• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    There are provided shaped catalysts, particularly for the formation and/or equipping of reaction chambers with catalytically active surfaces, consisting of a structural reinforcing agent of ferrous metal, a layer of a heat resistant carrier material on the structural reinforcing agent as well as a catalytically active component on the carrier material; the body of the structural reinforcing agent consists of iron or steel and its surface is provided with a nonscaling, adhesive and anchoring enhancing aluminum/iron diffusion layer obtained by a tempering of aluminum coated iron or steel at a temperature between 600 DEG and 1200 DEG C. for at least one minute. There is also disclosed a process for making the catalysts.
    公开号:SU1011035A3
    申请号:SU802981961
    申请日:1980-09-25
    公开日:1983-04-07
    发明作者:Фелькер Херберт；Коберштайн Эдгар；Боцон Альфред；Хензель Йерг
    申请人:Дегусса Аг (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to a catalyst carrier formed in the process of making the reactor or equipping reaction chambers with catalytically active surfaces and the method of fabricating the catalyst carrier, particularly in the form, for direct application in the chamber. The catalyst is used to purify exhaust gases.,
    . A limestone molded support for an exhaust gas purification catalyst for internal combustion engines consisting of a molded structural amplifier of oi-alumina and a surface oxide layer deposited from a sintering promoter — a compound selected from group ib, including silicon dioxide, TaHji, and zirconium; manganese oxide, calcium, magnesium, boron, chromium, copper CljCrfQCoo to obtain a well-known molded carrier for the catalyst OiHCTKH engine exhaust gases inside; -i; e G. O combustion consists of grinding a mixture of c-oxide and Lumini C. Promoter sintering - at least one compound selected from the group including silicon dioxide, tzcia, zirconium, manganese, and silicon oxide, magnesium, boron, chromium, copper, 3 additions of polyvinyl alcohol of water, mixing, extrusion -; ,: mass of a mass, resolution of ae: -; and tablets processing in po. Pellet torus, drying, caking to obtain a carrier having a spherical or columnar shape fl
    K; The known solution should include the sensitivity of the molded / carrier and mechanical load and thermal overheating. Carriage: -; the user is in motion mode; -1 comp CGiiraJi and 13 result of discontinuity impulse. Exhaust gas engine vibrations and vibrations during movement act as the carrier is destructive. For those:; overheating, sintering, melting and tracking of a monolithic or bulk structural amplifier with its layer may occur, resulting in partial or complete deactivation.
    The closest to the proposed essence and effect achieved is a molded carrier for the catalyst for purification of exhaust gases of internal combustion engines in the form and / or when the reaction chambers are equipped with catalytically active surfaces, consisting of molded structural metallic steel. with a carbon content of 0.12-0.25 wt.% with nansegun} - its coupling surface.; 1Go: a base, in which quality HOcviTej contains mets;
    copper or silver, and a layer of eta- and raMivia-alumina, cerium and: zirconium oxides, and a method for preparing a molded carrier for an exhaust gas purification catalyst for internal combustion engines in the form and / or when the reaction chambers are equipped with a catalytically active surface, including applying a bonding base (metallic copper or silver) by flame spraying onto the surface of a connecting element made of steel with a carbon content of 0.12-0.25 wt.% forming it into a housing serving as a structural amplifier; a layer of eta- and gamma-alumina drying at 120 ° C, annealing with, applying decomposed during heating compounds of cerium and zirconium or compounds of nickel and zirconium, followed by annealing at 500 ° C and 2J.
    However, in the known carrier and method for its preparation, the strength of the carrier obtained is insufficient. By means of long-term tests (250 hours), the pipe coating on the gas inlet side of the pipe was peeled off, and corrosion was found on the steel field. At the same time, if the conversion at the initial tests of the catalyst on a known molded carrier was for carbon monoxide 21, 11l hydrocarbons 32, nitrogen oxides 4.8%, then the conversion after aging the carrier (after testing for 250 h) is for oxide oh-lerode 8, hydrocarbons 16, nitrogen oxides 2.1%.
