CN201401209Y - POC Metal Carrier Post Processor with Buffer Gap at Inlet and Outlet - Google Patents
POC Metal Carrier Post Processor with Buffer Gap at Inlet and Outlet Download PDFInfo
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- CN201401209Y CN201401209Y CN200920093555XU CN200920093555U CN201401209Y CN 201401209 Y CN201401209 Y CN 201401209Y CN 200920093555X U CN200920093555X U CN 200920093555XU CN 200920093555 U CN200920093555 U CN 200920093555U CN 201401209 Y CN201401209 Y CN 201401209Y
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- 229910052751 metal Inorganic materials 0.000 claims abstract description 56
- 239000002184 metal Substances 0.000 claims abstract description 56
- 239000006260 foam Substances 0.000 claims abstract description 20
- 239000003054 catalyst Substances 0.000 claims abstract description 16
- 230000008676 import Effects 0.000 claims abstract 11
- 230000003647 oxidation Effects 0.000 claims abstract 2
- 238000007254 oxidation reaction Methods 0.000 claims abstract 2
- 238000000576 coating method Methods 0.000 claims description 9
- 239000011248 coating agent Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- 238000003466 welding Methods 0.000 claims description 7
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 6
- 239000010959 steel Substances 0.000 claims description 6
- -1 iron chromium aluminum Chemical compound 0.000 claims description 5
- 229910001220 stainless steel Inorganic materials 0.000 claims description 5
- 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
- 238000009413 insulation Methods 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- UPHIPHFJVNKLMR-UHFFFAOYSA-N chromium iron Chemical compound [Cr].[Fe] UPHIPHFJVNKLMR-UHFFFAOYSA-N 0.000 claims description 2
- 239000004411 aluminium Substances 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 238000005269 aluminizing Methods 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 239000000779 smoke Substances 0.000 abstract description 3
- 239000000969 carrier Substances 0.000 abstract 2
- 230000000052 comparative effect Effects 0.000 abstract 1
- 239000006262 metallic foam Substances 0.000 description 15
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 12
- 239000007789 gas Substances 0.000 description 11
- 238000000746 purification Methods 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 7
- 239000010410 layer Substances 0.000 description 6
- 238000012805 post-processing Methods 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000011049 filling Methods 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000005238 degreasing Methods 0.000 description 2
- QDOXWKRWXJOMAK-UHFFFAOYSA-N dichromium trioxide Chemical compound O=[Cr]O[Cr]=O QDOXWKRWXJOMAK-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002356 single layer Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- FTYBZKYILQIPFQ-UHFFFAOYSA-N [Fe].[Cr].[Ni].[Fe] Chemical compound [Fe].[Cr].[Ni].[Fe] FTYBZKYILQIPFQ-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
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 description 1
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000006261 foam material Substances 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- MRELNEQAGSRDBK-UHFFFAOYSA-N lanthanum oxide Inorganic materials [O-2].[O-2].[O-2].[La+3].[La+3] MRELNEQAGSRDBK-UHFFFAOYSA-N 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- KTUFCUMIWABKDW-UHFFFAOYSA-N oxo(oxolanthaniooxy)lanthanum Chemical compound O=[La]O[La]=O KTUFCUMIWABKDW-UHFFFAOYSA-N 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 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
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Classifications
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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 After Treatment (AREA)
Abstract
Description
技术领域:Technical field:
本实用新型涉及一种进口和出口端有缓冲间隙的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 a POC metal carrier post-processor with buffer gaps at the inlet and outlet ends, which is applied in the automobile engine industry and meets 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 2007 U.S. Environmental Protection Agency (EPA) 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 non-toxic NH 3 under ideal conditions. N 2 and H 2 O, so as to achieve the purpose of purification. However, the structure of the SCR post-processing system is complicated, and the cost of each set is between 11,000 yuan and 25,000 yuan, which has become an obstacle to popularization and application.
