Bildiriler Kitabı TMMOB Metalurji ve Malzeme Mühendisleri Odası Aysel Şen, Levent Kartal, Gülden Kartal Şireli, Servet Timur Selective Sulphide Precipitation of Copper, Nickel and Zinc from Industrial Wastewater İstanbul Technical University - Türkiye Abstract Metal sulphide precipitation is a fast, easy and environmentally friendly method which provides to work in wide pH ranges and to reuse/recycle them in metal smelting processes. In this research, the selective sulphide precipitations (SSP) of copper, nickel and zinc from industrial wastewater were investigated by using Na2S as the sulphur resource. The effects of pH and free sulphide concentration on the SSP were examined in two types of solutions; synthetically prepared wastewater and industrially supplied one from a gold refinery. The highest precipitation yields of Cu, Ni, and Zn were determined in the synthetic solution at the pH values of 2.3, 5.3, and 5.3, respectively. The precipitation efficiencies increased with increasing Na2S amount and reached its maximum at the ratio of 1:1.75 (Metal: Na2S in molar ratio). The refining wastewater, containing 10 g/L Cu2+, 0.3 g/L Ni2+ and 3 g/L Zn2+ ions, were treated at pH 2.3 and copper was precipitated as CuS with almost 100% of efficiency. In pH 5.3, the residual nickel and zinc ion concentration in the solution was decreased to 4 mg/L and 6 mg/L with the 44% and 52% of precipitation efficiencies, respectively. 1. Introduction The treatment of wastewater arisen from mining, electroplating, metal finishing and refining processes is a very crucial process for the conservation and reuse of natural resources. Therefore, the separation and recovery of metals from different kinds of industrial effluents by using chemical precipitation methods has been becoming more common application [1]. It is known that industrial treatment/recovery methods such as electrochemical based processes are required to make technological investments which not only cause to spend large amount of capital cost but lead to adaptation challenges as well [2,3,4]. The hydroxide precipitation technique, another well-known basic application, is the one applied in most manufacturing sectors of Turkey due to its simplicity and hence easy practicality. However, it creates huge volume of sludge wastes and consequently related long-term waste management problems [5]. The metal sulphide precipitation is an alternative way, which provides the precipitation of metal ions in a wide pH range and also in a short duration [6, 7]. Furthermore, the obtained metal sulphide precipitates can be reused as feeding materials to different metal smelting processes, namely CuS, Cu2S [8]. In the precipitation methods, very low-priced chemicals such as Na2S and Thioacetamide utilized which exhibit high solubility differences at low pH values [9, 10]. These advantages render the metal sulphide precipitation method more significant option. In this study, the selective sulphide precipitations (SSP) of copper, nickel and zinc were investigated from both synthetically prepared solutions and industrial wastewater by using Na2S as the sulphur resource. The effects of pH and free sulphide concentration on the efficiencies of SSP were examined in detail. 2. Experimental Procedure For the investigation of experimental data and the determination of reaction potentials and pH values at room temperature, Eh - pH diagrams of Cu-S-H2O, Ni-S-H2O, Zn-S-H2O, Cu-Ni-S-H2O, Ni-Zn-S-H2O were drawn by using the FactSage program. In this way, the optimum pH ranges were determined for the precipitation reactions, which were performed in the synthetic solution containing either a single metal ion or mixed metal ions. Afterwards, the optimized parameters were applied to the industrially supplied solutions from a gold refinery composing of Cu, Ni and Zn ions. The experimental studies were categorized into three groups: -First two group studies were conducted in the synthetic solutions (i.e., containing a single metal ion or mixed metal ions) to optimize pH and Na2S concentrations in order to reach the highest precipitation efficiencies of copper, nickel and zinc ions. - Based on data obtained from first two stages, in last experiment step were carried out for the selective sulfide 18. Uluslararası Metalurji ve Malzeme Kongresi | IMMC 2016 363 UCTEA Chamber of Metallurgical & Materials Engineers precipitation of Copper, Nickel and Zinc sulphide from refinery waste solutions. The precipitation efficiencies of Copper, Nickel and Zinc sulphide was also determined for the industrial case. Proceedings Book precipitation were additionally analyzed to determine the concentrations of remained metal ions. 2.1. Single metal precipitations from the single metal ion containing synthetic solution The first group of study was conducted in the synthetic solutions which contain single metal ions such as Copper, Nickel and Zinc to optimize process conditions, namely pH and Na2S values. Also the required reaction durations to complete precipitations were determined experimentally. Table 1. The synthetically prepared solutions used in the first two experimental stages Initial solution metal Solution Metal ion ion concentration Number (mg/L) Cu2+ 100 Ni2+ 1,200 I Zn2+ 12,500 Cu2+ 6,350 2+ Ni 2,935 II 2+ Zn 3,270 100 Cu2+ III Ni2+ 90 Zn2+ 100 The followed procedures applied in the experimental studies were given in Figure 1. During the preparation of synthetic solutions Merck chemicals, namely CuSO4.5H2O, NiSO4.6H2O, ZnSO4.7H2O and Na2S were used with distilled water. The pH values were adjusted with 10% NaOH and 10% H2SO4 solutions. 