    The purpose of the invention is to increase the strength of the carrier.
    To achieve this goal, a molded carrier for the catalyst for purification of exhaust gases of internal combustion engines in the form and / or when the reaction chambers are equipped with catalytically active surfaces, consisting of a molded structural metal amplifier of steel with a carbon content of 0, 12-0, is proposed. 25% by weight with an adhesive base (aluminum) deposited on its top and a layer of aluminum gammoxide, cerium oxides and zirconium
    The method of preparation of a molded carrier for catalyst purification of exhaust gases of internal combustion engines in the form and / or when the reaction chambers are equipped with catalytically active surfaces, including applying an adhesive base (which uses aluminum, 40-60 microns thick), on the surface of the connecting element of steel with a carbon content of 0.12-0.25 wt.% by immersing the element in an aluminum melt
    with subsequent molding it into a housing serving as a structural amplifier, and annealing at 850-900-C for 10-15 minutes, applying a layer of gamma-alumina, drying at il20 ° C, annealing at 500 ° C, applying decomposable during heating cerium and zirconium compounds or nickel and zirconium compounds with subsequent annealing at 500 ° C.
    The media obtained by the proposed method, in comparison with the known, has a higher durability. So, after prolonged testing (250 hours), the coating of the pipe from the gas inlet side of the pipe from the outside and the inside did not show any signs of corrosion or any other damage, the exfoliation of the active layer occurred. At the same time, if the conversion at the initial catalyst tests on the proposed carrier was 25% for carbon monoxide, 5.6% for hydrocarbons 39, and 3.5% for carbon monoxide after aging (after testing for 250 hours). , for hydrocarbons 20, nitrogen oxides 2.5%.
    The molded catalyst may be designed such that the body of the structural amplifier is at least partially covered with a layer which is a combination of carrier material and active component. The catalyst may have simple volumetric forms (granules). It can be made honeycomb coated with a carrier material. To do this, it is sufficient to reinforce wavy or flat wavy sheets covered with aluminum, or alternately wavy and flat sheets, forming separate flow channels separated from each other and parallel to each other, for which annealing is sufficient.
    The advantage of the molded catalyst carrier is that it covers the entire reaction chamber, and the catalytically active surface is rotated to the reaction chamber, which is known from 23. According to this principle, the structurally reinforced carrier of heat-resistant material is made in the form of an internal combustion chamber burnout For this purpose, the cylinder head of the internal combustion engine is made of a structural iron reinforced with a diffusion layer, the surface facing the combustion chamber is provided with a heat-resistant carrier material. It can also be made in the form of a pipe or a system of pipes, the inner walls of which are covered with a layer of heat-resistant carrier material. In one embodiment of the invention, such a pipe
    or, respectively, the piping system is designed as an exhaust pipe, a vapor pipe or a vapor pipe, a preliminary or main muffler of a car with an internal combustion engine.
    The molded catalyst carrier can be made in the form of an element diluted in a catalytic tube or a pipe system that interferes with the flow of gases or changes its direction, covered with a heat-resistant layer of carrier material on all sides. Built-in elements can be installed in a pipe or pipe system along their entire length or in areas
    five . at intervals. In the simplest case, this embodiment is covered inside with a layer of carrier material, an exhaust pipe equipped with built-in elements that prevent the flow of gases and / or change their flow direction, and coated carrier material with which the dynamic pressure is reached 0.3-2500 mm water Art.,
    5 measured at an air flow rate of 12 m / s at room temperature, which is higher compared to pipes without built-in elements.
    Performed according to images ethenia
    0 catalyst tubes or pipe systems, respectively, equipped with a vortex providing a certain mass transfer ratio, have significant advantages compared to known bulk or honeycomb catalysts. Exhaust gas pipelines achieve a high conversion rate of harmful substances and therefore either bulk and cellular systems can be rejected or their size can be significantly reduced. The structural amplifier body can be made of Iron materials typical for exhaust gas pipelines of any thickness. Before or after it is molded by conventional metalworking techniques, such as forging, stretching, casting, etc., the casing can be fully or partially provided with a layer of annealed aluminum.
