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Process for production of phosphoric acid by crystallization of phosphoric acid hemihydrate

机译:通过磷酸半水合物的结晶生产磷酸的方法

摘要

The invention relates to a process for producing simultaneously food-grade and fodder-grade phosphoric acid by crystallizing phosphoric acid hemihydrate, H3PO4×0.5H2O, from a prepurified feed acid, which is purified and crystallized with the help of the following steps,;a) after the step of froth-flotation of phosphate concentrate, the concentrate is directed to a strongly magnetic separation step in order to decrease the Mg ion amount,;b) the phosphate concentrate is leached in a mixture of sulfuric acid and phosphoric acid according to the wet process, the precipitated SO4 and As ions are removed, and a silicon source is added in order to adjust the F/Si molar ratio to 6,;c) the phosphoric acid is concentrated, the solids precipitate is removed, and the F ions are evaporated,;d) the feed acid obtained from step c, having a concentration of 58% P2O5, solids concentration of 0.05%, Mg ion concentration of 1.5%, SO4 ion concentration 1%, As ion concentration of 8 ppm and F ion concentration of 0.20%, is crystallized at a steady crystal growth rate of 10 &mgr;m/min, the temperature difference in the first crystallization being 17° C., and the crystals are washed with the undersaturated mother liquor of the subsequent recrystallization step,;e) the phosphoric acid crystallized in step d is melted, is diluted to a concentration of 63% P2O5, seed crystals are added, and crystallization is carried out as in step d, the temperature difference being 8° C., and the crystals are washed with an undersaturated solution of phosphoric acid, and;f) optionally the phosphoric acid crystallized in step e is melted, is diluted to a concentration of 63% P2O5, seed crystals are added, and crystallization is carried out as in step d, the temperature difference being 6° C., and the crystals are washed with an undersaturated washing solution prepared from product crystals.
机译:本发明涉及一种通过使半水合磷酸H 3 PO 4 ×0.5H 2同时结晶来生产食品级和饲料级磷酸的方法。 O,从预提纯的进料酸中提取,并通过以下步骤进行提纯和结晶; a)在磷酸盐精矿的泡沫浮选步骤之后,将精矿引入到强磁分离步骤中。为了降低Mg离子的含量,b)按照湿法将磷酸盐精矿浸入硫酸和磷酸的混合物中,除去沉淀的SO 4 和As离子,并添加硅源以将F / Si摩尔比调节至<6 ;; c)浓缩磷酸,除去固体沉淀物,并蒸发F离子; d)从步骤c获得的进料酸,P 2 O 5 的浓度> 58%,固体浓度<0.05%,镁离子浓度<1.5%, SO 4 离子浓度<1%,当离子浓度<8 ppm和F离子浓度<0.20%时,以稳定的晶体生长速率<10μm/ min结晶,温度第一次结晶的差异小于17°。结晶,然后用后续重结晶步骤的不饱和母液洗涤晶体; e)将步骤d中结晶的磷酸熔融,稀释至<63%P 2 的浓度O 5 ,加入晶种,并按照步骤d的步骤进行结晶,温度差为<8℃。结晶,并用磷酸的不饱和溶液洗涤;并且f)可选地,将步骤e中结晶的磷酸熔融,稀释至浓度<63%P 2 O 5 ,添加晶种,并与步骤d相同地进行结晶,温度差为<6℃。 ,然后用由产物晶体制备的不饱和洗涤溶液洗涤晶体。

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