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,但是面临成本的劣势,无法应用于国内市场的汽车的大批量生产,但其可靠性高,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,可以应用于出口型的车辆,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 the post-processing metal carrier. Although the above problems are solved, they face the disadvantage of cost and cannot be applied to the mass production of automobiles in the domestic market. However, their reliability is high, and the carrier unit needs to be structured. Improvement, in the case of guaranteed performance, lower cost, can be applied to export-oriented vehicles, such as the patent of 'composite photocatalytic antibacterial metal foam' with patent number '200320119469.4'; The patent for the preparation method of metal porous carrier material'; the patent number '200510024944.3' for 'metal carrier for automobile exhaust purifier catalyst and its preparation method'; the patent number '200410096609.X' for 'a metal foam hydrogenation catalyst And its preparation method and application' patent; the patent number of '200710034317.7' is '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柴油车用POC的金属载体和后处理装置[13],它由泡沫金属饼-A型载体(4)叠放组成;在载体的进口和出口设置了2个缓冲间隙;具备很高的机械强度,应用于装配车载POC后处理器的出口车辆,发动机排气烟度降低显著;无背压问题;在性能相当的情况下,价格相当于进口产品的1/2,节约成本。The purpose of this utility model is to provide the metal carrier and post-processing device [13] of POC for diesel vehicles, which is composed of foam metal cake-A type carrier (4) stacked; 2 buffer gaps are set at the inlet and outlet of the carrier ;With high mechanical strength, it is applied to export vehicles equipped with vehicle-mounted POC post-processors, and the exhaust smoke of the engine is significantly reduced; there is no back pressure problem; in the case of equivalent performance, the price is equivalent to 1/2 of imported products, save costs.
本实用新型的技术方案是这样实现的:进口和出口端有缓冲间隙的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、缓冲间隙D、载体壳体、出气扩张管、出气管、固定载体饼的档圈和压力传感器组成;其特征在于:载体由泡沫金属饼叠放组成;在载体的进口和出口设置了2个缓冲间隙;泡沫金属饼-A型载体上涂敷氧化型催化剂涂层;进口和出口的以及缓冲间隙的泡沫金属饼-A型载体采用金属挡圈同壳体焊接固定。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 technical scheme of the utility model is realized in this way: the POC metal carrier post-processor with a buffer gap at the inlet and outlet ends, the intake pipe exhausted by the engine, the intake expansion pipe, the connecting flange, the foam metal cake-A type carrier , buffer gap D, carrier shell, air outlet expansion pipe, air outlet pipe, retaining ring for fixing the carrier cake and pressure sensor; it is characterized in that: the carrier is composed of stacked foam metal cakes; two are set at the inlet and outlet of the carrier Buffer gap; the metal foam cake-A carrier is coated with an oxidized catalyst coating; the metal foam cake-A carrier of the inlet and outlet and the buffer gap is welded and fixed with the shell by a metal retaining ring. The shell is single-layer or with insulation layer, and the material of the shell 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50mm~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 50mm ~ 150mm.
载体的进口和出口设置了2个缓冲间隙;缓冲间隙D的大小为POC处理器内径的1/4~1/8。Two buffer gaps are set at the inlet and outlet of the carrier; the size of the buffer gap D is 1/4 to 1/8 of the inner diameter of the POC processor.
载体的进口和出口所使用A型载体的端头以及缓冲间隙D的两侧档圈的数量为6个。The number of the ends of the A-type carrier used for the inlet and outlet of the carrier and the number of retaining rings on both sides of the buffer gap D is 6.
本实用新型的积极效果是柴油车用POC的金属载体和后处理装置[13]的价格相当于进口产品价格的1/2,具备技术和经济方面的竞争力。The positive effect of the utility model is that the price of the metal carrier and post-processing device [13] of POC for diesel vehicles is equivalent to 1/2 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,进口和出口端有缓冲间隙的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、缓冲间隙D、载体壳体5、出气扩张管6、出气管7、固定载体饼的档圈8和压力传感器9组成;其特征在于:载体由泡沫金属饼4叠放组成;在载体的进口和出口设置了2个缓冲间隙;泡沫金属饼-A型载体4上涂敷氧化型催化剂涂层;进口和出口的以及缓冲间隙的泡沫金属饼-A型载体4采用金属挡圈同壳体焊接固定。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。Below in conjunction with accompanying drawing 1, the utility model is further described: as shown in Figure 1, there is the POC metal carrier postprocessor of buffer gap at the inlet and the outlet, connected by the intake pipe 1, the intake expansion pipe 2, of the exhaust of the engine Flange 3, metal foam cake-A type carrier 4, buffer gap D, carrier shell 5, air outlet expansion pipe 6, air outlet pipe 7, retaining ring 8 for fixing carrier cake and pressure sensor 9; it is characterized in that: the carrier is composed of Metal foam cake 4 is stacked; two buffer gaps are set at the inlet and outlet of the carrier; the metal foam cake-A type carrier 4 is coated with an oxidized catalyst coating; the metal foam cake at the inlet and outlet and the buffer gap- The A-type carrier 4 is welded and fixed with the shell by a metal retaining ring. The shell is single-layer or with insulation layer, and the material of the shell 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50mm~150mm。Foamed metal cake-type A carrier 4 is a foam made of nickel foam, nickel-chromium foam, nickel-chromium-aluminum foam, iron-chromium-aluminum foam, iron-chromium foam, etc. Material thickness is 50mm ~ 150mm.
