CN100402806C - A wall-flow diesel vehicle exhaust particulate filter-regeneration device - Google Patents
A wall-flow diesel vehicle exhaust particulate filter-regeneration device Download PDFInfo
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Abstract
本发明涉及柴油车尾气碳烟过滤系统,具体地说是一种壁流式柴油车尾气微粒过滤-再生装置,包括电源、可控喷油装置、燃油分散单元、电加热发热体、火焰分散单元、壁流式泡沫陶瓷微粒过滤器;其中电加热发热体以及电加热发热体前后的燃油分散单元、火焰分散单元与壁流式泡沫陶瓷微粒过滤器一起安装于与柴油发动机排气管相连的净化器封装外壳内;壁流式泡沫陶瓷微粒过滤器由多片碳化硅泡沫陶瓷板平行组合而成,碳化硅泡沫陶瓷板具有单一泡沫孔径或变化孔径。本发明装置具有高的净化效率和良好的原位再生能力,在对柴油车微粒进行有效过滤后,可在车载电源正常供电和车辆正常运行情况下,实现车载状态的智能化再生,从而具有很好的耐久性能。
The invention relates to a diesel vehicle exhaust soot filter system, in particular to a wall-flow type diesel vehicle exhaust particulate filter-regeneration device, including a power supply, a controllable fuel injection device, a fuel dispersion unit, an electric heating element, and a flame dispersion unit , wall-flow ceramic foam particulate filter; the electric heating element and the fuel dispersing unit before and after the electric heating heating element, the flame dispersing unit and the wall-flow ceramic foam particulate filter are installed in the purification system connected to the exhaust pipe of the diesel engine. The wall-flow ceramic foam particle filter is composed of multiple silicon carbide foam ceramic plates in parallel, and the silicon carbide foam ceramic plates have a single foam pore size or variable pore size. The device of the present invention has high purification efficiency and good in-situ regeneration ability. After effectively filtering the diesel vehicle particles, it can realize intelligent regeneration of the vehicle state under the normal power supply of the vehicle power supply and the normal operation of the vehicle, thus having great advantages. Good durability.
Description
技术领域 technical field
本发明涉及柴油车尾气碳烟过滤系统,具体地说是一种以碳化硅泡沫陶瓷为过滤装置载体的壁流式柴油车尾气微粒过滤-再生装置,可有效降低柴油车的碳烟排放并在柴油车正常供电和正常行驶状态下实现再生。The invention relates to a diesel vehicle exhaust soot filter system, specifically a wall-flow diesel vehicle exhaust particulate filter-regeneration device with silicon carbide foam ceramics as the carrier of the filter device, which can effectively reduce the soot emission of diesel vehicles Diesel vehicles realize regeneration under normal power supply and normal driving conditions.
背景技术 Background technique
由于混合和燃烧方式的不同,柴油机的排污成分中CO及HC比汽油机少很多,而碳烟却是汽油机的几十倍甚至更多,并且碳烟排放更易被人们从视觉上直观察觉,因此柴油车的排烟净化一直是柴油车排污治理的重点和难点。Due to the difference in mixing and combustion methods, the CO and HC in the exhaust components of diesel engines are much less than those of gasoline engines, while the soot is dozens of times or even more than that of gasoline engines, and the soot emissions are easier for people to visually perceive, so diesel engines The purification of vehicle exhaust has always been the focus and difficulty of diesel vehicle pollution control.
现有柴油车碳烟过滤技术从理论上讲主要分为面过滤和体内过滤两种。面过滤又叫滤饼过滤方式,过滤发生在过滤器表面,其原理是使含碳烟颗粒的尾气流过一块带有许多细小孔且密度较大的陶瓷壁。柴油机碳烟微粒不能穿过壁上的小孔而沉淀在过滤器的表面。这种过滤方式十分有效,但它的阻力较大,排气背压高。面过滤理论的代表技术是壁流式蜂窝陶瓷;体内过滤又叫深滤床过滤,过滤发生在过滤器内部,尾气流过过滤器时,其中的碳烟微粒与过滤器内部的筋多次碰撞,通过扩散及拦截的方式沉淀在过滤器的孔道中,这种结构排气阻力小,过滤器中沉淀下来的碳烟微粒分布较均匀。体内过滤的代表技术是泡沫陶瓷过滤器和纤维过滤器。Theoretically speaking, the existing soot filter technology for diesel vehicles is mainly divided into surface filter and body filter. Surface filtration is also called filter cake filtration. Filtration occurs on the surface of the filter. The principle is to make the exhaust gas containing soot particles flow through a ceramic wall with many small holes and high density. Diesel soot particles cannot pass through the small holes in the wall and settle on the surface of the filter. This filtering method is very effective, but it has a large resistance and high exhaust back pressure. The representative technology of surface filtration theory is wall-flow honeycomb ceramics; in-body filtration is also called deep filter bed filtration. Filtration occurs inside the filter. When the exhaust gas flows through the filter, the soot particles in it collide with the ribs inside the filter for many times. , precipitate in the pores of the filter by means of diffusion and interception. This structure has low exhaust resistance, and the soot particles deposited in the filter are evenly distributed. Representative technologies for in vivo filtration are ceramic foam filters and fiber filters.
碳烟微粒过滤器在工作一段时间后,随着过滤微粒数量的增加,会逐渐发生发生过滤器孔洞堵塞现象,堵塞累积到一定程度,就会使尾气流动不畅,从而使发动机排气背压急剧增加,影响发动机工作效率,此时就需要对过滤器进行再生。微粒过滤器的再生方式主要有下列几种,第一种利用催化剂再生,即在微粒过滤器表面添加催化剂,利用催化剂的催化作用降低微粒的起燃温度,使捕获到的微粒在较低温度下和尾气中的氧气或氧化氮反应生成二氧化碳而除去微粒。不过这种再生方式要求尾气的温度必须达到一定的要求,在汽车低速或轻载重条件下行驶时,尾气温度经常达不到这个要求;第二种再生方式是利用加热器或燃烧的方式提高尾气温度,使微粒在高温条件下燃烧除去。前两种方法都是原位再生方式,即再生时催化剂仍位于原安装位置。再有就是非原位再生方式,即当微粒过滤器捕集到一定数量的微粒以后,将微粒过滤器从汽车上拆下来放到空气炉等设备中加热,使微粒燃烧得以除去。又或者用大气流从反方向吹拆下的微粒过滤器,将碳烟微粒吹出并收集除去。After the soot particulate filter works for a period of time, as the number of filtered particles increases, the phenomenon of filter hole clogging will gradually occur. If the clogging accumulates to a certain extent, the flow of exhaust gas will be blocked, resulting in engine exhaust back pressure. The sharp increase will affect the working efficiency of the engine. At this time, the filter needs to be regenerated. The regeneration methods of the particulate filter mainly include the following types. The first one uses catalyst regeneration, that is, adding a catalyst on the surface of the particulate filter, and using the catalytic effect of the catalyst to reduce the ignition temperature of the particulates, so that the captured particulates are released at a lower temperature. It reacts with oxygen or nitrogen oxides in the exhaust gas to form carbon dioxide to remove particulates. However, this regeneration method requires that the temperature of the exhaust gas must meet a certain requirement. When the car is running at low speed or under light load conditions, the temperature of the exhaust gas often cannot meet this requirement; the second regeneration method is to use a heater or combustion to increase the temperature of the exhaust gas. Temperature, so that the particles are burned and removed under high temperature conditions. The first two methods are in-situ regeneration methods, that is, the catalyst is still in the original installation position during regeneration. Another is the non-situ regeneration method, that is, when the particulate filter captures a certain amount of particulates, the particulate filter is removed from the car and placed in an air furnace and other equipment for heating, so that the particulates can be removed by combustion. Or blow the dismantled particulate filter from the opposite direction with atmospheric airflow to blow out the soot particles and collect them for removal.