    In exhaust gas pipelines with a coating of a catalytically active material, the distribution of harmful gases released during combustion
    5 heat substances occur in a significantly enlarged, lengthwise zone, due to which local overheating typical for using bulk or cellular catalysts is eliminated, for example, in case of ignition problems. The catalyst formed by the method proposed is also suitable for protecting the known catalytic gas cleaning devices from overheating, for this purpose
    five
    Supply 1 st exhaust gas pipes are made as a catalyst. In addition, a molded support with a catalytic coating can be used as a preheater to activate the underlying catalyst activated (initiating catalyst
    According to the proposed method of manufacturing a molded carrier for a catalyst, the plating obtained multilayer material from coated aluminum with a thickness of 40-60 microns of carbon steel is formed into an element provided as a structural reinforcement, annealed for 7-30 minutes at BVO-EOO C, and a surface with a diffusion layer of aluminum and iron is applied a layer of heat-resistant alumina gamma-raya from a 30% aqueous dispersion, then calcined at 500 ° C, heat-sensitive compounds of prairie and zirconium or nickel are applied l and zirconium and calcined again at 500 ° C.
    Example 1. A repeatedly bent round pipe with a 4-rib, linearly-built, unalloyed carbon steel ST 45.8 CST 45.8 clad on both sides means: minimum tensile strength at 45 kg / mm; 8 - steel, resistant to DJ; to the influence of heat. The carbon content in steel is 0, 25 wt.%) Size: internal diameter 40, external diameter 43, length 1000 lm, thickness of the applied aluminum layer 60 microns. Aluminum cladding occurs by immersing the pickled steel tape in a large mass of molten aluminum and rolling directly thereafter. The plated strip is then molded into a tube and is inductively welded. Inside, the pipe is equipped with a 4-rib screw-in connector, which makes it turn 360 ° over a length of 1 m. The material of this insertion is also ST 45.8, as is an aluminum-clad pipe. The ends of the screw insert welded to the pipe.
    The aluminum-clad round tube with a screw insert is then annealed in an annealing furnace at 850s for air in an annealing furnace. Then, the structural enhancer is washed with a 30% aqueous dispersion of gamma-alumina and coated (filled) with 45 g of AlgO.
    It is then dried at 120 s and annealed for 1 hour at 500 ° C. Exhaust pipe - coated with heat-resistant nonsaturated material; I process 25 ml of an aqueous solution of 2.55 g of ammonium cerium nitrate and 4.13 g of zirconium nitrate, so that after drying and annealing at 500 ° С for 60 minutes 0.8 g cerium oxide and 1.5 g of zirconium oxide remain in the layer (coating) of A1.0. Then the tube is washed with 25 ml of an aqueous solution of 1.72 g of hexachloroplatinic acid and 0.215 g of rhodium chloride (weight ratio Pt: Rh 8.5: 1) and dried. The content of Pt 0,8945, the content of Rh 0,1055,
    0 finally, salts of the noble metals deposited on the washed layer are reduced in a stream of hydrogen at 500 ° С (1 h).
    The molded catalyst produced in this way is tested on an engine test bench in a fresh CO 2 and finally subjected to long-term tests for more than 250 hours at exhaust gas temperatures of 680-750 ° C (when using gasoline without lead). Finally, it is checked again for activity. After testing outside and inside no trace of corrosion or other
    5 damage on the applied coating is not detected. Peeling of the active layer did not occur. The activity of the coating decreased by the amount usually arising from a noble metal catalyst for a given test duration. Test conditions:
    Volumetric speed, 000 Exhaust temperature
    about.
    Gas, with
    300-690
    Composition of exhaust gases:
    Sob. % 0.5
    NSG. Million, 150
    40 QX2; million, 1800
    Soob.%, 14.9
    02% by volume
    Nitrogen residue and water vapor
    Activity during initial testing.
    Conversion at the temperature of exhaust gases 500 ° С, L 1.03,%: Q CO 65; HC 53; 6.
