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    • 41. 发明申请
    • CATALYTIC COMBUSTION PROCESS USING SUPPORTED PALLADIUM OXIDE CATALYSTS
    • 使用支持的氧化铝催化剂的催化燃烧工艺
    • WO1993018347A1
    • 1993-09-16
    • PCT/US1993001742
    • 1993-03-01
    • ENGELHARD CORPORATION
    • ENGELHARD CORPORATIONKENNELLY, TeresaFARRAUTO, Robert, J.HOBSON, Melvin, C., Jr.WATERMAN, Earl, M.
    • F23R03/40
    • F23C13/00F23C13/08F23R3/40
    • A process for operating a palladium oxide-containing catalytic combustor is useful, e.g., for powering a gas turbine. The palladium oxide is supported on a metal oxide such as alumina, lanthanide metal oxide-modified alumina, ceria, titania or tantalum oxide. The method involves maintaining control of the temperature within the combustor in such a manner as to insure the presence of palladium oxide. By maintaining the temperature below the decomposition onset temperature of palladium oxide (which is catalytically active for catalytic combustion) into metallic palladium (which is catalytically inactive) deactivation of the catalyst is avoided and high catalytic activity is retained. Regeneration of catalyst following inactivation resulting from an over-temperature is accomplished by using a heat soak in a regeneration temperature range which varies depending on the particular metal oxide used to support the palladium oxide.
    • 用于操作含氧化钯的催化燃烧器的方法是有用的,例如用于为燃气轮机供电。 氧化钯负载在氧化铝,镧系金属氧化物改性氧化铝,二氧化铈,二氧化钛或氧化钽等金属氧化物上。 该方法包括以确保氧化钯存在的方式维持燃烧室内温度的控制。 通过将低于催化燃烧的氧化钯(其对于催化燃烧具有催化活性)的分解开始温度维持在金属钯(其是催化无活性的)中,避免了催化剂的失活,并且保持了高催化活性。 通过使用根据用于支撑氧化钯的特定金属氧化物而变化的再生温度范围内的热浸泡来实现由过温引起的失活后催化剂的再生。
    • 48. 发明申请
    • CATALYTIC PYROLYSIS DEVICE AND PROCEDURE FOR THE PRODUCTION OF THE STRUCTURE OF THE HOUSING BODY OF THE CATALYTIC PYROLYSIS DEVICE
    • 用于生产催化热解装置的壳体结构的催化热解装置和方法
    • WO2009019520A2
    • 2009-02-12
    • PCT/HU2008000092
    • 2008-07-31
    • 3R CARBON CAPTURE AND STORAGEHARANGI ARPADSIKLOSI EDITSTREGOVA ERZSEBET
    • HARANGI ARPADSIKLOSI EDITSTREGOVA ERZSEBET
    • F23G7/07B01D53/864B01D2255/2047B01D2255/20753B01J23/78B01J37/023B01J37/0242B01J37/0244C04B35/195C04B35/20C04B35/6365C04B2235/3215C04B2235/3217C04B2235/3232C04B2235/349C04B2235/94F23C13/08
    • The subject of the invention relates to a catalytic pyrolysis device primarily for the neutralisation of dangerous combustion products and waste materials, the elimination of flue gases and the utilisation of complex carbon chains, which contains a housing body enclosing a reaction space and an active material coating covering at least part of the inner side of the housing body, where the housing body is a ceramic material with a solid core and a porous shell that has depressions suitable to receive the particles of the active material coating at least on the boundary surface of the core facing the reaction space, the active material coating has a nickel base containing magnesium. The characteristic feature of the device is that the core (21) of the housing body (20) is from a protoenstatite ceramic stabilised with a sintered glassy phase, and the porous shell (22) at least partially covering the core (21) is from 0.6-1.1 mm thick magnesium silicate with added alpha-corundum, and the active material coating (23) located on the porous external surface (22a) of the shell (22) is Ni-Mg oxide produced using