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石煤空白焙烧过程热力学分析 总被引:1,自引:0,他引:1
从热力学上对石煤空白焙烧过程中发生的相关氧化反应进行了分析.有机碳、黄铁矿及钒的氧化反应,在热力学上都可自发进行,有机质和黄铁矿比钒更容易氧化.有机碳和黄铁矿的存在,对钒的氧化有阻碍作用,若预先脱碳或脱除黄铁矿,则有利于钒的氧化. 相似文献
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通过单矿物和人工混合矿的浮选试验、Zeta电位测试、吸附量测试,研究了蛇纹石和石英异相凝聚的机理,以及对黄铁矿浮选的影响,以进一步探索多种矿物的体系中,蛇纹石对硫化矿物浮选影响的主要原因。结果表明:通过添加石英,可以恢复黄铁矿对捕收剂的吸附量,减弱蛇纹石的不良影响,不同粒级的石英与蛇纹石的异相凝聚作用强弱不同,粒级越细的石英,与蛇纹石的异相凝聚作用越强。 相似文献
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Tween80在一水硬铝石浮选中的作用 总被引:1,自引:0,他引:1
采用浮选试验、红外光谱和粒度分析研究Tween80对油酸钠浮选一水硬铝石的影响。结果表明:当Tween80与油酸钠以适宜的比例(质量比为1:9)混合时,有利于一水硬铝石的浮选;随着Tween80的增多,混合表面活性剂不利于一水硬铝石的浮选。加入Tween80强化了细粒级一水硬铝石的捕收,但没有明显改善油酸钠在低温下的捕收能力;油酸钠主要以阴离子形式吸附于一水硬铝石表面,且加入Tween80可能与油酸钠在一水硬铝石表面产生共吸附。 相似文献
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Sulfuric acid leaching process was applied to extract nickel from roasting-dissolving residue of a spent catalyst, the effect
of different parameters on nickel extraction was investigated by leaching experiments, and the leaching kinetics of nickel
was analyzed. The experimental results indicate that the effects of particle size and sulfuric acid concentration on the nickel
extraction are remarkable; the effect of reaction temperature is mild; while the effect of stirring speed in the range of
400–1 200 r/min is negligible. Decreasing particle size or increasing sulfuric acid concentration and reaction temperature,
the nickel extraction efficiency is improved. 93.5% of nickel in residue is extracted under suitable leaching conditions,
including particle size (0.074–0.100) mm, sulfuric acid concentration 30% (mass fraction), temperature 80 °C, reaction time
180 min, mass ratio of liquid to solid 10 and stirring speed 800 r/min. The leaching kinetics analyses shows that the reaction
rate of leaching process is controlled by diffusion through the product layer, and the calculated activation energy of 15.8
kJ/mol is characteristic for a diffusion controlled process.
Foundation item: Project (50574101) supported by the National Natural Science Foundation of China; Project (2003UDBEA00C020) supported by
the Collaborative Project of School and Province of Yunnan Province, China 相似文献
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A new technology was developed to recover multiple valuable elements from the spent Al2O3-based catalyst by X-ray phase analysis and exploratory experiments. The experimental results show that in the condition of roasting temperature of 750 ℃ and roasting time of 30 min, molar ratio of Na2O to Al2O3 of 1.2, the leaching rates of alumina, vanadium and molybdenum in the spent catalyst are 97.2%, 95.8% and 98.9%, respectively. Vanadium and molybdenum in sodium aluminate solution can be recovered by precipitators A and B, and the precipitation rates of vanadium and molybdenum are 94. 8% and 92. 6%. Al(OH)3 was prepared from sodium aluminate solution in the carbonation decomposition process, and the purity of Al2O3 is 99. 9% after calcination, the recovery of alumina reaches 90. 6% in the whole process; the Ni-Co concentrate was leached by sulfuric acid, a nickel recovery of 98. 2% and cobalt recovery over 98.5% can be obtained under the experimental condition of 30% H2SO4, 80 ℃, reaction time 4 h, mass ratio of liquid to solid 8, stirring rate 800 r/min. 相似文献