CN108368760A - Internal combustion engine exhaust gas purification system and internal combustion engine exhaust gas purification method - Google Patents
Internal combustion engine exhaust gas purification system and internal combustion engine exhaust gas purification method Download PDFInfo
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
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- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
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- F01N3/033—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices
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- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
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Abstract
Description
技术领域technical field
本专利是有关内燃机废气净化系统和内燃机废气净化方法。更为具体而言,公开了一种内燃机废气净化系统和内燃机废气净化方法,其中减少用于净化PM(微粒物质)的废气净化单元中的压力损失,从而使PM的再生为零或使PM再生的频率显著下降,即使使用的燃料中有高含量的硫,贵金属催化剂引发的硫中毒的发生率会减少,由此为了净化PM而耗费的燃料量也会减少。This patent relates to an internal combustion engine exhaust gas purification system and an internal combustion engine exhaust gas purification method. More specifically, an internal combustion engine exhaust gas purification system and an internal combustion engine exhaust gas purification method are disclosed, in which pressure loss in an exhaust gas purification unit for purifying PM (particulate matter) is reduced, thereby making regeneration of PM zero or regenerating PM The frequency of PM is significantly reduced, even if the fuel used has a high content of sulfur, the incidence of sulfur poisoning caused by noble metal catalysts will be reduced, and thus the amount of fuel consumed to purify PM will also be reduced.
背景技术Background technique
一般而言,在配备柴油发动机等内燃机的车辆中,如图3所示,采用了PM净化装置30来去除从内燃机中排出废气中的PM(微粒物质),该PM净化装置30是由前置的氧化催化剂单元31和载有催化剂的微粒捕集单元32构成。Generally, in a vehicle equipped with an internal combustion engine such as a diesel engine, as shown in FIG. The oxidation catalyst unit 31 and the particulate trapping unit 32 carrying the catalyst are constituted.
通常,氧化催化剂单元31使用贵金属催化剂31b氧化废气Ga当中的CO(一氧化碳)和HC,其中贵金属催化剂31b位于载体31a之上并含有贵金属,从此执行各种功能,例如升温功能,使得废气Ga的温度提升;去除SOOT的功能,将煤烟即PM的一种氧化;以及产生NO2(二氧化氮)的功能,将NO(一氧化氮)氧化而变成二氧化氮。而且设置在下游侧的载有催化剂的微粒捕集单元32能比较轻松的运行各种处理,例如,在平常的燃烧去除PM的处理;当PM再生时通过燃烧将其去除的处理;和载有催化剂的微粒捕集单元32有关的硫中毒再生的脱硫的处理。In general, the oxidation catalyst unit 31 oxidizes CO (carbon monoxide) and HC in exhaust gas Ga using a noble metal catalyst 31b which is placed on a carrier 31a and contains a noble metal, thereby performing various functions such as a temperature raising function so that the temperature of the exhaust gas Ga Lifting; the function of removing SOOT, which is a kind of oxidation of PM; and the function of generating NO 2 (nitrogen dioxide), which is the function of oxidizing NO (nitrogen monoxide) into nitrogen dioxide. Moreover, the catalyst-loaded particulate trap unit 32 disposed on the downstream side can relatively easily operate various processes, for example, the process of removing PM in normal combustion; the process of removing it by combustion when PM is regenerated; and carrying Catalyst particulate trap unit 32 related to desulfurization treatment of sulfur poisoning regeneration.
同时,氧化催化剂单元31使用包含铑(Rh)、钯(Pd)、铂(Pt)等铂族贵金属的贵金属催化剂31b,由此会导致高成本。由此开发了减少贵金属用量的贵金属催化剂31b。Meanwhile, the oxidation catalyst unit 31 uses a noble metal catalyst 31b containing a platinum group noble metal such as rhodium (Rh), palladium (Pd), platinum (Pt), and thus results in high cost. As a result, a noble metal catalyst 31b that reduces the amount of noble metal used was developed.
此外,仅仅氧化催化剂单元31的话,通过贵金属催化剂31b量少的低贵金属的催化剂涂层,能够净化附着在PM的SOOT之上的SOF(可溶性有机成分)。但是,由于没有过滤功能,因此对PM的净化率很低。In addition, if only the catalyst unit 31 is oxidized, the SOF (soluble organic fraction) adhering to the SOOT of PM can be purified by the low noble metal catalyst coating with a small amount of the noble metal catalyst 31b. However, since there is no filtering function, the purification rate of PM is very low.
因此,虽然设置有载有催化剂的微粒捕集单元32,但为了达到以质量为基准例如小于10%这样的非常小的微粒过滤效率,而对载有催化剂的微粒捕集单元32的过滤器采用多孔陶瓷的蜂窝状的通道的入口和出口交替密封的作为整体式的壁流式过滤器32a等,从而抑制了PM流向下游。Therefore, although the catalyst-loaded particulate trap unit 32 is provided, in order to achieve a very small particulate filtration efficiency of, for example, less than 10% on a mass basis, the filter of the catalyst-loaded particulate trap unit 32 is Inlets and outlets of porous ceramic honeycomb channels are alternately sealed as integral wall-flow filters 32 a and the like, thereby suppressing PM from flowing downstream.
另外,通过承载诸如贵金属催化剂、铂和碱性NOx吸收材料的组合、二氧化铈(CeO2)等的PM氧化催化剂等的催化剂32b,作用在于促进燃烧从而去除捕集的PM。In addition, by supporting the catalyst 32b such as a noble metal catalyst, a combination of platinum and a basic NOx absorbing material, a PM oxidation catalyst such as ceria (CeO 2 ), it acts to promote combustion to remove trapped PM.
