CN201401218Y - Special-shaped POC metal carrier post-processor with buffer gap at the outlet of three substrates - Google Patents
Special-shaped POC metal carrier post-processor with buffer gap at the outlet of three substrates Download PDFInfo
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- 229910018487 Ni—Cr Inorganic materials 0.000 claims description 4
- VNNRSPGTAMTISX-UHFFFAOYSA-N chromium nickel Chemical compound [Cr].[Ni] VNNRSPGTAMTISX-UHFFFAOYSA-N 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 3
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- UPHIPHFJVNKLMR-UHFFFAOYSA-N chromium iron Chemical compound [Cr].[Fe] UPHIPHFJVNKLMR-UHFFFAOYSA-N 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 3
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- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 2
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- 238000005245 sintering Methods 0.000 description 6
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- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 description 3
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 description 3
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- 239000012153 distilled water Substances 0.000 description 3
- MRELNEQAGSRDBK-UHFFFAOYSA-N lanthanum oxide Inorganic materials [O-2].[O-2].[O-2].[La+3].[La+3] MRELNEQAGSRDBK-UHFFFAOYSA-N 0.000 description 3
- KTUFCUMIWABKDW-UHFFFAOYSA-N oxo(oxolanthaniooxy)lanthanum Chemical compound O=[La]O[La]=O KTUFCUMIWABKDW-UHFFFAOYSA-N 0.000 description 3
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- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
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- 229910010413 TiO 2 Inorganic materials 0.000 description 1
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- FTYBZKYILQIPFQ-UHFFFAOYSA-N [Fe].[Cr].[Ni].[Fe] Chemical compound [Fe].[Cr].[Ni].[Fe] FTYBZKYILQIPFQ-UHFFFAOYSA-N 0.000 description 1
- QRRWWGNBSQSBAM-UHFFFAOYSA-N alumane;chromium Chemical compound [AlH3].[Cr] QRRWWGNBSQSBAM-UHFFFAOYSA-N 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
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- 239000006261 foam material Substances 0.000 description 1
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- 229910052742 iron Inorganic materials 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
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- 238000006722 reduction reaction Methods 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
本实用新型涉及一种三种基体出口有缓冲间隙的异型POC金属载体后处理器,其特征在于:载体由泡沫金属饼和单层丝网和铁铬铝金属丝网组成的饼交替排列组成,金属载体的进口和出口均为泡沫金属饼-A型载体;出口端设置了完全由泡沫金属饼构成的缓冲间隙;泡沫金属饼-A型载体、金属丝网饼-B型载体和单层丝网都涂敷氧化型催化剂涂层;缓冲间隙两侧以及进口和出口的泡沫金属饼-A型载体顶端用金属挡圈同壳体焊接固定。具备很高的机械强度,应用于车载POC后处理器,发动机排气烟度降低39~61%;无背压问题;在性能相当的情况下,价格相当于进口产品的1/4~1/5,节约成本。
The utility model relates to a special-shaped POC metal carrier post-processor with a buffer gap at the outlet of three kinds of substrates. The inlet and outlet of the metal carrier are metal foam cake-A-type carrier; the outlet end is provided with a buffer gap completely composed of foam metal cake; metal foam cake-A-type carrier, wire mesh cake-B-type carrier and single-layer wire The nets are all coated with an oxidation catalyst coating; the top of the foam metal cake-A type carrier on both sides of the buffer gap and the inlet and outlet is welded and fixed with the shell by a metal retaining ring. With high mechanical strength, it is applied to the vehicle-mounted POC post-processor, and the exhaust smoke of the engine is reduced by 39-61%; there is no back pressure problem; in the case of comparable performance, the price is equivalent to 1/4-1/ of the imported product 5. Cost saving.
Description
技术领域: Technical field:
本实用新型涉及三种基体出口有缓冲间隙的异型POC金属载体后处理器,应用于汽车发动机行业,满足了欧4以上的环保标准要求。The utility model relates to three types of special-shaped POC metal carrier post-processors with buffer gaps at the outlet of the base body, which are applied in the automobile engine industry and meet the requirements of environmental protection standards above Euro 4.