heat treatment from a Ni-Mg double salt and, in a given case, contains Ni-Si components. The subject of the invention also relates to the production of the housing body structure of a catalytic pyrolysis device primarily suitable for to the neutralisation of dangerous combustion products and waste materials, the destruction of flue gases and the utilisation of complex carbon chains, during which we form a core material, the formed core material is subject to heat treatment, following this it is coated with a shell former, then is again subjected to heat treatment, following this the shell is given an active material coating, and finally is subjected to a further heat treatment. The characteristic feature of the invention is that for the raw material for the production of the solid core (21) we use 50-65 mass% finely ground talcum powder, 15- 35 mass% talcum powder fired at 1200+50°C and/or talcum powder, 4-7 mass% magnesium carbonate and 5-9 mass% barium carbonate, and, in a given case, 0.1-0.2 mass% rutile titanium dioxide, then the raw material is shaped by pressing and is fired at 750±10 °C, then as a porous shell (22) by immersion and/or spraying we apply a fine ground material slurry to the boundary surface (21a) of the solid core (21) produced in this way consisting of 6-14 mass% fine grain calcinated alpha corundum, 4-9 mass% white burning plastic fine clay, 55-68 mass% raw talcum and 22-28 mass% talcum powder fired at 1200+50 and 3-12 mass% paper industry grade pulped cellulose fibre, 0.1-0.2 mass% ammonium lignosulphate and 0.2-0.8 mass% tri-methylcellulose with a molar mass of between 1000-5000, we apply a material mixture with a density of 1250-1300 g/l and we continue thickening the porous shell (22) until the theoretical post-firing thickness of the porous shell (22) reaches 0.6-1.1 mm, following creating the porous shell (22) the housing body (20) is dried and fired at 1200±10 °C, then the housing body (20) with its solid core (21) and porous shell (22) is dipped once or several times in a Ni-Mg double salt melt and then any surplus is removed from the housing body (20) an in this way an active material coating is applied to the housing body (20), then finally the housing body (20) with the applied active material coating (23) is heat- treated at 600±10 °C.
    • 本发明的主题涉及一种催化裂解装置,主要用于中和危险的燃烧产物和废料,消除烟道气和利用复杂的碳链,其中包含一个包围反应空间的壳体和活性物质涂层 覆盖壳体的内侧的至少一部分,其中壳体是具有固体芯的陶瓷材料和多孔壳,所述多孔壳具有适于至少在所述壳体主体的边界表面上接收活性材料涂层的颗粒的凹陷 核心面向反应空间,活性材料涂层具有含镁的镍基。 该装置的特征在于,壳体(20)的芯部(21)来自用烧结玻璃相稳定的原生态稳定陶瓷,并且至少部分覆盖芯部(21)的多孔壳体(22)来自 0.6-1.1mm厚的加入了α-刚玉的硅酸镁,并且位于外壳(22)的多孔外表面(22a)上的活性材料涂层(23)是使用Ni-Mg 双盐,在给定的情况下,含有Ni-Si成分。 本发明的主题还涉及主要用于中和危险燃烧产物和废料的催化裂解装置的壳体结构的生产,烟气的破坏和复杂碳链的利用,在此期间 形成芯材,将形成的芯材进行热处理,然后用壳形成器涂覆,然后再进行热处理,随后将壳体给予活性材料涂层,最后进行 进一步热处理。 本发明的特征在于,对于用于生产实芯(21)的原料,使用50-65质量%的细磨的滑石粉,在-1200 + 50℃下烧制15-35质量%的滑石粉和/ 或滑石粉,4-7质量%碳酸镁和5-9质量%碳酸钡,在给定情况下为0.1〜0.2质量%的金红石型二氧化钛,然后将原料通过压制成形,并以750± 10℃,然后通过浸渍和/或喷涂作为多孔壳体(22),将细碎的研磨材料浆料施加到以这种方式制备的实心芯(21)的边界面(21a)上,由6-14质量% 细粒煅烧α刚玉,4-9质量%白烧塑料细粘土,55-68质量%原滑石和22-28质量%滑石粉,1200 + 50和3-12质量%纸工业级制浆纤维素纤维, 0.1-0.2质量%的木质素铵铵和0.2-0.8质量%的摩尔质量在1000-5000之间的三甲基纤维素,我们应用密度为1250〜 1300g / l,继续加厚多孔壳(22)直到多孔壳(22)的理论烧成后厚度达到0.6-1.1mm,之后产生多孔壳(22),壳体(20)被干燥 并在1200±10℃下烧制,然后将其固体芯(21)和多孔壳(22)的壳体(20)在Ni-Mg双盐熔体中浸渍一次或数次,然后将任何剩余物从 壳体(20)以这种方式将活性材料涂层施加到壳体(20)上,然后最终将具有施加的活性材料涂层(23)的壳体(20)热处理为600±10° C。