    Activity after aging,
    Conversion at an exhaust gas temperature of 690 ° C and L 1.03 after 250 h of engine testing (engine with Otto cycle, 1.6 l)%:
    CO 40; NS 42; NOx, 2.6.
    Example 2. A straight exhaust pipe made according to Example 1, in the form of a molded catalyst, in which instead of a noble layer metal contains a 120 g layer of components of non-precious metals (weight ratio mbdie and chromium: aluminum: nickel oxide: zirconium oxide 70:30: 8:10 ;, subjected to long tests (over 250 hours), and lead fuel is used. The lead content in the fuel is 0.17 g / l. Test and aging conditions as in Example 1. Initial test activity x. Conversion at exhaust temperature Call and L 1.03%: CO 25 HC 39; N0 5.6. Activity after aging. Conversion at the temperature of exhaust gases and L 1.03 after 250 h engine tests (engine with Otto cycle, 1.6 l),% : CO 13; HC 20; NOx 2.5. The molded catalyst has no corrosion damage, the coating layer is unchanged. Example 2a (according to 2). The straight exhaust pipe of unalloyed ST 45.8 carbon steel is defatted. trichlorethylene, then electrolytic copper is introduced into the gun nozzle for gas plasma metallization and acetylene / oxygen in the flame when argon is used (to eliminate copper oxidation), 120 g of a mixture of copper-chromium oxide, gum Ma-AI Oj, nickel oxide and zirconium oxide are applied to the inner surface of the exhaust pipe at a weight ratio of 70: 30: 8: 10 by grinding and sieving, they are treated to the sizes of DIN 60 - 16 grains. The powder is applied by plasma spraying on a copper layer, but air is used as a sputtering gas. The test is carried out, as in Example 2, by long-term tests (over 250 hours), using conventional fuel containing lead (0.17 g / l. The test and aging conditions correspond to Example 1. The activity during the initial tests was x. Conversion at the temperature of the exhaust gases 500 ° C, 03,%: CO 21; HC 32; NOj "", 8. Activity after aging. Conversion at an exhaust gas temperature of 690 ° C, 03 after 250 hours of engine testing with a 1.6 liter through Otto cycle,%: CO 8; NA 16;, Pipe coating after testing from the side of the gas inlet into the pipe was removed, and a corr. Was found on the steel beneath it g. Example 3. Forward exhaust pipe. Length: 1000, internal diameter 40, external diameter 43 mm made of ST 34 steel (ST 34 means minimum tensile strength at 34 kg / mm, carbon content 0 , 12 wt.%) In a warm method, bilaterally clad with aluminum, the thickness of the layer of which is 40-60 microns. The aluminum cladding takes place by dipping the etched steel tape into the molten aluminum and subsequent rolling. The clad tape is molded into a tube and is inductively welded. The pipe is equipped inside with a 6-blade swirler having a turn on at a length of 1 m. The material is a swirler, like pipes, ST 34 steel, aluminum-clad. The ends of the swirler are welded to the pipe. The tube, fitted with an insert, heated in 15 minutes to 870-900 ° C, is thermally treated in a muffle furnace. To do this, the tube is placed in a furnace that is already heated to a high temperature, melted at this temperature, and the blue begins to diffuse into iron, and a rough-surface, corrosion-resistant, scaling-resistant and strongly adherent iron-rich alloy is formed, showing the method of research according to Debay-Scherrer, only the interference of iron and aluminum-iron. The oxides of these metals cannot be fixed on the surface. After heat treatment, the pipe is coated with a 30% alumina dispersion. To do this, heat-treated alumina is washed in water, dispersed and mixed with polyamine (added as a stabilizer). Grain size distribution in annealed alumina,%:. 100r. 10 50 (35 10 jvx 80 With the same washing solution (washing) the pipe is washed twice, blown with air and dried, 50 g of ip-AI O are precipitated. The pipe soaked up is annealed for 1 hour in a muffle furnace at 500 ° C in air, The solution contains 133 g of ammonium cerium nitrate and 185 ml of zirconium nitrate solution (with 20% ZrO) per 1 L. 60 ml of solution are needed for impregnation, which corresponds to CeOj and 3.3 ZrOo .. 