再者,在载有催化剂的微粒捕集单元32中,当由于废气Ga持续低温导致被捕集的PM量增加时,会导致载有催化剂的微粒捕集单元32前后的压力差也增加。因此为了将前后的压力差保持在规定的水平以下,必须进行周期性地将PM燃烧和去除的PM再生处理。而且,当载有催化剂的微粒捕集单元32上承载的催化剂32b因硫中毒而使得有关PM燃烧去除的催化功能退化时,必须执行硫中毒再生的处理,在硫中毒再生处理中,将催化剂温度设定在大于或等于例如600摄氏度的高温而且设为浓燃状态下进行脱硫。Furthermore, when the amount of PM trapped in the catalyst-loaded particulate trap unit 32 increases due to the continued low temperature of the exhaust gas Ga, the pressure difference across the catalyst-loaded particulate trap unit 32 also increases. Therefore, in order to keep the pressure difference between front and back at a predetermined level or less, it is necessary to perform a PM regeneration process that periodically burns and removes PM. Moreover, when the catalyst 32b carried on the particulate trapping unit 32 carrying the catalyst degrades the catalytic function related to the combustion and removal of PM due to sulfur poisoning, it is necessary to perform the treatment of sulfur poisoning regeneration. In the sulfur poisoning regeneration treatment, the catalyst temperature is set to Desulfurization is performed at a high temperature of 600 degrees Celsius or higher and in a rich combustion state.
同时,由于氧化催化剂单元31和载有催化剂的微粒捕集单元32的组合需要两个废气净化单元,因此例如在不设置氧化催化剂单元而采用了壁流式过滤器的载有催化剂的微粒捕集单元中,提出了一种废气净化过滤器,在废气流入侧的隔断墙上,承载由过渡金属和碱金属盐构成第一废气净化催化剂;在废气流出侧的隔断墙上承载含有贵金属的第二废气净化催化剂(例如,请参考专利文献1)。Meanwhile, since the combination of the oxidation catalyst unit 31 and the catalyst-loaded particulate trap unit 32 requires two exhaust gas purification units, for example, in the catalyst-loaded particulate trap using a wall flow filter without an oxidation catalyst unit, In the unit, an exhaust gas purification filter is proposed. On the partition wall on the exhaust gas inflow side, the first exhaust gas purification catalyst composed of transition metal and alkali metal salt is carried; Exhaust gas purification catalyst (For example, please refer to Patent Document 1).
然后,由于废气净化过滤器使用了含有贵金属的第二废气净化催化剂,所以在使用高硫燃料的区域,从废气中排除的硫成分会导致硫中毒,氧化功能会被弱化,PM的净化功能也会被弱化。而且在为了解决硫中毒的脱硫处理中,需要高温的浓燃环境,以至于硫中毒再生时所耗的燃料增加,因此燃料利用的效率也降低了。Then, since the exhaust gas purification filter uses the second exhaust gas purification catalyst containing precious metals, in areas where high-sulfur fuel is used, the sulfur components removed from the exhaust gas cause sulfur poisoning, the oxidation function is weakened, and the PM purification function is also reduced. will be weakened. In addition, in the desulfurization treatment for solving sulfur poisoning, a high-temperature rich combustion environment is required, so that the fuel consumed in regeneration of sulfur poisoning increases, and thus the efficiency of fuel utilization also decreases.
关于硫中毒的问题,近来由多种金属构成的复合金属氧化物和特定的碱金属硫酸盐的混合催化剂对PM具有高活性并且具有高度的耐受性,因此提出了一种不需要使用铂族金属且替代贵金属催化剂的柴油机废气净化催化剂(参考专利文献2和非专利文献1)。With regard to the problem of sulfur poisoning, recently, a mixed catalyst composed of a complex metal oxide composed of various metals and a specific alkali metal sulfate has high activity against PM and is highly tolerant, so a method that does not require the use of a platinum group has been proposed. Diesel engine exhaust gas purification catalyst that is a metal and replaces a noble metal catalyst (refer to Patent Document 2 and Non-Patent Document 1).
与现有技术中的贵金属催化剂相比较,柴油机废气净化催化剂不是用NO2中的氧去燃烧PM。具体而言,是通过将空气中的氧直接提供给PM来使其燃烧,而且这种催化剂的特征在于使废气中的气态的氧分子被分解,之后被分解的氧分子提供给PM,从而达到高效能的燃烧,进而去除PM。这种柴油机废气净化催化剂不同于贵金属催化剂,几乎不会导致硫中毒。Compared with the noble metal catalysts in the prior art, the diesel exhaust gas purification catalyst does not use the oxygen in NO2 to burn PM. Specifically, it burns by directly supplying oxygen in the air to PM, and this catalyst is characterized in that the gaseous oxygen molecules in the exhaust gas are decomposed, and then the decomposed oxygen molecules are provided to PM, thereby achieving High-efficiency combustion to remove PM. Unlike noble metal catalysts, this diesel exhaust gas purification catalyst hardly causes sulfur poisoning.
与此同时,代替能去除废气中90%以上的PM的壁流式过滤器,提出了一种柴油机排放处理系统,具有少于10%的细微颗粒可以被过滤掉的细微颗粒过滤效率,并且在以质量为基准具有约30%-60%的范围的颗粒过滤效率的颗粒过滤器(partial filter)上承载具有NOX转换效果的SCR催化剂(例如,参见专利文献3)。At the same time, instead of the wall-flow filter that can remove more than 90% of PM in exhaust gas, a diesel engine emission treatment system is proposed that has a fine particle filtration efficiency in which less than 10% of fine particles can be filtered out, and in An SCR catalyst having a NOx conversion effect is supported on a partial filter having a particle filtration efficiency in the range of about 30% to 60% on a mass basis (for example, see Patent Document 3).
颗粒过滤器由孔隙度在60%到95%之间的金属泡沫过滤器、金属网等组成。另外,粒状的陶瓷也可以作为颗粒过滤器来使用,氧化催化剂和PM氧化催化剂附着在陶瓷粒子的表面上,由此能够通过废气的热来燃烧在颗粒过滤器中捕集并堆积的PM。此外,也存在其他类型的颗粒过滤器,其中壁流式过滤器中单元的一端的封口部分被减少。The particle filter is composed of a metal foam filter with a porosity between 60% and 95%, metal mesh, etc. In addition, granular ceramics can also be used as a particulate filter, and the oxidation catalyst and PM oxidation catalyst are attached to the surface of the ceramic particles, whereby PM trapped and accumulated in the particulate filter can be burned by the heat of exhaust gas. In addition, there are other types of particulate filters in which the plugged portion of one end of the unit is reduced in the wall-flow filter.
