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METHOD OF PRODUCING MANGANESE (II) FUMARATE FROM MANGANESE METAL AND MANGANESE (III) OXIDE

机译:由锰酸金属和氧化锰(III)生产富马酸锰(II)的方法

摘要

FIELD: chemistry.;SUBSTANCE: invention relates to an improved method of producing manganese (II) fumarate from manganese metal and its oxide (III) through direct reaction of the metal and its oxide Mn2O3 with an acid in the presence of a liquid phase and a stimulating iodine additive in a vertical type bead mill with glass beads as grinding agent. The metal and its oxide are loaded in molar ratio (2±0.1):1 in total amount of 7.87 to 10.93% of the mass of the load. Acid is added with 15 to 25% excess of the calculated value, equal to the number of moles of metal and twice the number of moles of metal oxide in the load. The base of the liquid phase is isoamyl alcohol, in which the iodine stimulating additive is dissolved in amount of 0.02 to 0.05 mol/kg. Glass beads are loaded first, in mass ratio to the reaction mixture of 1.35:1, and then later the liquid phase solvent, acid and stimulating additive, and after brief stirring, metal oxide and metal, stirring all the while. Taking this moment as the beginning of the process, forced cooling is introduced right away. Operating temperature is stabilised in the range 33 to 45°C and in this mode, the process is carried out until virtually quantitative conversion of metal and its oxide to the target salt, after which stirring and forced cooling are stopped. The reaction mixture is separated from the glass beads, cooled to temperature 5 to 6°C and kept at that temperature for 1 to 2 hours. The solid phase of the target salt is filtered off and washed with isoamyl on a filter cooled to approximately the same temperature, after which it is taken for purification by recrystallisation. The filtrate and the cleaning solvent, containing excess acid, the bulk of the stimulating additive and a certain amount of dissolved target salt, are returned for loading in the repeated process. The process is carried out in light temperature conditions. The target substance can be easily separated.;EFFECT: design of a low-waste method, which allows for obtaining target product from available manganese oxide with an easy to implement process.;9 ex
机译:发明领域本发明涉及一种通过锰金属及其氧化物Mn 2 O 刺激碘。金属及其氧化物以摩尔比(2±0.1)∶1负载,其总量为负载质量的7.87至10.93%。添加的酸超出计算值的15%到25%,这等于负载中金属的摩尔数和金属氧化物的摩尔数的两倍。液相的碱是异戊醇,其中碘刺激添加剂以0.02至0.05mol / kg的量溶解。首先将玻璃珠按质量比加载至1.35:1的反应混合物中,然后加载液相溶剂,酸和刺激性添加剂,并在短暂搅拌后将金属氧化物和金属搅拌,一直搅拌。以这一刻作为过程的开始,立即引入了强制冷却。工作温度稳定在33至45°C的范围内,在这种模式下,过程进行到金属和其氧化物几乎定量转化为目标盐为止,然后停止搅拌和强制冷却。将反应混合物与玻璃珠分离,冷却至5至6℃的温度,并在该温度下保持1至2小时。滤出目标盐的固相,并在冷却至大约相同温度的过滤器上用异戊基洗涤,然后将其用于重结晶纯化。将包含过量酸,大量刺激性添加剂和一定量的溶解目标盐的滤液和清洁溶剂返回以供重复过程中加载。该过程在光照温度条件下进行。目标物质易于分离。效果:一种低浪费方法的设计,该方法可通过易于实施的方法从可用的氧化锰中获得目标产品。9ex

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