载体的进口和出口设置了2个缓冲间隙;缓冲间隙D的大小为POC处理器内径的1/4~1/8。Two buffer gaps are set at the inlet and outlet of the carrier; the size of the buffer gap D is 1/4 to 1/8 of the inner diameter of the POC processor.
载体的进口和出口所使用A型载体4的端头以及缓冲间隙D的两侧档圈9的数量为6个。The number of ends of the A-type carrier 4 used for the inlet and outlet of the carrier and the retaining rings 9 on both sides of the buffer gap D are six.
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150mm,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泡沫金属饼-A型载体4。When in use, first 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 diameter of the cake is 300mm, and the thickness of the cake is 150mm, and then go through the degreasing and degreasing process of the alkaline medium; 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; rinse with tap water twice, then rinse twice with distilled water; dry at 110°C 2 hours; apply the catalyst coatings of the following materials and ratios in turn, and complete the sintering. The ratio of the coating is 1 part of Al2O3, 0.2 parts of TiO2, 0.04 parts of La2O3, 0.1 part of CeO2, and 0.06 parts of Cr2O3; The sintering temperature is 250-550°C, and the time is 2-3 hours. Processed into metal foam cake-A type carrier 4 with catalyst.
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5。The selected material is 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 carrier shell 5 .
在园桶状载体壳体5的出口端完成固定载体饼的档圈8焊接。Complete the retaining ring 8 welding of the fixed carrier cake at the outlet end of the barrel-shaped carrier shell 5 .
先在桶内的档圈上方,放入规定层数的泡沫金属饼-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,放入规定层数的泡沫金属饼-A型载体4饼,完成第二段载体的填装;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处焊接第三个档圈9,档圈上方,放入规定层数的泡沫金属饼-A型载体4饼,完成第三段载体的填装;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,完成进口端的档圈9的焊接。Firstly, above the retaining ring in the barrel, put a specified number of layers of metal foam cake-A-type carrier 4 cake to complete the filling of the first stage of carrier; the carrier is placed vertically and placed on the surface of the uppermost A-type carrier 4 A flat steel plate with a diameter of 10 to 20 mm in diameter smaller than the A-type carrier 4, and then place a 10-kilogram metal weight on it to make the entire carrier stack densely, reduce gaps and radial movement, and complete the welding of the retaining ring 9; then Weld the second retaining ring 9 at 6 mm above the metal foam cake-A-type carrier 4, and put a specified number of layers of metal foam cake-A-type carrier 4 above the retaining ring to complete the filling of the second stage of the carrier The carrier is vertically placed, and a flat steel plate with a diameter of 10-20 mm in diameter smaller than the A-type carrier 4 is placed on the surface of the uppermost A-type carrier 4, and then a 10-kg metal weight is placed on it, so that the entire carrier is stacked. Dense, reduce the gap and radial movement, and complete the welding of the retaining ring 9; then weld the third retaining ring 9 at 6 mm above the metal foam cake-A-type carrier 4, above the retaining ring, put a specified number of layers of foam Metal cake-A-type carrier 4 cakes, complete the filling of the third stage carrier; the carrier is placed vertically, and a flat steel plate with a diameter of 10-20mm smaller than the diameter of the A-type carrier 4 is placed on the surface of the uppermost A-type carrier 4, Then place 10 kilograms of metal weights on it, so that the entire carrier is stacked densely, reducing gaps and radial movement, and completing the welding of the retaining ring 9 at the inlet end.
按顺序完成出气扩张管6、出气管7、进气管1、进气扩张管2、连接法兰3的焊接和压力传感器9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 6, the outlet pipe 7, the intake pipe 1, the intake expansion pipe 2, the connecting flange 3 and the installation of the pressure sensor 9 in order, and complete the manufacturing and processing of the POC metal carrier post-processor.
Claims (5)
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| CN200920093555XU CN201401209Y (en) | 2009-04-29 | 2009-04-29 | POC Metal Carrier Post Processor with Buffer Gap at Inlet and Outlet |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101629507A (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 two buffer gaps and preparation process thereof |
| CN112459869A (en) * | 2020-12-14 | 2021-03-09 | 艾蓝腾新材料科技(上海)有限公司 | Electric heating type foam alloy filter core |
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2009
- 2009-04-29 CN CN200920093555XU patent/CN201401209Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101629507A (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 two buffer gaps and preparation process thereof |
| CN112459869A (en) * | 2020-12-14 | 2021-03-09 | 艾蓝腾新材料科技(上海)有限公司 | Electric heating type foam alloy filter core |
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