背景技术: Background technique:
汽车发动机排气中的有害成分主要是PM、NOX、HC及CO等。在过去2~3年里,低排放发动机已经成为人们争论、关心、甚至渴望实现的一个理想。The harmful components in automobile engine exhaust are mainly PM, NOX, HC and CO. In the past 2 to 3 years, low-emission engines have become an ideal that people debate, care about, and even aspire to achieve.
美国国家环保局(EPA)2007排放法规要求汽车制造商同时减少汽车尾气中的颗粒(PM)和氮氧化物(NOX)两种主要的污染物。这需要有相当的技巧,解决这个问题没有什么捷径可走。按传统的方法,减少一种污染势必导致另一种污染的增加。汽车制造商似乎已经陷入了困境。The United States Environmental Protection Agency (EPA) 2007 emissions regulations require automakers to simultaneously reduce particulate (PM) and nitrogen oxides (NOX), two major pollutants, in vehicle exhaust. This requires considerable skill, and there are no shortcuts to solving this problem. According to the traditional method, the reduction of one kind of pollution will inevitably lead to the increase of another kind of pollution. Automakers appear to be in trouble.
在排放法规的压力下,一方面车用柴油机正不断进行技术升级和改进,另一方面,选择恰当的后处理技术策略和装备,例如,SCR、DPF、DOC、POC等后处理措施来满足欧4或欧5排放标准。Under the pressure of emission regulations, on the one hand, vehicle diesel engines are constantly undergoing technical upgrades and improvements; 4 or Euro 5 emission standards.
SCR后处理器技术的本质是利用尿素在高温下分解出NH3,作为还原剂的NH3和发动机排气中的NOX在催化剂和温度的综合作用下进行反应,理想工况下生成无毒的N2和H2O,从而达到净化的目的。但是SCR后处理系统的结构复杂,每套的成本在11000元~25000元,成为推广应用的障碍。The essence of SCR post-processor technology is to use urea to decompose NH 3 at high temperature, and NH 3 as a reducing agent reacts with NOX in engine exhaust under the combined action of catalyst and temperature, and produces
DPF后处理器技术的本质是利用一种特殊的载体,例如进口和出口端的蜂窝孔交替封堵后的‘壁流’式陶瓷或碳化硅载体,新鲜的DPF后处理器样件对柴油车排出的PM一类的‘黑烟’的过滤效率最高可以达到90%,新车出厂检测完全可以达到欧4或欧5排放标准,但是,这种陶瓷DPF载体的价格昂贵,无法国产,世界范围内都被美国的‘Corning’公司和日本的‘NGK’公司专利垄断,不仅每套的成本在7000元~12000元,而且,最容易堵塞失效,成为推广应用的障碍。The essence of the DPF post-processor technology is to use a special carrier, such as a 'wall-flow' ceramic or silicon carbide carrier after the honeycomb holes at the inlet and outlet ends are blocked alternately. The filtration efficiency of 'black smoke' such as PM can reach up to 90%, and the factory inspection of new cars can fully meet the Euro 4 or Euro 5 emission standards. However, this kind of ceramic DPF carrier is expensive and cannot be produced domestically. Monopolized by American 'Corning' company and Japan's 'NGK' company, not only the cost of each set is 7,000 to 12,000 yuan, but also, it is most likely to block and fail, which becomes an obstacle to popularization and application.
DOC后处理器技术的本质是类似于汽油乘用车的三元催化转化器(TWC),用来脱除尾气中的CO和HC,载体和催化剂技术比较成熟,均能国产化,价格低,效率高。但应用于柴油车后,由于其主要的处理的主要对象为PM,对PM的去除效率仅仅在10~30%,因此,效率低,成为推广应用的障碍。The essence of DOC post-processor technology is similar to the three-way catalytic converter (TWC) of gasoline passenger cars, which is used to remove CO and HC in exhaust gas. The carrier and catalyst technology are relatively mature, can be localized, and the price is low. efficient. However, after being applied to diesel vehicles, since the main object of treatment is PM, the removal efficiency of PM is only 10-30%. Therefore, the low efficiency has become an obstacle to popularization and application.
