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Gold Science and Technology ›› 2019, Vol. 27 ›› Issue (3): 449-457.doi: 10.11872/j.issn.1005-2518.2019.03.449

• Mining Technology and Mine Management • Previous Articles    

Reduction and Sulfur-fixing Roasting and Combination of Beneficiation and Metallurgy for Extraction of Gold-stibnite Concentrate

Zhen OUYANG1(),Yifeng CHEN1,Yujie HU1,Chaobo TANG2,Yongming CHEN2,Longgang YE1()   

  1. 1. School of Metallurgical and Material Engineering,Hunan University of Technology,Zhuzhou 412007,Hunan,China
    2. School of Metallurgy and Environment,Central South University,Changsha 410083,Hunan,China
  • Received:2018-07-11 Revised:2018-11-12 Online:2019-06-30 Published:2019-07-09
  • Contact: Longgang YE E-mail:1032168134@qq.com;yelonggang@sina.cn

Abstract:

Antimony-bearing gold ore is a kind of refractory gold deposit.Because gold is generally shown in microscopic particles wrapped in antimony,iron and arsenic sulfide,the general gold leaching method is not very effective in dealing with this mine.In views of the extraction difficulty of antimony-bearing gold ore,a new process based on the reduction and sulfur-fixing roasting and combination of beneficiation and metallurgy was proposed.Using ZnO and carbon as sulfur fixing agent and reductant,antimony sulfide is transformed to metal Sb and ZnS,and the gold is gathered in the former.Then the mixture is separated by mineral separation method.Gold enter the crude antimony powder following antimony.Crude antimony powder has been refined to obtain fine antimony powder,while zinc sulfide concentrate can be directly used in the smelting of zinc to produce metal zinc.The mechanism of the roasting process were investigated in detail,and the results show that overall reaction contained two steps.When the temperature is below 800 ℃,the main reaction are performed between Sb2S3 and ZnO to yield Sb2O3.Less antimony oxide is reduced and no more metal antimony is obtained.When the temperature is higher than 800 ℃,a large amount of the Sb2O3 is reduced to metallic antimony.The particle of antimony and zinc sulfide distributed respective without parcel.Both sulfur-fixing and reducing reactions are engaged completely,and with the increase of temperature,the sulfur-fixing rate and the production rate of metal antimony increased.The sulfur-fixing rate of ZnO and generation rate of antimony reached 98.96% and 92.99% respectively at 1 000 ℃.In a gravity separation and flotation test of the roasting product of Sb-bearing gold concentrate,Sb could be extracted with a direct recovery rate of 90.57%,while the grade of cured antimony and content of gold were 92.06% and 134×10-6,meanwhile,the sulfur-fixing rate reached 94.35%.So the new process is feasibility with the advantages of low temperature and low carbon,cleaning and environmental process.

Key words: Sb-bearing gold ore, reduction roasting, sulfur-fixing, combination of beneficiation and metallurgy, cleaning metallurgy

CLC Number: 

  • TF8

Table 1

Chemical composition of gold-antimony"

元素 质量分数 元素 质量分数
Sb 37.21 As 0.034
Fe 13.27 Au* 56
S 30.60 SiO2 7.14
Cu 0.085 Al2O3 2.26
Pb 0.18 CaO 0.079
Bi 0.026

Fig.1

Connection schematic of test device"

Fig.2

TG-DSC-MS analysis results of Sb2S3-ZnO-C mixture at mole rate of 1∶3∶3"

Fig.3

Influence of roasting time on the pH of SO2 absorbing solution at different temperature"

Fig.4

Sulfur-fixing rate of roasted samples at different temperatures"

Fig.5

Influence of roasting time on the pH of CO2 absorbing solution at different temperature"

Fig.6

Residual carbon content in roasted products at different temperatures"

Fig.7

XRD diagram of roasting product under 600 ℃"

Fig.8

Phase content change of Sb at different temperatures"

Fig.9

Map scanning results of roasting product at 800 ℃"

Table 2

Experiments results of overall process"

试验编号 粗锑粉 锌精矿
质量/g 锑品位/% 金含量/×10-6 锑直收率/% 金富集率/% 质量/g ZnS含量/% Zn直收率/% 固硫率/%
平均值 73.22 92.06 134 90.57 87.82 156.58 79.10 89.23 94.35
1 74.31 90.38 138 90.25 91.56 154.16 79.27 88.04 95.08
2 73.76 93.16 129 92.33 84.96 158.69 79.33 90.70 95.86
3 71.60 92.64 136 89.13 86.94 156.89 78.70 88.95 92.11

Fig.10

Elements content of impurity of crude Sb powder (a) and ZnS concentrate (b)"

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