Gold Science and Technology
img

Wechat

Adv. Search
Online Submission Peer Review Office Work

Gold Science and Technology ›› 2019, Vol. 27 ›› Issue (1): 129-136.doi: 10.11872/j.issn.1005-2518.2019.01.129

Previous Articles     Next Articles

Optimization Study on the Sulfur Separation Process for Cyanide Tailing

Wenqiang ZHAO1,Chuanjin JIANG1,Baobao SHI2   

  1. 1. Shandong Jinchuang Gold and Silver Smelting Finite Company，Yantai 265615，Shandong，China
    2. Shandong Gold Jinchuang Group Daliuhang Gold Mine，Yantai 265615，Shandong，China
  • Received:2018-02-20 Revised:2018-08-17 Online:2019-02-28 Published:2019-03-19

RichHTML

8

PDF (PC)

531

Abstract:

Since cyanide has a certain inhibitory effect on pyrite，the effect of directly using flotation to recover pyrite in cyanide tailings is not satisfactory.Therefore，the inhibited mineral flotation activity must be recovered by pretreatment of the cyanide tailings.In the gold industry，the cyanide tailings S separation process uses acid addition cyanide removal method，metal ion precipitation cyanide method and addition of redox and cyanide removal agent cyanide method or a combination method to restore the inhibited pyrite.Research papers specifically for the flotation of pyrite in cyanide tailings are rarely seen in domestic industry research.There are many problems in the pretreatment and flotation，such as the mechanism is not clear，the dosage of the drug is extensive，the production cost is high，and the index is unstable.In this study，the synergistic pretreatment method of adding reducing agent and concentrated sulfuric acid was used to restore the inhibited mineral activity，and the effects of dosing order，sodium pyrosulfite dosage and pH value on the recovery rate of sulfur concentrate and tailing grade were investigated.Pretreatment tests show that:Adding sodium pyrosulfite first and then adding concentrated sulfuric acid is better than the reverse; When the sodium pyrosulfite in an amount of 2 000 g/t and pH=2~3 can achieve the best results.The flotation tests adopt the process of one roughing，one refining and two scavenging，and the effects of pH adjusters，ammonium salts and composite inhibitors on the recovery rate of sulfur concentrate and tailing grade were investigated.The flotation test found that using CaO as a pH adjuster has an inhibitory effect on the flotation activity of pyrite，and the addition of an ammonium salt can restore this activity，but there is still a problem of foam sticking.Although the use of composite inhibitors can improve the concentrate grade and reduce the impurity content of Pb and Zn in the concentrate，the Pb and Zn in the concentrate are too fine to be entrained by the foam，so the Pb and Zn grades of the S concentrate cannot be further reduced by the flotation method alone.The test finalizes the optimum process conditions for the pretreatment：The first step was added 2 000 kg/t Na2S2O5 regent for pretreatment for 1 h，concentrated sulfuric acid was then added to the slurry,and the pH value was adjusted to 2~3 and maintained 2 h，NaOH and then adjusted to pH=6~7.The optimum flotation conditions are as follows：the dosage of dibutyl dithiophosphate is 500 g/t，the dosage of composite inhibitor is 300~500 g/t， and the good results of sulfur concentrate grade of 40 % ~42 % and S element grade of tailings of 6 % ~8 % are obtained through experiments.

Key words: pyrite, pretreatment, sodium metabisulfite, activate, ammonium salt, compound agent, cyanide tailings

CLC Number: 

  • TD95

Table 1

Analysis of main elements in tailings（%）"

元素 含量 元素 含量
Au* 0.5~1.0 Pb 0.18~0.32
Ag* 20~30 Zn 0.07~0.20
Fe 12~16 S 20~25

Fig.1

Flow chart of open circuit experiment"

Table 2

Statistics of open circuit test results of scheme 1"

