for both the driving economy and the environment.
    Exhaust gas treatment systems also use at least one diesel oxidation catalyst (DOC), as well as one or more diesel particulate filters (DPFs) which are often coated with a catalytic coating. The purpose of this is, among other things, to generate a sufficient amount of NO 2 to effect passive oxidation of soot which is captured by DPF. This is done according to the reaction: C + 2NO 2 -> CO 2 + 2NO.
    In cases where not all ammonia has been consumed for the desired reduction in the SCR catalyst, it can either be stored in the SCR catalyst, follow the exhaust gases from the SCR catalyst or react in the SCR catalyst to N 2 O. To avoid unwanted ammonia emissions, a so-called ammonia oxidation catalyst (ASC - Ammonia Slip Catalyst), hereinafter ASC catalyst, is often used downstream of the SCR catalyst to take care of any remaining ammonia.
    The function of the ASC catalyst depends, among other things, on the temperature of the exhaust gases, in such a way that if ammonia is oxidized in the ASC catalyst in a state when the temperature in the ASC is high and the mixture is good, NOX will primarily be produced. If, on the other hand, ammonia is oxidized in a state where the state in the ASC is less favorable, N20 (nitrous oxide) will instead be produced. The ability of the SCR catalyst to store ammonia decreases with increasing temperature, so that ammonia then preferably either leaves the SCR catalyst or changes to N 2 O. This means that the ASC normally only receives 3 high levels of ammonia at high temperatures. Emissions of N 2 O will thus depend on the temperature in both the SCR catalyst and the ASC catalyst. In the case where the condition is less favorable, the amount of ammonia and NOX will decrease downstream of the ASC, while the N20 is emitted. Since N20 is a gas that is a very powerful greenhouse gas, about 300 times stronger than carbon dioxide, it is desirable that emissions of N20 into the atmosphere are reduced.
    Published patent application EP-2143901 describes a method intended to estimate the amount of N2 O produced in vehicle exhaust gases. This is done, among other things, by sensing the NOX concentrations upstream and downstream of the SCR catalyst. By then regulating the urea dosage based on these estimates, one can thereby reduce the formation of nitrous oxide in the exhaust gas purification.
    US-5270025 relates to a method for reducing nitrous oxide emissions while reducing NOX. To regulate emissions, a combination of urea and additional substances is used, e.g. glutamate.
    US-5 547650 discloses an exhaust gas purification system in which N 2 O is removed by heating the exhaust gases, and finally US-2009/0324453 discloses a catalyst for NOX purification of exhaust gases by dosing urea.
    Thus, there is a need to reduce nitrous oxide emissions and the object of the present invention is to provide an improved exhaust gas treatment system where the emissions of N 2 O are reduced or completely avoided.
    Summary of the invention The above objects are achieved by the invention defined by the independent claims.
    Preferred embodiments are defined by the dependent claims.
    The invention generally relates to a method of reducing nitrous oxide emissions, and more specifically to a method of an exhaust gas treatment system adapted to reduce the amount of N 2 O produced in a selective catalytic reduction catalyst (SCR catalyst) and / or in an ammonia oxidation catalyst (ASC catalyst) placed in exhaust gas an internal combustion engine, wherein the exhaust after-treatment system comprises an SCR catalyst located upstream of an optional ASC catalyst, a reducing agent being adapted to be added to the exhaust gas upstream of the SCR catalyst at a dosing frequency F. According to the method, the dosing frequency F is adjusted so that, with the amount retained, The N 2 O produced in the SCR catalyst and / or the ASC catalyst is minimized.
    According to one embodiment, the dosing frequency is adjusted so as to increase if the exhaust gas temperature upstream of the SCR catalyst and / or the ASC catalyst is higher than a predetermined threshold value. For example, the increase in the dosing frequency means a doubling of the frequency compared with when the temperature fell below said threshold value.
    The invention also comprises an exhaust after-treatment system in which the above-mentioned method has been implemented.
    The reducing agent is added in pulse form where the dosing frequency today is normally in the range 0.1 - 10 Hz.
    The invention is based on the inventor's insight that by adding the reducing agent at a higher frequency compared to the one used today, the variations of the reducing agent in the exhaust gases reacting in and coming out of the SCR catalyst are reduced, which is advantageous for reducing the amount of N 2 O produced in SCR. catalyst or in the subsequent ASC catalyst.