无论采用何种再生方式都面临着两个问题:一是再生效率的问题,再有就是当前所用的微粒过滤器材料很容易因微粒燃烧急剧放热造成温度极度不均而炸裂。这两个问题是目前碳烟过滤-再生技术的主要难题。本发明采用高热导率、低膨胀系数、高熔点的碳化硅泡沫陶瓷制作的壁流式碳烟微粒过滤器,兼有面过滤和体内过滤的优点,过滤效率高,抗热震性好,能有效避免再生时的过滤器炸裂现象,保证过滤器的使用可靠性;再生采用尾气加注燃油结合电加热的方式,实现过滤器的低成本再生,延长了过滤器使用寿命。No matter what kind of regeneration method is used, there are two problems: one is the problem of regeneration efficiency, and the other is that the currently used particulate filter material is easy to burst due to the extreme temperature unevenness caused by the rapid heat release of particulate combustion. These two problems are the main problems of the current soot filtration-regeneration technology. The present invention adopts the wall-flow soot particulate filter made of silicon carbide foam ceramics with high thermal conductivity, low expansion coefficient and high melting point, which has the advantages of surface filtration and body filtration, high filtration efficiency, good thermal shock resistance, and Effectively avoid filter bursting during regeneration and ensure the reliability of the filter; regeneration uses exhaust gas fuel injection combined with electric heating to achieve low-cost regeneration of the filter and prolong the service life of the filter.
发明内容 Contents of the invention
本发明的目的在于提供一种壁流式柴油车尾气微粒过滤-再生装置,使用该装置能有效过滤发动机排放的碳烟,在过滤达到一定程度后可以用燃烧燃油结合电加热的方式对微粒过滤器进行原位再生,并且安装该装置不会造成发动机功率的明显损失。The purpose of the present invention is to provide a wall-flow type diesel vehicle exhaust particle filter-regeneration device, which can effectively filter the soot emitted by the engine, and can filter the particles by burning fuel oil combined with electric heating after the filter reaches a certain level The engine can be regenerated in situ, and the installation of the device will not cause a significant loss of engine power.
为实现上述目的,本发明采用的技术方案是:In order to achieve the above object, the technical scheme adopted in the present invention is:
一种壁流式柴油车尾气微粒过滤-再生装置,包括电源、可控喷油装置、燃油分散单元、电加热发热体、火焰分散单元、壁流式泡沫陶瓷微粒过滤器以及电控部分。其中电加热发热体由泡沫陶瓷电加热单元构成,泡沫陶瓷电加热单元由导电碳化硅泡沫陶瓷、焊接在位于导电碳化硅泡沫陶瓷两端的碳化硅陶瓷电极基座上的两个金属电极构成,电源通过金属电极与导电碳化硅泡沫陶瓷构成回路,为导电碳化硅泡沫陶瓷供电。可控喷油装置由电泵、电磁阀、燃油喷嘴组成,该装置通过输油管线从汽车油箱取油。燃油分散单元、电加热发热体、火焰分散单元和壁流式泡沫陶瓷微粒过滤器一起安装于与柴油发动机排气管相连的净化器封装外壳内,可控喷油装置的燃油喷嘴位于电加热发热体的上游。电控部分与泡沫陶瓷电加热发热体电极相连。A wall-flow type diesel vehicle exhaust particle filter-regeneration device includes a power supply, a controllable fuel injection device, a fuel dispersion unit, an electric heating element, a flame dispersion unit, a wall-flow type foam ceramic particle filter and an electric control part. The electric heating element is composed of a foam ceramic electric heating unit, and the foam ceramic electric heating unit is composed of conductive silicon carbide foam ceramics and two metal electrodes welded on the silicon carbide ceramic electrode bases at both ends of the conductive silicon carbide foam ceramics. The metal electrode and the conductive silicon carbide foam ceramic form a circuit to supply power to the conductive silicon carbide foam ceramic. The controllable fuel injection device consists of an electric pump, a solenoid valve, and a fuel nozzle. The device takes fuel from the fuel tank of the vehicle through the fuel pipeline. The fuel dispersing unit, electric heating heating element, flame dispersing unit and wall-flow ceramic foam particle filter are installed together in the purifier package shell connected to the exhaust pipe of the diesel engine, and the fuel nozzle of the controllable fuel injection device is located in the electric heating heating upstream of the body. The electric control part is connected with the electrodes of the foam ceramic electric heating heating element.
所述壁流式泡沫陶瓷微粒过滤器由多片碳化硅泡沫陶瓷板平行组合而成,每两片复合碳化硅泡沫陶瓷板之间的距离为1.5~3mm。过滤器内部相错排列众多互不直接相通的短通道,气体只有穿过碳化硅泡沫陶瓷板才能由一个通道进入另外的通道,碳烟微粒在穿越过程中被过滤。The wall-flow ceramic foam particle filter is composed of multiple silicon carbide foam ceramic plates in parallel, and the distance between every two composite silicon carbide foam ceramic plates is 1.5-3 mm. Inside the filter, there are many short channels that are not directly connected to each other. The gas can only pass through the silicon carbide foam ceramic plate to enter the other channel from one channel, and the soot particles are filtered during the passage.
所述构成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷板可具有单一泡沫孔径或变化孔径。变化孔径的碳化硅泡沫陶瓷板为如下三种制备方式之一:a、由两种或两种以上不同孔径的碳化硅泡沫陶瓷板复合而成;b、在单一孔径的碳化硅泡沫陶瓷板上制备微孔涂层;c、前两种方法的结合,即在a中提到的复合后的碳化硅泡沫陶瓷板上再制备微孔涂层。当采用变化孔径泡沫陶瓷时,大孔径泡沫陶瓷面为尾气进入面,小孔径或微孔面为尾气流出面。The silicon carbide foam ceramic plate constituting the wall-flow ceramic foam particulate filter may have a single foam pore size or a variable pore size. The silicon carbide foam ceramic plate with variable pore size is prepared in one of the following three ways: a. It is composed of two or more silicon carbide foam ceramic plates with different pore sizes; b. On a silicon carbide foam ceramic plate with a single pore size Prepare the microporous coating; c, the combination of the first two methods, that is, prepare the microporous coating on the composite silicon carbide foam ceramic plate mentioned in a. When using variable-pore-diameter foam ceramics, the surface of the large-pore foam ceramics is the exhaust gas entry surface, and the small-pore or micropore surface is the exhaust gas exit surface.
所述泡沫陶瓷电加热发热体为至少一个泡沫陶瓷电加热单元组成,当过滤器由二个或二个以上单元构成时,各单元之间为并联关系,通过电极之间焊接的方式连成一个整体,电加热尾气净化器的体积控制在50~400ml之间,厚度控制在10~50mm范围内。The foam ceramic electric heating heating element is composed of at least one foam ceramic electric heating unit. When the filter is composed of two or more units, the units are connected in parallel, and are connected into one by welding between electrodes. Overall, the volume of the electric heating exhaust gas purifier is controlled between 50-400ml, and the thickness is controlled within the range of 10-50mm.
