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Process for producing wet process phosphoric acid from phosphate rocks containing fluochlorapatite and related minerals

机译:由含氟氯磷灰石及相关矿物的磷矿生产湿法磷酸的方法

摘要

Phosphoric acid is produced by the wet process from phosphate rock containing fluochlorapatite. The rock is ground in a crusher (10) to a size such that from about 50% to about 90% by weight will be passed by a - 200 mesh U.S.S. sieve before being passed into a digestor (14) where it is mixed with sulfuric acid and recycled phosphoric acid to form a slurry. A suitable reductant such as sulphur dioxide is added to the slurry to maintain the oxidation-reduction potential in the range from about +150 mv to about +750 mv. The gypsum by-products are then removed from the slurry at filter (16) and a portion of the acid is recycled to digestor (14). The remaining acid is either concentrated and further processed to make fertilizers or is further processed via path (20) to remove aluminum and/or iron impurities. Select amounts of fluoride and sodium containing compounds are added to the acid in a stirred reactor (30) to cause precipitation of aluminum, principally as Na.sub.2 AlF.sub. 5. After about 15 to about 60 minutes of stirring at a temperature below about 70° C., the precipitate is removed at filter (32) where the acid is either processed to make fertilizer or subjected to additional processing to remove iron contaminants. Iron contaminants are removed from the filter acid or from aluminum removed acid from filter (32) by adding sufficient ammonia to the acid in a stirring reactor (40) to cause precipitation of iron principally as NH.sub.4 Fe.sub.2 H.sub.8 (PO.sub.4). sub.5.AH.sub.2 O, to reduce the level of iron to desired levels. After aging in the reactor from about 2 to about 24 hours at a temperature below the boiling point of the acid, the precipitate is removed at filter (42) and the resulting iron reduced acid is concentrated and subjected to conventional processing for making fertilizers.
机译:磷酸是通过湿法从含有氟氯磷灰石的磷酸盐岩中产生的。将岩石在破碎机(10)中研磨成一定大小,以使约50%至约90%的重量通过200目美国。在进入蒸煮器(14)之前先将其筛分,然后将其与硫酸和再循环的磷酸混合形成浆液。将合适的还原剂例如二氧化硫加入到浆料中,以将氧化还原电势维持在约+ 150mv至约+ 750mv的范围内。然后在过滤器(16)处从浆料中除去石膏副产物,并将一部分酸再循环至消化器(14)。剩余的酸被浓缩并进一步处理以制造肥料,或者经由路径(20)进一步处理以去除铝和/或铁杂质。在搅拌的反应器(30)中,将一定量的氟化物和含钠化合物加入到酸中,以引起铝的沉淀,主要是Na 2 AlF 3。 5.在低于约70℃的温度下搅拌约15至约60分钟之后,在过滤器(32)处除去沉淀物,在过滤器(32)处将酸加工成肥料或进行另外的加工以去除铁污染物。通过在搅拌反应器(40)中向酸中添加足够的氨,从过滤器酸或从过滤器(32)去除的铝酸中除去铁污染物,从而使铁主要以NH 4 Fe 2 H的形式沉淀出来。 sub.8(PO.sub.4)。 sub.5.AH.sub.2 O,以将铁含量降低至所需水平。在低于酸的沸点的温度下在反应器中老化约2至约24小时后,在过滤器(42)上除去沉淀物,并将所得的还原铁酸浓缩并进行常规的制造肥料的处理。

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