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Application and Mechanism of Modified Sodium Silicate on Fluorite Ore Flotation

机译:改性硅酸钠在萤石矿浮选中的应用及机理

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A new type of depressant and a new process were used in floatation test of a high-carbonate and sludge content fluorite ore. Part of calcite and most of fluorite were separated with sludge by floating in the conventional conditions through a first step rougher, and then fluorite and calcite were separated by a second step rougher. First step rougher was carried out in alkaline pulp without any depressant to pull off most of the sludge and the second step rougher was carried in weak acid conditions with NSOH as depressant Several stage of cleaning flotation was also needed to obtain desirable concentrate. Desirable fluorite concentrate could be produced by a process of one stage grinding-two step rougher-two stage scavenging and five stage cleaning flotation. The content of CaF2 in concentrate is 95. 37% with a recovery of 76. 61%, and the content of CaCO3 in concentrate is 3.06%. Theoretical study showed that Si(OH)4 and SiO2(OH)42-were the main components which could depress calcite minerals in modified sodium silicate and the sequence of depress ability was SiO2(OH)42-> Si(OH)4 >HSiO3-. The depress ability was mainly due to different adsorption ability of Si(OH)4 and SiO2(OH)42-between different minerals. Those had strong adsorption ability could have a firm adsorption and much more adsorption capacity, thus could be easily depressed. Minerals that had no or less adsorption of Si (OH) 4 and SiO2 (OH)42~ were not easily depressed or could not be depressed. As the adsorption capacity of calcite to Si(OH)4 and SiO2(OH)42-was much more than that of fluorite, the sodium silicate could selectively depress calcite mineral. Modified sodium silicate could also selectively depress silicate minerals activated by Ca2+, Mg2+ ions.
机译:一种新型抑制剂和新工艺被用于高碳酸盐和污泥含量萤石矿的浮选试验中。在常规条件下通过第一步粗选机浮选,将部分方解石和大部分萤石与污泥分离,然后通过第二步粗选机将萤石和方解石分离。第一步粗选在碱性纸浆中进行,没有任何抑制剂,以除去大部分污泥,第二步粗选在弱酸性条件下,以NSOH作为抑制剂进行。还需要进行数步浮选以获得理想的浓缩物。理想的萤石精矿可以通过一阶段研磨-两步粗制-两阶段清除和五阶段清洁浮选的方法来生产。精矿中CaF2含量为95. 37%,回收率为76. 61%,精矿中CaCO3含量为3.06%。理论研究表明,Si(OH)4和SiO2(OH)42-是压抑改性硅酸钠中方解石矿物的主要成分,其压抑能力顺序为SiO2(OH)42-> Si(OH)4> HSiO3 -抑制能力的提高主要是由于不同矿物之间Si(OH)4和SiO2(OH)42的吸附能力不同。具有强吸附能力的那些可以具有牢固的吸附和更多的吸附能力,因此容易被压低。没有或几乎没有吸附Si(OH)4和SiO2(OH)42〜的矿物。由于方解石对Si(OH)4和SiO2(OH)42的吸附能力远大于萤石,硅酸钠可以选择性地抑制方解石矿物。改性硅酸钠还可以选择性地抑制被Ca2 +,Mg2 +离子活化的硅酸盐矿物。

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