<引用列表><reference list>
专利文献patent documents
专利文献1:日本专利特开2009-247931号公报Patent Document 1: Japanese Patent Laid-Open No. 2009-247931
专利文献2:日本专利特开2014-508号公报Patent Document 2: Japanese Patent Laid-Open No. 2014-508
专利文献3:日本专利特表2012-528705号公报Patent Document 3: Japanese Patent Application Publication No. 2012-528705
非专利文献non-patent literature
非专利文献1:宫川达郎(Tatsuro MIYAGAWA)、中岛隆弘(Takahiro NAKAJIMA)、久保雅大(Masahiro KUBO)和须贺亮介(Ryosuke SUGA),《Catalyst consisting ofcombined metal oxide and alkali metal sulfate for diesel exhaust emissions》,第20-24页,第57卷第1号,《Panasonic Technical Journal》,2011年4月。Non-Patent Document 1: Tatsuro MIYAGAWA, Takahiro NAKAJIMA, Masahiro KUBO and Ryosuke SUGA, "Catalyst consisting of combined metal oxide and alkali metal sulfate for diesel exhaust emissions”, pp. 20-24, Vol. 57, No. 1, Panasonic Technical Journal, April 2011.
发明内容Contents of the invention
技术问题technical problem
同时,在采用了专利文献2和非专利文献1中公开的壁流过滤器的载有催化剂的微粒捕集单元不仅很容易收集PM,其对PM的净化率也很高。然而,载有催化剂的微粒捕集单元也存在一些问题,例如,压力减损巨大、PM捕集时容易造成堵塞,以及因为堵塞之后更容易使载有催化剂的微粒捕集单元之前和之后的压力差变得更加明显。因此,因为PM再生而引起的废气温度的升高,在NO2生成过程中PM再生的频率也增加,因此为了PM再生而耗费的燃料量也会增加,由此导致燃料利用效率变差。Meanwhile, the catalyst-loaded particulate trap unit using the wall flow filter disclosed in Patent Document 2 and Non-Patent Document 1 not only easily collects PM, but also has a high purification rate for PM. However, the catalyst-loaded particulate trap unit also has some problems, such as large pressure loss, easy clogging during PM capture, and pressure difference between before and after the catalyst-loaded particulate trap unit due to clogging. become more apparent. Therefore, because of the increase in exhaust gas temperature caused by PM regeneration, the frequency of PM regeneration during NO2 generation also increases, and thus the amount of fuel consumed for PM regeneration also increases, resulting in poor fuel efficiency.
此外,在专利文献3中公开的颗粒过滤器,与壁流式过滤器相比较,其初始阶段的压力损失要更小,而且在PM捕集时压力损失的增加也更小。因此,采用颗粒过滤器是降低载有催化剂的微粒捕集单元压力损失的有效的途径。同时,PM的细颗粒过滤的效能也很高,因此PM可能不会被完全净化。In addition, the particulate filter disclosed in Patent Document 3 has a smaller pressure loss in the initial stage and a smaller increase in pressure loss during PM capture than a wall-flow filter. Therefore, the use of particulate filters is an effective way to reduce the pressure loss of particulate trapping units loaded with catalysts. At the same time, the fine particle filtering efficiency of PM is also high, so PM may not be completely purified.
本专利所公开的内燃机废气净化系统和内燃机废气净化的方法不仅可以减少因为捕集PM的载有催化剂的微粒捕集单元导致的压力损失的增加,也能够避免在使用含有高浓度的硫的燃料之时的贵金属中的硫中毒,因此有可能在较长时间阶段保持PM净化的能力。结果,载有催化剂的微粒捕集单元的PM再生可以是零或者PM再生频率可能会显著降低。The internal combustion engine exhaust gas purification system and the internal combustion engine exhaust gas purification method disclosed in this patent can not only reduce the increase in pressure loss caused by the catalyst-loaded particle trapping unit that traps PM, but also avoid the use of fuels containing high concentrations of sulfur. Sulfur poisoning in precious metals at that time, so it is possible to maintain the ability of PM purification for a longer period of time. As a result, the PM regeneration of the catalyst-loaded particulate trap unit may be zero or the PM regeneration frequency may be significantly reduced.
解决问题的手段means of solving problems
本发明的内燃机废气净化系统包括:设置在内燃机的排气通道中的载有催化剂的微粒捕集单元,其中承载贵金属催化剂的废气净化单元并非设置在所述载有催化剂的微粒捕集单元的上游侧的排气通路中,其中所述载有催化剂的微粒捕集单元的过滤器由颗粒过滤器(partial filter)构成,而且所述颗粒过滤器所承载的催化剂是不含有贵金属的非贵金属催化剂。The internal combustion engine exhaust gas purification system of the present invention includes: a catalyst-loaded particulate trap unit arranged in an exhaust passage of the internal combustion engine, wherein the exhaust gas purification unit loaded with a noble metal catalyst is not arranged upstream of the catalyst-loaded particulate trap unit In the exhaust passage on the side, wherein the filter of the catalyst-loaded particulate trap unit is composed of a partial filter, and the catalyst carried by the particulate filter is a non-precious metal catalyst that does not contain noble metal.
