Abstract:
PURPOSE: Provided is a simplified method for preparing an amorphous strontium titanate precursor, from which strontium titanate ultrafine spherical particles having uniform Sr-Ti bonds and a narrow particle size distribution are obtained. CONSTITUTION: The method for preparing an amorphous strontium titanate(SrTiO3) precursor comprises: dissolving 1 mol of strontium nitrate(Sr(NO3)2) and 9-20 mol of urea(CO(NH2)2) into the least amount of water to form a mixed solution A; mixing 1 mol of titanium tetrachloride(TiCl4) with 4-6 mol of nitric acid(HNO3) and heating the mixture to form a mixed solution B; mixing the mixed solution A with the mixed solution B and carrying out the combustion of the resultant mixture at a furnace maintained at a temperature of 380-450 deg.C.
Abstract:
PURPOSE: A negative electrode solution of a two-pack type reagent for the Karl-Fisher coulometric titration and a two-pack type reagent containing the negative electrode solution for the determination of moisture content are provided, to reduce the manufacturing cost by employing choline chloride instead of expensive diethanolamine·HCl at a negative electrode solution. CONSTITUTION: The negative electrode solution comprises 1.5-3 mol of imidazole; 13.5-25.0 g of iodine; 63-66.5 g of choline chloride; about 1-2 mol of dry sulfurous acid gas; and the balance volume of a solvent per 1,000 mL of the total volume. Preferably the solvent is methanol. The two-pack type reagent comprises 3-5 vol% of a positive electrode solution; and 100 vol% of the negative electrode solution. Preferably the positive electrode solution comprises 100-105 g of imidazole; 13-15 g of iodine; about 1-2 mol of dry sulfurous acid gas; and the balance volume of a solvent per 500 mL of the total volume. Preferably the solvent is methanol.
Abstract:
PURPOSE: A method for manufacturing high purity spherical silica for chromatography is provided to control a surface, an air gap volume, and an air gap diameter. CONSTITUTION: An emulsion is formed by stirring an emulsifying agent of 1 to 20 weight, sodium silicate of 100 weight, and organic solvent of 50 to 200 weight(S1). Silica dispersion solutions are formed by reacting the emulsion with the reactive materials in aqueous solvents at 20 to 80 degrees centigrade for 5 to 40 hours(S2). Silica particles are obtained by neutralizing and filtering silica dispersion solutions(S3). Metal ions are removed from the silica particles by processing silica particles with acid(S4). High purity spherical silica particles are obtained by cleaning and drying the silica particles processed with acid(S5).
Abstract:
Provided is a process for preparing zinc oxide powder with uniform particle size through a single-step of surface treatment and the preparation of zinc oxide, to thereby simplify the overall process. The process for preparing zinc oxide powder comprises the steps of: mixing 5-10wt.% silicon group surface treatment agent and 0.5-1.5wt% of binder in presence of 100wt.% of an organic solvent, and blending the resulting solution with 300-700wt% acidic solution; neutralizing, at 10-20 deg.C, the acidic mixture by slowly adding an alkaline solution at speed of 0.5-1.0wt.%/min with respect to a total quantity of the alkaline solution to be added; and performing a hydrothermal process at 80-100deg.C for 20-30 hours. The alkaline solution is used at an amount of 500-1000wt.% of 100wt.% of the organic solvent.
Abstract:
Provided are a manganese oxide prepared by using coprecipitation, its preparation method, a spinel type positive electrode active material for a lithium secondary battery which is high in structural stability at a high temperature and is improved in volume energy density, and its preparation method. The manganese oxide comprises Mn3O4 prepared by coprecipitation and is a monodisperse spherical powder. Preferably the manganese oxide has a particle size of 5-15 micrometers and a tap density of 2.5 g/cc or more. The spinel type positive electrode active material has a composition represented by Li_(1+alpha)[Mn_(2-alpha)]O4, wherein 0
Abstract translation:本发明提供一种通过共沉淀法制备的氧化锰及其制备方法,其具有高温结构稳定性和体积能量密度提高的锂二次电池用尖晶石型正极活性物质及其制备方法。 锰氧化物包含通过共沉淀制备的Mn 3 O 4,并且是单分散球形粉末。 优选地,氧化锰的粒度为5-15微米,振实密度为2.5g / cc以上。 尖晶石型正极活性物质具有由Li_(1 +α)[Mn_(2-α)] O4表示的组成,其中0≤α≤0.15。 此外,尖晶石型正极活性物质具有由Li_(1+α)[Mn_(2-α)] O_(4-z)F_z表示的组成,其中0≤α≤0.15; 和0.01 <= z <= 0.15。
Abstract:
PURPOSE: A one liquid type reagent for the titration of Karl-Fisher electricity quantity is provided, to improve the precision and the reproducibility for allowing the content of moisture in a sample to be measured conveniently. CONSTITUTION: The one liquid type reagent comprises about 3 mol of imidazole, about 60 g of iodine, about 0.5 mol of an amine, about 3 mol of dry sulfurous acid gas and a small amount of a stabilizer in 1,000 ml of a solvent. Preferably the solvent is methanol, chloroform or an alcohol-based compound; the amine is imidazole or diethanolamine; and the stabilizer carbon dioxide gas. Also the one liquid type reagent comprises about 150 g of trimethylene-dipiperidine, about 55 g of iodine, about 1.2 mol of an amine, about 3 mol of dry sulfurous acid gas, about 1.5 mol of polypropylene carbonate, about 121 g of choline chloride and a small amount of a stabilizer in 1,000 ml of a solvent. Preferably the solvent is methanol, chloroform or an alcohol-based compound; the amine is imidazole, ethanolamine, morpholine or guanidine; and the stabilizer carbon dioxide gas.
Abstract:
A manganese complex oxide using a co-precipitation method is provided to ensure a uniform particle size distribution, an excellent life characteristic, and high volumetric energy density. A method for preparing manganese complex oxides using a co-precipitation method includes the steps of: (a) charging distilled water and an aqueous ammonia solution into a co-precipitation reactor, and introducing air into the reactor to stir the materials; (b) charging an aqueous solution of a manganese transition metal compound comprising a manganese salt and a transition metal salt in a molar ratio of 1:1 to 4:1, an aqueous ammonia solution as a complexing agent, and an aqueous alkaline solution as a pH controller into the reactor sequentially, and mixing the admixture to form manganese composite hydroxides; and (c) introducing air into the reactor and oxidizing the manganese composite hydroxides to obtain manganese composite oxides[Mn_(1-x)M_x]_3O_4(wherein, 0.2