产品名称 试验编号 产品产率/% 元素含量/% 回收率/%
S Pb Zn S Pb Zn
一次粗选 F-k1 33.25 43.00 0.18 0.20 60.53 18.56 50.39
一次扫选 F-k2 6.85 42.00 0.22 0.14 12.18 4.67 7.26
二次扫选 F-k3 6.60 32.00 0.36 0.12 8.94 7.37 6.00
二扫尾矿 F-X 53.30 8.13 0.42 0.09 18.35 69.41 36.35
平衡原矿 F-N 100.00 24.00 0.32 0.13 100.00 100.00 100.00

"

产品名称 试验编号 产品产率/% 元素含量/% 回收率/%
S Pb Zn S Pb Zn
一次粗选 F-k1 34.50 40.28 0.20 0.15 60.73 22.30 43.44
一次扫选 F-k2 10.79 41.98 0.20 0.06 19.80 6.97 5.43
二次扫选 F-k3 7.16 29.00 0.40 0.12 9.08 9.26 7.22
二扫尾矿 F-X 47.55 5.00 0.40 0.11 10.39 61.47 43.91
平衡原矿 F-N 100.00 23.00 0.31 0.12 100.00 100.00 100.00

Table 4

Comparative analysis of test results of two schemes（%）"

编号 方案1尾矿元素含量 方案2尾矿元素含量
S Pb Zn S Pb Zn
1# 8.2 0.3 0.11 5 0.4 0.11
2# 7.6 0.32 0.09 6.4 0.36 0.09
3# 5.6 0.35 0.08 5.7 0.33 0.12
4# 8.7 0.36 0.12 5.8 0.34 0.08
5# 10.3 0.28 0.09 3.9 0.36 0.15
6# 6.9 0.3 0.15 4.5 0.31 0.09

Fig.2

Distribution of S（Ⅳ） components in solution at 25 ℃"

Fig.3

Relationship between tailing’s grade and dosage of Na2S2O5 "

Table 5

Experimental results statistics of changing pH value（%）"

pH值 方案1尾矿元素含量
S Pb Zn
8~9 19.2 0.28 0.14
5~6 10.5 0.31 0.11
2~3 4.7 0.32 0.09
0~1 4.2 0.29 0.10

Table 6

Experiment results of flotation using CaO as pH value regulator instead of NaOH"

产品名称 试验编号 产品产率/% 元素含量/% 回收率/%
S Pb Zn S Pb Zn
一次粗选 F-k1 33.18 39.95 0.18 0.12 62.62 20.78 34.77
一次扫选 F-k2 6.10 25.00 0.20 0.09 7.21 4.25 4.80
二次扫选 F-k3 5.98 22.00 0.40 0.15 6.22 8.32 7.84
二扫尾矿 F-X 54.74 9.26 0.35 0.11 23.95 66.65 52.59
平衡原矿 F-N 100.00 21.00 0.29 0.11 100.00 100.00 100.00

"

产品名称 试验编号 产品产率/% 元素含量/% 回收率/%
S Pb Zn S Pb Zn
一次粗选 F-k1 35.40 38.57 0.33 0.24 66.39 39.98 56.56
一次扫选 F-k2 10.20 25.28 0.20 0.18 12.54 6.98 12.23
二次扫选 F-k3 6.72 23.02 0.39 0.13 7.52 8.97 5.82
二扫尾矿 F-X 47.69 5.84 0.27 0.08 13.54 44.07 25.40
平衡原矿 F-N 100.00 21.00 0.29 0.15 100.00 100.00 100.00

Fig.4

Relationship between tailing’s grade and dosage of ammonium salt"

Table 8

Statistical results of inhibition of lead and zinc by compound inhibitors"

抑制剂用量/（g·t-1） 一次粗选硫精矿品位 尾矿品位 一次粗选铅品位 一次粗选锌品位
0 38.55 5.84 0.33 0.24
100 39.01 5.81 0.26 0.18
300 43.66 4.63 0.18 0.12
500 45.36 5.26 0.16 0.11
1 000 43.33 6.24 0.16 0.13

Fig.5

Schematic diagram of closed circuit experimental process"

Table 9

Statistical results of closed circuit experiment"