POC后处理器技术的本质是先把PM‘过滤’或‘截留’下来,然后在催化剂的作用下进行氧化,把PM中的主要成分SOF部分氧化成CO2和H2O,把PM颗粒尺寸降低,消除其毒性和危害的因素,因此,解决了PM超标的本质问题。POC后处理器对PM的处理效率可以达到50~80%,被堵塞的故障率也远远低于DPF。因此,POC是国外研究的热点,其中,以Ecocat公司最具代表性。The essence of POC post-processing technology is to 'filter' or 'retain' PM first, and then oxidize it under the action of a catalyst to partially oxidize SOF, the main component in PM, into CO2 and H2O, reduce the particle size of PM, and eliminate Its toxicity and hazard factors, therefore, solve the essential problem of PM exceeding the standard. The processing efficiency of POC post-processor to PM can reach 50-80%, and the failure rate of being blocked is far lower than that of DPF. Therefore, POC is a hotspot of foreign research, among which Ecocat is the most representative.
POC后处理器的本质是先进的载体和催化剂技术的结合。其中,载体最为关键,不仅影响性能,也影响成本和寿命。The essence of the POC post-processor is the combination of advanced carrier and catalyst technologies. Among them, the carrier is the most critical, not only affecting performance, but also affecting cost and life.
Ecocat公司POC载体是其专利技术,其本质是结构独特的金属蜂窝板和超细金属纤维纺织毡的组合体。但价格昂贵,国产的柴油车不可能大批量采用。Ecocat's POC carrier is its patented technology, and its essence is a combination of uniquely structured metal honeycomb panels and ultrafine metal fiber textile felts. But the price is high, and domestic diesel vehicles cannot be adopted in large quantities.
POC载体成为POC后处理器应用的关键。一些利用超薄耐热不锈钢板制造的一些‘蜂窝状板以及其组合’,例如,专利号为‘02241118.6’的‘三元净化器金属载体’专利;专利号为‘200720088652.0’的‘机动车三元催化净化器金属载体的波纹带及其金属载体’专利;专利号为‘200810091662.9’的‘废气净化金属载体、所用层合物废气净化过滤器’专利;专利号为‘200610114608.2’的‘一种汽车尾气金属载体三元催化器制备方法’专利;专利号为‘200480036580.4’的‘废气净化金属载体的制造方法、废气净化金属载体和废气净化过滤器’专利;专利号为‘200710003694.4’的‘金属载体及金属载体的制造方法’专利;专利号为‘99201749.1’的‘机动车尾气净化催化剂的金属载体’专利;专利号为‘00268303.2’的‘蜂窝状金属载体’专利;专利号为‘00243739.2’的‘机外三元催化净化器的金属载体’专利;专利号为‘02202495.6’的‘用于废气排放控制的金属载体’专利;专利号为‘200410022788.2’的‘新型陶瓷化处理的金属载体’专利;专利号为‘98125354.7’的‘催化剂用金属载体’专利;专利号为‘03208434.X’的‘蜂窝状金属载体’专利;专利号为‘99101110.4’的‘一种带氧化铝层的催化剂金属载体’专利;专利号为‘98119279.3’的‘用于内燃机排气系统的金属载体’专利;专利号为‘00100560.X’的‘废气净化用金属载体’专利;专利号为‘01111387.1’的‘用于废气净化的金属载体催化剂’专利等等,由于气体的传质和传热的通道是贯通型或等同于贯通,因此,对PM的处理效果不好,无法适用于POC后处理装置。The POC carrier becomes the key to the application of the POC post-processor. Some 'honeycomb plates and their combinations' made of ultra-thin heat-resistant stainless steel plates, for example, the 'three-way purifier metal carrier' patent with the patent number '02241118.6'; the 'motor vehicle three The corrugated belt of the metal carrier of the elemental catalytic converter and its metal carrier' patent; the patent of 'exhaust gas purification metal carrier and laminated exhaust gas purification filter' with the patent number of '200810091662.9'; the patent of '200610114608.2' Automobile exhaust metal carrier three-way catalytic converter' patent; patent number '200480036580.4' patent for 'manufacturing method of exhaust gas purification metal carrier, exhaust gas purification metal carrier and exhaust gas purification filter' patent; patent number '200710003694.4' for 'metal Carrier and metal carrier manufacturing method' patent; patent number '99201749.1' for 'metal carrier for motor vehicle exhaust purification catalyst'; patent number '00268303.2' for 'honeycomb metal carrier' patent; patent number '00243739.2' "Metal carrier for external three-way catalytic converter" patent; patent number "02202495.6" for "metal carrier for exhaust emission control"; patent number "200410022788.2" for "new metal carrier for ceramic treatment" Patents; Patent No. '98125354.7' of 'Metal Support for Catalysts'; Patent No. '03208434.X' of 'Honeycomb Metal Support'; Patent No. '99101110.4' of 'A Catalyst with an Alumina Layer' Metal carrier' patent; patent number '98119279.3' for 'metal carrier for internal combustion engine exhaust system'; patent number '00100560.X' for 'metal carrier for exhaust gas purification'; patent number '01111387.1' Patents of 'Metal Carrier Catalyst for Exhaust Gas Purification', etc., because the gas mass transfer and heat transfer channels are through-type or equivalent to through-type, therefore, the treatment effect on PM is not good, and cannot be applied to POC after-treatment devices.
