Effects of lime sulphur synthetic solution on leaching characteristic of gold concentrates

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25 3 2015 3 Volume 25 Number 3 The Chinese Journal of Nonferrous Metals March 2015 1004-0609(2015)-03-0786-07 ( 100083) ph XRD H 2 O 2:1:(50~75) 45 min 97.57% ph 10.5 15% 73.42% ph ph ph TF803.21 A Effects of lime sulphur synthetic solution on leaching characteristic of gold concentrates ZHAO Liu-cheng, SUN Chun-bao, LI Shao-ying, GONG Dao-zhen (Key Laboratory of High-Efficient Mining and Safety of Metal Mines, Ministry of Education, University of Science and Technology Beijing, Beijing 100083, China) Abstract: Lime sulphur synthetic solution (LSSS) method was applied in gold concentrates leaching. The effect of mass ratio of sulphur, lime and water and synthetic time on sulfur conversion rate and ph value in synthetic process and gold leaching rate were investigated. X-ray diffraction was used to detect the main component of the residue aiming to uncover the transformation way of sulphur in LSSS synthetic process. The results show that the lime sulphur synthetic solution with sulfur conversion rate of 97.57% and ph of 10.5 is obtained when the synthesis conditions for mass ratio of sulphur, lime and water of 2:1:(50 75) and the time of 45 min. When the dilute concentration is 15%, the gold leaching rate reaches 73.42%. The mass ratio of sulfur to lime is the main reason affecting the sulfur conversion and ph value of mother solution. Both of sulfur conversion rate and ph value of mother solution show a declining tendency with the increase of the mass ratio of sulfur to lime. The mass ratio of water to lime and synthetic time has great effects on the ph value of mother solution, and has no effect on sulfur conversion rate. After LSSS preparation, sulfur mainly transfers into solution, a small amount of sulfur exists in the form of elemental sulfur in the residue, and the amount of this elemental sulfur increases with increasing the mass ratio of sulfur to lime. Key words: lime sulphur synthetic solution; leaching characteristics; gold concentrates; cyanide-free leaching of gold; conversion rate [1 2] 2014-05-052014-12-29 010-62334953 E-mail suncb@ustb.edu.cn

25 3 787 [3] [4 5] (CaS x ) (CaS 2 O 3 ) [6 9] ( 1/4 ) [10 11] [7] (Au 3.08 g/t As 1.5%) (Au 59.99 g/t Cu 3.9% Pb 11% S 32.03%)(Au 54 g/t As 3.5%) (Au 7.1 g/t As 0.51%) 90% [12] 3 h 94% [13] 96% [14] 85% [15] H 2 O 2 [16] SO 3 NH 3 H 2 O Cu 2+ 88% ph 1 1.1 1 1 X X 1 Table 1 Analysis results of chemical multi-element (mass fraction, %) Au 1) Ag 1) Fe S Cu SiO 2 MgO CaO Al 2 O 3 70.03 102.7 19.65 16.92 0.24 35.51 4.59 4.12 12.71 1) g/t. 1 XRD Fig. 1 XRD patterns of gold concentrates 1.2 ( ) m m1 w α = 100% (1) m α % m g m 1 g w % 1250~1300

788 2015 3 XRD X X Rigaku-RA X (12 kw) Cu K α (λ=0.15418 nm) 0.02 10 ~100 5 ( )/min 40 kv 150 ma 67% XMQ 240 90 38 μm 90% 50 g 50 g 500 ml SZCL-4 2 ph Fig. 2 Effect of mass ratio of sulfur to lime on sulfur conversion rate and ph mα m1γ ph η= 100% (2) mα η % m g m 1 g α g/t γ g/t 38 μm 90% 50 6:1 5 h 450 r/min CuSO 4 0.06 mol/l NH 3 H 2 O 0.8 mol/l Na 2 SO 3 0.08 mol/l Na 2 CO 3 0.1 mol/l 1.5:1 2.0:1 2.5:1 3.0:1 3 3 1.5:1 15%~25% 60% 2 2.1 x:1:50 x 1.5 1.75 2.0 2.25 2.5 2.75 3.0 300 ml 60 min 2 2 ph 1.5:1 ph 11.5 1.5:1 3:1 100% 70.81% ph 11.5 10.3 ph ph (2~3):1 3 Fig. 3 Effect of mass ratio of sulfur to lime on gold leaching rate (m 1 : mass of sulphur; m 2 : mass of lime)