产品名称 产率/% 品位/% 回收率/%
S Pb Zn S Pb Zn
硫精矿 39.50 49.26 0.12 0.24 86.46 26.06 63.70
尾矿 60.50 5.14 0.22 0.09 13.54 73.94 36.30
原矿 100.00 23.02 0.18 0.15 100.00 100.00 100.00
1 王资 .浮游选矿技术［M］.北京：冶金工业出版社，2006：143-144.
Wang Zi .The Technology of Flotation［M］.Beijing：Metallurgical Industry Press，2006：143-144.
2 何辉，贾学国，谢建宏，等 .氰化尾矿再选回收硫的试验研究［J］.矿业研究与开发，2013，33（1）：32-34.
He Hui ， Jia Xueguo ， Xie Jianhong ，et al .Experimental study on recovery of sulphur from a cyanidation tailings［J］.Mining Research and Development，2013，33（1）：32-35.
3 孙淑慧，付国燕，钱鹏，等 .氰化尾渣高效脱氰富集硫铁的试验研究［J］.计算机与应用化学，2013，30（3）：229-235.
Sun Shuhui ， Fu Guoyan ， Qian Peng ，et al .The research on the efficient destruction of cyanide and recovery of pyrite from the residue of cyanide［J］.Computers and Applied Chemistry，2013，30（3）：229-235.
4 丘学民，陈国宝，张勤，等 .从超细粒高铅锌氰化尾渣中浮选回收有价金属的试验研究［J］.黄金科学技术，2017，25（6）：61-67.
Qiu Xuemin ， Chen Guobao ， Zhang Qin ，et al .Experimental study on flotation recovery of valuable metals from ultrafine cyanide tailing containing high grade lead and zinc［J］.Gold Science and Technology，2017，25（6）：61-67.
5 李婷，尹艳芬，方夕辉，等 .从金氰化尾渣中回收铜、铅、锌、硫的工艺技术现状［J］.现代矿业，2011，4（4）：28-29.
Li Ting ， Yin Yanfen ， Fang Xihui ，et al .Technological status of recovering copper，lead，zinc，sulfur from gold cyaniding tailings［J］.Modern Mining，2011，4（4）：28-29.
6 李仕熊，李学强，张学政 .从氰化尾渣高效回收铜、铅、锌、硫的新工艺研究［J］.湖南有色金属，2009，25（1）：13-16.
Li Shixiong ， Li Xueqiang ， Zhang Xuezheng .Study on new techniques for effective recovery of Cu、Pb、Zn and S from cyanide residue［J］.Hunan Nonferrous Metals，2009，25（1）：13-16.
7 李新民，张占良，李萍，等 .氰化尾矿中铜铅硫综合回收试验研究［J］.金属矿山，2002，32（增）：70-72.
Li Xinmin ， Zhang Zhanliang ， Li Ping ，et al .Test research of the comprehensive recovery of copper,lead and sulfur from cyanidation tailings［J］.Metal Mine，2002，32（Supp.）：70-72.
8 霍奇金森G，郑健 .从浸金渣中浮选黄铁矿［J］.国外金属矿选矿，1995（6）：17-23.
Hodgkinson G ， Zheng Jian .The flotation of pyrite from gold dregs［J］.Metallic Ore Dressing Abroad，1995（6）：17-23.
9 韩跃新，马艺闻，朱一民，等 .黄铁矿表面氰根离子的吸附规律研究［J］.金属矿山，2013，42（1）：70-72.
Han Yuexin ， Ma Yiwen ， Zhu Yimin ，et al .Research on adsorption rule of cyanide ions on the pyrite surface［J］.Metal Mine，2013，42（1）：70-72.
10 杨秀丽，黄雄，邱廷省 .焦亚硫酸钠在氰化尾渣中硫化铜锌矿表面的活化作用［J］.中国有色金属学报，2016，26（9）：1982-1989.
Yang Xiuli ， Huang Xiong ， Qiu Tingsheng .Activation of sodium metabisulfite on surfaces of copper-zinc sulfide ore in cyanidation tailings［J］.The Chinese Journal of Nonferrous Metals，2016，26（9）：1982-1989.
11 唐宇，赵博 .浅析黄铁矿的可浮性及抑制活化机理［J］.城市建设理论研究，2015，5（29）：20-22.
Tang Yu ， Zhao Bo .The shallow analysis of the flotation of pyrite and the inhibition and activation mechanism［J］.Construction，2015，5（29）：20-22.
12 Murphy R ， Strongin D R .Surface reactivity of pyrite and related sulfides［J］.Surface Science Reports，2009，64（1）：1-45.