所述燃油分散单元和火焰分散单元均为碳化硅泡沫陶瓷材料,利用泡沫陶瓷特有的三维连通结构,促进燃油和火焰的横向扩散。Both the fuel dispersing unit and the flame dispersing unit are made of silicon carbide foam ceramics, which promote the lateral diffusion of fuel and flame by utilizing the unique three-dimensional interconnected structure of foam ceramics.
所述碳化硅泡沫陶瓷按重量分数计,其成份由90%~98%的碳化硅和10%~2%的硅组成。The silicon carbide foamed ceramics is composed of 90% to 98% of silicon carbide and 10% to 2% of silicon in terms of weight fraction.
所述碳化硅泡沫陶瓷以多边型封闭环为基本单元,各基本单元相互连接形成三维连通网络;构成多边形封闭环单元的陶瓷筋的相对致密度≥99%,平均晶粒尺寸在50nm~10μm。The silicon carbide foam ceramics uses a polygonal closed ring as a basic unit, and each basic unit is connected with each other to form a three-dimensional connected network; the relative density of the ceramic ribs constituting the polygonal closed ring unit is ≥ 99%, and the average grain size is 50nm-10μm.
所述燃油分散单元、电加热发热体、火焰分散单元上可制备活性氧化铝涂层,并担载催化剂,以碳化硅泡沫陶瓷为载体,每升载体的涂层含量在80~130g,涂层中各物质的重量比为:Al2O3∶CeO2∶La2O3∶BaO=50~55∶30~40∶2~8∶1~10;催化剂所用活性物质可以是Pt或Pd,每升载体中Pt或Pd总含量为1~5g。The fuel dispersing unit, the electric heating element, and the flame dispersing unit can be prepared with an active alumina coating, and the catalyst is loaded, and the silicon carbide foam ceramic is used as the carrier, and the coating content per liter of the carrier is 80-130g. The weight ratio of each substance is: Al 2 O 3 : CeO 2 : La 2 O 3 : BaO=50~55:30~40:2~8:1~10; the active material used in the catalyst can be Pt or Pd, each The total content of Pt or Pd in the carrier is 1-5g.
本发明主要包含三个部分:a.安装可控喷油装置,过滤器需要再生时,该装置在电加热发热体前部喷入燃油;b.采用导电碳化硅泡沫陶瓷做发热体,以车载蓄电池作电源,在设定条件下给发热体通电,点燃可控喷油装置送入的燃油,加热尾气使壁流式微粒过滤器中的微粒燃烧;c.采用具有三维网状连通结构的碳化硅泡沫陶瓷组合壁流式微粒过滤器,所得到的过滤器兼有面过滤和体过滤的优点。通过调整泡沫陶瓷的平均孔径大小、陶瓷的体积分数、陶瓷板厚度等参数,可以在合理的背压条件下得到很高的过滤效率。并且,由于碳化硅泡沫陶瓷具有低膨胀系数、高导热率和高熔点等特性,所以抗热震能力强,不会在再生时发生炸裂现象。The present invention mainly includes three parts: a. install a controllable fuel injection device, when the filter needs to be regenerated, the device sprays fuel into the front of the electric heating heating element; b. use conductive silicon carbide foam ceramics as the heating element, and use the vehicle The battery is used as the power supply, and the heating element is energized under the set conditions to ignite the fuel fed by the controllable fuel injection device, and heat the exhaust gas to burn the particles in the wall-flow particulate filter; c. Silicon foam ceramics are combined with wall-flow particulate filters, and the obtained filters have the advantages of both surface filtration and volume filtration. By adjusting the average pore size of the foamed ceramics, the volume fraction of the ceramics, the thickness of the ceramic plate and other parameters, a high filtration efficiency can be obtained under reasonable back pressure conditions. Moreover, due to the characteristics of low expansion coefficient, high thermal conductivity and high melting point of silicon carbide foam ceramics, it has strong thermal shock resistance and will not burst during regeneration.
与现有技术相比,本发明更具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
①碳烟过滤体由碳化硅泡沫陶瓷构成,该过滤体具有如下特点:a、热传导性良好,保证过滤体温度分布均匀,避免过大热应力的产生并减少再生死角的存在;b、抗热冲击性好,可承受再生时微粒氧化燃烧造成的温度剧变;c、熔点高,在2000℃以上,确保在高温下有较长的使用寿命。①The soot filter body is made of silicon carbide foam ceramics. The filter body has the following characteristics: a. Good thermal conductivity, ensuring uniform temperature distribution of the filter body, avoiding excessive thermal stress and reducing the existence of regeneration dead angle; b. Heat resistance It has good impact resistance and can withstand the drastic temperature change caused by the oxidation and combustion of particles during regeneration; c. The melting point is high, above 2000°C, ensuring a long service life at high temperatures.
②电加热发热体采用碳化硅泡沫陶瓷,实现了加热、过滤功能一体化,结构简单,且电阻率可根据实际需要在大范围内调整。另外碳化硅陶瓷具有良好的抗氧化、抗高温、抗酸碱性能,与金属电阻丝发热体相比,更适合在汽车尾气环境中使用。②The electric heating element adopts silicon carbide foam ceramics, which realizes the integration of heating and filtering functions, has a simple structure, and the resistivity can be adjusted in a wide range according to actual needs. In addition, silicon carbide ceramics have good oxidation resistance, high temperature resistance, and acid and alkali resistance. Compared with metal resistance wire heating elements, they are more suitable for use in automobile exhaust environments.
③采用燃油注入与电加热相结合的再生方式,提高了再生效率。③The regeneration method combining fuel injection and electric heating is adopted to improve the regeneration efficiency.
④过滤体采用的泡沫陶瓷壁流式结构,拥有极大的过滤面积,既增加了微粒物与过滤体的碰撞几率,提高过滤效率,促进微粒物在过滤体中均匀分散,又有助于降低背压,减少发动机功率损耗。④The foam ceramic wall-flow structure adopted by the filter body has a large filtration area, which not only increases the collision probability of the particulate matter and the filter body, improves the filtration efficiency, promotes the uniform dispersion of the particulate matter in the filter body, but also helps reduce the Back pressure, reducing engine power loss.
⑤该装置采用车载蓄电池作为电加热电源,无须外加电源,汽车改造范围小,成本低。⑤ The device adopts the vehicle-mounted storage battery as the electric heating power source, and does not need an external power source. The scope of vehicle modification is small and the cost is low.
⑥控制系统智能化,可根据水温、发动机转速以及背压等条件控制再生状态。⑥The control system is intelligent, and the regeneration state can be controlled according to conditions such as water temperature, engine speed and back pressure.
⑦采用钎焊的方式制备金属电极,使接触电阻降至最低,提高了能量利用效率。⑦ Brazing is used to prepare metal electrodes to minimize contact resistance and improve energy utilization efficiency.
⑧本发明装置具有良好、可控的过滤-再生性能,在车载电源正常供电并且车辆正常行驶和车辆正常运行的情况下,可实现对柴油车微粒的有效过滤,并智能化原位再生,使柴油车排放在较长的时间内都能满足严格的净化标准,具有效果好、原位再生、寿命长的特点。⑧The device of the present invention has good and controllable filtration-regeneration performance, and can realize effective filtration of diesel vehicle particles and intelligent in-situ regeneration when the vehicle power supply is normally powered and the vehicle is running normally and the vehicle is running normally. Diesel vehicle emissions can meet strict purification standards for a long period of time, and have the characteristics of good effect, in-situ regeneration, and long life.