也就是说,废气中的PM净化功能的实施不是基于配置在上游侧的氧化催化剂单元和配置在下游侧的载有催化剂的微粒捕集单元的配合来完成,其运行是基于这么一种结构,在该结构中不包括氧化催化剂单元而仅有载有催化剂的微粒捕集单元。此外,颗粒过滤器上承载的非贵金属催化剂由不含贵金属的化合物构成,由此氧化和燃烧PM是通过非贵金属催化剂来完成的。That is, the performance of the PM purification function in the exhaust gas is not performed based on the cooperation of the oxidation catalyst unit arranged on the upstream side and the catalyst-carrying particulate trap unit arranged on the downstream side, and its operation is based on such a structure that In this structure, no oxidation catalyst unit is included but only a catalyst-loaded particle trap unit. In addition, the non-precious metal catalyst supported on the particulate filter is composed of a compound that does not contain noble metal, whereby oxidation and combustion of PM are performed by the non-precious metal catalyst.
此处,颗粒过滤器指的是具有以质量为基准30%和60%之间的微粒可以被过滤的微粒过滤效率的过滤器。颗粒过滤器可以由金属发泡体、金属网、粒状陶瓷等构成。此外,颗粒过滤器的初始压力损失与壁流式过滤器相比较少,并且在捕集PM时压力损失的增加率较低。因此,在颗粒过滤器中,氧化催化剂和PM氧化催化剂被承载在金属发泡体孔、金属网和粒状陶瓷的表面上。Here, the particle filter refers to a filter having a particle filtration efficiency at which particles between 30% and 60% by mass can be filtered. The particle filter can be composed of metal foam, metal mesh, granular ceramics, and the like. In addition, the initial pressure loss of the particulate filter is less than that of the wall-flow filter, and the increase rate of the pressure loss is lower when trapping PM. Therefore, in the particulate filter, the oxidation catalyst and the PM oxidation catalyst are supported on the surfaces of the pores of the metal foam, the metal mesh, and the granular ceramics.
根据上述结构,由于使用颗粒过滤器作为捕集PM的过滤器结构,因此与使用将多孔质陶瓷的蜂窝状流路的入口和出口交替进行密封的整体蜂窝型的壁流式过滤器的情况相比,可以显著降低由压力损失和PM捕集引起的压力损失的增加比例。因此,用于解决压力损失的增长的PM再生可以是零或者其频率可以显著减小,并且由此可以减少用于生成PM而被消耗的燃料量,从而提高燃料的利用效率。According to the above structure, since the particulate filter is used as the filter structure for trapping PM, it is comparable to the case of using a monolithic honeycomb type wall flow filter in which the inlet and outlet of the honeycomb flow path of porous ceramics are alternately sealed. ratio, the increase ratio of pressure loss caused by pressure loss and PM trapping can be significantly reduced. Accordingly, PM regeneration for addressing the increase in pressure loss may be zero or its frequency may be significantly reduced, and thus the amount of fuel consumed for generating PM may be reduced, thereby improving fuel utilization efficiency.
此外,颗粒过滤器上承载的催化剂是不含有贵金属的非贵金属催化剂,因此,即使使用含硫量高的燃料而使排出的废气中的硫的成分相对较高,因为催化剂中不含有贵金属,仍然可能避免硫中毒的发生。此外,由于非贵金属的催化剂包含了极少量硫中毒,因此可以抑制PM氧化功能弱化从而维持PM净化功能,由此可以补偿因为采用颗粒过滤器导致的PM净化率的弱化的问题。In addition, the catalyst carried on the particulate filter is a non-precious metal catalyst that does not contain noble metals. Therefore, even if the sulfur content in the exhaust gas is relatively high due to the use of fuel with a high sulfur content, the catalyst does not contain noble metals. It is possible to avoid the occurrence of sulfur poisoning. In addition, since the non-noble metal catalyst contains a very small amount of sulfur poisoning, it is possible to suppress the weakening of the PM oxidation function to maintain the PM purification function, thereby compensating for the weakening of the PM purification rate due to the use of the particulate filter.
另外,内燃机废气净化系统不含承载贵金属催化剂的废气净化单元,即氧化催化剂单元,因此可以减少因为使用氧化催化剂单元而引发的压力损失。In addition, the exhaust gas purification system of an internal combustion engine does not contain an exhaust gas purification unit carrying a noble metal catalyst, that is, an oxidation catalyst unit, so that the pressure loss caused by the use of the oxidation catalyst unit can be reduced.
此外,在该内燃机废气净化系统中,非贵金属催化剂可以是由多种金属构成的复合金属氧化物和碱金属硫酸盐构成的混合催化剂。Furthermore, in this internal combustion engine exhaust gas purification system, the non-noble metal catalyst may be a mixed catalyst composed of a composite metal oxide composed of a plurality of metals and an alkali metal sulfate.
根据以上描述的结构,这一有多种金属构成的复合金属氧化物和碱金属硫酸盐构成的混合催化剂并没有使用铂金属催化剂。而且,和贵金属催化剂不同,这种混合催化剂没有利用NO2中的氧来燃烧PM,而是通过向PM中直接提供大气中的氧气而使PM燃烧,因此可以抑制硫中毒的发生率,而且使得PM有更好的净化效率。其结果是,可以补偿颗粒过滤器的低PM收集率并且提高作为载有催化剂的微粒捕集单元的PM净化率。According to the structure described above, this mixed catalyst composed of composite metal oxide composed of multiple metals and alkali metal sulfate does not use platinum metal catalyst. Moreover, unlike noble metal catalysts, this hybrid catalyst does not use oxygen in NO2 to burn PM, but burns PM by directly supplying atmospheric oxygen to PM, so the incidence of sulfur poisoning can be suppressed, and it makes PM has better purification efficiency. As a result, it is possible to compensate the low PM collection rate of the particulate filter and improve the PM purification rate as the catalyst-loaded particulate trap unit.