一些专利采用金属丝交叉纺织成平面的金属网,再把这些网片叠放在一起,例如专利号为‘98248772.X’的‘网状陶瓷载体’专利;专利号为‘99253757.6’的‘网状陶瓷载体’专利;专利号为‘200710010357.8’的‘催化还原氮氧化物的蜂窝状金属丝网载体’专利;专利号为‘200710010359.7’的‘一种具有氧化铝涂层的蜂窝状金属丝网载体及其制备方法’专利;专利号为‘200810011365.9’的‘蜂窝状金属丝网载体上涂覆氧化铝涂层的方法’专利;专利号为‘200810011366.3’的‘用于净化废气的蜂窝状金属丝网载体’专利;专利号为‘200420094705.6’的‘表面负载纳米TiO2金属滤网’专利等等,由于气体的传质和传热的通道是近似于贯通型,气流通道紊乱的程度不高,PM颗粒被碰撞和截留的几率不高,因此,对PM的处理效果不好,无法适用于POC后处理装置。Some patents use metal wires to cross weave into a flat metal mesh, and then stack these mesh sheets together, such as the 'net ceramic carrier' patent with the patent number '98248772.X'; Patent No. '200710010357.8' for 'Honeycomb Metal Mesh Carrier for Catalytic Reduction of Nitrogen Oxides'; Patent No. '200710010359.7' for 'A Honeycomb Wire Mesh with Aluminum Oxide Coating Carrier and its preparation method'patent; patent number '200810011365.9' patent 'method for coating aluminum oxide coating on honeycomb wire mesh carrier'patent; patent number '200810011366.3''honeycomb metal for purifying exhaust gas Screen carrier'patent; Patent No. '200420094705.6''Surface Loaded Nano TiO 2 Metal Filter' patent, etc., because the gas mass transfer and heat transfer channels are similar to through-type, the degree of air flow channel disorder is not high , the probability of PM particles being collided and trapped is not high, therefore, the treatment effect on PM is not good, and it cannot be applied to POC post-processing devices.
一些专利采用完整的泡沫金属作为后处理金属载体,虽然解决了上述问题,可以应用于小规模的场合,但是面临成本的劣势,无法应用于汽车的大批量生产,需要对载体单元进行结构的改进,在保证性能的情况下,降低成本,例如专利号为‘200320119469.4’的‘复合光催化抗菌泡沫金属’专利;专利号为‘200610156330.5’的‘一种高孔隙率金属多孔载体材料的制备方法’专利;专利号为‘200510024944.3’的‘汽车尾气净化器催化剂金属载体及其制备方法’专利;专利号为‘200410096609.X’的‘一种泡沫金属加氢催化剂及其制备方法和应用’专利;专利号为‘200710034317.7’的‘一种多孔金属载体及其制备方法’专利等等。Some patents use complete metal foam as post-processing metal carrier. Although the above problems are solved, it can be applied to small-scale occasions, but facing the disadvantage of cost, it cannot be applied to mass production of automobiles, and the structure of the carrier unit needs to be improved. , in the case of ensuring performance, reduce costs, such as the patent of 'composite photocatalytic antibacterial metal foam' with patent number '200320119469.4'; patent number '200610156330.5' of 'a preparation method of a high-porosity metal porous carrier material' Patents; Patent No. '200510024944.3' on 'Metal Carrier for Automobile Exhaust Purifier Catalyst and Its Preparation Method'; Patent No. '200410096609.X' on 'A Metal Foam Hydrogenation Catalyst and Its Preparation Method and Application'; Patent No. '200710034317.7', 'a porous metal carrier and its preparation method' patent and so on.