附图说明 Description of drawings
图1为壁流式柴油车尾气微粒过滤-再生装置工作示意图。Figure 1 is a working schematic diagram of a wall-flow diesel vehicle exhaust particulate filter-regeneration device.
图2为一个泡沫陶瓷电加热再生发热体单元(电加热单元)的示意图。Fig. 2 is a schematic diagram of a ceramic foam electric heating regenerative heating element unit (electric heating unit).
图3为壁流式泡沫陶瓷微粒过滤器结构示意图。Fig. 3 is a schematic diagram of the structure of a wall-flow ceramic foam particulate filter.
图4为复合式碳化硅泡沫陶瓷板的结构示意图。Fig. 4 is a schematic structural view of a composite silicon carbide foam ceramic plate.
图中,1柴油发动机;2水温传感器;3转速传感器;4控制单元;5功率组件;6车载蓄电池;7电缆;8净化器封装外壳;9壁流式泡沫陶瓷微粒过滤器(主过滤器);10金属电极;11金属电极;12电加热发热体;13排气管;14压力传感器;15火焰分散单元;16燃油分散单元;17燃油喷嘴;18电磁阀;19电泵;20输油管线;21汽车油箱;22碳化硅陶瓷电极基座;23碳化硅陶瓷电极基座;24导电碳化硅泡沫陶瓷发热体;25(复合碳化硅泡沫陶瓷板中的)大孔径碳化硅泡沫陶瓷板;26(复合碳化硅泡沫陶瓷板中的)小孔径碳化硅泡沫陶瓷板或具有微孔的涂层。In the figure, 1 diesel engine; 2 water temperature sensor; 3 speed sensor; 4 control unit; 5 power assembly; 6 vehicle battery; 7 cable; ; 10 metal electrode; 11 metal electrode; 12 electric heating heating element; 13 exhaust pipe; 14 pressure sensor; 15 flame dispersion unit; 16 fuel dispersion unit; 17 fuel nozzle; 18 solenoid valve; 19 electric pump; 20 oil pipeline; 21 automobile fuel tank; 22 silicon carbide ceramic electrode base; 23 silicon carbide ceramic electrode base; 24 conductive silicon carbide foam ceramic heating element; 25 (composite silicon carbide foam ceramic plate) large-pore silicon carbide foam ceramic plate; 26 ( Composite silicon carbide foam ceramic plates) small-pore silicon carbide foam ceramic plates or coatings with micropores.
具体实施方式 Detailed ways
本发明壁流式柴油车尾气微粒过滤-再生装置的制备过程具体如下:The preparation process of the wall-flow diesel vehicle exhaust particulate filter-regeneration device of the present invention is as follows:
①采用按照《一种高强度致密的泡沫碳化硅陶瓷材料及其制备方法》(中国科学院金属研究所申请,申请号03134039.3,申请日:2003年9月22日)所做的导电碳化硅泡沫陶瓷,作为本发明中所用全部碳化硅泡沫陶瓷的来源。①Adopt conductive silicon carbide foam ceramics according to "A High-Strength and Dense Foamed Silicon Carbide Ceramic Material and Its Preparation Method" (applied by the Institute of Metal Research, Chinese Academy of Sciences, application number 03134039.3, application date: September 22, 2003) , as the source of all silicon carbide foam ceramics used in the present invention.
②将碳化硅泡沫陶瓷材料组合成为如图3所示的壁流式泡沫陶瓷微粒过滤器,作为壁流式柴油车尾气微粒过滤-再生装置的主过滤器。气流由开口通道进入主过滤器,穿过碳化硅泡沫陶瓷壁,进入相邻的通道,如图3的箭头所示,在此过程中碳烟微粒被过滤净化。采用具有过渡孔径的复合泡沫陶瓷时,大孔径陶瓷面为尾气流入面,小孔径陶瓷面为尾气流出面。主过滤器体积和通道的数目、以及碳化硅泡沫陶瓷的平均孔径等参数可根据尾气流量和背压的要求进行调整。② The silicon carbide foam ceramic material is combined into a wall-flow ceramic foam particle filter as shown in Figure 3, which is used as the main filter of the wall-flow diesel vehicle exhaust particle filter-regeneration device. The air flow enters the main filter through the open channel, passes through the silicon carbide foam ceramic wall, and enters the adjacent channel, as shown by the arrow in Figure 3, during which the soot particles are filtered and purified. When composite foam ceramics with transitional apertures are used, the large-aperture ceramic surface is the exhaust gas inflow surface, and the small-aperture ceramic surface is the exhaust gas outflow surface. Parameters such as the volume of the main filter and the number of channels, and the average pore size of silicon carbide foam ceramics can be adjusted according to the requirements of exhaust gas flow and back pressure.
③根据不同汽车的状况,可控喷油装置的喷油频率、喷油量等参数可调整。③According to the conditions of different vehicles, parameters such as fuel injection frequency and fuel injection volume of the controllable fuel injection device can be adjusted.
④根据电阻的需求,选择一个或多个合适的碳化硅泡沫陶瓷电加热单元,如采用多个单元,则各单元之间为并联关系,并通过在金属电极上焊接金属板的方式连接成一个整体。④ Select one or more suitable silicon carbide foam ceramic electric heating units according to the resistance requirements. If multiple units are used, the units are connected in parallel and connected into one by welding metal plates on the metal electrodes. overall.
⑤在泡沫陶瓷燃油分散单元、电加热发热体和火焰分散单元上可制备活性氧化铝涂层,并担载催化剂,以促进碳烟颗粒加速燃烧并降低冷启动阶段的气态污染物排放。⑤ Activated alumina coatings can be prepared on the ceramic foam fuel dispersing unit, electric heating element and flame dispersing unit, and the catalyst can be loaded to promote the accelerated combustion of soot particles and reduce the emission of gaseous pollutants during the cold start stage.
催化剂制备的具体过程如下:The concrete process of catalyst preparation is as follows:
a、将碳化硅泡沫陶瓷在浓度为2~5M的NaOH或KOH溶液中浸泡5~10分钟,去除其表面的油污等杂质,之后用水清洗、再于100~150℃空气气氛中1~4小时烘干;a. Soak silicon carbide foam ceramics in a NaOH or KOH solution with a concentration of 2-5M for 5-10 minutes to remove impurities such as oil stains on the surface, then wash with water, and then place it in an air atmosphere at 100-150°C for 1-4 hours drying;
b、取γ-Al2O3110~160份、CeO250~70份、La2O32~10份、BaO 4~20份,混合后加水500份,球磨2~4小时得到涂层浆料;b. Take 110-160 parts of γ-Al 2 O 3 , 50-70 parts of CeO 2 , 2-10 parts of La 2 O 3 , 4-20 parts of BaO, mix them, add 500 parts of water, and ball mill for 2-4 hours to obtain a coating slurry;
c、将泡沫陶瓷在浆料中浸渍2~5分钟,以压缩空气吹去多余浆料,然后置于100~150℃空气气氛中干燥20~30分钟,冷却后再次浸渍料浆。如此重复多次,直至使涂层含量达到80~130g/(L载体),最后于450~500℃焙烧4~5小时,涂层制备完毕;c. Immerse the foamed ceramics in the slurry for 2-5 minutes, blow off the excess slurry with compressed air, then dry it in an air atmosphere at 100-150°C for 20-30 minutes, and then dip into the slurry again after cooling. Repeat this many times until the coating content reaches 80-130g/(L carrier), and finally bake at 450-500°C for 4-5 hours, and the coating is prepared;
d、如以Pt为催化活性组分,则取H2PtCl610~15份,加水500份配制成混合溶液,然后将带有活性涂层的泡沫陶瓷在溶液中真空浸渍10~15分钟,之后将浸渍后的陶瓷在烘箱中烘干,烘箱温度100~150℃,时间20~30分钟;烘干后的样品在氢气气氛中450~500℃还原2~4小时,可得到以碳化硅泡沫陶瓷为载体、以Pt为催化活性组分的具有催化功能的碳化硅泡沫陶瓷电加热发热体和壁流式泡沫陶瓷微粒过滤器。d. If Pt is used as the catalytic active component, take 10-15 parts of H 2 PtCl 6 and add 500 parts of water to prepare a mixed solution, and then vacuum-immerse the foamed ceramics with active coating in the solution for 10-15 minutes. Afterwards, the impregnated ceramics are dried in an oven at a temperature of 100-150°C for 20-30 minutes; the dried samples are reduced in a hydrogen atmosphere at 450-500°C for 2-4 hours to obtain silicon carbide foam A silicon carbide foam ceramic electric heating heating element with catalytic function and a wall-flow foam ceramic particle filter with ceramics as the carrier and Pt as the catalytic active component.
