摘要:
The invention relates to a catalyst comprising: a) a catalyst support made of a ceramic, the support comprising an arrangement of crystallites having the same size, the same isodiametric morphology and the same chemical composition or substantially the same size, the same isodiametric morphology and the same chemical composition, in which each crystallite makes point contact or almost point contact with the surrounding crystallites; and b) at least one active phase comprising metallic particles that interact chemically with said catalyst support made of a ceramic and that are mechanically anchored to said catalyst support in such a way that the coalescence and mobility of each particle are limited to a maximum volume corresponding to that of a crystallite of said catalyst support.
摘要:
A method of preparing a composite includes the following steps. A powder blend is sintering while an oxygen partial pressure (pO2) of a gaseous atmosphere surrounding the powder blend is controlled. Before the sintering, a shape is formed from the powder blend. After the forming and before the sintering, binder is removed from the powder blend. The powder blend comprises binder, a mixed electronic/oxygen O2− anionic conducting compound (C1) and a compound (C2) chosen from MgO and BaTiO3. The resultant composite comprises at least 75 vol % of compound (C1), from 0.01 to 25 vol % of compound (C2), and from 0 vol % to 2.5 vol % of compound (C3).
摘要:
A catalytic composition comprising a catalytically active metal and a solid support, characterized in that said catalytically active metal is included into the core structure of said solid support, and said solid support is a refractory and ionic conductive oxide, process for their preparation and its use as a catalyst in synthesis gas production.
摘要:
The invention relates to an architecture comprising ceramic or metallic foam, characterized in that the foam has at least one continuous and/or discontinuous, axial and/or radial porosity gradient ranging from 10 to 90%, and a pore size from 2 ppi to 60 ppi, and in that the architecture has a micro structure comprising specific area ranging between 0.1 to 30 m2/g, a grain size between 100 nm and 20 microns and a skeleton densification above 95%. One process to obtain this architecture can be based on the preparation of a ceramic foam with porosity gradient comprising: choosing at least one polymeric sponge, impregnation of the polymeric sponge by a ceramic slurry, drying of the impregnated sponge, pyrolysing the organics including the polymeric sponge, and sintering, and characterized in that we realize a pre-step to obtain a continuous and/or discontinuous porosity gradient.
摘要:
The invention concerns a mixed electronic and O2− anion conductive perovskite material, of formula (I): A(a)(1-x-u)A′(a−1)xA″(a″)uB(b)(1-s-y-v)B(b+1)sB′(b+β)yB″(b″)vO3-d, wherein: a, a−1, a″, b, b+1, b+β et b″ are integers representing respective valences of the atoms A, A′, A″, B, B′, B″; a, a″, b, b″, β, x, y, s, u, v et δ such that the electrical neutrality of the crystal lattice is preserved; A represents an atom selected among scandium, yttrium or in the families of lanthanides, actinides or alkaline-earth metals; A″ represents an atom selected among Al, Ga, In, or Tl; B, B′, B″ represents an atom selected among the transition metals, Al, In, Ga, Ge, Sb, Bi, Sn or Pb. The invention also concerns the method for preparing said material and its use as mixed conductive material of a catalytic membrane reactor, for use in synthesizing synthetic gas by oxidation of methane or natural gas.
摘要:
A composite material (M) comprising: at least 75% by volume of a mixed electronic conductor compound oxygen anions O (C1) selected from doped ceramic compounds which, at the temperature of use, are present in the form of a crystalline network having ion oxide lattice vacancies and, more particularly, in the form of a cubic phase, a fluorite phase, a perovskite phase, of the aurivillius variety, a Brown-Millerite phase or a pyrochlore phase; and 0.01%-25% by volume of a compound (C2) which is different from compound (C1), selected from oxide-type ceramic materials, non-oxide type ceramic materials, metals, metal alloys or mixtures of said different types of material; and 0%-2.5% by volume of a compound (C3) produced from at least one chemical reaction represented by the equation: xFC1+yFC2 - - - >zFC3, wherein FC1, FC2 and FC3 represent the raw formulae of compounds (C1), (C2) and (C3) and x, y and z represent rational numbers above or equal to 0. The invention also relates to a method for the preparation and use thereof as mixed conductor material for a membrane catalytic reactor used to synthesize synthetic gas by catalytic oxidation of methane or natural gas and/or as mixed conductor material for a ceramic membrane.