发明内容: Invention content:
本实用新型的目的在于提供一种三种基体出口有缓冲间隙的异型POC金属载体后处理器,它包括泡沫金属饼-A型载体、金属丝网饼-B型载体和单层丝网以及3者的叠放组合,其具备很高的机械强度,发动机排气烟度降低39~61%;无背压问题;在性能相当的情况下,价格相当于进口产品的1/4~1/5,节约成本。The purpose of this utility model is to provide a kind of special-shaped POC metal carrier post-processor with a buffer gap at the outlet of three kinds of substrates, which includes foam metal cake-A-type carrier, metal mesh cake-B-type carrier and single-layer wire mesh and 3 The stacking combination of the former has high mechanical strength, and the exhaust smoke of the engine is reduced by 39-61%; there is no back pressure problem; in the case of equivalent performance, the price is equivalent to 1/4-1/5 of imported products ,save costs.
本实用新型的技术方案是这样实现的:三种基体出口有缓冲间隙的异型POC金属载体后处理器,由发动机排气的进气管、进气扩张管、连接法兰、泡沫金属饼-A型载体、金属丝网饼-B型载体、载体壳体、出气扩张管、出气管、固定载体饼的档圈、单层丝网和压力传感器组成;其特征在于:载体由泡沫金属饼和单层丝网和铁铬铝金属丝网组成的饼交替排列组成,金属载体的进口和出口均为泡沫金属饼-A型载体;出口端设置了完全由泡沫金属饼构成的缓冲间隙;泡沫金属饼-A型载体、金属丝网饼-B型载体和单层丝网都涂敷氧化型催化剂涂层;缓冲间隙两侧以及进口和出口的泡沫金属饼-A型载体顶端用金属挡圈同壳体焊接固定。The technical scheme of the utility model is realized in this way: three types of special-shaped POC metal carrier post-processors with buffer gaps at the outlet of the substrate, the intake pipe exhausted by the engine, the intake expansion pipe, the connecting flange, and the foam metal cake-A type Carrier, wire mesh cake-B-type carrier, carrier shell, air outlet expansion pipe, air outlet pipe, retaining ring for fixing the carrier cake, single-layer wire mesh and pressure sensor; it is characterized in that: the carrier is made of foamed metal cake and single-layer The cakes composed of wire mesh and iron-chromium-aluminum wire mesh are arranged alternately. The inlet and outlet of the metal carrier are both metal foam cakes-A-type carrier; the outlet end is provided with a buffer gap completely composed of metal foam cakes; the metal foam cake- A-type carrier, metal mesh cake-B-type carrier and single-layer wire mesh are coated with oxidation catalyst coating; foam metal cake on both sides of the buffer gap and the inlet and outlet-A-type carrier top with a metal retaining ring with the shell Welding fixed.
壳体为单层的或带保温层壳体,壳体材料为SUS441铁素体不锈钢或表面镀铝的St11普通钢板;载体的进口和出口分别同进气或出气扩张管相联结。The shell is single-layer or with insulation layer, and the shell material is SUS441 ferritic stainless steel or St11 ordinary steel plate with aluminized surface; the inlet and outlet of the carrier are respectively connected with the air inlet or outlet expansion pipe.
泡沫金属饼-A型载体为每英寸透气的孔数15~65ppi,孔的密度大于90%的泡沫镍、泡沫镍铬、泡沫镍铬铝、泡沫铁铬铝、泡沫铁铬等成分的泡沫材料,厚度为2.5mm~150mm。Metal foam cake-type A carrier is a foam material composed of foamed nickel, foamed nickel-chromium, foamed nickel-chromium-aluminum, foamed iron-chromium-aluminum, foamed iron-chrome, etc. , the thickness is 2.5mm ~ 150mm.
