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Alkaline Metal Cyanide Granules and Alkaline Metal Cyanide Granules Manufacturing Method and High Purity Alkali Metal Cyanide Granules Obtained by the Method

机译:碱金属氰化物颗粒和碱金属氰化物颗粒的制造方法以及通过该方法获得的高纯度碱金属氰化物颗粒

摘要

Preparation of alkali or alkaline earth metal cyanide granules involves spraying an aqueous alkali metal hydroxide solution or an aqueous alkaline earth metal hydroxide suspension onto a fluidised product seed bed at 100-250 degrees C in a fluidised bed spray granulation reactor which is supplied with a hydrogen cyanide-containing gas in amount 1 mol HCN per metal equivalent, the introduced and formed water being evaporated by the fluidising gas supplied at 110-500 degrees C. Also claimed are sodium or potassium cyanide granules having a spherical particle shape with a smooth or raspberry-like surface structure, 0.1-20 mm particle diameter for 99 wt.% of the granules, 600 g/dm3 bulk density, less than 1 wt.% wear measured by the roller wear test (Erwaka TAR wear tester, 20 g sample, 60 minutes, 20 rpm.) and a clumping index of NOTGREATER 4 (measured by 14 day 10g load application onto a 100 g sample in a 5.5 cm inside diameter cylinder), the novelty being that the alkali metal carbonate content is less than 0.5 wt.% and the alkali metal formate content is less than 0.3 wt.%, the alkali metal in these by-products being the same as that in the cyanide. Preferably, the total alkali metal carbonate and alkali metal formate content is less than 0.4 wt.% and the granules are prepared by the above process using reaction gas from a BMA process and superheated steam as fluidising gas.
机译:碱金属或碱土金属氰化物颗粒的制备涉及在流化床喷雾制粒反应器中将碱金属氢氧化物水溶液或碱土金属氢氧化物水溶液悬浮液在流化床喷雾制粒反应器中于100-250摄氏度下喷雾到流化产物种子床上每金属当量1 mol HCN的含氰化物气体,引入的水和形成的水由在110-500摄氏度下供应的流化气体蒸发。还要求保护的是球形或氰基球形的氰化钠或钾氰化钠颗粒状表面结构,颗粒重量的99%(重量)为0.1-20毫米,堆积密度为600 g / dm 3,通过辊子磨损试验(Erwaka TAR磨损测试仪,20磨损小于1%) g样品,在60分钟内,以20 rpm的转速旋转。)的结块指数为NOTGREATER 4(通过在直径为5.5 cm的圆筒中对100 g样品施加14天10g载荷来测量),新颖之处在于碱金属约碳酸氢根含量小于0.5重量%,碱金属甲酸盐含量小于0.3重量%,这些副产物中的碱金属与氰化物中的碱金属相同。优选地,碱金属碳酸盐和碱金属甲酸盐的总含量小于0.4重量%,并且颗粒通过上述方法使用来自BMA方法的反应气体和过热蒸汽作为流化气体来制备。

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