摘要翻译:一种复合材料(M),其包含:至少75体积%的混合电子导体化合物氧阴离子O 2(C1),其选自掺杂的陶瓷化合物,其在使用温度下以 具有离子氧化物晶格空位的晶体网络,更具体地,呈立方相,萤石相,钙钛矿相,褐铁矿相或烧绿石相的形式; 和不同于化合物(C1)的化合物(C 2 H 2)的0.01体积%〜25体积%,选自氧化物型陶瓷材料,非氧化物型陶瓷材料,金属,金属合金 或所述不同类型材料的混合物; 和由以下等式表示的至少一种化学反应产生的化合物(C 3 S 3)的0%-2.5体积%,其中FC1,FC2和FC3表示 化合物(C1),(C2H2)和(C3-C3)的原始化学式,x,y和z表示高于或等于0的有理数。本发明还 涉及一种用于制备和用作用于通过甲烷或天然气的催化氧化和/或作为陶瓷膜的混合导体材料合成合成气体的膜催化反应器的混合导体材料的方法。
摘要:
Preparation of a supported tubular ceramic membrane composed of two coaxial layers along a axis (x), a first layer with a non-zero thickness es of a support material (S) and a second layer with a non-zero thickness eM of an active material (M), characterised in that it comprises the following steps in sequence: a step (a) to shape said supported membrane by simultaneous coaxial co-extrusion of a paste PS of the support material (S) at a flow velocity along the axis (x) VS and a paste PM of active material (M) with a flow velocity along the axis (x) VM, where VS=VM; a step (b) to dry the co-extrudate formed in step (a); a step (c) to debind the co-extrudate dried in step (b), and a step (d) to apply a heat treatment to co-sinter the two coaxial layers of the product obtained in step (c); Device for implementation of step (a).
摘要翻译:制备由轴(x)两个同轴层组成的支撑管状陶瓷膜,具有非零厚度的支承材料(S)的第一层和非零厚度的第二层 M的活性物质(M),其特征在于,其顺序包括以下步骤:步骤(a)通过同时同时共挤出糊状物来形成所述负载膜, 沿着轴线(x)V S S的流速和活性材料(M)的浆料P M M的流速(S)的支撑材料(S) 沿着轴线(x)V M M,其中V S = V M; 步骤(b)干燥步骤(a)中形成的共挤出物; 剥离步骤(b)中干燥的共挤出物的步骤(c)和步骤(d),以进行热处理以共烧烧步骤(c)中获得的产物的两个同轴层; 用于实施步骤(a)的装置。
摘要:
Device for the purification of exhaust gases from a thermal combustion engine comprising:one or several ceramic catalyst carriers comprising an arrangement of crystallites of the same size, same isodiametric morphology and same chemical composition, or approximately the same size, same isodiametric morphology and same chemical composition in which each crystallite is in point or quasi-point contact with the surrounding crystallites, andone or several active phases for chemical destruction of impurities in the exhaust gas comprising metallic particles mechanically anchored in said catalyst carrier such that coalescence and mobility of each particle are limited to a maximum volume corresponding to the volume of a crystallite of said ceramic catalyst carrier.
摘要:
Catalyst comprising: a) a catalytic ceramic support comprising an arrangement of crystallites of the same size, same isodiametric morphology and same chemical composition or substantially of the same size, same isodiametric morphology and same chemical composition in which each crystallite is in point contact or virtually point contact with crystallites that surround it, and b) at least one active phase comprising metallic particles mechanically anchored into said catalytic support so that the coalescence and the mobility of each particle are limited to a volume corresponding to that of a crystallite of said catalytic ceramic support.
摘要:
An architecture made of a ceramic or a metallic foam has at least one continuous and/or discontinuous, axial and/or radial porosity gradient ranging from 10 to 90% associated to a pore size range from 2 to 60 ppi, at least one continuous and/or discontinuous, axial and/or radial concentration gradient of catalytic active(s) phase(s) from 0.01 wt % to 100 wt % preferentially from 0.1 wt % to 20 wt %, and a microstructure with a specific area ranging between 0.1 to 30 m2/g, a grain size between 100 nm and 20 microns and a skeleton densification above 95%.