Transactions of Nonferrous Metals Society of China The Chinese Journal of Nonferrous Metals

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中國有色金屬學(xué)報(bào)

ZHONGGUO YOUSEJINSHU XUEBAO

第26卷    第2期    總第203期    2016年2月

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文章編號(hào):1004-0609(2016)02-0471-07
HNO3/NH4NO3預(yù)處理工藝強(qiáng)化低鉬焙砂浸出
甘敏1, 2,曾金林1,范曉慧1,張麟2,陳許玲1,王勇2,鄧瓊1,王海波1

(1. 中南大學(xué)資源加工與生物工程學(xué)院,長沙410083;
2. 大冶有色金屬集團(tuán)控股有限公司,黃石435100
)

摘 要: 采用濕法浸出法提取低鉬焙砂中的鉬元素。采用XRD分析低鉬精礦氧化焙燒所得鉬焙砂的物相組成,發(fā)現(xiàn)鉬焙砂中因存在鉬酸鹽及低價(jià)鉬,導(dǎo)致氨浸的鉬浸出率低。采用含HNO3/NH4NO3預(yù)處理的方法研究了低品位鉬焙砂的強(qiáng)化提鉬。結(jié)果表明:HNO3/NH4NO3預(yù)處理使難溶鉬酸鹽轉(zhuǎn)化為可溶于氨水的鉬酸,同時(shí),在酸鹽效應(yīng)的作用下抑制預(yù)處理過程鉬的損失,從而提高鉬的綜合回收率。HNO3/NH4NO3預(yù)處理的適宜工藝參數(shù):HNO3濃度120 g/L、NH4NO3濃度100 g/L、液固比3:1、浸出時(shí)間120 min、浸出溫度90 ℃。與非預(yù)處理的直接氨浸相比,氨浸渣中殘留的鉬含量從20.00%降低到5.13%,鉬的回收率從75.90%提高到95.38%。

 

關(guān)鍵字: 低品位鉬精礦;鉬焙砂;難溶鉬酸鹽;預(yù)處理;氨浸

Strengthening leaching for low grade molybdenum calcine by HNO3/NH4NO3 pretreatment technology
GAN Min1, 2, ZENG Jin-lin1, FAN Xiao-hui1, ZHANG Lin2, CHEN Xu-ling1, WANG Yong2, DENG Qiong1, WANG Hai-bo1

1. School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, China;
2. Daye Non-Ferrous Metals Group Holdings Co., Ltd., Huangshi 435100, China

Abstract:Molybdenum was extracted by hydrometallurgy leaching from low grade molybdenum calcine. The mineral compositions of the calcine roasted from low grade molybdenum concentrate were tested by X-ray diffraction. The results indicate that the leaching rate by ammonia is low because of the existence of molybdate and low state of molybdenum phase in the molybdenum calcine. The strengthening leaching for low grade molybdenum calcine by HNO3/NH4NO3 pretreatment was investigated. The results show that the undissolved molybdate is translated into dissolved molybdate in ammonia leaching by the HNO3/NH4NO3 pretreatment. Meanwhile, the loss of molybdenum is restrained with the effect of acid and salt. Thus, the comprehensive recovery rate of molybdenum is improved. The operating parameters of optimum process is established as follows: HNO3 concentration is 120 g/L, NH4NO3 concentration 100 g/L, liquid-solid ratio 3:1, pretreating time 120 min, reaction temperature 90 ℃. Compared with the direct ammonia leaching without pretreatment, the molybdenum content in the ammonia leaching residue reduces from 20.00% to 5.13%, and the comprehensive recovery rate of molybdenum increases from 75.90% to 95.38% with the processing of pretreating-ammonia leaching.

 

Key words: low grade molybdenum concentrate; molybdenum calcine; undissolved molybdate; pretreatment; ammonia leaching

ISSN 1004-0609
CN 43-1238/TG
CODEN: ZYJXFK

ISSN 1003-6326
CN 43-1239/TG
CODEN: TNMCEW

主管:中國科學(xué)技術(shù)協(xié)會(huì) 主辦:中國有色金屬學(xué)會(huì) 承辦:中南大學(xué)
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