    According to the invention, the dosing frequency must be equal to or higher than 2 Hz and with the retained total dosed amount of reducing agent compared to a conventionally set dosing frequency.
    By controlling the dosage of the reducing agent, it is thus possible in some cases to regulate the formation of nitrous oxide and thereby reduce it. Substantial hardware for reducing agent supply can be used without having to make changes to the SCIUASC catalysts, which is an advantage since the costs of implementing the invention in existing systems will be low.
    Brief Description of the Drawings Figure 1 is a block diagram schematically illustrating an embodiment of the present invention.
    Figure 2 are graphs intended to illustrate the present invention.
    Figure 3 is a flow chart illustrating the method of an embodiment of the present invention.
    Detailed Description of Preferred Embodiments of the Invention The invention will now be described in detail with reference to the accompanying figures.
    Figure 1 shows a block diagram illustrating an embodiment of the invention.
    The invention relates to an exhaust gas aftertreatment system 2 adapted to reduce the amount of N 2 O produced in a selective catalytic reduction catalyst (SCR catalyst) 6 and / or in an ammonia oxidation catalyst (ASC catalyst) 4 placed in the exhaust gas from an internal combustion engine 3. The ASC catalyst aims ammonia in the exhaust gas fl to thereby reduce emissions of ammonia.
    The exhaust after-treatment system comprises an SCR catalyst 6 arranged in an exhaust line 8, upstream of an optional ASC catalyst 4 and the exhaust gases from the combustion engine 3 thus pass through the SCR catalyst 6 and the optional ASC catalyst 4 before being released to the environment via the exhaust outlet 10.
    The exhaust after-treatment system further comprises an injection device 12 adapted to inject a reducing agent into the exhaust gas. The exhaust line 8 is sprayed with the SCR catalyst 6 at a dosing frequency F.
    The reducing agent, e.g. urea, is thus injected by means of an injection device 12 into the exhaust gas of the exhaust line 8 upstream of the SCR catalyst 6. The injection device 12 comprises one or two injection means 26 arranged in the exhaust line 8 in the form of injection nozzles or the like, and a storage container 22 for 6 connected thereto. The injection device 12 also comprises a control means 20 connected to a control means 24. The control means 24 is controlled by the control means 20, which determines the amount of reducing agent to be injected into the exhaust gases based on the prevailing operating conditions of the internal combustion engine 3 and the catalyst 6. control unit 14.
    The reducing agent may be, for example, urea (CO (NH 2) 2), ammonia (NH 3) or hydrocarbon (fuel). The reducing agent is added by the injecting device 12 by injecting the agent with a dosing frequency F, with a dosing period time L (L = 1 / F) which is denoted as the time between the beginning of two consecutive injections, the injection taking place during an adjustable dosing time t of said dosing period Reducing agent is varied by varying the dosing frequency F and / or the dosing time t for the injection of the reducing agent.
    It is further possible to vary the amount of reducing agent added by changing the dosing pressure, i.e. the pressure applied to the product during injection. This can be done in combination with a variation of the dosing frequency F and / or the dosing time t.
    According to the invention, the exhaust aftertreatment system 2 comprises a control unit 14 adapted to generate a control signal 16 intended to adjust the dosing frequency F so that, while maintaining the amount of reducing agent added, the amount of N 2 O produced in the SCR catalyst and / or in the ASC catalyst is minimized.
    According to one embodiment, the dosing frequency F is adjusted so that the variation of the amount / content of reducing agent upstream of the SCR catalyst is lower than a predetermined threshold value AR, where AR is +/- 5%.
    For example, the dosing frequency F is adjusted so that the variation of the amount / content of reducing agent upstream of the SCR catalyst is lower than a predetermined threshold value AR, where AR is +/- 1%.
    According to a further example, the dosing frequency F is adjusted so that the variation of the amount / content of reducing agent upstream of the ASC catalyst is lower than a predetermined threshold value AR, where AR is +/- 5%. The variation of the amount / content of reducing agent can e.g. modeled with folder (s) / table (s) or applicable formula, based on one or fl era of: - dosing frequency; - total injection of reducing agent fl; - time percentage of dosing agent in progress (eg expressed as a percentage (%) of the time between two started dosing); - exhaust gas fl fate (eg kg exhaust per minute); - exhaust gas temperature.
    In some operating cases and with certain sensor locations, NOx and NH3 sensors can also emit signals that fluctuate at the same frequency as the dosing and then the amplitude of one or fl of these signals can also be included in the model, either alone or in combination with one or fl are of the above parameters.
