A method of processing zinc-containing raw ore with barium zincate synthesis route
A synthesis approach, barium zincate technology, applied in the direction of zinc compounds, chemical instruments and methods, process efficiency improvement, etc., can solve the problem of the inability to economically and effectively utilize low-grade zinc-containing raw ore, and the unreasonable utilization of low-grade zinc-containing raw ore. Satisfaction, the production of barium zincate and barium zincate, etc., to avoid the pressure of water treatment, avoid a large amount of co-precipitation of impurities, and achieve the effect of high recovery rate
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Embodiment 1
[0115] In a zinc mine in Yunnan, the zinc content is 5.6%, and the oxidation rate of the raw ore is 96.3%. The main form of zinc in this mine is zinc carbonate.
[0116] Get 300 grams of zinc-containing raw ore, put into 900 milliliters of ammonia-ammonium bicarbonate mixed solution (10% of total ammonia mass concentration, 3% of carbonate root mass concentration) and carry out stirring and leaching, the leaching temperature is normal temperature, and the stirring time is 2 hours, Then filter, the filtered liquid contains 1.632% zinc (calculated in zinc oxide equivalent), the mass concentration of carbonate in the liquid is 4.23%, and the increased part is brought in by zinc carbonate in the raw ore. According to the test data, the recovery rate of soluble zinc in the raw ore during the leaching process is 90.79%, and the recovery rate of total zinc is 87.43%.
[0117] Purify the zinc ammonia complex solution obtained by filtering.
[0118] Take 600 ml of zinc-ammonia complex...
Embodiment 2
[0121] In a zinc mine in Chongqing, the zinc content is 4.7%, and the oxidation rate of the raw ore is 95.52%. The main form of zinc in this mine is zinc silicate.
[0122] Get 300 grams of zinc-containing raw ore, put into 900 milliliters of ammonia-ammonium bicarbonate mixed solution (10% of total ammonia mass concentration, 3% of carbonate root mass concentration) and carry out stirring and leaching, the leaching temperature is normal temperature, and the stirring time is 2 hours, Then filter, the filtered liquid contains 1.367% zinc (calculated in zinc oxide equivalent), the mass concentration of carbonate in the liquid is 3.54%, and the increased part is brought in by zinc carbonate in the raw ore. According to the inspection data, the recovery rate of soluble zinc in the raw ore during the leaching process is 91.35%, and the recovery rate of total zinc is 87.26%.
[0123] Purify the zinc ammonia complex solution obtained by filtering.
[0124] Take 600 ml of zinc-ammoni...
Embodiment 3
[0127] The difference from Example 1 is that in Example 3, calcium oxide precipitated carbonate is added to the zinc-ammonia complex solution obtained by leaching and filtered, and 500 milliliters of the filtered liquid is taken, and 3 mg of dodecylbenzenesulfonate is added first. Sodium acid, then add 6.6 grams of barium oxide for the synthesis of barium zincate. All the other steps and reagent consumption of Example 3 are the same as in Example 1.
[0128] Sampling analysis was carried out on the obtained final product, and the content of barium zincate in the solid was checked to be 99.53%, and the average particle diameter was 54.1nm.
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