2.3. Wastewater solution precipitation Figure 1. Applied procedure in the experimental studies 3. Results and Discussion Experimental studies conducted for the determination the reaction duration for the single copper precipitation from the synthetically prepared solution revealed that the precipitation rates were quite high at the beginning. The whole metal sulphide precipitation reactions complete at around 45 min. to 60 min. (please see Figure 2). These results show that metal sulphide precipitation reactions occur very fast compared to the other precipitation reactions, such as metal hydroxide. 700 Cu2+ metal ion concentration(mg/L) 2.2. Metal precipitations from the mixed metal ions containing synthetic solution In the second step, the precipitations of three metal ions (Cu, Ni, Zn) were investigated in the synthetically prepared solutions according to the obtained results in the previous single metal ion precipitation studies. The synthetically prepared solutions used in the first two experimental stages were given in Table 1 with their initial metal ions concentrations. 635 600 500 400 300 274 272 234 176 200 163 161 100 0 0 10 20 30 40 50 60 Time (min) The Last part of studies were carried out in the strong acidic refinery waste solutions containing 10 g/L Cu2+, 0.3 g/L Ni2+ ve 3 g/L Zn2+ ions. After pH adjustment, Na2S were added to the main solution to initiate the precipitations. Afterward, the treated solutions were filtered and the obtained precipitates were washed with distillated water, and dried in an oven then send pieces of them for the chemical analyses. The residual solutions after the 364 IMMC 2016 | Figure 2. Variation of Cu2+ ion concentration as a function of time [25ºC, Cu2+:Na2S=1:1 in mole, pH= 2.3] The most two significant factors, namely pH and the free sulphide concentration in the solution, are additionally studied. During these experiments, the pH values of solution measured by pH electrode before the addition of Na2S. However it is strongly recommended that pH 18 th International Metallurgy & Materials Congress Bildiriler Kitabı TMMOB Metalurji ve Malzeme Mühendisleri Odası electrodes be integrated in industrial applications despite the pH controlling problem in huge volumes. With these pH measurement attachments in real practices, the pH variations during the reactions can be prevented, as well as sulphide ion species can be tracked and so potential hazardous gas (H2S) formation could be controlled. Likewise, the usage of mixer is needed to provide the homogeneity. The ideal pH values for the highest precipitation yields of CuS, NiS and ZnS were calculated as 2-2.5, 5.3-5.5 and 5.3-5.5, respectively by FactSage. The sulphide precipitations from the synthetically prepared solutions was initially carried out for copper ions and precipitated as CuS at the pH of 2 -2.5. Then nickel and zinc ions were precipitated as NiS and ZnS respectively at pH range of 5.3-5.5. The effect of Na2S amount added into the solution on the precipitation efficiencies of Cu2+, Ni2+ and Zn2+ ions were given in Figure 7. The precipitation efficiencies increased with Na2S addition. The maximum precipitation yields were achieved at the ratio of 1:1.75 where the metal ion (Me2+) molar concentration was 1 and Na2S molar concentration was 1.75. However, the excess free sulphide ions were consumed by other metal ions rather than targeted ions in the wastewater solutions. It should be emphasized that the ion selectivity in the precipitation started to disappear when applying the more Na2S than stoichiometric amount. This observation seen in excess Na2S addition is also consistence with the synthetically prepared mixed solution containing different types of metal ions. The pH variation experiments showed that the maximum precipitation efficiency could be obtained by adjusting pH (Figure 2). However, it was observed that while pH value is arranged to reach the maximum efficiency, the selectivity of precipitation decreases. Consequently, the highest precipitation yields achieved for Cu2+, Ni2+ and Zn2+ ions at the pH of 2.3, 5.3 and 5.3 respectively. Precipitation efficiency [%] Cu2+ Ni2+ Zn2+ 100% 80% Figure 5. XRD diffraction patterns of precipitated particles in pH 2.3 [Me2+:Na2S 1:1.75 (mole); T=25 ºC, pH 2.3, duration: 1 hour] 60% 40% 20% 0% 2,3 2.3 pH 5,3 5.3 Figure 3. Precipitation efficiency of Cu2+, Ni2+ and Zn2+ ions from wastewater solutions with respect to adjusted pH values [Me2+:Na2S 1:1.75 in mole; 25 ºC, 1 hour] The XRD analyses revealed that the obtained precipitate at pH 2.3 was composed of CuS and Cu2S (Figure 4). At the second part, the pH value was increase for the precipitation of Ni and Zn, the acquired deposit at the pH of 5.3 was in the composition of mixed Ni- and Zn- sulphur, NiS33.3Zn32.3 (please see Figure 6). Last part of the experimental study was conducted in the strong acidic refinery waste solutions. The pH adjustment step is more challenging in this case due to the industrial waste water buffer tendency. Figure 6. XRD diffraction patterns of precipitated particles in pH 5.3 [Me2+:Na2S 1:1.75 (mole); T=25 ºC, pH 5.3, duration: 1 hour] The excess Na2S additions are always consumed by other ions in the solution with very fast reaction rates. The 18. Uluslararası Metalurji ve Malzeme Kongresi | IMMC 2016 365 UCTEA Chamber of Metallurgical & Materials Engineers optimized pH values couldn’t be determined in the industrial wastewater due to the co-precipitation of metal. For this reason, in industrial wastewater applications, the measurement of free sulphide ion concentration is required by using a selective ion electrode. concentration in the solution decreased to 6 mg/L and the precipitation yield for zinc was determined as 52 %. 80 x Based on the obtained results, the metal sulphide precipitation is an alternative way compared to other wastewater treatment technologies in terms of its fast reaction rates, easy practicality and reusability of produces as a feeding material in metallurgical smelting processes as well as requests of economical raw materials. 60 References 40 [1] H. Shi, Industrial wastewater types, amounts and effects, “Point sources of pollution, local effects and it’s control”, 1 Beijing, Çin. [2] M. Ahmaruzzaman, 2011, “Industrial wastes as lowcost potential adsorbents for the treatment of wastewater laden with heavy metals.” Adv. Colloid Interface Sci., 166, no. 1–2, 36–59. [3] G. Chen., 2004, Electrochemical technologies in wastewater treatment, Seperation and Purification. Technology, 38, no. 1, 11–41. [4] A. Chmielewski, T. UrbaĔski, and W. Migdaá,, (1997). “Separation technologies for metals recovery from industrial wastes,” Hydrometallurgy, 45, 333-344. [5] U.S.E.P.A, (2000). ‘‘Rapor’’ Wastewater Technology Fact Sheet Chemical Precipitation. [6] A. E. Lewis,, 2010, Review of metal sulphide precipitation, Hydrometallurgy, 104, no. 2, 222–234. [7] D. Bhattacharyya, A. B. Jumawan, R. B. Grieves, 1979, Separation of Toxic Heavy Metals by Sulfide Precipitation, Sep. Sci. Technol., 14, no. 5, 441–452. [8] F. Fu, Q. Wang, (2011). Removal of heavy metal ions from wastewaters: a review, Journal of Environmental Management, 92, 407–418. [9] A. ùen, 2015, Endüstriyel AtÕk Sularda BakÕr, Nikel, Çinko Sülfür Selektif Çöktürme ùartlarÕnÕn Optimizasyonu, Istanbul, Turkey. [10] M. Gharabaghi, M. Irannajad, and Azadmehr, A. R., (2012). Selective Sulphide Precipitation of Heavy Metals from Acidic Polymetallic Aqueous Solution by Thioacetamide, Ind. Eng. Chem. Res., 51, no. 2, 954–963. Cu2+ Precipitation efficiency [%] Proceedings Book Ni2+ Zn2+ 100 20 0 1 ,10 0 11.25 ,25 11.50 ,50 1,75 1.75 Metal ions [mol]: Na2S [mol] Figure 7. Precipitation efficiency of industrial wastewater as a function of Na2S addition [Me2+:Na2S 1:1-1.75 in mole; 25 ºC, 1 hour]. 4. Conclusion The selective sulphide precipitations (SSP) of copper, nickel and zinc were investigated from both synthetically prepared solutions and industrial wastewater by using Na2S as the sulphur resource and the obtained results of this research could be summarized as following: x The single copper precipitation studies from the synthetically prepared solution revealed that the precipitation rates were quite high at the beginning. Total metal sulphide precipitation reactions complete at around 45 min. x The highest precipitation yields achieved for Cu2+, Ni2+ and Zn2+ ions were at the pH of 2.3, 5.3 and 5.3 respectively. x The ion selective precipitation began to disappear when applying the more Na2S than the stoichiometric amount. x In last part of the investigation, the SSP was applied to the refining wastewater containing10 g/L Cu2+, 0.3 g/L Ni2+ and 3 g/L Zn2+ ions. The copper concentration was achieved to decrease 40 mg/L by precipitating CuS and Cu2S at pH=2.3 with almost 100% of efficiency. At the pH value of 5.3, the nickel ion concentration in the solution was reduced to 4 mg/L with the 44 % of precipitation efficiency. When the precipitation reactions completed in at pH 5.3, the residual zinc ion 366 IMMC 2016 | 18 th International Metallurgy & Materials Congress
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