    The variation of the amount / content of reducing agent upstream of the SCR catalyst and / or the ASC catalyst can thus be determined in one of a number of applicable ways. Based on this, the dosing frequency F can be determined / adjusted so that the resulting variation of the amount / content of reducing agent upstream of the SCR catalyst and / or the ASC catalyst becomes lower than a predetermined threshold value AR.
    The adjustment of the dosing frequency F preferably means that the dosing frequency F is increased and the dosing time t is reduced. This can be achieved, for example, by doubling the dosing frequency F and halving the dosing time t. This example is illustrated in Figure 2, which are two graphs where the top graph shows a number of pulsed doses of reducing agent with the dosing time t, which is thus the time when the control means is open and reducing agent is injected into the exhaust gas fl. The dosing period time in this case is L, which means that the dosing frequency F = 1 / L.
    The lower graph illustrates an embodiment of the invention where the dosing frequency F is doubled and the dosing time t is halved. This means that the same amount of reducing agent is released during the same time period. In the two graphs in Figure 2, the content of reducing agents for the two situations has also been indicated - these have been denoted by R1 and R2 respectively.
    In the upper graph, where the dosing frequency is F, injection of a relatively large amount of reducing agent means that not everything has time to be consumed in the SCR catalyst, but some is passed on with the exhaust gases to the ASC catalyst where residual ammonia, under certain conditions, is oxidized to NOX , but under other conditions, for example at too low exhaust gas temperatures, is instead emitted as N20.
    In the lower graph, the dosing frequency F has doubled and the dosing time t has been halved, ie. the same amount of reducing agent is released during the same time period. In this case, under certain conditions a smaller amount of residual ammonia will be passed on to the ASC catalyst because a larger part of the reducing agent has time to be consumed in the SCR catalyst and thus the emissions of N 2 O will be less than in the case illustrated by the upper graph. .
    Figure 2 clearly illustrates the advantages of the present invention by the smoothing of the content of reducing agent which the curve R2 shows compared to the curve R1. This is shown by the fact that the variations for the curve R2 are smaller than for the curve R1.
    According to one embodiment, the dosing frequency is at least 2 Hz.
    According to a further embodiment, the exhaust after-treatment system comprises a temperature sensor 18 which is adapted to measure the temperature in the exhaust gas upstream of the SCR catalyst 6 and / or the ASC catalyst 4. The read temperature T is delivered to the control unit 14. In the control unit 14 the read temperature is compared with a predetermined threshold value. TTH and if the read temperature T is higher than TTH, the dosing frequency is adjusted so that it is increased. The increase in the dosing frequency may, for example, mean a doubling of the frequency compared with when the temperature fell below said threshold value TTH.
    The predetermined threshold value TTH is, for example, in the range 300-450 ° C. 9 An alternative to arranging a temperature sensor as described above is to instead measure a temperature related to the temperature in the exhaust gas flow and calculate the temperature for the exhaust gas flow using known relationships between the measured temperature and the temperature in the exhaust gas flow. According to a further alternative, a calculation model is instead used to determine the temperature in the exhaust gas flow, where the model uses a number of other known parameters to determine the temperature. The temperature T measured, or determined according to the alternatives given above, is output to the control unit 14 where the comparison described above is performed.
    According to another embodiment, the dosing frequency F will instead be adjusted continuously depending on the exhaust gas temperature upstream of the SCR catalyst and / or the ASC catalyst in such a way that an increased temperature leads to an increased frequency.
    Associated values for temperature and dosing frequency, and of course other parameters related to the release of the reducing agent, are stored, for example, in a table in the control unit 14.
    The present invention also includes a method of an exhaust gas aftertreatment system adapted to reduce the amount of N 2 O produced in a selective catalytic reduction catalyst (SCR catalyst) and / or in an ammonia oxidation catalyst (ASC catalyst) placed in the exhaust gas from an internal combustion engine, where the ASC catalyst to oxidize ammonia in the exhaust gas. The exhaust after-treatment system comprises an SCR catalyst located upstream of an optional AS C catalyst. A reducing agent is adapted to be added to the exhaust gas upstream of the SCR catalyst with a dosing frequency F. The system has been described in more detail above with reference to Figure 1 and we refer here to that description.