e、如以Pd为催化活性组分,则取PdCl25~20份,加水500份配制成混合溶液,然后将带有活性涂层的泡沫陶瓷在溶液中真空浸渍10~15分钟,之后将浸渍后的陶瓷在烘箱中烘干,烘箱温度100~150℃,时间20~30分钟;烘干后的样品在氢气气氛中450~500℃还原2~4小时,可得到以碳化硅泡沫陶瓷为载体、以Pd为催化活性组分的具有催化功能的碳化硅泡沫陶瓷电加热发热体和壁流式泡沫陶瓷微粒过滤器。e. If Pd is used as the catalytic active component, take 5-20 parts of PdCl 2 and add 500 parts of water to prepare a mixed solution, then vacuum-immerse the foamed ceramics with active coating in the solution for 10-15 minutes, and then put The impregnated ceramics are dried in an oven at a temperature of 100-150°C for 20-30 minutes; the dried samples are reduced in a hydrogen atmosphere at 450-500°C for 2-4 hours, and silicon carbide foam ceramics can be obtained. The carrier, the silicon carbide foam ceramic electric heating heating element with catalytic function and Pd as the catalytic active component, and the wall flow type foam ceramic particle filter.
⑥将燃油分散单元16、电加热发热体12、火焰分散单元15和壁流式泡沫陶瓷微粒过滤器9一起封装于过滤器外壳8内,过滤器外壳由2毫米厚的不锈钢板焊接而成,过滤器外壳8与泡沫陶瓷电加热发热体12及壁流式泡沫陶瓷微粒过滤器9之间有防震隔层。封装后的过滤器在进气端与柴油发动机排气管13相连。将可控喷油装置的进油端通过输油管线20与汽车油箱21相连,燃油喷嘴17位于电加热发热体12的上游。⑥ Encapsulate the
如图1~2所示,壁流式柴油车尾气微粒过滤-再生装置包括壁流式泡沫陶瓷微粒过滤器9、火焰分散单元15、电加热发热体12、燃油分散单元16、可控喷油装置及电控部分,其中电加热发热体12、火焰分散单元15、燃油分散单元16与壁流式泡沫陶瓷微粒过滤器9一起安装于与柴油发动机排气管13相连的净化器封装外壳8内,电加热发热体12由泡沫陶瓷电加热单元构成,泡沫陶瓷电加热单元为以导电碳化硅泡沫陶瓷24为主体、两个金属电极焊接在位于导电碳化硅泡沫陶瓷24两端的碳化硅陶瓷电极基座22、23上,电源6通过金属电极10、11与导电碳化硅泡沫陶瓷24构成回路,为导电碳化硅泡沫陶瓷24供电;电控部分与电加热发热体12电极相连。可控喷油装置由输油管线20、电泵19、单向电磁阀18和燃油喷嘴17组成,输油管线20与汽车油箱21相连,燃油喷嘴17位于电加热发热体12的上游,燃油喷嘴17与汽车油箱21之间的输油管线上设有电泵19、电磁阀18。所述电控部分由控制单元4和功率组件5组成。本发明电控部分采用中国发明专利申请,申请号:200510046472.1,申请日:2005年5月20日,详见其中的图5和相关的文字说明。不同之处仅在于:功率组件的输出端并联电加热发热体、可控喷油装置的电磁阀和电泵,可控喷油装置可进行可控的连续或脉冲式燃油喷射,脉冲频率和喷射时间由控制单元4采用常规方式即可实现控制。该控制单元4可接收来自压力传感器14、水温传感器2、转速传感器3的相应信号,并根据信号控制可控喷油装置和电加热发热体的启动或关闭。As shown in Figures 1 and 2, the wall-flow diesel vehicle exhaust particulate filter-regeneration device includes a wall-flow foam ceramic particulate filter 9, a
柴油汽车启动后,含碳烟微粒的汽车尾气由柴油发动机1排出,经由排气管13到达燃油分散单元16、电加热发热体12、火焰分散单元15和壁流式泡沫陶瓷微粒过滤器9,在此过程中碳烟微粒被泡沫陶瓷过滤截流。由柴油发动机冷却水水温传感器2和转速传感器3以及压力传感器14监测到的冷却水水温、转速和背压信号被控制单元4接收,然后再将信号传送至功率组件5。当背压高于设定值时,在冷却水水温和发动机转速均达到指定数值的情况下,功率组件5接通电路,车载蓄电池6即开始通过电缆7给电加热发热体12供电,通电时间可由控制单元设定;通电一段时间后,控制单元4打开电泵19和单向电磁阀18,通过输油管线20从汽车油箱21中抽取燃油输送至燃油喷嘴17,由燃油喷嘴喷出燃油。燃油首先到达燃油分散单元16,被均匀分散,然后到达电加热发热体12。处于通电加热状态的电加热发热体12将燃油点燃,燃油燃烧释放的热量被尾气带往下游的火焰分散单元15,泡沫陶瓷火焰分散单元15可将火焰均匀分散然后传至壁流式泡沫陶瓷微粒过滤器9,使过滤器中过滤的碳烟在各处均匀燃烧,避免过滤器再生时的温度不均匀现象。经过这些过程,整个过滤系统达到再生的目的。After the diesel vehicle is started, the automobile exhaust containing soot particles is discharged from the
如图2所示,泡沫陶瓷电加热单元由导电碳化硅泡沫陶瓷24、焊接在位于导电碳化硅泡沫陶瓷24两端的碳化硅陶瓷电极基座22、23上的两个金属电极10、11构成,两个金属电极10、11一端通过钎焊方式与碳化硅陶瓷电极基座连接,另一端与电缆相连。一个完整的电加热发热体可由一个或多个泡沫陶瓷电加热单元组合而成。在组合情况下,各单元之间为并联关系,通过电极之间焊接的方式连成将一个整体。电加热发热体的体积控制在100~400ml之间,厚度控制在10~50mm范围内。As shown in Figure 2, the foam ceramic electric heating unit is made of conductive silicon
图3所示为壁流式泡沫陶瓷微粒过滤器结构示意图,壁流式泡沫陶瓷微粒过滤器9由多片碳化硅泡沫陶瓷板平行组合而成,每两片复合碳化硅泡沫陶瓷板之间的距离为1.5~3mm。过滤器内部相错排列众多互不直接相通的短通道,气流由进气端的开口处进入,穿越泡沫陶瓷壁进入相邻通道,在此过程中,碳烟颗粒被碳化硅泡沫陶瓷板过滤。Fig. 3 shows the structural representation of the wall-flow type ceramic foam particle filter, the wall-flow type ceramic foam particle filter 9 is formed by parallel combination of multiple silicon carbide foam ceramic plates, and the gap between every two composite silicon carbide foam ceramic plates The distance is 1.5-3mm. Inside the filter, there are many short passages that are not directly connected to each other. The airflow enters from the opening of the air inlet, passes through the foam ceramic wall and enters the adjacent passage. During this process, the soot particles are filtered by the silicon carbide foam ceramic plate.