25 3 789 10% 15% 60% 73% 25% ph 2:1 15% 97.57% ph 10.5 73.42% 2.2 2.5:1:x x 12.5 25 50 75 100 6 g 60 min 4 4 80% 12.5:1 100:1 ph 11.2 9.7 5 15% 5 75:1 77.96% ph ph ph 5 Fig. 5 Effect of mass ratio of water to lime on gold leaching rate (50~75):1 2.3 15 30 45 60 75 min 1:2.5:50 6 g 6 6 ph 15 min 45 min 1.32% 81.7% ph 11.3 10.5 30 min ph 4 ph Fig. 4 Effect of mass ratio of water to lime on sulfur conversion rate and ph value of mother solution 6 ph Fig. 6 Effect of synthetic time on sulfur conversion rate and ph value of mother solution

790 2015 3 7 15% 7 15 min 45 min 70.36% 81.10% 75 min 77.06% 45 min ph ( (3)~(6)) [17] 45 min x 2 2 3 2 2 3 2 2 3 3 x + 2 2 3 + x 2 3 + 2 4 + SS + CO + HO=CO + HS + xs S O + CO + H O=HCO + HSO + S 2S S 3O =2S O 2( 1)S 2S O O =2SO 2S (3) (4) (5) (6) Ca 2+ Mg 2+ CaO Mg 2+ Ca 2+ Mg 2+ CO 2 CaCO 3 CaMg(CO 3 ) 2 2+ + 2 3 + 2 Ca CO +2OH =CaCO 2H O Ca 2+ 2+ + Mg + 2CO2 + 4OH = CaMg(CO 3) 2 + 2H2 (7) O (8) 8 XRD Fig. 8 XRD patterns of residue of lime sulphur synthetic solution 3 7 Fig. 7 Effect of synthetic time on gold leaching rate 2.4 [18] CaSO 4 2H 2 O CaSO 4 5H 2 O SO 4 SO 4 Ca 2+ CaSO 4 2H 2 O CaSO 4 5H 2 O XRD 8 2:1:50 6 g 45 min 8 S CaCO 3 CaMg(CO 3 ) 2 [17] 2 2 6OH 4S Δ + 2S + S O + 3H O (9) 2 3 2 Δ + + 2 2 3 + 2 Δ + 3 + 2 3 + 2 Δ + + 4 2 3 + 2 Δ 5 2 3 2 6OH 6S 2S S O 3H O 6OH 8S 2S S O 3H O 6OH 10S 2S S O 3H O (10) (11) (12) 6OH + 12S 2S + S O + 3H O (13) (9)~ (13) 2 (9) ΔG Θ 2 [17,19] Table 2 Δ fg Θ m of ions and molecules [17, 19] (kj/mol) S S S 2 S 3 S 4 S 5 S 2 O 3 OH H 2 O 0 85.8 79.5 73.7 69.1 62.3 522.5 157.24 237.13

