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A pilot-scale study of cryolite precipitation from high fluoride-containing wastewater in a reaction-separation integrated reactor

机译:反应分离综合反应器中高含氟废水中冰晶石沉淀的中试研究

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摘要

Fluoride removal by traditional precipitation generates huge amounts of a water-rich sludge with low quality, which has no commercial or industrial value. The present study evaluated the feasibility of recovering fluoride as low water content cryolite from industrial fluoride-containing wastewater. A novel pilot-scale reaction-separation integrated reactor was designed. The results showed that the seed retention time in the reactor was prolonged to strengthen the induced crystallization process. The particle size of cryolite increased with increasing seed retention time, which decreased the water content. The recovery rate of cryolite was above 75% under an influent fluoride concentration of 3500 mg/L, a reaction temperature of 50℃, and an influent flow of 40 L/hr. The cryolite products that precipitated from the reactor were small in volume, large in particle size, low in water content, high in crystal purity, and recyclable.
机译:传统沉淀法去除氟化物会产生大量低质量的富水污泥,没有商业或工业价值。本研究评估了从工业含氟废水中回收低水冰晶石作为氟化物的可行性。设计了新型中试规模的反应分离集成反应器。结果表明,延长了种子在反应器中的停留时间,以增强诱导的结晶过程。冰晶石的粒径随着种子保留时间的增加而增加,从而降低了水分含量。在进水氟化物浓度为3500 mg / L,反应温度为50℃,进水流量为40 L / hr的条件下,冰晶石的回收率达到75%以上。从反应器中沉淀出来的冰晶石产物体积小,粒径大,水含量低,晶体纯度高并且可回收。

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