本发明构成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷板可以具有单一泡沫孔径或变化孔径,变化孔径的泡沫陶瓷板为如下三种制备方式之一:a、由两种或两种以上不同孔径的泡沫陶瓷板复合而成;b、在单一孔径的碳化硅泡沫陶瓷板上制备微孔涂层;c、前两种方法的结合,即在a中提到的复合后的陶瓷板上再制备微孔涂层。将碳化硅泡沫陶瓷的原始制备料浆在碳化硅泡沫陶瓷上合成不超过0.5mm厚的涂层,经烧结后即可得到微孔涂层。采用上述方法,可实现复合碳化硅泡沫陶瓷孔径从1mm到0.01mm之间大范围的孔径过渡。当采用变化孔径泡沫陶瓷时,大孔径泡沫陶瓷面为尾气进入面,小孔径或微孔面为尾气流出面。如图4所示具有变化孔径的复合碳化硅泡沫陶瓷板,小孔碳化硅泡沫陶瓷板或具有微孔的涂层26孔径为0.01mm~0.5mm;大孔碳化硅泡沫陶瓷板25孔径为0.1mm~1mm。The silicon carbide foam ceramic plate constituting the wall-flow type ceramic foam particle filter of the present invention can have a single foam pore size or a variable pore size, and the foam ceramic plate with a variable pore size is one of the following three preparation methods: a, consisting of two or more than two Composite foam ceramic plates with different pore diameters; b. Microporous coatings are prepared on silicon carbide foam ceramic plates with a single pore size; c. The combination of the first two methods, that is, the composite ceramic plates mentioned in a A microporous coating is then prepared. The original preparation slurry of silicon carbide foam ceramics is synthesized on the silicon carbide foam ceramics into a coating with a thickness of no more than 0.5mm, and the microporous coating can be obtained after sintering. By adopting the above method, a wide range of pore diameter transition from 1 mm to 0.01 mm in the pore diameter of the composite silicon carbide foam ceramic can be realized. When using variable-pore-diameter foam ceramics, the surface of the large-pore foam ceramics is the exhaust gas entry surface, and the small-pore or micropore surface is the exhaust gas exit surface. As shown in Figure 4, the composite silicon carbide foam ceramic plate with variable pore diameter, the small-pore silicon carbide foam ceramic plate or the
本发明尾气净化装置主要由上述泡沫陶瓷碳烟过滤-电加热再生净化器(含燃油分散单元16、电加热发热体12、火焰分散单元15与壁流式泡沫陶瓷微粒过滤器9)和智能控制单元4、可控喷油装置构成,净化器中的电加热发热体以导电碳化硅泡沫陶瓷为功能主体,具有良好、可控的导电性能;壁流式泡沫陶瓷微粒过滤器由泡沫陶瓷为组成材料,具有多孔、可变化孔径、表面粗糙、耐高温及热冲击的特点,可实现对柴油车排放微粒的有效过滤;在燃油分散单元16、电加热发热体12和火焰分散单元15上可负载催化剂;智能控制单元能够接收来自控制单元平台的冷却水水温、背压和发动机转速信号,并根据信号自动控制壁流式柴油车尾气微粒过滤-再生装置的再生状态。在车载电源供电且不影响车辆正常行驶的情况下,即可实现泡沫陶瓷碳烟壁流式柴油车尾气微粒过滤-再生装置的原位再生。The exhaust gas purification device of the present invention is mainly composed of the above-mentioned foam ceramic soot filter-electric heating regenerative purifier (including fuel
实施例和相关比较例Examples and related comparative examples
在各实施例和相关比较例的测试中采用的发动机型号为SOFIM8140.43,测试方式采用柴油机13工况。The engine model used in the tests of each embodiment and related comparative examples is SOFIM8140.43, and the test method adopts the
实施例1Example 1
①取导电碳化硅泡沫陶瓷130×40×20mm,在浓度为3M的NaOH溶液中浸泡8分钟,去除其表面的油污等杂质,之后用水清洗、再于120℃空气气氛中2小时烘干;① Take conductive silicon carbide foam ceramics 130×40×20mm, soak them in NaOH solution with a concentration of 3M for 8 minutes, remove oil stains and other impurities on the surface, then wash them with water, and then dry them in an air atmosphere at 120°C for 2 hours;
②将两个直径6mm的不锈钢柱钎焊在位于①所述导电碳化硅泡沫陶瓷两端的碳化硅陶瓷电极基座上作为与导线相连的电极。一个电加热发热体单元制备完毕;② Brazing two stainless steel columns with a diameter of 6 mm on the silicon carbide ceramic electrode bases located at both ends of the conductive silicon carbide foam ceramics described in ① as electrodes connected to wires. An electric heating unit is prepared;
③按照上述①~②的步骤,制作两个电加热发热体单元,然后将两个电加热发热体单元通过在金属电极上焊接金属板的方式连并联焊接在一起,得到一个完整的电加热发热体;电加热发热体的电阻为50mΩ。③According to the
④如图3,将体积分数30%、平均孔径0.5mm的碳化硅泡沫陶瓷板组合成为壁流式泡沫陶瓷微粒过滤器,每片碳化硅泡沫陶瓷板厚5mm,每两片陶瓷板之间间距为2mm,最终的过滤器外形为220×130×150mm3;④ As shown in Figure 3, the silicon carbide foam ceramic plates with a volume fraction of 30% and an average pore diameter of 0.5 mm are combined to form a wall-flow type ceramic foam particle filter. The thickness of each silicon carbide foam ceramic plate is 5 mm, and the distance between every two ceramic plates is 2mm, and the final filter shape is 220×130×150mm 3 ;
⑤以平均孔径1.5mm、体积分数30%的碳化硅泡沫陶瓷为原料,用机械加工方式制备燃油分散单元16和火焰分散单元15,其中,燃油分散单元16中心厚度为30mm,边缘厚度5mm,长与宽分别是220mm和130mm;火焰分散单元15的外形为220×130×20mm3;⑤ Using silicon carbide foam ceramics with an average pore diameter of 1.5mm and a volume fraction of 30% as raw materials, prepare the
⑥将燃油分散单元16、电加热发热体12、火焰分散单元15和壁流式泡沫陶瓷微粒过滤器9封装在一个外壳内,电加热发热体12所在层的空余空间由与电加热发热体12同样厚度的碳化硅泡沫陶瓷填充;6. Encapsulate the
⑦将壁流式柴油车尾气微粒过滤-再生装置与发动机相连接。测试使用的发动机型号为SOFIM8140.43,测试方式采用柴油机13工况;测试过程中不通电。⑦ Connect the wall-flow diesel vehicle exhaust particulate filter-regeneration device with the engine. The engine model used in the test is SOFIM8140.43, and the test method adopts the
实施例2Example 2
与实施例1不同之处在于:The difference from Example 1 is:
在测试前将壁流式柴油车尾气微粒过滤-再生装置安装于柴油发动机排气通路的指定位置,保持发动机在转速2160rpm、扭矩188Nm、功率42.5kW的高浓度碳烟排放状态下持续运行,由控制单元监测背压传感器信号,当背压信号大于20kPa时,认为过滤器需要再生。此时,控制单元接通电加热电路,由12V车载直流蓄电池供电,5秒后打开可控喷油装置,以200ml/min的流量在电加热发热体上游以12次/min的频率喷燃油5次,每次5ml,然后断电停油,并关闭发动机。Before the test, the wall-flow diesel vehicle exhaust particulate filter-regeneration device was installed in the designated position of the diesel engine exhaust passage, and the engine was kept running at a high-concentration soot emission state with a speed of 2160rpm, a torque of 188Nm, and a power of 42.5kW. The control unit monitors the signal of the back pressure sensor, and when the back pressure signal is greater than 20kPa, it is considered that the filter needs to be regenerated. At this time, the control unit is connected to the electric heating circuit, which is powered by the 12V vehicle-mounted DC battery. After 5 seconds, the controllable fuel injection device is turned on, and the fuel is injected at a flow rate of 200ml/min at a frequency of 12 times/min upstream of the electric heating heating element. times, 5ml each time, then cut off the power, stop the oil, and shut down the engine.