13 Chandra A R ， Gerson A R .A review of the fundamental studies of the copper activation mechanisms for selective flotation of the sulfide minerals，sphalerite and pytite［J］.Advances in Colloid and Interface Science，2009，145（1/2）：97-100.
14 黄尔君，冯育武 .铵盐对黄铁矿的活化作用及其机理研究［J］.有色金属（选矿部分），2006（2）：33-37.
Huang Erjun ， Feng Yuwu .The study on the activation and mechanism of ammonium salt for pyrite［J］.Nonferrous Metals（Mineral Processing Section），2006（2）：33-37.
15 肖骏，陈代雄，杨建文，等 .草酸对含伴生金硫化矿中贵金属活化的研究及应用［J］.黄金，2015，36（5）：50-54.
Xiao Jun ， Chen Daixiong ， Yang Jianwen ，et al .Research on the activation of precious metals in gold associated sulfide ores by oxalic acid and its application［J］.Gold，2015，36（5）：50-54.
16 邱沙，郭鹏智，郑其，等 .焦亚硫酸钠—空气法处理含氰尾矿浆［J］.有色金属（冶炼部分），2015，16（12）：59-62.
Qiu Sha ， Guo Pengzhi ， Zheng Qi ，et al .Treament of cyanide tailing slurry by Na2S2O5-air method［J］.Nonferrous Metals（Extractive Metallurgy），2015，36（5）：50-54.
17 张英，覃武林，孙伟，等 .石灰和氢氧化钠对黄铁矿浮选抑制的电化学行为［J］.中国有色金属学报，2011，21（3）：675-680.
Zhang Ying ， Qin Wulin ， Sun Wei ，et al .Electrochemical behaviors of pyrite flotation using lime and sodium hydroxide as depressantors［J］.The Chinese Journal of Nonferrous Metals，2011，21（3）：675-680.
18 孙伟，张英，覃武林，等 .被石灰抑制的黄铁矿的活化浮选原理［J］.中南大学学报（自然科学版），2010，41（3）：813-814.
Sun Wei ， Zhang Ying ， Qin Wulin ，et al .Activated flotation of pyrite once depressed by lime［J］.Journal of Central South University（Science and Technology），2010，41（3）：813-814.
19 黄有成，赵礼兵 .无机抑制剂在低碱度铅锌硫分离中的作用研究［J］.现代矿业，2011，1（1）：23-30.
Huang Youcheng ， Zhao Libing .The effect of inorganic inhibitors on separation of lead，zinc and sulfur in low alkalinity condition［J］.Mordern Mining，2011，1（1）：23-30.
20 欧乐明，黄思捷，冯其明，等 .高品质硫精矿生产工艺技术研究［J］.化工矿物与加工，2009，38（11）：1-4.
Leming Ou ， Huang Sijie ， Feng Qiming ，et al .Processing technology of high quality sulfur concentrate［J］.Chemical Minerals and Processing，2009，38（11）：1-4.
21 衣德强 .硫精矿降杂工业试验研究［J］.中国矿山工程，2005，34（6）：27-30.
Yi Deqiang .Industrial test study of reducing sulfur concentrate impurities［J］.China Mine Engineering，2005，34（6）：27-30.
[1] Qingwei LUO,Baoguo WANG,Aiwen YI,Kechuan ZHANG,Ze PAN,Shengya ZHANG. Typomorphic Characters and Significance of Pyrite in a Greenstone Belt Type Gold Deposit in Tanzania [J]. Gold Science and Technology, 2019, 27(1): 15-24.
[2] Yanhua LIU,Guobao CHEN,Hongying YANG,Zhenan JIN,Gairong WANG. Research on Mechanical Activation Properties and Leaching Test of Arseno-pyrite [J]. Gold Science and Technology, 2018, 26(5): 669-676.
[3] Leilei ZHANG, Jing ZHANG, Qisong WANG, Liang CHEN, Xu’an CHEN. Characteristics of Pyrite from Huaishuping Gold Deposit in Xiong’ershan District and Its Geological Significance [J]. Gold Science and Technology, 2018, 26(4): 481-491.