    The method involves adjusting the dosing frequency F so that, while maintaining the amount of reducing agent added, the amount of N 2 O produced in the SCR catalyst and / or the AS C catalyst is minimized.
    According to one embodiment of the method, the dosing frequency is adjusted so that the variation of the amount / content of reducing agent upstream of the SCR catalyst and / or the ASC catalyst is lower than a predetermined threshold value AR, where AR is +/- 5%. For example, the dosing frequency F is adjusted so that the variation of the amount / content of reducing agent upstream of the SCR catalyst is lower than a predetermined threshold value AR, where AR is +/- 1%.
    According to a further example, the dosing frequency F is adjusted so that the variation of the amount / content of reducing agent upstream of the ASC catalyst is lower than a predetermined threshold value AR, wherein AR is +/- 5%.
    The adjustment of the dosing frequency F preferably means that the dosing frequency F is increased and the dosing time t is reduced. This can be achieved, for example, by doubling the dosing frequency F and halving the dosing time t.
    According to a further embodiment, the method comprises measuring the temperature in the exhaust gas upstream of the SCR catalyst and / or the ASC catalyst. The read temperature T is delivered to the control unit. In the control unit, the read temperature is compared with a predetermined threshold value TTH and if the read temperature T is higher than TTH, the dosing frequency f is adjusted so that it is increased. This embodiment is schematically illustrated by the fate diagram in Figure 3.
    Reference is also made here to the alternative ways of determining the temperature discussed in OVaII. The increase of the dosing frequency F can, for example, mean a doubling of the dosing frequency compared with when the temperature fell below said threshold value TTH.
    The predetermined threshold value TTH is, for example, in the range 300-450 ° C.
    According to another embodiment, the dosing frequency F will instead be adjusted continuously depending on the exhaust gas temperature upstream of the SCR catalyst and / or the ASC catalyst in such a way that an increased temperature leads to an increased dosing frequency.
    Associated values for temperature and dosing frequency, and of course other parameters related to the release of the reducing agent, are stored, for example, in a table in the control unit 14. The present invention is not limited to the preferred embodiments described above.
    Various alternatives, modifications and equivalents can be used. The above embodiments are, therefore, not to be construed as limiting the scope of the invention as defined by the appended claims.
    权利要求:
    Claims (22)
    [1]
    A method of an exhaust after-treatment system adapted to reduce the amount of N 2 O produced in a selective catalytic reduction catalyst (SCR catalyst) and / or in an ammonia oxidation catalyst (ASC catalyst) placed in the exhaust gas from an internal combustion engine, the exhaust after-treatment catalyst comprising an SC after-treatment catalyst upstream of an ASC catalyst, and wherein a reducing agent is adapted to be added, the exhaust gas upstream of the SCR catalyst having a dosing frequency F, characterized in that the method comprises adjusting the dosing frequency F so that, while maintaining the amount of reducing agent added, the amount of N 2 O produced in SCR and / or the AS C catalyst is minimized.
    [2]
    The method of claim 1, wherein the dosing frequency is adjusted so that the variation of the amount of reducing agent upstream of the SCR catalyst is lower than a predetermined threshold value AR, wherein AR is +/- 5%.
    [3]
    The method according to any one of claims 1 or 2, wherein the dosing frequency is adjusted so that the variation of the amount of reducing agent upstream of the SCR catalyst is lower than a predetermined threshold value AR, wherein AR is +/- 1%.
    [4]
    The method according to any one of claims 1-3, wherein the dosing frequency is adjusted so that the variation of the amount of reducing agent upstream of the ASC catalyst is lower than a predetermined threshold value AR, wherein AR is +/- 5%.
    [5]
    The method according to any one of claims 1-4, wherein the method comprises that the adjustment of the dosing frequency means that the dosing frequency F is increased and a dosing time t is reduced.
    [6]
    The method according to claim 5, wherein the increase of the dosing frequency F means a doubling of the dosing frequency and a halving of the dosing time t.
    [7]
    The method according to any one of the preceding claims, wherein the dosing frequency is adjusted so that it is increased if the exhaust gas temperature upstream of the SCR and / or ASC catalyst is higher than a predetermined threshold value.
    [8]
    The method according to claim 7, wherein the increase of the dosing frequency means a doubling of the dosing frequency compared to when the temperature fell below said threshold value.
    [9]
    The method of any of claims 7 or 8, wherein said predetermined threshold is in the range of 300-450 ° C.