本发明的内燃机废气净化是内燃机废气净化的方法,其中废气中的微粒物质由设置在废气排气通道中的载有催化剂的微粒捕集单元来净化,包括从内燃机的排气通道排出的废气通过载有催化剂的微粒捕集单元,该单元是承载不含有重金属的非贵金属催化剂的颗粒过滤器,而不是使废气通过载有贵金属催化剂的废气净化单元。根据内燃机废气净化方法,可以获得与内燃机废气净化系统相同的效果。The internal combustion engine exhaust gas purification of the present invention is a method for internal combustion engine exhaust gas purification, wherein the particulate matter in the exhaust gas is purified by a catalyst-loaded particle trapping unit arranged in the exhaust gas exhaust passage, including exhaust gas discharged from the exhaust passage of the internal combustion engine passing through A catalyst-loaded particulate trap unit, which is a particulate filter that carries a non-precious metal catalyst that does not contain heavy metals, instead of passing exhaust gas through an exhaust gas purification unit that carries a noble metal catalyst. According to the internal combustion engine exhaust gas purification method, the same effect as that of the internal combustion engine exhaust gas purification system can be obtained.
突出的效果outstanding effect
根据本发明内燃机废气净化系统和内燃机废气净化方法公开的内容,采用颗粒过滤器作为捕集PM(颗粒物)的过滤器结构,压力损失和压力损失的增加会显著降低,从而能使得为解决压力损失的增加问题的PM再生为零或者其频率可以显著减小。结果,可以减少用于生成PM而被消耗的燃料量,从而提高燃料的利用效率。According to the disclosed content of the internal combustion engine exhaust gas purification system and the internal combustion engine exhaust gas purification method of the present invention, the particle filter is used as the filter structure for trapping PM (particulate matter), and the pressure loss and the increase of the pressure loss can be significantly reduced, thereby enabling to solve the problem of pressure loss The increase in the problem of PM regeneration is zero or its frequency can be significantly reduced. As a result, the amount of fuel consumed for generating PM can be reduced, thereby improving fuel utilization efficiency.
另外,因为颗粒过滤器上承载的催化剂采用的是非贵金属催化剂,因此即使在使用硫浓度高的燃料的情况下,也能够避免硫中毒的发生。由此,能够抑制PM氧化功能弱化并保持PM净化功能,因而能够补偿由于采用颗粒过滤器而导致的PM净化率的弱化。In addition, since the catalyst carried on the particulate filter is a non-precious metal catalyst, sulfur poisoning can be avoided even when fuel with a high sulfur concentration is used. Thereby, deterioration of the PM oxidation function can be suppressed and the PM purification function can be maintained, thus compensating for the deterioration of the PM purification rate due to the use of the particulate filter.
此外,由于不设置承载贵金属催化剂的排气净化单元,因此可以降低压力损失。In addition, since an exhaust gas purification unit carrying a noble metal catalyst is not provided, pressure loss can be reduced.
也就是说,通过不使用氧化催化剂单元和采用颗粒过滤器的这种组合,用于净化PM的废气净化单元中的压力损失和其中的压力损失的增加会减少。另外,通过采用颗粒过滤器和采用非贵金属催化剂的这种组合,不仅可以避免硫中毒,也能保持低程度的压力损失和高程度的PM净化率。根据以上三种组合产生的两种效果,不仅可以减低PM的再生频率,通过消除硫中毒的再生,也能减少由于要保持PM净化率而导致的燃料消耗的增加。That is, by this combination of not using the oxidation catalyst unit and using the particulate filter, the pressure loss in the exhaust gas purification unit for purifying PM and the increase in pressure loss therein can be reduced. In addition, by using this combination of particulate filter and non-precious metal catalyst, not only sulfur poisoning can be avoided, but also a low degree of pressure loss and a high degree of PM purification rate can be maintained. According to the two effects produced by the above three combinations, not only the frequency of PM regeneration can be reduced, but also the increase in fuel consumption due to maintaining the PM purification rate can be reduced by eliminating the regeneration of sulfur poisoning.
附图说明Description of drawings
图1是表示根据本发明公开的一个实施例,即内燃机的废气净化系统的构成图。FIG. 1 is a configuration diagram showing an exhaust gas purification system of an internal combustion engine according to an embodiment disclosed in the present invention.
图2是表示仅由载有催化剂的微粒捕集单元构成的PM净化单元的构成图。FIG. 2 is a configuration diagram showing a PM purification unit composed only of a catalyst-carrying particulate trap unit.
图3是表示PM净化单元由氧化催化剂单元和载有催化剂的微粒捕集单元的组合形成的构成图。FIG. 3 is a configuration diagram showing a PM purification unit composed of a combination of an oxidation catalyst unit and a catalyst-carrying fine particle trap unit.
具体实施方式Detailed ways
以下是通过参考附图,来具体描述公开的内燃机废气净化系统和内燃机废气净化方法的实施方式。The following is a detailed description of the embodiments of the disclosed internal combustion engine exhaust gas purification system and internal combustion engine exhaust gas purification method with reference to the accompanying drawings.
如图1所示,对内燃机废气净化系统1进行说明。在装有内燃机废气净化系统1的发动机(内燃机)10中,从大气导入的新鲜空气A依次通过进气通路14中的空气净化器17、涡轮增压装置(涡轮式增压器)18中的压缩机18b、中冷器19a和进气节流阀19b,之后新鲜空气A从进气阀12进入汽缸10a。根据需要,废气Ge(EGR gas)会随同新鲜空气A从EGR通路16流入进气通路14。As shown in FIG. 1 , an internal combustion engine exhaust gas purification system 1 will be described. In the engine (internal combustion engine) 10 equipped with the internal combustion engine exhaust gas purification system 1, the fresh air A introduced from the atmosphere passes through the air cleaner 17 in the intake passage 14, the turbocharger (turbocharger) 18 in the Compressor 18b, intercooler 19a and intake throttle valve 19b, after which fresh air A enters cylinder 10a from intake valve 12. Exhaust gas Ge (EGR gas) flows from the EGR passage 16 into the intake passage 14 along with the fresh air A as required.
