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Treatment of a highly-concentrated sulphate-rich synthetic wastewater using calcium hydroxide in a fluidised bed crystallizer

机译:在流化床结晶器中使用氢氧化钙处理高浓度的富含硫酸盐的合成废水

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This study aimed to investigate factors that affect the conversion of sulphates and magnesium, and the recovery of gypsum and magnesium hydroxide in the neutralization of a sulphate rich stream using calcium hydroxide, in a laboratory scale seeded fluidised bed crystallizer. Particular focus was on reducing the precipitated fines that escaped with the treated water, through the use of seeds, while removing as much sulphate-compounds from the waste stream as possible. The composition of the total sulphate salts was as follows: 80% magnesium sulphate, calcium sulphate remaining at its saturation concentration (1.5 g/L), with the remainder being sodium sulphate based on typical reverse osmosis retentate concentrations ranging from 1.5 - 120 g/L of total sulphate salts. The fluidised bed crystallizer, using silica seeds, was found to be effective at reducing the formation of gypsum and magnesium hydroxide fines by almost half. Feed concentrations of 35 g/L of total salts yielded better sulphate conversions (±75%), compared to a feed concentration of 8 g/L (±30%). It was possible to remove 99% of the magnesium in the saline wastewater stream using a calcium to sulphate ratio of 1:1 for feed concentrations of 15 g/L and higher. Excess calcium hydroxide suspension improved sulphate conversions.
机译:这项研究旨在调查在实验室规模的种子化流化床结晶器中,在利用氢氧化钙中和富含硫酸盐的物流中,影响硫酸盐和镁的转化以及石膏和氢氧化镁的回收率的因素。特别关注的是通过使用种子减少从处理过的水中逸出的沉淀细粉,同时从废物流中去除尽可能多的硫酸盐化合物。总硫酸盐的组成如下:80%的硫酸镁,硫酸钙以其饱和浓度(1.5 g / L)保留,其余是基于典型反渗透渗余物浓度为1.5-120 g / L的硫酸钠。 L总硫酸盐。发现使用二氧化硅晶种的流化床结晶器可有效减少石膏和氢氧化镁细粉的形成近一半。进料浓度为35 g / L的总盐产生的硫酸盐转化率更好(±75%),而进料浓度为8 g / L(±30%)。对于进料浓度为15 g / L或更高的溶液,使用钙与硫酸盐的比例为1:1时,可以去除盐水废水中99%的镁。过量的氢氧化钙悬浮液改善了硫酸盐转化率。

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