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Gold Science and Technology ›› 2023, Vol. 31 ›› Issue (2): 349-358.doi: 10.11872/j.issn.1005-2518.2023.02.166

• Metallurge and Equipment • Previous Articles    

Experimental Study on Recovery of Gold from Ammonium Thiocyanate Leaching Solution by Electrodeposition

Chaocong ZENG1(),Guangsheng ZHANG2,Weirong WU2,Wanfu HUANG1,3,4(),Xindong LI3,4,Zekai WANG1,Guanfa LIU1   

  1. 1.School of Resources and Environmental Engineering, Jiangxi University of Science and Technology, Ganzhou 341000, Jiangxi, China
    2.Jiangxi Sanhe Gold Industry Co. , Ltd. , Dexing 334200, Jiangxi, China
    3.Ganzhou Innovation Center for Water Quality Security Technology at Ganjiang River Basin, Jiangxi University of Science and Technology, Ganzhou 341000, Jiangxi, China
    4.Ganzhou Key Laboratory of Basin Pollution Simulation and Control, Jiangxi University of Science and Tech-nology, Ganzhou 341000, Jiangxi, China
  • Received:2022-11-07 Revised:2023-02-15 Online:2023-04-30 Published:2023-04-27
  • Contact: Wanfu HUANG E-mail:1697284463@qq.com;sim2008@sina.com

Abstract:

The leaching agent cyanide has been on the verge of elimination due to its great harm to the environment and human health.The non-cyanide agent thiocyanate as an efficient and environmentally friendly gold leaching agent has become the object of research by scholars both domestic and foreign.However,the recovery methods from thiocyanate leachate are less studied,and there are problems with low efficiency and high cost of gold recovery.Therefore,it is urgent to find a highly productive,low-cost,and simple method to recover gold from leaching solution efficiently.On the basis of the above problems,ammonium thiocyanate was used for the leaching test of bio-oxidized slag from a difficult gold concentrate,and recovered gold from the leaching solution by electrodeposition.The single factor method was used to study the influence of various factors on the gold deposition rate.The results show that the self-made electrode with a large surface area,good corrosion resistance,and high metal deposition efficiency is an excellent cathode.The graphite rods with good conductivity,not involved in the reaction process,reused,is a good choice for anode materials.Stainless steel rods are not suitable as electrode materials due to their susceptibility to corrosion.Under the conditions of electrode spacing of 10 mm,cell voltage of 4 V,solution pH value of 12,and solution temperature of 35 ℃,using a graphite rod as an anode and a self-made electrode as a cathode,the gold deposition rate can reach 98.95%.The interaction between tank voltage,solution pH value,and solution temperature and the effect on gold deposition rate were investigated by response surface methodology,and the electrodeposition gold response surface regression model was established.The P value and mismatch value of the model are within a reasonable range,and the predicted value and actual value of the gold deposition rate basically fell in a straight line,shows that the model fits well and is highly reliable.The correlation between the test factors and the gold deposition rate can be described.The final results show that the degree of each factor on the gold deposition rate is cell voltage>solution pH value>solution temperature,among them,the interaction between cell voltage and solution pH value is the most significant,and the interaction between solution pH value and solution temperature is the least significant.Under the optimal conditions of cell voltage 4.10 volts,solution pH value of 12.40,and solution temperature of 39.58 ℃,the predicted value of the model is 99.06%,and the experimental average value is 99.04%.The two results are remarkably close,which proves that the model can accurately analyze and predict the gold deposition rate.This study further improves the theoretical system of thiocyanate gold extraction process.

Key words: thiocyanate leaching solution, electrodeposition method, electrode material, gold deposition rate, response surface analysis

CLC Number: 

  • TF831

Fig.1

Flow chart of electrolytic stock solution preparation"

Table 1

Main ion content of electrolytic stock solution"

离子种类质量浓度/(mg·L-1离子种类质量浓度/(mg·L-1
Au+15.25Pb2+0.05
Fe3+520Ag+2.69
SCN-1 718.712Cu2+11.25

Fig.2

Effect of different cathode materials on gold deposition"

Fig.3

Effect of anode materials in electrodeposit process"

Fig.4

Effect of electrode spacing on electrodeposit process"

Fig.5

Effect of different cell voltage on gold deposition"

Fig.6

Effect of solution pH value on gold deposition rate"

Fig.7

Effect of solution temperature on gold deposition rate"

Table 2

Test scheme and results"

序号ABC金沉积率/%
实际值预测值残差值
100099.1098.810.2860
210-195.5395.510.0200
300098.8998.810.0760
4-10-190.8191.02-0.2075
50-1194.2994.43-0.1412
6-1-1090.2390.070.1613
700098.9598.810.1360
81-1094.7694.83-0.0662
9-11091.5491.470.0663
100-1-193.5193.460.0463
11-10191.7091.72-0.0200
1210197.7797.560.2075
1300098.8198.81-0.0040
1401196.6196.66-0.0462
1511096.8997.05-0.1612
1600098.3298.81-0.4940
1701-195.0194.870.1413

Table 3

Results of variance analysis of regression model"

项目平方和自由度均方差FP显著性
总计149.6516
模型149.11916.57213.97< 0.0001显著
A-槽电压53.41153.41689.75< 0.0001
B-溶液pH值6.5916.5985.09< 0.0001
C-溶液温度3.8013.8049.010.0002
AB0.168110.16812.170.1841
AC0.455610.45565.880.0457
BC0.168110.16812.170.1841
A242.60142.60550.17< 0.0001
B221.85121.85282.26< 0.0001
C211.89111.89153.62< 0.0001
残差0.542070.0774
失拟误差0.191930.06400.73070.5853不显著
纯误差0.350140.0875

Fig.8

Analysis chart of actual value and predicted value of gold deposition rate"

Fig.9

Response surface"

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