25 3 791 Θ Θ 2 Θ m m 2 3 ΔG =2 ΔG (S ) ΔG (S O ) Θ Θ m(oh ) Θ m(h2o) Δ Δ m ΔG G G 2 85.8+( 522.5)+3 ( 237.13) (S)= 6 ( 157.24) 4 0= 118.85 kj/mol (14) (10)~ (13) ΔG Θ 131.45 143.05 152.25 165.85 kj/mol ΔG Θ (CaS 4 CaS 5 ) (CaS 2 O 3 ) [7] (12) (13) (1.9~2.3):1 2:1 4 1) ph ph ph 2:1:(50~75) 45 min 97.57% ph 10.5 2) 15% 73.42% 3) REFERENCES [1] ZHANG Jian-tao, SHEN Shao-bo, CHENG Yao, LAN Hai-feng, HU Xing, WANG Fu-ming. Dual lixiviant leaching process for extraction and recovery of gold from ores at room temperature[j]. Hydrometallurgy, 2014, 144/145: 114 123. [2] YANG Xi-yun, MICHAEL S M, JAN D M, WANG Xu-ming, SHI Xi-chang, XU Hui. Thiourea-thiocyanate leaching system for gold[j]. Hydrometallurgy, 2011, 106(1/2): 58 63. [3] HA Vinh Hung, LEE Jae-chun, JEONG Jin-ki, HAI Huynh Trung, Jha Manis K. Thiosulfate leaching of gold from waste mobile phones[j]. Journal of Hazardous Materials, 2010, 178(1/3): 1115 1119. [4],,,,. [J]., 2014, 24(3): 814 819. LI Shao-ying, WANG Hai-xia, YUAN Xi-zhen, ZHAO Liu-cheng, SUN Chun-bao. Leaching dynamics of gold concentrates by iodine-iodide solution[j]. The Chinese Journal of Nonferrous Metals, 2014, 24(3): 814 819. [5],,,,. [J]., 2013, 23(5): 1434 1439. LI Shao-ying, WANG Hai-xia, SUN Chun-bao, ZHAO Liu-cheng, YAN Zhi-qiang. Effects of different iodide on gold concentrates leaching process in iodine-iodide solution[j]. The Chinese Journal of Nonferrous Metals, 2013, 23(5): 1434 1439. [6]. [J]., 2011, 19(6): 57 61. ZHONG Jun. Research and application status of non-cyanide gold leaching technology[j]. Gold Science and Technology, 2011, 19(6): 57 61. [7],,,. [J]., 1997, 18(2): 58 61. YANG Bing-yu, LAN Xin-zhe, ZHANG Jian, HAN Ai-yu. Lime sulphur synthetic solution(lsss)-a new nontoxic reagent for extraction of gold[j]. Precious Metals, 1997, 18(2): 58 61. [8] CHANDRA I, JEFFREY M I. An electrochemical study of the effect of additives and electrolyte on the dissolution of gold in thiosulfate solutions[j]. Hydrometallurgy, 2004, 73(3/4): 305 312. [9] AYLMORE M G, MUIR D M, STAUNTON W P. Effect of minerals on the stability of gold in copper ammoniacal thiosulfate solutions-the role of copper, silver and polythionates[j]. Hydrometallurgy, 2014, 143: 122. [10],,,. [J]., 2012, 33(2): 67 70. FU Ping-feng, SUN Chun-bao, KANG Jin-xing, GONG Dao-zhen. Progress of gold extraction mechanism, stability of extraction reagents and its application of lime sulphur synthetic solution(lsss) method[j]. Precious Metals, 2012, 33(2): 67 70. [11],. [J]., 2009(1): 41 42, 52. CHEN Jiang-an, ZHOU Yuan. Discussion on gold leaching system by LSSS[J]. Modern Mining, 2009(1): 41 42, 52. [12],. (LSSS) [J]., 2005, 26(3): 74 77, 82. CHEN Jiang-an, ZHOU Yuan. The study of leaching gold concentrate by lime sulphur synthetic solution(lsss) method[j]. Journal of Southern Institute of Metallurgy, 2005, 26(3): 74 77, 82. [13],. [J]., 2012, 33(3): 43 46. CHEN Yi, SONG Yong-hui. Study on leaching gold from carbonaceous gold ores by lime sulphur synthetic solution[j]. Gold, 2012, 33(3): 43 46.

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