吸入气体(A+Ge)被设置在汽缸10a内的活塞10b压缩,从燃料喷射装置11喷射的燃料开始燃烧,由此产生发动机10的动力。燃料燃烧产生的废气G通过排气阀13流出到排气通道15中,并且一部分废气G作为EGR气体Ge流入EGR通道16中。此时,剩余的废气Ga(=G-Ge)经由涡轮式增压器18的涡轮18a通过排气净化装置20之后被净化,然后剩余的废气Ga经由消声器(未标示)作为净化的废气Gc排放到空气中去。The intake gas (A+Ge) is compressed by the piston 10 b provided in the cylinder 10 a, and the fuel injected from the fuel injection device 11 starts to combust, thereby generating power of the engine 10 . Exhaust gas G generated by fuel combustion flows out into exhaust passage 15 through exhaust valve 13, and a part of exhaust gas G flows into EGR passage 16 as EGR gas Ge. At this time, the remaining exhaust gas Ga (=G-Ge) is purified after passing through the exhaust purification device 20 via the turbine 18a of the turbocharger 18, and then the remaining exhaust gas Ga is discharged as purified exhaust gas Gc through a muffler (not shown). into the air.
此外,排气净化装置20不配备前置(pre-stage)氧化催化剂单元,而是在上游侧依次配有载有催化剂的微粒捕集单元21、选择性还原型催化剂单元(SCR)22和后置的(rear-stage)氧化催化剂单元(DOC)23。另外,还具有压力传感器24和温度传感器25,通过该压力传感器24能检测载有催化剂的微粒捕集单元21之前和之后的压力差;通过该温度传感器25,可以提供流入废气净化装置20中的废气Ga的温度。In addition, the exhaust purification device 20 is not equipped with a pre-stage oxidation catalyst unit, but is sequentially equipped with a catalyst-loaded particulate trap unit 21, a selective reduction catalyst unit (SCR) 22, and a post-stage oxidation catalyst unit on the upstream side. A rear-stage oxidation catalyst unit (DOC) 23 is installed. In addition, it also has a pressure sensor 24 and a temperature sensor 25, through which the pressure difference before and after the particle trapping unit 21 loaded with catalyst can be detected; The temperature of the exhaust gas Ga.
此外,设置将燃料F喷射入废气Ga中的燃料喷嘴26,作用在于必要时帮助载有催化剂的微粒捕集单元21中的PM再生,该过程发生在位于载有催化剂的微粒捕集单元21的上游侧的排气通道15中。另外,在选择性还原型催化剂单元22的上游侧存在尿素喷射装置27,尿素喷射装置27作用是将作为NOx还原剂的尿素供给到用于NOx净化的选择性还原型催化剂单元22上。In addition, a fuel nozzle 26 for injecting fuel F into the exhaust gas Ga is provided to assist PM regeneration in the catalyst-loaded particulate trap unit 21 when necessary, and this process occurs in the catalyst-loaded particulate trap unit 21. In the exhaust passage 15 on the upstream side. In addition, on the upstream side of the selective reduction catalyst unit 22, there is a urea injection device 27 for supplying urea as a NOx reducing agent to the selective reduction catalyst unit 22 for NOx purification.
设有控制燃料喷嘴26中的燃料喷射和尿素喷射装置27中的尿素喷射的控制器41。控制器41可以集成到控制发动机10的整体运行状态的整体系统控制器40中,或者该控制器也可以单独设置。A controller 41 is provided which controls fuel injection in the fuel nozzle 26 and urea injection in the urea injection device 27 . The controller 41 may be integrated into the overall system controller 40 that controls the overall operating state of the engine 10, or the controller may be provided separately.
如图2所示,载有催化剂的微粒捕集单元21的过滤器构造由颗粒过滤器21a形成,颗粒过滤器21a上承载的催化剂是非贵金属催化剂21,其中并不含有贵金属。As shown in FIG. 2, the filter structure of the catalyst-loaded particulate trap unit 21 is formed of a particulate filter 21a on which the catalyst is a non-precious metal catalyst 21 that does not contain noble metal.
颗粒过滤器21a是具有以质量为基准30%和60%之间的微粒可被过滤的微粒过滤效率的过滤器。与壁流式过滤器相比,颗粒过滤器21的初始压力损失较低,并且在收集PM时的压力损失的增长也较低。The particle filter 21a is a filter having a particle filtration efficiency at which particles between 30% and 60% by mass can be filtered. Compared with the wall-flow filter, the initial pressure loss of the particulate filter 21 is lower, and the increase in pressure loss when collecting PM is also lower.
颗粒过滤器21a可以由金属发泡体、金属网,粒状陶瓷等形成。通过将壁流式过滤器的端部处的密封部分地去除来形成。在颗粒过滤器21a中,在金属发泡体的孔的表面、金属网的表面和粒状陶瓷等的表面等上载有非贵金属催化剂21b。The particulate filter 21a may be formed of metal foam, metal mesh, granular ceramics, or the like. Formed by partially removing the seal at the end of the wall flow filter. In the particulate filter 21a, the non-precious metal catalyst 21b is supported on the surface of the pores of the metal foam, the surface of the metal mesh, the surface of granular ceramics, and the like.
非贵金属的催化剂21b可能以混合催化剂的形式来体现,由具有多种金属的复合金属氧化物和碱金属硫酸盐构成。过渡金属硫酸盐或过渡金属氧化物与碱金属硫酸盐的混合物具有理想的PM燃烧活性,五氧化二钒(V2O5)和硫酸钾(K2SO4)的混合物以及硫酸氧钒(VOSO4)和铯硫酸盐(Cs3SO4)等也可以达到以上的效果。The non-noble metal catalyst 21b may be embodied in the form of a mixed catalyst composed of a composite metal oxide with multiple metals and an alkali metal sulfate. The mixture of transition metal sulfate or transition metal oxide and alkali metal sulfate has ideal PM combustion activity, the mixture of vanadium pentoxide (V 2 O 5 ) and potassium sulfate (K 2 SO 4 ) and vanadyl sulfate (VOSO 4 ) and cesium sulfate (Cs 3 SO 4 ) can also achieve the above effects.
