摘要:
Catalyst for steam cracking reactions consisting of pure mayenite having the general formula:12CaO.7Al2O3having an X-ray diffraction spectrum as indicated in Table I, obtained with a preparation process comprising the following steps: dissolution of salts containing calcium and aluminum with water; completing of the dissolved salts by means of polyfunctional organic hydroxyacids; drying of the solution resulting from the completing in order to obtain a solid precursor product; calcination of the solid precursor product at a temperature ranging from 1300 to 1400null C. for at least two hours.
摘要翻译:用于蒸汽裂解反应的催化剂,其由具有以下通式的纯钙铝石组成:具有表C所示的X射线衍射光谱的12CaO.7Al 2 O 3,其制备方法包括以下步骤:用水溶解含钙和铝的盐; 通过多官能有机羟基酸完成溶解的盐; 干燥由此完成的溶液,以获得固体前体产物; 在1300〜1400℃的温度下煅烧固体前体产物至少2小时。
摘要:
Catalyst for steam cracking reactions consisting of pure mayenite having the general formula: 12CaO.7Al2O3 having an X-ray diffraction spectrum as indicated in Table I, obtained with a preparation process comprising the following steps: dissolution of salts containing calcium and aluminum with water; complexing of the dissolved salts by means of polyfunctional organic hydroxyacids; drying of the solution resulting from the complexing in order to obtain a solid precursor product; calcination of the solid precursor product at a temperature ranging from 1300 to 1400null C. for at least two hours.
摘要:
A process is described for the contemporaneous preparation of mesitylene and durene, characterized in that mesitylene and durene are obtained exclusively starting from pseudo-cumene without the use of any further chemical compound, operating in continuous, at a temperature ranging from 210 to 400null C., at a pressure ranging from 1 to 50 bar, with a weight space velocity ranging from 0.1 to 20 hoursnull1 and in the presence of a catalyst based on crystalline metal-silicates in acid form. After the recovery of mesitylene and durene from the reaction raw product, some of the remaining components of the raw product itself are recycled and fed to the reactor together with the pseudo-cumene.
摘要:
Process for preparing catalytic systems consisting of: a vanadium oxide; a bismuth oxide; and a carrier consisting of magnesium oxide, wherein the vanadium, expressed as V2O5, is in a quantity ranging from 2 to 35% by weight, the bismuth, expressed as Bi2O3, ranges from 2 to 40% by weight, the complement to 100 being the carrier, characterized in that it essentially comprises the following steps: preparation of solutions based on derivatives of the components of the catalytic system; mixing of the solutions prepared and optional aging; drying of the solution obtained; first heating, in the presence of air, of the solid obtained from the drying at a temperature ranging from room value to a temperature of between 290 and 310null C., for a time ranging from 1 to 3 hours; optional second heating, in the presence of air, of the solid for a time ranging from 0.5 to 2 hours at a constant temperature, ranging from 290 to 310null C., reached in the first heating; additional heating, in the presence of air, of the solid for a time ranging from 2 to 4 hours at the calcination temperature ranging from 600 to 850null C.; calcination, in the presence of air, of the solid at a constant temperature, ranging from 600 to 850null C., reached in the additional heating, for a time ranging from 8 to 16 hours.
摘要翻译:制备催化剂体系的方法,包括:氧化钒; 氧化铋; 和由氧化镁组成的载体,其中以V 2 O 5表示的钒的量为2至35重量%,以Bi 2 O 3表示的铋为2至40重量%,100的互补为 载体,其特征在于其基本上包括以下步骤:基于催化体系的组分的衍生物制备溶液; 混合制备的溶液和任选的老化; 干燥得到的溶液; 在空气存在下,首先在从室温至290〜310℃的温度范围内干燥得到的固体加热1〜3小时; 在空气存在下,在第一次加热达到290〜310℃的恒定温度下,任选地在空气存在下第二次加热0.5〜2小时。 在600至850℃的煅烧温度下,在空气存在下,额外加热固体2至4小时; 在空气存在下,在额定加热下达到在600至850℃的恒定温度下煅烧固体8至16小时。
摘要:
The present invention regards a catalytic composition comprising gallium, at least one element chosen in the group of the lanthanides, and a zeolite belonging to the MFI, MEL or MFI/MEL families, the crystal lattice of which is made up of silicon oxide and at least one metal oxide chosen from among aluminium oxide, boron oxide and gallium oxide. Preferably, in the catalytic compositions of the present invention a zeolite is used belonging to the MFI family characterized by crystallites which for at least 90% have diameters smaller than 500 null and which can form agglomerates of submicron dimensions characterized by possessing at least 30% of the extrazeolitic porosity in the region of the mesopores. The catalytic compositions of the present invention can, in addition, contain rhenium. These catalytic compositions are useful in processes of aromatization of hydrocarbons containing from 3 to 6 carbon atoms, preferably, hydrocarbon mixtures containing olefins.
摘要:
A highly selective process is described for preparing 2,6-dimethylnaphthalene which comprises reacting a naphthalene hydrocarbon selected from naphthalene, methylnaphthalenes, dimethylnaphthalenes, trimethylnaphthalenes, polymethylnaphthalenes, and/or their mixtures with one or more benzene hydrocarbons selected from benzene, toluene, xylenes, trimethylbenzenes, tetramethylbenzenes, pentamethylbenzene and/or hexamethylbenzene, under at least partially liquid phase conditions and in the presence of a catalytic composition comprising a zeolite belonging to the MTW structural type and at least one element selected from P, B and Si. The process is preferably carried out in the presence of a methylating agent.