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METHOD OF PRODUCING MAGNESIA OF DESIRED COMPOSITION FROM NATIVE MAGNESITE
METHOD OF PRODUCING MAGNESIA OF DESIRED COMPOSITION FROM NATIVE MAGNESITE
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机译:由天然菱镁矿生产所需组成的镁砂的方法
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摘要
Technical magnesia is manufactured by caustic calcination of a magnesite of suitable SiO 2 and Al 2 O 3 content and subjecting it to the action of hydrogen chloride gas, in the absence of combustible or reducible gases, at a temperature between 800 and 1100 C., iron and manganese being converted to volatile chlorides, whilst calcium is converted to its chloride which remains in the material to give an intermediate product which by a post-treatment of the residual chlorides is converted to technical magnesia of the desired final composition and at least a part of the hydrogen chloride used is recovered from the volatile chlorides. Products of the process which are practically free from iron and manganese may be (a) more than 97% by weight MgO with SiO 2 and CaO, (b) more than 94% by weight MgO with CaO and SiO 2 less than 5% by weight in a weight ratio either greater than 2 to 1 or less than 1 to 1 respectively. The CaO and SiO 2 content is preferably less than 4% by weight. The post-treatment comprises an oxidation of the residual chlorides by means of steam. The amount of calcium in the product may be regulated by leaching out a part or all of the calcium chloride present prior to the steam oxidation. The recovery of hydrogen chloride is carried out using known methods.
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机译:工业氧化镁是通过在800至1100℃之间的温度下,对合适的SiO 2和Al 2 O 3含量的菱镁矿进行苛性煅烧,然后在不存在可燃或可还原气体的情况下,使其经受氯化氢气体的作用而制得的,铁和锰转化为挥发性氯化物,而钙转化为残留在材料中的氯化物,得到一种中间产物,该产物通过对残留氯化物的后处理转化为所需最终成分的工业镁砂,至少从挥发性氯化物中回收部分使用的氯化氢。该方法的实际上不含铁和锰的产物可以是(a)大于97重量%的MgO与SiO 2和CaO,(b)大于94重量%的MgO,具有CaO和SiO 2小于5重量%。重量比分别大于2比1或小于1比1。 CaO和SiO 2的含量优选小于4重量%。后处理包括借助于蒸汽氧化残留的氯化物。可以通过在蒸汽氧化之前浸出存在的部分或全部氯化钙来调节产品中钙的量。氯化氢的回收使用已知方法进行。
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