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    • 1. 发明公开
    • 붕소 제거를 위한 마그네슘-알루미늄 이금속산화물의 제조방법
    • 制备用于去除硼的MG-AL二元氧化物的方法
    • KR1020130074404A
    • 2013-07-04
    • KR1020110142461
    • 2011-12-26
    • 재단법인 포항산업과학연구원
    • 문정기곽명화윤영기
    • C04B35/581C02F1/28C04B35/64
    • C04B35/58C02F1/281C04B35/64C04B2235/3852
    • PURPOSE: A manufacturing method of magnesium-aluminum bimetallic oxide for removing boron is provided to use an optimal ratio of magnesium nitrate and aluminium nitrate, thereby synthesizing Mg-Al bimetallic oxide with high de-boronation efficiency. CONSTITUTION: A manufacturing method of magnesium-aluminum bimetallic oxide for removing boron comprises following steps. (i) The caustic soda is added in the mixture of aluminium nitrate and magnesium nitrate. The mixture is heated and dried. Precipitation is obtained. And (ii) the precipitate is baked. The molar ratio of the aluminium nitrate and magnesium nitrate is 2:1. The temperature of the baking step is 60 to 400°C. [Reference numerals] (AA) 0.1M Mg(NO3)2 + 0.05M AI(NO3)3 fluid; (BB) Heating at 45°C; (CC) Curing for two hours at 85°C; (DD) Centrifugation/ cleaning; (EE) Drying; (FF) Calcinating
    • 目的:提供用于除去硼的镁 - 铝双金属氧化物的制造方法,以使用硝酸镁和硝酸铝的最佳比例,从而合成具有高脱硼效率的Mg-Al双金属氧化物。 构成:用于除去硼的镁 - 铝双金属氧化物的制造方法包括以下步骤。 (i)将苛性钠加入到硝酸铝和硝酸镁的混合物中。 将混合物加热并干燥。 获得沉淀。 和(ii)沉淀物被烘烤。 硝酸铝和硝酸镁的摩尔比为2:1。 烘烤步骤的温度为60〜400℃。 (标号)(AA)0.1M Mg(NO 3)2 + 0.05M AI(NO 3)3流体; (BB)在45℃加热; (CC)在85℃下固化2小时; (DD)离心/清洗; (EE)干燥; (FF)煅烧
    • 2. 发明公开
    • 농축해수를 이용한 해수마그네시아 제조방법
    • 海水浓缩海水制造方法
    • KR1020130073500A
    • 2013-07-03
    • KR1020110141377
    • 2011-12-23
    • 재단법인 포항산업과학연구원
    • 문정기윤영기곽명화
    • C01F5/02C01F5/14B01D21/02
    • C01F5/08B01D21/02C01F5/22
    • PURPOSE: A producing method of seawater magnesia using concentrated seawater is provided to produce seawater magnesia with high productivity and simple processes by using a solid-liquid separator and the concentrated seawater obtained from a seawater desalination process. CONSTITUTION: A producing method of seawater magnesia using concentrated seawater comprises the following steps: decarbonating the concentrated seawater obtained from a seawater desalination process; precipitating magnesium hydroxide by adding a precipitation agent to supernatant of the decarbonated concentrated seawater; separating and filtering magnesium hydroxide from the supernatant using a solid-liquid separator; and plasticizing the separated magnesium hydroxide. The seawater desalination process is a reverse osmotic pressure type seawater desalination process. The precipitation agent is one or more selected from Ca (OH)2 or NaOH. The producing method of seawater magnesia processes the supernatant without magnesium hydroxide with a nanofilter into concentrated water and processed water. [Reference numerals] (AA) Seawater; (BB) Pre/preprocess; (CC) Product water; (DD) Corrosiveness; (EE) Concentrate; (FF) Decarbonation; (GG) Precipitation; (HH,KK) Supernatant; (II) Ca (OH)_2 injection; (JJ) Separation (decanter); (LL) Processed water; (MM) Discharging; (NN) Plasticity
    • 目的:提供一种使用浓缩海水的海水氧化镁的生产方法,通过使用固体 - 液体分离器和从海水淡化过程获得的浓缩海水,以高生产率和简单的工艺生产海水氧化镁。 构成:使用浓缩海水的海水氧化镁的生产方法包括以下步骤:从海水淡化过程中获得的浓缩海水脱碳; 通过向脱碳酸浓缩海水的上清液中加入沉淀剂沉淀氢氧化镁; 使用固液分离器从上清液中分离和过滤氢氧化镁; 并分离氢氧化镁。 海水淡化过程是反渗透压型海水淡化过程。 沉淀剂是选自Ca(OH)2或NaOH中的一种或多种。 海水氧化镁的生产方法将不含氢氧化镁的上清液用纳滤膜加工成浓缩水和加工水。 (附图标记)(AA)海水; (BB)预处理/预处理; (CC)产品水; (DD)腐蚀性; (EE)浓缩液; (FF)脱碳; (GG)降水; (HH,KK)上清液; (II)Ca(OH)_2注射液; (JJ)分离(滗析器); (LL)加工水; (MM)放电; (NN)可塑性