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金属矿山 ›› 2014, Vol. 43 ›› Issue (08): 69-73.

• 矿物工程 • 上一篇    下一篇

陕西五洲矿业石煤提钒降耗减排工艺研究

危青1,李桂英1,戴子林1,孔振兴1,汪虎2   

  1. 1.广州有色金属研究院,广东 广州 510651;2.陕西五洲矿业股份有限公司,陕西 商洛 711400
  • 出版日期:2014-08-15 发布日期:2015-03-31

Vanadium Extraction & Consumption and Emission Reduction Process of Stone Coal in Shaanxi Wuzhou Mining Co.,Ltd.

Wei Qing1,Li Guiying1,Dai Zilin1,Kong Zhenxing1,Wang Hu2   

  1. 1.Guangzhou Research Institute of Nonferrous Metals,Guangzhou 510651,China;2.Shaanxi Wuzhou Mining Co.,Ltd.,Shangluo 711400,China
  • Online:2014-08-15 Published:2015-03-31

摘要: 针对陕西五洲矿业股份有限公司在石煤全湿法硫酸提钒生产过程中存在的浸出用硫酸、浸出液中和用石灰、生产用水消耗高,尾渣排放量大等问题,开展了浸出余酸随浸出液返回利用的实验室试验和工业试验。实验室试验考察了余酸返回后V2O5在浸出液中的积累情况对浸出效果的影响,并比较了余酸返回和余酸不返回时浸出液中和所消耗的石灰量以及中和后滤渣的产生量。工业试验根据实验室结果,采取浸出液V2O5浓度在8~18 g/L时将浸出液补加适量新硫酸返回利用、浸出液V2O5浓度超过18 g/L时停止返回而全部使用新硫酸、待浸出液V2O5浓度重新降到8 g/L时再开始返回的办法,使得浸出—中和环节硫酸、石灰、生产用水的消耗量及中和后滤渣的产生量分别降低了22.1%、16.3%、71.4%、15.3%,从而显示出余酸回用技术具有显著的降耗减排效果。

关键词: 石煤, 酸浸提钒, 余酸返回, 降耗减排

Abstract: On account of the shortcomings of high consumption of sulfuric acid for leaching, lime for neutralizing leaching solution and water during the process, as well as large emission of tailing, both laboratory and pilot experiment are conducted on returning and reuse of residual acid by adding to solution. Effect of the accumulation of V2O5 in leaching solution on leaching efficiency after residue acid returning in laboratory scale is investigated. Lime consumption for neutralization and the output of filter residual before and after neutralization on residual acid returning is compared. Pilot experiment is based on laboratory experiment. Appropriate fresh sulfuric acid and the returning acid are added into solution when V2O5 concentration is 8~18 g/L, only fresh acid is used when V2O5 concentration is above 18 g/L, and only returning acid when the V2O5 concentration is less than 8 g/L. By this method, consumption of sulfuric acid, lime and water during leaching-neutralization process are decreased by 22.1%, 16.3%, 71.4% respectively, also the residual solution output decreased by 15.3%, which indicates that the residual acid returning technology can significantly lower the consumption and emission.

Key words: Stone coal, Vanadium extraction by acidic leaching, Residual acid returning, Consumption and emission reduction