[4] LI Jiafeng, YANG Hongying, TONG Linlin, JIN Zhenan, ZHANG Dengchao. Experimental Study on Bacterial Oxidation-Gold Extraction of Paodaoling Refractory Gold Concentrate [J]. Gold Science and Technology, 2018, 26(2): 248-253.
[5] LIU Zilong, YANG Hongying, ZHANG Jingang, SONG Yan. Experimental Study on Arsenic Enrichment of Gold Concentrate Containing Arsenic [J]. Gold Science and Technology, 2018, 26(2): 254-260.
[6] SONG Xuewen，ZHU Jiaqian，LUO Zengxin，CHEN Bo. Study on the Gold Flotation Technology and Process Mineralogy of a Cyanide Residue [J]. Gold Science and Technology, 2018, 26(1): 89-97.
[7] PAN Haodan1，2，YANG Hongying，TONG Linlin，LI Chengzhuo，DU Shilin，HAN Xinyi，HAN Shuang. Effects of Initial pH on ASH-07 Bacterial Growth and Chalcopyrite Bio-leaching Process [J]. Gold Science and Technology, 2018, 26(1): 115-123.
[8] QIU Xuemin，CHEN Guobao，ZHANG Qin，YANG Hongying. Experimental Study on Flotation Recovery of Valuable Metals from Ultrafine Cyanide Tailing Containing High Grade Lead and Zinc [J]. Gold Science and Technology, 2017, 25(6): 61-67.
[9] DANG Xiao’e，WANG Lu，MENG Yusong，SONG Yonghui，Lü Chaofei. Performance of an Environmental Gold Leaching Agent and Activated Carbon Adsorption Characteristics of Gold in the Liquid [J]. Gold Science and Technology, 2017, 25(6): 114-120.
[10] WANG Xiaoqing，YANG Xingke，RUI Huichao. The Crystal Form Typomorphism of Pyrite and Its Variation Regularity and Prospecting Significance in Daiwangshan Gold Deposit， Inner Mongolia [J]. Gold Science and Technology, 2017, 25(5): 39-46.
[11] SHI Guiming，ZHAO Jieming，WU Caibin，HE Shuichun. Research on the Beneficiation Tests of Mafic Igneous Rock Type Gold Deposit in Sichuan Province [J]. Gold Science and Technology, 2016, 24(6): 96-101.
[12] LIU Chunbo，ZHANG Shugen，HUANG Chaowen，LIU Xuan，MO Jinglong，LI Kailin. Genetic Mineralogical Characteristics of Pyrite in Boka Gold Deposit from Dongchuan Area，Yunnan Province [J]. Gold Science and Technology, 2016, 24(5): 40-47.
[13] WANG Hao，TIAN Qinghua，XIN Yuntao，GUO Xueyi. Research on the Process of Pretreatment of Refractory Gold Ores Containing Antimony by Ozonation Leaching [J]. Gold Science and Technology, 2016, 24(4): 154-159.
[14] WANG Yongliang，LV Cuicui，XIAO Li，DING Jian，FU Guoyan，YE Shufeng. [J]. Gold Science and Technology, 2016, 24(4): 144-148.
[15] DING Wentao，CAI Chuangkai，GUO Jinyi，XU Xiaoyang. Recovery of Gold and Silver from Pressure Oxidative Slag of Refractory Gold Ore [J]. Gold Science and Technology, 2016, 24(1): 108-112.
Viewed
Full text


Abstract

Cited
  Shared   
  Discussed   
No Suggested Reading articles found!

©2018 Gold Science and Technology　

Telephone：0931-8277791　

E-mail: hjkx@lzb.ac.cn Postcode：730000　

Powered by Beijing Magtech Co. Ltd

陇ICP备17001318号-1