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    • 1. 发明授权
    • Magnesium hydroxide and process for production thereof
    • 氢氧化镁及其生产方法
    • US5476642A
    • 1995-12-19
    • US247784
    • 1994-05-23
    • Pavol SkublaStefan BezakLadislav LencsesEve Kukova
    • Pavol SkublaStefan BezakLadislav LencsesEve Kukova
    • C01F5/14C01F5/20C08K3/22
    • B82Y30/00C01F5/14C01F5/20C08K3/22C01P2002/60C01P2004/54C01P2004/61C01P2004/64C01P2006/12C01P2006/90C08K2201/016
    • Magnesium hydroxide of the formula Mg(OH).sub.2 having a crystallite size in the direction greater than 150 .ANG. and smaller than 500 .ANG., an aspect ratio in the range from 2 to 5, a strain in the direction not greater than 4.2.times.10.sup.-3 and a strain in the direction not greater than 3.0.times.10.sup.-3. 50% of secondary particles with diameters smaller than 1.4 .mu.m and 100% of secondary particles with diameters not greater than 4.0 .mu.m, and a specific surface, determined by the BET method, smaller than 25 m.sup.2 /g. It is prepared by a two-step procedure; in the first step, magnesium nitrate is treated by an alkaline substance, preferably by ammonia, in an aqueous medium, with 1.5 to 6.0-multiple excess of ammonia, at a temperature of not more than 85.degree. C., at the atmospheric pressure, causing that basic magnesium nitrate is formed which, in the second step, decomposes at a temperature of 110.degree. to 150.degree. C. and at a pressure not greater than 1.5 MPa. It is profitable to use 3.0 to 5.0-multiple excess of ammonia at a temperature of 50.degree. to 75.degree. C. and to decompose the nitrate at a temperature of 120.degree. to 130.degree. C. at a pressure of 0.3 to 1.3 MPa.
    • 方向大小为150以上且小于500的微晶尺寸的Mg(OH)2的氢氧化镁,纵横比在2至5之间,方向不是 大于4.2×10 -3,方向<110>的应变不大于3.0×10 -3。 50%的直径小于1.4μm的二次粒子和100%的直径不大于4.0μm的二次粒子,通过BET法测定的比表面积小于25m 2 / g。 它是通过两步法制备的; 在第一步骤中,在大气压下,在不高于85℃的温度下,在含水介质中,用1.5〜6.0倍多的氨处理硝酸镁,优选用氨水, 导致形成碱性硝酸镁,其在第二步中在110℃至150℃的温度和不高于1.5MPa的压力下分解。 在50〜75℃的温度下使用3.0〜5.0倍的氨,在0.3〜1.3MPa的压力下,在120〜130℃的温度下分解硝酸盐是有利可图的。