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Continuous prodn. of dust free anhydrous aluminium fluoride - by predrying and precalcining, removing fines and final drying and calcination

机译:连续产品无尘无水氟化铝-通过预干燥和预煅烧,除去细料,最后干燥和煅烧

摘要

In the continuous multistage prodn. of dust-free AlF3 (I) from its hydrates (II), esp. AlF3.3H2O (IIA), by drying and calcination, (II) is predried and/or precalcined, freed from fines and completely dehydrated and calcined in an (indirectly heated) rotary calciner. If a disc drier is used in the first stage, the fines are sepd. by air sepn. and deposition on a cloth filter. With a flow drier, a cyclone and cloth filter are employed for sepn. The hydrate obtd. by precalcination in the first stage is in the AlF3.3H2O to AlF3.O.3H2O range. The size of the fines sepd. is max. 60 (max. 40) microns and the particle size distribution of the end prod. varied accordingly. Dehydration is completed at a temp. gradient rising continuously to the calcination temp. of 500-600 deg.C within a time span of up to 45 min. The fines are granulated in an intensive mixer with metastable AlF3 soln. with a concn. of 5 to max. 30 (10-15) wt.% and completely dehydrated and calcined as above, pref. after mixing with the prod. freed from fines. The formation of deposits retarding heat transfer on the walls of the calciner is prevented. A purer prod. is obtd. by sepn. of the fines, which include a considerable amt. of SiO2, which is desirable for (I) used in Al mfr. by electrolysis of a (I) melt.
机译:在连续多级产品中。从其水合物(II)中分离出无尘的AlF3(I),尤其是通过干燥和煅烧AlF3.3H2O(IIA)(II),将其预干燥和/或预煅烧,除去细粉,然后完全脱水并在(间接加热的)旋转煅烧炉中煅烧。如果在第一阶段使用圆盘干燥机,则会罚款。通过空气隔垫。并沉积在滤布上。使用流动干燥器时,旋风除尘器和滤布用于隔垫。水合物过大。在第一阶段中通过预煅烧得到的AlF3.3H2O为AlF3.O.3H2O。罚款的数额sepd。是最大。 60(最大40)微米和最终产品的粒度分布。相应地变化。脱水在一定温度下完成。梯度不断上升到煅烧温度。在长达45分钟的时间范围内达到500-600摄氏度。将细粉在带有亚稳态AlF3溶液的强力混合器中制粒。与concn。 5至最大30(10-15)wt。%并按上述方法完全脱水和煅烧。与产品混合后。免于罚款。防止了在煅烧炉壁上形成阻碍传热的沉积物。纯粹的产品。很笨。九月罚款,其中包括相当大的罚款。 SiO 2,对于Al mfr中使用的(I)是理想的。 (I)熔体的电解。

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