金属丝网饼-B型载体为丝径为0.2~0.6mm的铁铬铝丝织成的气液过滤网,厚度为2.5mm~150mm,直径同A型载体相同。Metal mesh cake-type B carrier is a gas-liquid filter mesh woven by iron-chromium-aluminum wire with a wire diameter of 0.2-0.6mm, the thickness is 2.5mm-150mm, and the diameter is the same as that of type A carrier.
单层丝网为丝径为0.5~1mm的铁铬铝线材,编织成每英寸透气的孔数15~65ppi的单层丝网;单层丝网直径同A型载体相同。The single-layer wire mesh is iron-chromium-aluminum wire with a wire diameter of 0.5-1mm, which is woven into a single-layer wire mesh with a per-inch air-permeable hole number of 15-65ppi; the diameter of the single-layer wire mesh is the same as that of the A-type carrier.
载体是按泡沫金属饼-A型载体、铁铬铝金属丝网组成的饼-B型载体、单层丝网、铁铬铝金属丝网组成的饼-B型载体、单层丝网、铁铬铝金属丝网组成的饼-B型载体和泡沫金属饼-A型载体、缓冲间隙、泡沫金属饼-A型载体顺序安装在载体壳体内。The carrier is based on metal foam cake-A carrier, cake-B-type carrier composed of iron-chromium-aluminum wire mesh, single-layer wire mesh, cake-B-type carrier composed of iron-chromium-aluminum wire mesh, single-layer wire mesh, iron The cake-B type carrier composed of chromium-aluminum wire mesh, the metal foam cake-A type carrier, the buffer gap, and the metal foam cake-A type carrier are sequentially installed in the carrier shell.
泡沫金属饼-A型载体放置在铁铬铝金属丝网组成的饼-B型载体的两边,单层丝网放置在铁铬铝金属丝网组成的饼-B型载体的中间。The metal foam cake-type A carrier is placed on both sides of the cake-type B carrier composed of iron-chromium-aluminum wire mesh, and the single-layer wire mesh is placed in the middle of the cake-type B carrier composed of iron-chromium-aluminum wire mesh.
载体的出口端设有缓冲间隙D的大小为POC处理器内径的1/4~1/8。The outlet end of the carrier is provided with a buffer gap D whose size is 1/4-1/8 of the inner diameter of the POC processor.
载体的进口和出口所用A型载体的端头用档圈焊接固定。The end of the A-type carrier used for the inlet and outlet of the carrier is welded and fixed with a retaining ring.
本实用新型的积极效果是价格相当于进口产品价格的1/4~1/5,具备技术和经济方面的竞争力。The positive effect of the utility model is that the price is equivalent to 1/4 to 1/5 of the price of imported products, and has technical and economic competitiveness.
附图说明: Description of drawings:
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
具体实施方式:Detailed ways:
下面结合附图1对本实用新型做进一步的描述:如图1所示,三种基体出口有缓冲间隙的异型POC金属载体后处理器,由发动机排气的进气管1、进气扩张管2、连接法兰3、泡沫金属饼-A型载体4、金属丝网饼-B型载体5、载体壳体6、出气扩张管7、出气管8、固定载体饼的档圈9、单层丝网10和压力传感器11组成;其特征在于:载体由泡沫金属饼4和单层丝网10和铁铬铝金属丝网组成的饼5交替排列组成,金属载体的进口和出口均为泡沫金属饼-A型载体4;出口端设置了完全由泡沫金属饼构成的缓冲间隙;泡沫金属饼-A型载体4、金属丝网饼-B型载体5和单层丝网10都涂敷氧化型催化剂涂层;缓冲间隙两侧以及进口和出口的泡沫金属饼-A型载体4顶端用金属挡圈同壳体焊接固定。Below in conjunction with accompanying
壳体为单层的或带保温层壳体,壳体材料为SUS441铁素体不锈钢或表面镀铝的St11普通钢板;载体的进口和出口分别同进气或出气扩张管相联结。The shell is single-layer or with insulation layer, and the shell material is SUS441 ferritic stainless steel or St11 ordinary steel plate with aluminized surface; the inlet and outlet of the carrier are respectively connected with the air inlet or outlet expansion pipe.
