摘要:
Solid particles are coated in a fluidized bed by application of a gaseous coating agent from a plasma, wherein the plasma is generated outside the fluidized bed under 0.01-500 mbar, and the plasma-activated gas is passed into the fluidized bed, which is operated under 0.1-500 mbar, wherea. the plasma is generated from the total amount of gaseous coating agent with or without another gas, orb. the plasma is generated from a portion of the gaseous coating agent with or without another gas, and the remaining portion is introduced directly into the fluidized bed, orc. the plasma is generated from another gas, and the total amount of gaseous coating agent is introduced directly into the fluidized bed.
摘要:
A coated catalyst is prepared by depositing an alloy by physical vapor deposition and/or chemical vapor deposition on a molding, at least one alloy component being a metal selected from the group consisting of aluminum, gallium, silicon, germanium, tin, lead, bismuth, yttrium, titanium, zirconium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, iron, cobalt, ruthenium, rhodium, palladium, osmium, iridium, platinum, copper, silver, gold and zinc.
摘要:
The invention relates to a process for preparing a catalyst support, in which zirconium dioxide powder is mixed with a binder, if desired a pore former, if desired an acid, water and, if desired, further additives to give a kneadable composition and the composition is homogenized, shaped to produce shaped bodies, dried and calcined, wherein the binder is a monomeric, oligomeric or polymeric organosilicon compound. Suitable binders are monomeric, oligomeric or polymeric silanes, alkoxysilanes, aryloxysilanes, acryloxysilanes, oximinosilanes, halosilanes, aminoxysilanes, aminosilanes, amidosilanes, silazanes or silicones. The invention also provides the catalyst support which has been prepared in this way, a catalyst comprising the support and its use as dehydrogenation catalyst.
摘要:
A process for the catalytic gas-phase oxidation of propene to acrylic acid, in which the reaction gas starting mixture is oxidized, with a high propene loading, in a first reaction stage, over a first fixed-bed catalyst which is housed in two successive reaction zones A, B, the reaction zone B being kept at a higher temperature than the reaction zone A, and the acrolein-containing product gas mixture of the first reaction stage is then oxidized in a second reaction stage, with a high acrolein loading, over a second fixed-bed catalyst which is housed in two successive reaction zones C, D, the reaction zone D being kept at a higher temperature than the reaction zone C.
摘要:
Hydrogenous gases are prepared by reacting hydrocarbons with air and/or water at temperatures of from 300 to 1000° C. and a pressure of from 1 to 20 bar in the presence of a catalyst by using a spinel catalyst which comprises at least one element of transition group VIII of the periodic table.
摘要:
Catalysts for preparing carboxylic acid salts from alcohols which a) consist of copper or b) comprise from 99.9 to 10% by weight of copper and from 0.01 to 90% by weight of iron and from 0 to 50% by weight of one or more other metals, and may optionally be doped, the hydroxides being obtained by precipitation of copper salt solutions or by coprecipitation of copper and iron salt solutions optionally containing salts of other metals using a base, and being reduced by hydrogen.
摘要:
A magneto-optical disk having at least one optically transparent, dimensionally stable substrate and at least one magneto-optical recording layer of a chromium-containing lanthanide/transition metal alloy, wherein the chromium concentration changes in the horizontal direction, and a process for the producton of the magneto-optical disks.
摘要:
In a magnetooptical computer disk having one or more optically transparent dimensionally stable substrates and one or more double layer systems consisting of two exchange-coupled magnetic layers which consist of alloys of rare earth metals with transition metals and have vertical magnetic anisotropy, the first magnetic layer adjacent to the substrate has a composition corresponding to the formula IRE.sub.x TM.sub.100-x-y-a Pt.sub.y A.sub.a Iand the second magnetic layer, which is arranged on that side of the first magnetic layer which faces away from the substrate, has a composition corresponding to the formula IIRE.sub.u TM.sub.100-u-b B.sub.b IIwhereRE is one or more elements from the group consisting of Gd, Tb, Dy and Ho,TM is one or more elements from the group consisting of Fe and Co,A and B independently of one another are elements from the group consisting of Cr, Nb, Ta, Al, Si, Ni and Mo,and5.ltoreq.x.ltoreq.30,0.5.ltoreq.y.ltoreq.20,15.ltoreq.u.ltoreq.30,0.ltoreq.a.ltoreq.25 and0.5.ltoreq.b.ltoreq.25.
摘要翻译:在具有一个或多个光学透明的尺寸稳定的基板和一个或多个双层系统的磁光计算机盘中,所述双层系统由由稀土金属与过渡金属的合金构成并且具有垂直的磁各向异性的两个交换耦合磁性层组成,第一磁性层 与基板相邻的具有对应于式I的组成RExTM100-xy-aPtyAa和布置在第一磁性层背离基板的那侧的第二磁性层具有对应于式II的组成 REuTM100-u-bBb II其中RE是由Gd,Tb,Dy和Ho组成的组中的一种或多种元素,TM是由Fe和Co组成的组中的一种或多种元素,A和B彼此独立地是元素 来自由Cr,Nb,Ta,Al,Si,Ni和Mo组成的组,5≤x≤30,0.5≤y≤20,15 u> 30, 0 = a = 25和0.5 = b = 25。
摘要:
A catalyst suitable for the gas-phase oxidation of organic compounds to α,β-unsaturated aldehydes and/or carboxylic acids and having an active phase comprising a multimetal oxide material is prepared by a process in which a particulate catalyst precursor which contains oxides and/or compounds of the elements other than oxygen which constitute the multimetal oxide material, which compounds can be converted into oxides, is prepared and said catalyst precursor is converted by calcination into a catalytically active form, wherein a stream of the particulate catalyst precursor is passed at substantially constant speed through at least one calcination zone at constant temperature for calcination.
摘要:
The invention relates to a method of controlling a hydrogenation of a starting material in a hydrogenation reactor, in which the amount of hydrogen reacted in the hydrogenation is firstly determined, the ratio of the amount of hydrogen reacted to the amount of starting material fed in is then derived, this ratio is compared with a prescribed value and, finally, at least one process parameter is altered if the ratio of the amount of hydrogen reacted to the amount of starting material fed in deviates by a prescribed amount from the prescribed value.