    [10]
    The method according to claim 7, wherein the frequency is continuously adjusted depending on the temperature of the exhaust gas upstream of the SCR catalyst and / or the ASC catalyst in such a way that an increased temperature results in an increased dosing frequency.
    [11]
    11. ll. The method according to any one of claims 1-10, wherein the dosing frequency is equal to or higher than 2 Hz.
    [12]
    An exhaust gas after-treatment system (2) adapted to reduce the amount of N2O produced in a selective catalytic reduction catalyst (SCR catalyst) (6) and / or in an ammonia oxidation catalyst (ASC catalyst) (4) placed in the exhaust gas from an internal combustion engine (3) , the exhaust after-treatment system (2) comprising an SCR catalyst (6) arranged in an exhaust line (8), upstream of an ASC catalyst (4) and the exhaust gases from the internal combustion engine (3) pass through the SCR catalyst (6) and the ASC catalyst ( 4) before being released to the environment via the exhaust outlet (10), the exhaust after-treatment system (2) further comprising an injector (12) adapted to inject a reducing agent into the exhaust gases in the exhaust line (8) upstream of the SCR catalyst (6) with a dosing frequency F , characterized in that the exhaust after-treatment system comprises a control unit (14) adapted to generate a control signal (16) intended to adjust the dosing frequency F so that, while maintaining the amount added reducing agent, the amount of N 2 O produced in the SCR catalyst (6) and / or the ASC catalyst (4) is minimized.
    [13]
    The exhaust after-treatment system according to claim 12, wherein the dosing frequency is adjusted so that the variation of the amount of reducing agent upstream of the SCR catalyst (6) is lower than a predetermined threshold value AR, wherein AR is +/- 5%.
    [14]
    The exhaust after-treatment system according to any one of claims 12 or 13, wherein the dosing frequency is adjusted so that the variation of the amount of reducing agent upstream of the SCR catalyst (6) is lower than a predetermined threshold value AR, wherein AR is +/- 1%.
    [15]
    The exhaust gas treatment system according to any one of claims 12 to 14, wherein the dosing frequency is adjusted so that the variation of the amount of reducing agent upstream of the ASC catalyst (4) is lower than a predetermined threshold value AR, wherein AR is +/- 5%.
    [16]
    The exhaust after-treatment system according to any one of claims 12-15, wherein the adjustment of the dosing frequency F means that the dosing frequency F is increased, and a dosing time t is reduced.
    [17]
    The exhaust after-treatment system according to claim 16, wherein the increase of the dosing frequency F means a doubling of the dosing frequency F and a halving of the dosing time t.
    [18]
    The exhaust after-treatment system according to any one of claims 12-17, wherein the system comprises a temperature sensor (18) adapted to measure the temperature in the exhaust gas upstream of the SCR catalyst (6) and / or the ASC catalyst (4) and that the dosing frequency is adjusted so as to increase the exhaust fate. temperature upstream of the SCR and / or AS C catalyst is higher than a predetermined threshold value.
    [19]
    The exhaust after-treatment system according to claim 18, wherein the increase of the dosing frequency means a doubling of the dosing frequency compared to when the temperature fell below said threshold value.
    [20]
    The exhaust aftertreatment system according to any one of claims 18 or 19, wherein said predetermined threshold value is in the range 300-450 ° C. 15
    [21]
    The exhaust after-treatment system according to claim 18, wherein the frequency is continuously adjusted depending on the temperature of the exhaust gas, the SCR catalyst and / or the ASC catalyst are sprinkled in such a way that an increased temperature leads to an increased dosing frequency.
    [22]
    The exhaust aftertreatment system of any of claims 12-21, wherein the dosing frequency is equal to or less than 2 Hz.
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    同族专利:
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE1250439|2012-05-03|
    SE1350535A|SE539586C2|2012-05-03|2013-05-02|Exhaust after-treatment system, and method in connection with such a system|US14/396,157| US9333462B2|2012-05-03|2013-05-02|Exhaust aftertreatment system and method pertaining to such a system|
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    CN201380023372.XA| CN104271910A|2012-05-03|2013-05-02|Exhaust aftertreatment system and method pertaining to such a system|
    PCT/SE2013/050482| WO2013165309A1|2012-05-03|2013-05-02|Exhaust aftertreatment system and method pertaining to such a system|
    KR1020147033945A| KR101652454B1|2012-05-03|2013-05-02|Exhaust aftertreatment system and method pertaining to such a system|
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