泡沫金属饼-A型载体4为每英寸透气的孔数15~65ppi,孔的密度大于90%的泡沫镍、泡沫镍铬、泡沫镍铬铝、泡沫铁铬铝、泡沫铁铬等成分的泡沫材料,厚度为2.5mm~150mm。Foamed metal cake-
金属丝网饼-B型载体5为丝径为0.2~0.6mm的铁铬铝丝织成的气液过滤网,厚度为2.5mm~150mm,直径同A型载体4相同。The wire mesh cake-
单层丝网10为丝径为0.5~1mm的铁铬铝线材,编织成每英寸透气的孔数15~65ppi的单层丝网10;单层丝网10直径同A型载体4相同。The single-
载体是按泡沫金属饼-A型载体4、铁铬铝金属丝网组成的饼-B型载体5、单层丝网10、铁铬铝金属丝网组成的饼-B型载体5、单层丝网10、铁铬铝金属丝网组成的饼-B型载体5和泡沫金属饼-A型载体4、缓冲间隙、泡沫金属饼-A型载体4顺序安装在载体壳体6内。The carrier is based on metal foam cake-A
泡沫金属饼-A型载体4放置在铁铬铝金属丝网组成的饼-B型载体5的两边,单层丝网10放置在铁铬铝金属丝网组成的饼-B型载体5的中间。Foam metal cake-
载体的出口端设有缓冲间隙D的大小为POC处理器内径的1/4~1/8。The outlet end of the carrier is provided with a buffer gap D whose size is 1/4-1/8 of the inner diameter of the POC processor.
载体的进口和出口所用A型载体4的端头用档圈9焊接固定。The end of the used
使用时首先选择每英寸透气的孔数35ppi,孔的密度大于90%的泡沫镍铬铁片材,饼的直径为300mm,饼的厚度为15mm,分别经过碱性介质的除油脱脂工序;然后在650~750℃的条件下烧却2小时;移入含有0.5%HCl和0.2%Cr(NO3)2的处理液中处理4小时;先用自来水冲洗2遍,再用蒸馏水冲洗2遍;110℃干燥2小时;依次涂敷以下材料和比例的催化剂涂层,完成烧结,涂层的比例为1份的Al2O3,0.2份的TiO2,0.04份的La2O3,0.1份的CeO2,0.06份的Cr2O3;涂层的烧结温度为250~550℃,时间为2~3小时。加工成带有催化剂的泡沫金属饼-A型载体(4)。When in use, firstly select a foamed nickel-chromium-iron-iron sheet with a per-inch air-permeable hole number of 35ppi and a hole density greater than 90%. The cake has a diameter of 300mm and a cake thickness of 15mm, and undergoes the degreasing and degreasing process of the alkaline medium respectively; Burn at 650-750°C for 2 hours; transfer to a treatment solution containing 0.5% HCl and 0.2% Cr(NO3)2 for 4 hours; first rinse with tap water twice, then rinse twice with distilled water; 110°C Dry for 2 hours; apply the catalyst coatings of the following materials and ratios in turn to complete sintering. The ratio of the coating is 1 part of Al2O3, 0.2 parts of TiO2, 0.04 parts of La2O3, 0.1 parts of CeO2, and 0.06 parts of Cr2O3; The sintering temperature of the layer is 250-550° C., and the time is 2-3 hours. Processed into metal foam cake with catalyst-type A carrier (4).
