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Processing the Sb-Pb-Ag Alloy by the Distillation Method

机译:通过蒸馏法加工Sb-Pb-Ag合金

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The topicality of this work is due to the necessity of developing environmetally safe, highly efficient, and economical complex vacuum distillation technology for processing lead-containing middlings and wastes, in particular, the alloy fabricated when recovering the silicate slag of smelting copper-electrolyte slime (SPA) with the purpose of fabricating commerical monoelement concentrates of antimony, lead, and silver. Laboratory investigations into processing the SPA alloy and caclualtoins of temperature-composition (T-x) equlibrium phase diagrams (vapor-liquid equilibrium (VLE)) for analyzing the behavior of Sb-Pb and Pb-Ag binary alloys during processing; the preliminary selection of temperature and pressure in the system; and the separation efficiency of components under conditions of T = 900-2100 K, P = 1-133 Pa, and = 8-16 h are performed. The influence of temperature and pressure in the system; sublimation duration on the recovery completeness; and degree of separation of antimony, lead, and silver from the SPA alloy is investigated. When constructing equilibrium VLE phase diagrams, activity coefficients of binary alloys are calculated using the molecular volume interaction model (MVIM). Information is found on the influence of temperature and vacuum depth on the degree of sublimation and separation of metals from Sb-P and Pb-Ag formulations of various compositions. Saturated poar pressures are calculated for Sb (p* = 273.664-67436.9 Pa), Pb (0.149-485.9), and Ag (5.054 x 10(-5)-6.558) at T = 1073-1773 K. It is shown that high ratios = 1832.98-138.79, = 2948.16-74.09) and separation coefficients (log(Sb) = 2.099-3.33 and log(Pb) = 1.813-3.944) give the theoretical prerequisites for the selective isolation of these metals by vacuum distillations when antimony and lead are sequentially enriched in the gas phase ((Sb) > 1, (Pb) > 1), and for, silver, in the liquid phase. It is established that the molar fraction of poorly sublimable lead/silver in the gas phase y(Pb)/y(Ag) = (1.55-982) x 10(-3)/(36-772) x 10(-3) increases with an increase in temperature 894-1601/1399-2099 K, pressure 1.33-133 Pa, and metal content in alloy x(Pb)/x(Ag) = 0.9-0.9999/0.9-0.99. Activity coefficients for antimony (Sb) = 0.832-0.999, lead (Pb) = 0.474-1.0, and silver (Ag) = 0.331-0.999 for Sb/Pb and Pb/Ag alloys of the composition 0.1-0.9/0.9-0.1 in the temperature range under study are calculated using MIVM. The practical significance of revealed dependences of the amount and composition of sublimation products of polymetallic alloys on the mentioned process parameters is caused by the development of the principal processing technology of the SPA alloy by vacuum distillation.
机译:这项工作的主题是由于需要开发环境安全,高效,经济的复杂真空蒸馏技术,用于加工含铅的含量和废物,特别是在回收熔炼铜电解质粘液的硅酸盐渣时制造的合金(SPA)目的是制造锑,铅和银的商业单元素浓缩物。实验室研究加工温度 - 组合物(T-X)Qulibrium相图(蒸汽 - 液平衡(VLE))加工过程中Sb-Pb和Pb-Ag二元合金的行为的含水组合物(蒸汽平衡(VLE));系统中温度和压力的初步选择;在T = 900-2100k,p = 1-133Pa和= 8-16h条件下,组分的分离效率。温度和压力在系统中的影响;升华持续时间恢复完整性;研究了来自水疗合金的锑,铅和银的分离程度。当构建平衡VLE相图时,使用分子量相互作用模型(MVIM)计算二元合金的活性系数。关于温度和真空深度对升华程度的影响和来自各种组合物的SB-P和PB-AG配方的升华程度和分离的信息。计算饱和诗压力,用于Sb(P * = 273.664-67436.9Pa),Pb(0.149-485.9),Ag(5.054×10(-5)-6.558),在T = 1073-1773 K.显示出高比率= 1832.98-138.79,= 2948.16-74.09)和分离系数(log(sb)= 2.099-3.33和log(pb)= 1.813-3.944)给出了在锑和蒸馏时通过真空蒸馏选择性分离这些金属的理论先决条件在液相中依次富集在气相((Sb)> 1,(Pb)> 1)中依次富集液相。建立气相Y(Pb)/ y(Ag)=(1.55-982)×10(-3)/(36-772)×10(-3)中的升温铅/银中较差的引线/银的摩尔分数随着温度894-1601 / 1399-2099 K,压力1.33-133Pa和合金x(Pb)/ x(Ag)的金属含量增加而增加,金属含量= 0.9-0.9999 / 0.9-0.99。锑的活性系数(Sb)= 0.832-0.999,铅(Pb)= 0.474-1.0,SB / Pb和Pb / Ag合金的银(Ag)= 0.331-0.999 0.1-0.9 / 0.9-0.1使用MIVM计算研究的温度范围。揭示多金属合金升华产物的量和组合物的实际意义在提到的过程参数上是由真空蒸馏开发SPA合金的主要加工技术引起的。

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