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作 者:杜冬云[1] 倪冲[1] 赵燕鹏[1] 阮福辉[1] 卢娜[1]
机构地区:[1]中南民族大学环境科学与工程研究所化学与材料科学学院/催化材料科学国家民委-教育部共建重点实验室,武汉430074
出 处:《中南民族大学学报(自然科学版)》2012年第4期6-10,共5页Journal of South-Central University for Nationalities:Natural Science Edition
基 金:武汉市重点科技攻关资助项目(201160638173)
摘 要:采用氨浸法回收含砷石灰铁盐渣中锌,研究了不同浸取剂、浸取剂的组成、总氨浓度、氨水与铵盐配比、液固比等工艺条件对锌浸出效果的影响,分析了锌的浸出动力学.结果表明:以氨水和碳酸铵组成的浸取体系为浸取剂,当总氨浓度为5 mol/L,氨-铵盐摩尔浓度比为2∶3,液固比为4∶1时,锌的浸出率为56.21%.由宏观模型得出锌的浸出在温度为288~323 K内遵循"未反应核缩减"模型,受内扩散控制,浸出动力学方程为:1-2α3-(1-α)2/3=232×exp(-32245/RT)t,浸出表观活化能为32.24 kJ/mol.Zinc from solid waste containing arsenic was recovered by ammonia leaching method. The effects of different leachant, leachant composition, total ammonia concentration, molar concentration ratio of NH3 to NH4+ , liquid-solid ratio on zinc leaching were investigated and its kinetics of was also analyzed. The results indicated that 56.21% of zinc was recovered when c(ammonia) = 5 mol/L, c ( NH3 ) : c ( NH4+ ) = 2: 3, L/S ratio = 4: 1. And the leaching process by macro model followed the shrinking-core model at the temperature ranging from 288 K to 328 K, which was controlled by the inner ~ - 32245, diffusion of reactants. The leaching kinetics equation was established as 1-2α3-(1-α)2/3=232×exp(-32245/RT)t, and the apparent activation energy is 32.24 kJ/mol.
分 类 号:X758[环境科学与工程—环境工程]
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