1 After drying, the tube is re-treated for 1 hour at 500 ° C in air to decompose the nitrate. active coating ki 1 g of noble metals (0,8945 Pt and 0,1055 Rh), which corresponds to the weight ratio between Pt and Rh 8,5: 1), 5 g atsetiladetonata alumina and 120 ml of methanol. 91011 Use 3.578 g of HnPtClj, (solution with 25% Pt) and 0.639 g of RhCla (solution with 16.49% Rh). The inside of the pipe, treated with a washing solution containing cerium and zirconium, is impregnated twice with this solution with 5 rum, respectively, after which the methanol impregnation is ignited and the methanol is burned out. Thermal decomposition takes place in a muffle furnace at 600 ° C for 10 min with pro-10 ml. The tube thus treated on the engine test bench showed the following catalytic activity (condition of test and aging correspond to example 1). Activity at initial tests. Conversion 1 three temperature of exhaust gases 500 С and, 03, f: СО / О; NA 3; MO5, Activity after aging. , Conversion at an exhaust gas temperature of 690 C and ID 1.03 after 250 hours of engine testing (engine, cycling otto, Ij6 l),%: (; ot3; HC31; NOxi), 3. Formed as an exhaust pipe, the catalyst has no signs of corrosion or damage to the coating.
    权利要求:
    Claims (2)
    [1]
    1. A molded carrier for a catalyst for purification of exhaust gases of internal combustion engines in the form and / or when equipping the reaction chambers with catalytically active surfaces, consisting of a molded structural metal amplifier made of steel with a carbon content of 0.12-0.25 wt.% With deposited on its surface there is an adhesive base and a layer of gamma-alumina, oxide of cerium and zirconium, which is related to the fact that, in order to increase the strength of the support, it contains aluminum as an adhesive base.
    [2]
    2. A method of preparing a molded carrier for a catalyst for purification of exhaust gases of internal combustion engines in the form and / or when equipping the reaction chambers with catalytically active surfaces, comprising applying an adhesion base to the surface of a steel connecting element with a carbon content of 0.12-0.25 weight%. , ^ yurmovanie it into the housing, which serves a structural enhancer, applying a layer of aluminum gammaokisi, drying at 120 ° C, annealing at 500 ° C, then applying a degradable by heating compounds of cerium and of zirconium compounds or n nickel and zirconium followed by annealing at 500 ° C, characterized in that, in order to prepare a carrier with increased strength, aluminum is used as a bonding base, the application of which with a layer thickness of 4060 μm on the surface of the connecting element is carried out by immersing the element in molten aluminum followed by molding and annealing at 850-900 ° C for 10 15 minutes
    类似技术:
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    同族专利:
    公开号 | 公开日
    DE2745188C3|1980-05-08|
    FR2405093B1|1982-11-19|
    GB2005149B|1982-03-10|
    PL113116B1|1980-11-29|
    NL184150C|1989-05-01|
    JPS6133621B2|1986-08-02|
    JPS5467587A|1979-05-31|
    DE2745188A1|1979-04-12|
    DE2745188B2|1979-08-16|
    US4188309A|1980-02-12|
    NL7802395A|1979-04-10|
    AU3743378A|1980-01-03|
    IT7867999D0|1978-05-02|
    GB2005149A|1979-04-19|
    SE438450B|1985-04-22|
    AU522621B2|1982-06-17|
    SE7802925L|1979-04-08|
    DD140989A5|1980-04-09|
    IT1111471B|1986-01-13|
    NL184150B|1988-12-01|
    CS199526B2|1980-07-31|
    CA1122956A|1982-05-04|
    FR2405093A1|1979-05-04|
    PL210059A1|1979-06-18|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE2745188A|DE2745188C3|1977-10-07|1977-10-07|Shaped catalyst, process for its manufacture and use|
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