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Arsenic and antimony extraction from high arsenic smelter ash with alkaline pressure oxidative leaching followed by Na2S leaching

机译:高砷冶炼灰砷和锑萃取具有碱性压力氧化浸出,然后是Na2S浸出

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摘要

In this study, a combined process of alkaline pressure oxidative leaching (APOL) and Na2S leaching was proposed to extract arsenic and antimony from high arsenic smelter ash. The arsenic was selectively dissolved into the leachate during APOL, while the antimony was separated into the residue as insoluble NaSb(OH)(6). The effects of different process parameters on the extraction of arsenic and antimony were investigated based on thermodynamic calculation. The results indicated that the extraction of arsenic was as high as 96% after APOL process under the conditions: 2 mol/L of NaOH concentration, 95 degrees C of leaching temperature, 90 min of leaching time, 1.5 MPa of oxygen partial pressure, 10:1 of liquid-to-solid ratio. The NaSb(OH)(6) generated after APOL could be converted to Na3SbS4 center dot 10H(2)O and thus was leached out by Na2S leaching. The optimum conditions were established as: 2.75 mol/L of Na2S concentration, 95 degrees C of leaching temperature, 120 min of leaching time and 10:1 of liquid-to-solid ratio, under which the extraction of antimony was as high as 97.01%. A series of tests indicated that the leaching toxicity of the leaching residue met the Chinese identification standards.
机译:在该研究中,提出了碱性压力氧化浸出(APOL)和Na2S浸出的组合过程,从高砷涂料灰烬中提取砷和锑。将砷选择性地溶解在APOL期间的浸出物中,同时将锑分离成残余物作为不溶性NASB(OH)(6)。基于热力学计算,研究了不同工艺参数对砷和锑提取的影响。结果表明,砷的提取高达96%,在乙醇过程中的条件下:2 mol / l NaOH浓度,浸出温度为95℃,浸出时间90分钟,氧分压为1.5MPa,10 :1液体至固体比例。在APOL之后产生的NASB(OH)(6)可以转换为NA3SBS4中心点10H(2)o,因此通过NA2S浸出浸出。确定最佳条件为:2.75mol / L的Na 2 S浓度,浸出温度为95℃,浸出时间120分钟,液体与固体比例为10:1,锑的提取高达97.01 %。一系列测试表明浸出残留物的浸出毒性达到了中国鉴定标准。

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