也就是说,废气Ga中的PM净化功能不是基于位于上游侧的氧化催化剂单元和位于下游侧的载有催化剂的微粒捕集单元21的组合来完成,而是基于废止了氧化催化剂单元而仅设置载有催化剂的微粒捕集单元21这样的构造来完成。此外,作为净化催化剂的非贵金属催化剂,由不包含例如铂(Pt)、钯(Pd)等贵金属的化合物组成,被负载在颗粒过滤器21a上,由此通过以上非贵金属的催化剂21b的催化作用来氧化和燃烧PM。That is, the PM purification function in the exhaust gas Ga is not performed based on the combination of the oxidation catalyst unit located on the upstream side and the catalyst-carrying particulate trap unit 21 located on the downstream side, but only based on the abolished oxidation catalyst unit Such a configuration of the catalyst-loaded particulate trapping unit 21 is completed. In addition, a non-noble metal catalyst as a purification catalyst, composed of a compound that does not contain noble metals such as platinum (Pt), palladium (Pd), is loaded on the particulate filter 21a, thereby passing through the catalytic action of the above non-noble metal catalyst 21b to oxidize and burn PM.
如本发明公开的实施例中的实施方式所示,内燃机废气净化方法是在载有催化剂的微粒捕集单元21中来净化废气Ga中的PM,其中载有催化剂的微粒捕集单元21位于发动机10的排气通道15中。此外,内燃机废气净化方法被运行,从而从发动机10排出的废气Ga不通过载有贵金属催化剂的废气净化单元,而是通过具有由颗粒过滤器21a形成的过滤器结构并且承载的催化剂是不含有贵金属的非贵金属催化剂21b的载有催化剂的微粒捕集单元21。以上就是废气Ga的净化处理过程。As shown in the implementation of the disclosed embodiments of the present invention, the exhaust gas purification method of the internal combustion engine is to purify the PM in the exhaust gas Ga in the particulate trap unit 21 loaded with the catalyst, wherein the particulate trap unit 21 loaded with the catalyst is located in the engine 10 in the exhaust passage 15. In addition, the internal combustion engine exhaust gas purification method is operated so that the exhaust gas Ga exhausted from the engine 10 does not pass through the exhaust gas purification unit carrying the noble metal catalyst, but passes through the filter structure having a particulate filter 21a and the carried catalyst does not contain the noble metal The catalyst-loaded particulate trapping unit 21 of the non-noble metal catalyst 21b. The above is the purification treatment process of exhaust gas Ga.
根据本发明公开的内燃机废气净化系统1和内燃机废气净化方法,与壁流式过滤器32a相比,由于采用了颗粒过滤器21a作为捕集PM的构造,由此可以显著减少压力损失和减低由PM收集带来的压力损失的增加。结果,用于解决压力损失增加的PM再生可以为零,或PM再生的频率可以显着降低。因此,可以减低生成PM所消耗的燃料用量和提高燃料利用的效率。According to the internal combustion engine exhaust gas purification system 1 and the internal combustion engine exhaust gas purification method disclosed in the present invention, compared with the wall flow filter 32a, since the particle filter 21a is used as the structure for trapping PM, the pressure loss and the pressure loss caused by the PM can be significantly reduced. Increased pressure loss from PM collection. As a result, PM regeneration to account for increased pressure loss may be zero, or the frequency of PM regeneration may be significantly reduced. Therefore, it is possible to reduce the amount of fuel consumed to generate PM and improve the efficiency of fuel utilization.
此外,有不含贵金属的非贵金属的催化剂21b承载在颗粒过滤器21a上。因此,即使使用了高含量硫的燃料,使得较高浓度的硫成分流入废气Ga中,也就是说发动机10的燃料中硫的成分比较高,但是由于没有使用含有贵金属的催化剂,因此仍然能够避免运用贵金属催化剂时常发生硫中毒。此外,由于使用的是非贵金属催化剂21b,所以可以抑制PM氧化功能的弱化并保持PM净化功能,因此也可以补偿由于采用颗粒过滤器21a而引起的PM净化率的弱化。In addition, a non-noble metal catalyst 21b containing no noble metal is supported on the particulate filter 21a. Therefore, even if fuel with a high sulfur content is used, so that a relatively high concentration of sulfur components flows into the exhaust gas Ga, that is to say, the fuel of the engine 10 has a relatively high sulfur content, but it can still be avoided because no catalyst containing noble metals is used. Sulfur poisoning often occurs with noble metal catalysts. In addition, since the non-precious metal catalyst 21b is used, it is possible to suppress the deterioration of the PM oxidation function and maintain the PM purification function, so it is also possible to compensate for the deterioration of the PM purification rate due to the use of the particulate filter 21a.
另外,根据图3中现有技术中的PM净化装置30所示,内燃机废气净化系统1不配备有氧化催化剂单元31,因此可以降低由于使用氧化催化剂单元31而引起的压力损失。In addition, according to PM purification device 30 in the prior art shown in FIG. 3 , internal combustion engine exhaust gas purification system 1 is not equipped with oxidation catalyst unit 31 , so pressure loss due to use of oxidation catalyst unit 31 can be reduced.
也就是说,通过不采用氧化催化剂单元31和采取颗粒过滤器21的组合,在废气净化单元21中净化PM导致的压力损失和由此带来的压力的增长都会降低。此外,通过采用颗粒过滤器21a和采用非贵金属催化剂21b的组合,可以避免硫中毒,同时保持低程度的压力损失和高程度的PM净化率。根据上述三种组合而产生的两种效果,减少PM再生的频率,并且通过消除硫中毒再生,也能抑制为了保持PM净化能力而导致的燃料消耗的增加。That is, by the combination of not employing the oxidation catalyst unit 31 and employing the particulate filter 21, the pressure loss caused by purifying PM in the exhaust gas purifying unit 21 and the resulting increase in pressure are reduced. Furthermore, by a combination of using the particulate filter 21a and using the non-precious metal catalyst 21b, sulfur poisoning can be avoided while maintaining a low degree of pressure loss and a high degree of PM purification rate. According to the two effects produced by the above three combinations, the frequency of PM regeneration is reduced, and by eliminating sulfur poisoning regeneration, an increase in fuel consumption for maintaining PM purification capability can also be suppressed.
