某高镁低品位软锰矿锰镁分离试验

高镁低品位软锰矿石传统的锰镁分离工艺均存在污染严重、锰镁离子分离效率低等问题。为了实现高镁低品位软锰矿的高效、低污染开发利用,以广西某高镁低品位软锰矿为原料,对采用酸化还原焙烧+尾气(SO2)还原软锰矿矿浆—还原产物合并浸出—浸出液除杂工艺制得的高纯Mn SO4与Mg SO4混合溶液,进行了NH4HCO3沉Mn2+(锰镁高效分离)工艺条件研究。结果表明,在NH4HCO3与Mn SO4物质的量之比为2.25,反应时间为60 min,反应温度为30℃,搅拌速度为120 r/min情况下,锰镁分离率可达96.96%。该锰镁分离工艺既解决了酸化还原焙烧尾气(SO2)的高效回收利用问题,又高效地实现了浸出液中锰镁离子的分离。

High Efficient Separation and Recycling of Mg and Mn for a Rich Magnesia Low-grade Pyrolusite

The traditional separation process to treat the rich magnesia low-grade pyrolusite usually results in such problems as worse pollution and lower efficiency in separation of manganese and magnesia.In order to solve these problems and achieve development and utilization of high magnesium low-grade pyrolusite,and taking a rich magnesium low grade pyrolusite in Guangxi as raw material,mix solution of high pure MnSO₄ and MgSO₄ prepared by the process of acidizing reduction roasting +reduction of pyrolusite pulp by tail gas (SO₂)-combined leaching of reduction products-impurity removal from leaching solution was adopted to make conditioning tests for Mn2+ concentration by NH₄HCO₃.The results showed that with mole ratio of NH₄HCO₃ and MnSO₄ as 2.25,the reaction time for 60 min,the reaction temperature at 30 ℃,and stirring speed of 120 r/min,separation rate of magnesium and manganese reached 96.96%.The Mn-Mg separation process not only achieve comprehensive utilization of tail gas (SO₂) from acidizing reduction roasting,but also effectively separates from manganese and magnesia in leaching solution.