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作 者:梁文娟 邓博纳 叶青 欧阳学臻 余俊杰 Liang Wenjuan;Deng Bona;Ye Qing;Ouyang Xuezhen;Yu Junjie(School of Minerals Processing and Bioengineering,Central South University,Changsha 410083,China)
机构地区:[1]中南大学资源加工与生物工程学院,湖南长沙410083
出 处:《金属矿山》2018年第7期118-122,共5页Metal Mine
摘 要:广西贵港某高铁三水铝石型铝土矿石铁含量达31.76%,Al2O3和Si O2含量分别为21.33%和7.09%,铝硅比为3.01,属典型的高铁、低铝、高硅、低铝硅比的铝土矿石。在常规开发利用工艺难以有效分离铁、铝、硅的情况下,确定采用钠化还原焙烧—磨矿—弱磁选—碱浸—深度脱硅—铝酸钠结晶工艺对该矿石进行开发利用工艺研究,在课题组已报道过焙烧—磨矿—弱磁选工艺的基础上,对富铝渣进行了碱浸与深度脱硅工艺条件研究。结果表明:(1)在富铝渣的碱浸过程中,随着碱初始浓度的增大、浸出温度的升高、浸出时间的延长,铝、硅、铁的浸出率均呈不同程度的上升趋势。碱浓度为200 g/L、浸出温度为220℃、浸出时间为1.0 h情况下的铝、硅、铁浸出率分别为60.51%、6.12%、5.82%。(2)在深度脱硅过程中,随着Ca O添加量的增加,脱硅率逐渐增大;随着温度的升高,脱硅率呈现先上升后下降的趋势;随着反应时间的延长,脱硅率先上升后下降。在Ca O添加量为2 g/L,反应温度为80℃,脱硅时间为2 h情况下,硅的脱除率达90.34%。较好地实现了铝的碱浸和硅的深度脱除。There is a high iron gibbsite-type bauxite ore from Guangxi. The ore is a kind of typical bauxite with high iron content,low aluminum content,low silicon content and the low ratio of alumina to silicon. The iron content of the ore is31.76%,while the content of Al2 O3 and Si O2 is 21.33% and 7.09% respectively,and the ratio of aluminum to silicon is 3.01.Due to the difficulty of effectively separation of iron,aluminum and silicon,the process of sodium reduction roasting-grinding low intensity magnetic separation-alkaline leaching-deep desilication-sodium aluminate crystallization had been used for the development and utilization of the bauxite. On the basis of the process of reported roasting-grinding-magnetic separation process,the conditions of alkali leaching and deep silica removal of aluminum-rich slag were studied. The results showed that:(1)the leaching ratio of aluminum,silicon and iron increased with the increase of initial alkali concentration,leaching temperature and leaching time in the alkali leaching process of aluminum-rich slag. The leaching ratio of aluminum,silicon and iron was 60.51%,6.12% and 5.82% respectively,when alkali concentration was 200 g/L,leaching temperature was 220 ℃ and leaching time was 1.0 h.(2) In the process of deep silicon removal,the desilication ratio gradually increased with the dosage of Ca O increased. As the temperature increased,the desilication ratio was firstly increased and then decreased,and with the extension of reaction time,the desilication ratio was first increased and then decreased. The desilication ratio was 90.34% when the dosage of Ca O was 2 g/l,the reaction temperature was 80 ℃ and the reaction time was 2 h. The alkali leaching of aluminum and deep removal of silicon were well achieved by the process.
关 键 词:高铁三水铝石型铝土矿 碱浸 深度脱硅 综合利用
分 类 号:TD952[矿业工程—选矿] TF111.31[冶金工程—冶金物理化学]
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