本申请要求的优先权是基于2015年12月14日提交的日本专利申请(JP-2015-243228),其全部内容通过引用并入本文。The priority claimed by this application is based on Japanese Patent Application (JP-2015-243228) filed on December 14, 2015, the entire contents of which are incorporated herein by reference.
产业应用能力Industrial Application Capability
根据内燃机废气净化系统和内燃机废气净化方法,用于净化PM的废气净化单元中的压力损失减少,因此能够使PM再生为零,或PM再生的的频率显著降低,甚至即使使用含有高硫的燃料时,能够避免发生贵金属催化剂的硫中毒,并且为了净化PM所消耗的燃料量也显著降低。According to the internal combustion engine exhaust gas purification system and the internal combustion engine exhaust gas purification method, the pressure loss in the exhaust gas purification unit for purifying PM is reduced, so that PM regeneration can be made zero, or the frequency of PM regeneration can be significantly reduced, even when fuel containing high sulfur is used When , the sulfur poisoning of the noble metal catalyst can be avoided, and the amount of fuel consumed to purify PM is also significantly reduced.
附图标记说明Explanation of reference signs
1:内燃机废气净化系统1: Internal combustion engine exhaust gas purification system
10:发动机(内燃机)10: Engine (internal combustion engine)
15:排气通道15: exhaust channel
20:废气净化装置20: Exhaust gas purification device
21:载有催化剂的微粒捕集单元21: Particle trapping unit loaded with catalyst
21a:颗粒过滤器21a: Particle filter
21b:净化催化剂21b: Purification Catalyst
22:选择性还原型催化剂单元(SCR)22: Selective reduction catalyst unit (SCR)
23:后置氧化催化剂单元(DOC)23: Post Oxidation Catalyst Unit (DOC)
26:燃料喷嘴26: Fuel nozzle
27:尿素喷射装置27: Urea injection device
40:整体系统控制器40: Overall System Controller
41:控制器41: Controller
A:新鲜空气A: fresh air
A+Ge:吸入的气体A+Ge: inhaled gas
G:产生的废气G: Exhaust gas generated
Ga:进入废气净化系统中的废气(G-Ge)Ga: Exhaust gas entering the exhaust gas purification system (G-Ge)
Gc:净化了的废气Gc: Purified exhaust gas
Ge:废气(EGR气体)Ge: exhaust gas (EGR gas)
Claims (3)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2015243228A JP2017110499A (en) | 2015-12-14 | 2015-12-14 | Exhaust gas purification system for internal combustion engine and exhaust gas purification method for internal combustion engine |
| JP2015-243228 | 2015-12-14 | ||
| PCT/JP2016/087082 WO2017104668A1 (en) | 2015-12-14 | 2016-12-13 | Internal-combustion engine exhaust gas purification system, and internal-combustion engine exhaust gas purification method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108368760A true CN108368760A (en) | 2018-08-03 |
Family
ID=59056730
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201680072500.3A Withdrawn CN108368760A (en) | 2015-12-14 | 2016-12-13 | Internal combustion engine exhaust gas purification system and internal combustion engine exhaust gas purification method |
Country Status (4)
| Country | Link |
|---|---|
| JP (1) | JP2017110499A (en) |
| CN (1) | CN108368760A (en) |
| PH (1) | PH12018501202A1 (en) |
| WO (1) | WO2017104668A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110925065A (en) * | 2019-12-17 | 2020-03-27 | 东风汽车集团有限公司 | Active regeneration and classification control method of particle filter |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002174111A (en) * | 2000-12-07 | 2002-06-21 | Matsushita Electric Ind Co Ltd | Exhaust gas purification material |
| JP2011522694A (en) * | 2008-05-29 | 2011-08-04 | コーニング インコーポレイテッド | Partial wall flow filter and method |
| WO2012147333A1 (en) * | 2011-04-28 | 2012-11-01 | パナソニック株式会社 | Molten salt-type off gas purification catalyst and off gas purification filter |
| CN104285049A (en) * | 2012-05-11 | 2015-01-14 | 五十铃自动车株式会社 | Exhaust gas purification system and exhaust gas purification method |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005144378A (en) * | 2003-11-18 | 2005-06-09 | Hino Motors Ltd | Exhaust purification equipment |
-
2015
- 2015-12-14 JP JP2015243228A patent/JP2017110499A/en active Pending
-
2016
- 2016-12-13 WO PCT/JP2016/087082 patent/WO2017104668A1/en not_active Ceased
- 2016-12-13 CN CN201680072500.3A patent/CN108368760A/en not_active Withdrawn
-
2018
- 2018-06-06 PH PH12018501202A patent/PH12018501202A1/en unknown
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002174111A (en) * | 2000-12-07 | 2002-06-21 | Matsushita Electric Ind Co Ltd | Exhaust gas purification material |
| JP2011522694A (en) * | 2008-05-29 | 2011-08-04 | コーニング インコーポレイテッド | Partial wall flow filter and method |
| WO2012147333A1 (en) * | 2011-04-28 | 2012-11-01 | パナソニック株式会社 | Molten salt-type off gas purification catalyst and off gas purification filter |
| CN104285049A (en) * | 2012-05-11 | 2015-01-14 | 五十铃自动车株式会社 | Exhaust gas purification system and exhaust gas purification method |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110925065A (en) * | 2019-12-17 | 2020-03-27 | 东风汽车集团有限公司 | Active regeneration and classification control method of particle filter |
| CN110925065B (en) * | 2019-12-17 | 2021-11-12 | 东风汽车集团有限公司 | Active regeneration grading control method for particle catcher |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2017104668A1 (en) | 2017-06-22 |
| PH12018501202A1 (en) | 2019-02-11 |
| JP2017110499A (en) | 2017-06-22 |
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Application publication date: 20180803 |