选择材料为铁铬铝,丝径为0.4mm的气液过滤网,剪切成直径为300mm,厚度为15mm的丝片,叠放,封边,分别经过碱性介质的除油脱脂工序;然后在650~750℃的条件下保温2小时;移入含有0.5%HCl和0.2%Cr(NO3)2的处理液中处理4小时;先用自来水冲洗2遍,再用蒸馏水冲洗2遍,110℃干燥2小时;依次涂敷以下材料和比例的催化剂涂层,完成烧结,涂层的比例为1份的Al2O3,0.2份的TiO2,0.04份的La2O3,0.1份的CeO2,0.06份的Cr2O3;涂层的烧结温度为250~550℃,时间为2~3小时。加工成带有催化剂的金属丝网饼-B型载体(5)。The material is iron-chromium-aluminum, gas-liquid filter with a wire diameter of 0.4 mm, cut into wire pieces with a diameter of 300 mm and a thickness of 15 mm, stacked, edge-sealed, and degreased by alkaline media; and then Insulate at 650-750°C for 2 hours; transfer to a treatment solution containing 0.5% HCl and 0.2% Cr(NO3)2 for 4 hours; first rinse with tap water twice, then rinse twice with distilled water, and dry at 110°
选择丝径为1mm的铁铬铝线材,编织成每英寸透气的孔数15~65ppi的金属丝网;丝网的直径为300mm,分别经过碱性介质的除油脱脂工序;然后在650~750℃的条件下保温2小时;移入含有0.5%HCl和0.2%Cr(NO3)2的处理液中处理4小时;先用自来水冲洗2遍,再用蒸馏水冲洗2遍;110℃干燥2小时;依次涂敷以下材料和比例的催化剂涂层,完成烧结,涂层的比例为1份的Al2O3,0.2份的TiO2,0.04份的La2O3,0.1份的CeO2,0.06份的Cr2O3;涂层的烧结温度为250~550℃,时间为2~3小时。加工成带有催化剂的单层丝网10。Select iron-chromium-aluminum wire with a wire diameter of 1mm, and weave it into a wire mesh with air permeable holes of 15-65ppi per inch; Insulate for 2 hours under the condition of ℃; transfer to the treatment solution containing 0.5% HCl and 0.2% Cr(NO3) 2 for 4 hours; first rinse with tap water for 2 times, then rinse with distilled water for 2 times; dry at 110°C for 2 hours; Coat the catalyst coating of following material and ratio, finish sintering, the ratio of coating is the Al2O3 of 1 part, the TiO2 of 0.2 part, the La2O3 of 0.04 part, the CeO2 of 0.1 part, the Cr2O3 of 0.06 part; The sintering temperature of coating is 250~550℃, the time is 2~3 hours. Processed as a single
选取材料为SUS44不锈钢板材料,板厚度为1.5mm,焊接内径为302mm,长度为480mm园桶状载体壳体6。The selected material is a SUS44 stainless steel plate material, the plate thickness is 1.5mm, the welding inner diameter is 302mm, and the length is 480mm. The garden barrel-shaped
在园桶状载体壳体6的出口端完成固定载体饼的档圈9焊接。Complete the retaining
先在桶内的档圈上方,放入一层泡沫金属饼-A型载体4饼,完成第一段载体的填装;该载体垂直摆放,在最上端的A型载体4表面上放置一个直径小于A型载体4的直径10~20mm的平面钢板,然后在其上放置10千克的金属砝码,使整个载体叠放密实,减少空隙和径向移动,完成档圈9的焊接;然后在此泡沫金属饼-A型载体4的上方6mm处焊接第二个档圈9,档圈上方,放入一层泡沫金属饼-A型载体4饼,依次交替放入规定数量的金属丝网饼-B型载体5和单层丝网10,最后放入一层泡沫金属饼-A型载体4,完成第二段载体的填装;在最上端的A型载体4表面上放置一个直径小于A型载体4的直径10~20mm的平面钢板,然后在其上放置10千克的金属砝码,使整个载体叠放密实,减少空隙和径向移动,完成进口端的档圈9的焊接。First, put a layer of metal foam cake-
按顺序完成出气扩张管7、出气管8、进气管1、进气扩张管2、连接法兰3的焊接和压力传感器11安装,完成POC金属载体后处理器的制造加工。Complete the welding of the outlet expansion pipe 7, the outlet pipe 8, the
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| CN101629508A (en) * | 2009-04-29 | 2010-01-20 | 中国第一汽车集团公司 | Particulate oxidation catalyst postprocessor using metal carriers with one buffer gap and preparation process thereof |
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