待发动机冷却后重启发动机,在与实施例1相同的条件下进行13工况测试,检验再生的效果。Restart the engine after the engine cools down, and carry out the 13 working conditions test under the same conditions as in Example 1 to check the effect of regeneration.
实施例3Example 3
与实施例2不同之处在于:The difference from Example 2 is:
以200ml/min的流量在电加热发热体上游以12次/min的频率喷燃油5次,每次10ml。Inject
实施例4Example 4
与实施例2不同之处在于:The difference from Example 2 is:
以200ml/min的流量在电加热发热体上游以12次/min的频率喷燃油5次,每次20ml。Inject
实施例5Example 5
与实施例2不同之处在于:The difference from Example 2 is:
以200ml/min的流量在电加热发热体上游以12次/min的频率喷燃油5次,每次30ml。Inject
实施例6Example 6
与实施例2不同之处在于:The difference from Example 2 is:
以200ml/min的流量在电加热发热体上游持续喷燃油200ml。Continuously inject 200ml of fuel oil upstream of the electric heating element at a flow rate of 200ml/min.
实施例7Example 7
与实施例2不同处在于:The difference with
电加热发热体的电阻为70mΩ;以200ml/min的流量在电加热发热体上游以12次/min的频率喷燃油5次,每次30ml。The resistance of the electric heating element is 70mΩ; fuel is injected 5 times at a flow rate of 200ml/min at a frequency of 12 times/min, 30ml each time, upstream of the electric heating element.
实施例8Example 8
与实施例2不同处在于:The difference with
电加热发热体的电阻为90mΩ;以200ml/min的流量在电加热发热体上游以12次/min的频率喷燃油5次,每次30ml。The resistance of the electric heating element is 90mΩ; fuel is injected 5 times at a flow rate of 200ml/min at a frequency of 12 times/min, 30ml each time, upstream of the electric heating element.
实施例9Example 9
与实施例1不同处在于:The difference from Example 1 is:
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%、平均孔径为0.5mm。The volume fraction of silicon carbide foam ceramics constituting the wall-flow ceramic foam particulate filter is 40%, and the average pore diameter is 0.5 mm.
实施例10Example 10
与实施例5不同处在于:Different from
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%、平均孔径为0.5mm。The volume fraction of silicon carbide foam ceramics constituting the wall-flow ceramic foam particulate filter is 40%, and the average pore diameter is 0.5mm.
实施例11Example 11
与实施例1不同之处在于:The difference from Example 1 is:
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为50%、平均孔径为0.5mm。The volume fraction of silicon carbide foam ceramics constituting the wall-flow type foam ceramic particulate filter is 50%, and the average pore diameter is 0.5mm.
实施例12Example 12
与实施例5不同处在于:Different from
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为50%、平均孔径为0.5mm。The volume fraction of silicon carbide foam ceramics constituting the wall-flow type foam ceramic particulate filter is 50%, and the average pore diameter is 0.5mm.
实施例13Example 13
与实施例1不同之处在于:The difference from Example 1 is:
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%、平均孔径为0.2mm。The volume fraction of silicon carbide foam ceramics constituting the wall-flow ceramic foam particulate filter is 40%, and the average pore diameter is 0.2mm.
实施例14Example 14
与实施例5不同之处在于:The difference with
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%、平均孔径为0.2mm。The volume fraction of silicon carbide foam ceramics constituting the wall-flow ceramic foam particulate filter is 40%, and the average pore diameter is 0.2 mm.
实施例15Example 15
与实施例1不同之处在于:The difference from Example 1 is:
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%,碳化硅泡沫陶瓷板为复合结构,具体为由3mm厚、平均孔径为0.2mm的碳化硅泡沫陶瓷板和2mm厚、平均孔径为0.05mm的碳化硅泡沫陶瓷板组合在一起。The volume fraction of silicon carbide foam ceramics forming the wall-flow type ceramic foam particle filter is 40%, and the silicon carbide foam ceramic plate is a composite structure, specifically, a silicon carbide foam ceramic plate with a thickness of 3mm and an average pore diameter of 0.2mm and a thickness of 2mm, Silicon carbide foam ceramic plates with an average pore diameter of 0.05 mm are assembled together.
实施例16Example 16
与实施例5不同之处在于:The difference with
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%,碳化硅泡沫陶瓷板为复合结构,具体为由3mm厚、平均孔径为0.2mm的碳化硅泡沫陶瓷板和2mm厚、平均孔径为0.05mm的碳化硅泡沫陶瓷板组合在一起。The volume fraction of silicon carbide foam ceramics forming the wall-flow type ceramic foam particle filter is 40%, and the silicon carbide foam ceramic plate is a composite structure, specifically, a silicon carbide foam ceramic plate with a thickness of 3mm and an average pore diameter of 0.2mm and a thickness of 2mm, Silicon carbide foam ceramic plates with an average pore diameter of 0.05 mm are assembled together.
实施例17Example 17
与实施例1不同之处在于:The difference from Example 1 is:
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%,碳化硅泡沫陶瓷板为复合结构,具体为在5mm厚、平均孔径0.2mm的碳化硅泡沫陶瓷板上复合微孔涂层,微孔涂层的平均孔径为0.01mm左右。The volume fraction of silicon carbide foam ceramics constituting the wall-flow type ceramic foam particle filter is 40%, and the silicon carbide foam ceramic plate is a composite structure, specifically a composite microporous coating on a silicon carbide foam ceramic plate with a thickness of 5 mm and an average pore diameter of 0.2 mm. layer, the average pore diameter of the microporous coating is about 0.01mm.
