Abstract:
A description follows of a bimetallic catalyst, obtained by dispersing in sequence and alternating the precursors of the single metal components of the catalyst on a carrier, and a process for the synthesis of hydrogen peroxide by the direct reaction of hydrogen with oxygen, in a solvent medium containing a halogenated promoter and an acid promoter, in the presence of said catalyst.
Abstract:
PURPOSE: An MFI-type zeolite based catalyst and its preparation method are provided, which catalyst is useful for the transformation of oximes into amides. CONSTITUTION: The MFI-type zeolite based catalyst is prepared by: preparing silicate oligomer by hydrolyzing silicon alkoxide; mixing the oligomer with an aqueous or aqueous alcoholic dispersion solution of sub micro particles of MFI-type zeolite which is acidified to pH below 5; emulsifying the aqueous or aqueous alcoholic ligand/zeolite mixture in an organic solvent; contacting the emulsion with a basic solution to bind the dispersed micro drops; and washing calcining the obtained micro sphere. Preferably the MFI-type zeolite is selected from the zeolite whose mole ratio of Si/Al (or Si/B, Si/Ga, Si/In, or Si/Ti) is more than 1,000, and silicalite-1. The MFI-type zeolite based catalyst is such that the silicate ligand represented by SiO2 is more than 30 wt%, the outer surface area is 60-80 square meter per gram, the specific volumes of micro pore and mesopore are 0.2-0.3 ml/g and 0.1-0.4 ml/g, respectively, the bulk density is 0.7-0.85 g/ml, and the Davison index is less than 6.
Abstract:
PURPOSE: A manufacturing method of a new catalyst and hydrogen peroxide is provided to inform a user the synthesizing method of hydrogen peroxide from hydrogen and oxide using a catalyst which is consisting of a VIII metal supported on the acid-activated hydrogen. CONSTITUTION: The new catalyst is manufactured by the steps of: filling a one-liter glass flask including 5% of HCl aqueous solution of 600 ml with 20 g of powder-typed activated maritime pinewood CECA; heating the agitated suspension at a temperature of 80°C for 2.5 hours; filtrating the suspension, washing the re-collected carbon with distilled water until a chloride is eliminated and drying it in an oven at a temperature of 120°C for 2 hours after cooling it at the normal temperature of 20 to 25°C; equalizing the carbon-acid mixture by adding 96% of H2SO4 40 ml after filling the glass flask with 250 ml of activated carbon; heating the mixture at a temperature of 120°C for 8 hours; and suspending the activated carbon in 150 ml of H2O2 aqueous solution by filling the one-liter glass flask including 500 ml of distilled water with the activated carbon and filtrating the carbon.
Abstract translation:目的:提供新型催化剂和过氧化氢的制造方法,以使用由负载在酸活化氢上的VIII族金属组成的催化剂从氢和氧化物的合成方法通知用户。 构成:新催化剂是通过以下步骤制造的:将含有5%的600ml HCl水溶液的1升玻璃烧瓶与20克粉状活化海洋松木CECA填充; 将搅拌的悬浮液在80℃的温度下加热2.5小时; 过滤悬浮液,用蒸馏水洗涤再收集的碳,直到氯化物除去,并在烘箱中,在20〜25℃的常温冷却下,在120℃的温度下干燥2小时; 通过在250ml活性炭填充玻璃烧瓶后,加入96%的H 2 SO 4 40ml使碳酸混合物平衡; 在120℃的温度下加热混合物8小时; 并通过用活性炭填充含有500ml蒸馏水的1升玻璃烧瓶并过滤碳来将活性炭悬浮在150ml H 2 O 2水溶液中。