实施例18Example 18
与实施例5不同之处在于:The difference with
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%,碳化硅泡沫陶瓷板为复合结构,具体为在5mm厚、平均孔径0.2mm的碳化硅泡沫陶瓷板上复合微孔涂层,微孔涂层的平均孔径为0.01mm左右。The volume fraction of silicon carbide foam ceramics constituting the wall-flow type ceramic foam particle filter is 40%, and the silicon carbide foam ceramic plate is a composite structure, specifically a composite microporous coating on a silicon carbide foam ceramic plate with a thickness of 5 mm and an average pore diameter of 0.2 mm. layer, the average pore diameter of the microporous coating is about 0.01mm.
实施例19Example 19
与实施例1不同之处在于:The difference from Example 1 is:
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%,碳化硅泡沫陶瓷板为复合结构,具体为由3mm厚、平均孔径为0.2mm的碳化硅泡沫陶瓷板和2mm厚、平均孔径为0.05mm的碳化硅泡沫陶瓷板组合在一起,然后在孔径为0.05mm的碳化硅泡沫陶瓷板上再复合微孔涂层,微孔涂层的平均孔径为0.01mm左右。The volume fraction of silicon carbide foam ceramics forming the wall-flow type ceramic foam particle filter is 40%, and the silicon carbide foam ceramic plate is a composite structure, specifically, a silicon carbide foam ceramic plate with a thickness of 3mm and an average pore diameter of 0.2mm and a thickness of 2mm, Silicon carbide foam ceramic plates with an average pore diameter of 0.05mm are combined together, and then a microporous coating is compounded on the silicon carbide foam ceramic plate with a pore diameter of 0.05mm. The average pore diameter of the microporous coating is about 0.01mm.
实施例20Example 20
与实施例5不同之处在于:The difference with
组成壁流式泡沫陶瓷微粒过滤器的碳化硅泡沫陶瓷体积分数为40%,碳化硅泡沫陶瓷板为复合结构,具体为由3mm厚、平均孔径为0.2mm的碳化硅泡沫陶瓷板和2mm厚、平均孔径为0.05mm的碳化硅泡沫陶瓷板组合在一起,然后在孔径为0.05mm的碳化硅泡沫陶瓷板上再复合微孔涂层,微孔涂层的平均孔径为0.01mm左右。The volume fraction of silicon carbide foam ceramics forming the wall-flow type ceramic foam particle filter is 40%, and the silicon carbide foam ceramic plate is a composite structure, specifically, a silicon carbide foam ceramic plate with a thickness of 3mm and an average pore diameter of 0.2mm and a thickness of 2mm, Silicon carbide foam ceramic plates with an average pore diameter of 0.05mm are combined together, and then a microporous coating is compounded on the silicon carbide foam ceramic plate with a pore diameter of 0.05mm. The average pore diameter of the microporous coating is about 0.01mm.
实施例21Example 21
与实施例19不同之处在于:The difference from Example 19 is:
燃油分散单元、电加热发热体和火焰分散单元表面有催化涂层,涂层含量为80~130g/(L载体),涂层中各物质的重量比为:Al2O3∶CeO2∶La2O3∶BaO=55∶35∶3∶7。Pt含量为1.5g/(L载体)。There are catalytic coatings on the surface of the fuel dispersion unit, electric heating element and flame dispersion unit, the coating content is 80-130g/(L carrier), and the weight ratio of each substance in the coating is: Al 2 O 3 : CeO 2 : La 2 O 3 :BaO=55:35:3:7. The Pt content was 1.5 g/(L carrier).
实施例22Example 22
与实施例20不同之处在于:The difference from Example 20 is:
燃油分散单元、电加热发热体和火焰分散单元表面有催化涂层,涂层含量为80~130g/(L载体),涂层中各物质的重量比为:Al2O3∶CeO2∶La2O3∶BaO=55∶35∶3∶7。Pt含量为1.5g/(L载体)。There are catalytic coatings on the surface of the fuel dispersion unit, electric heating element and flame dispersion unit, the coating content is 80-130g/(L carrier), and the weight ratio of each substance in the coating is: Al 2 O 3 : CeO 2 : La 2 O 3 :BaO=55:35:3:7. The Pt content was 1.5 g/(L carrier).
相关比较例Related comparative examples
在与实施例相同的发动机上进行不安装过滤器条件下的柴油机13工况测试。The
实施例及相关比较例的结果见表1。表1中实验1~22为实施例,实验23为相关比较例。将各实施例与比较例的结果相比较,可发现在采用壁流式碳化硅泡沫陶瓷的情况下,过滤效率最高达到90%以上,过滤效率随着体积分数的增加和平均孔径的减小而增加,然而体积分数的增加和平均孔径的减小也会引起背压的增加。贵金属催化剂的加入能显著降低CO和THC的排放,但对于微粒排放的降低效果不是很显著;再生时喷入的燃油量不能小于150ml,否则再生不完全;The results of the examples and related comparative examples are shown in Table 1.
另外,电加热发热体的电阻不能太大,大电阻会导致功率降低,不能点燃喷入的燃油,也会导致再生不完全,在本专利条件下,电加热发热体的电阻最好控制在50毫欧左右;合适条件下再生后的过滤器仍能保持良好的过滤效率,表明壁流式柴油车尾气微粒过滤-再生装置不但具有良好的净化过滤性能,并且能够有效再生,具有较长的使用寿命。In addition, the resistance of the electric heating element should not be too large. A large resistance will lead to a reduction in power, failure to ignite the injected fuel, and incomplete regeneration. Under the conditions of this patent, the resistance of the electric heating element should preferably be controlled at 50 The regenerated filter can still maintain good filtration efficiency under suitable conditions, indicating that the wall-flow diesel vehicle exhaust particulate filter-regeneration device not only has good purification and filtration performance, but also can be effectively regenerated and has a long service life. life.
表1Table 1
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JP5135629B2 (en) * | 2007-09-21 | 2013-02-06 | 株式会社小松製作所 | Engine fuel supply system |
CN103124837B (en) * | 2010-07-02 | 2016-06-22 | 马克卡车公司 | Process the method for diesel engine exhaust, Diesel engine and exhaust after treatment system and vehicle |
CN107587926B (en) * | 2017-09-21 | 2023-08-22 | 东莞职业技术学院 | Efficient purification method and purifier for tail gas of diesel vehicle |
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JP3021313B2 (en) * | 1995-03-22 | 2000-03-15 | 川崎製鉄株式会社 | Metal strip casting equipment |
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CN1554859A (en) * | 2003-12-23 | 2004-12-15 | 清华大学 | Exhaust particulate trapping device for diesel vehicles |
CN1600742A (en) * | 2003-09-22 | 2005-03-30 | 中国科学院金属研究所 | A high-strength and dense foamed silicon carbide ceramic material and its preparation method |
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JPH0321313A (en) * | 1989-06-16 | 1991-01-30 | Matsushita Electric Ind Co Ltd | Exhaust gas filter |
US5082478A (en) * | 1989-10-06 | 1992-01-21 | Kyocera Corporation | Particulate trap filter regenerative system |
JP3021313B2 (en) * | 1995-03-22 | 2000-03-15 | 川崎製鉄株式会社 | Metal strip casting equipment |
JPH11280451A (en) * | 1998-03-26 | 1999-10-12 | Isuzu Ceramics Res Inst Co Ltd | Exhaust emission control device |
WO2004067927A1 (en) * | 2003-01-27 | 2004-08-12 | Iljin Electronic Co., Ltd | Fumes reducing device for diesel engines and method of manufacturing the same |
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