Document Type : Regular Article

Authors

Department of chemistry, Science faculty, University of Tehran, Tehran, Iran

Abstract

In the present study, a new method has been suggested to solve the problems of the very low solubilityof sulfide ores in acidic solution and also the production of toxic impurities for the first time. In this work, the polyoxometalate (POM) oxidizer was applied for the dissolution of sulfide ores, extraction of metals, and removal of toxic and harmful wastes. In this procedure, POMs were used as strong oxidizers of sulfur compounds to dissolve sulfide ores. Also, acid was applied as a solvent and catalyst to increase the reaction rate. The Taguchi experimental design along with the ProMax simulation software was applied for studying the leaching of sulfide ores by POM oxidizers as a novel plan in experimental to industrial scales. The optimum data achieved by the Taguchi method was used as the input data to the simulation and sensitivity analysis of the process was executed by the ProMax software. The effects of curicital operating parameters such as the concentration of acid (CA) in the 60-90 g/l range, the  reaction temperature (TR) with the values of 60-90 ºC, the rotation rate (R) with the amounts of 50- 300 rpm, the retention time (τ) in the 0.5-2.0 h range, the concentration of polyoxometalate oxidizer with the values of 0.1- 0.5 g/l, the acid types of H2SO4, HNO3, HCl, H3PO4, the grain sizes of sulfide ores (Sparticle) in the 0.5-3.0 mm range and polyoxometalate with the types of [Mo6O19]2-, [Mo8O26]4-, [V10O28]6- and [H2W12O40]10- on the extraction efficiency of metals and removal of toxic heavy metals from sulfide ores by polyoxometalates were investigated. The optimum conditions to extract maximize metals from the sulfide ores were obtained as the CA; 80 g/l, TR; 90 ºC, R; 300 rpm, τ; 1.0 h, m POMs; 0.5g/l, acid type of H2SO4, Sgrain;1.0 mm and POMs type of [H2W12O40]10-. Under optimized conditions, the extraction efficiency of zinc, copper, and lead and the removal of toxic heavy metals from sulfide ores were determined as above 85%, 81%, 83%, and 99.9% receptivity.

Keywords

Main Subjects

[1] Pan, W., et al., Experimental and theoretical study on strengthening leaching of sulfide ores by surfactants. Process Safety and Environmental Protection, 2020. 137: p. 289-299.
[2] Hernández, P.C., et al., Accelerating copper leaching from sulfide ores in acid-nitrate-chloride media using agglomeration and curing as pretreatment. Minerals, 2019. 9(4): p. 250.
[3] Lee, J., et al., Comparative bioleaching and mineralogy of composited sulfide ores containing enargite, covellite and chalcocite by mesophilic and thermophilic microorganisms. Hydrometallurgy, 2011. 105(3-4): p. 213-221.
[4] Zhang, X., Y. Han, and S. Kawatra, Effects of grinding media on grinding products and flotation performance of sulfide ores. Mineral Processing and Extractive Metallurgy Review, 2020: p. 1-12.
[5] Mu, W., et al., Synchronous extraction of nickel and copper from a mixed oxide-sulfide nickel ore in a low-temperature roasting system. Journal of cleaner production, 2018. 177: p. 371-377.
[6] Cui, F., et al., Sodium sulfate activation mechanism on co-sulfating roasting to nickel-copper sulfide concentrate in metal extractions, microtopography and kinetics. Minerals Engineering, 2018. 123: p. 104-116.
[7] Yan, G., et al., Pressure acid leaching of zinc sulfide concentrate. Transactions of Nonferrous Metals Society of China, 2010. 20: p. s136-s140.
[8] Muszer, A., et al., Covellinisation of copper sulphide minerals under pressure leaching conditions. Hydrometallurgy, 2013. 137: p. 1-7.
[9] Kuz'Min, V. and D. Kuz'Min, Sorption of nickel and copper from leach pulps of low-grade sulfide ores using Purolite S930 chelating resin. Hydrometallurgy, 2014. 141: p. 76-81.
[10] Cerda, C.P., et al., Effect of pretreatment on leaching primary copper sulfide in acid-chloride media. Minerals, 2018. 8(1): p. 1.
[11] Nikoloski, A.N., G.P. O'Malley, and S.J. Bagas, The effect of silver on the acidic ferric sulfate leaching of primary copper sulfides under recycle solution conditions observed in heap leaching. Part 1: Kinetics and reaction mechanisms. Hydrometallurgy, 2017. 173: p. 258-270.
[12] Saidi, M. and H. Kadkhodayan, Toxic heavy metal removal from sulfide ores using potassium permanganate: Process development and waste management. Journal of Environmental Management, 2020. 276: p. 111354.
[13] Torkmahalleh, M.A., et al., Simulation of environmental impact of an existing natural gas dehydration plant using a combination of thermodynamic models. Process Safety and Environmental Protection, 2016. 104: p. 38-47.
[14] Esmaili, H., E. Kowsari, and S. Ramakrishna, Significance of nanostructure morphologies in photoelectrochemical water splitting cells: a brief review. Journal of Molecular Structure, 2021: p. 129856.
[15] Mondal, S., et al., Parametric optimization for leaching of cobalt from Sukinda ore of lateritic origin–A Taguchi approach. Separation and Purification Technology, 2015. 156: p. 827-834.
[16] Mbuya, B.I., M.B. Kime, and A.M. Tshimombo, Comparative study of approaches based on the Taguchi and ANOVA for optimising the leaching of copper–cobalt flotation tailings. Chemical Engineering Communications, 2017. 204(4): p. 512-521.
[17] Copur, M., M. Kizilca, and M.M. Kocakerim, Determination of the optimum conditions for copper leaching from chalcopyrite concentrate ore using taguchi method. Chemical Engineering Communications, 2015. 202(7): p. 927-935.
[18] Jassim, H.M., H.Z. Toma, and L.S. Oudah, Solvent Extraction and Electro-Wining from Copper Leaching Product of Mawat Sulfide Ore Using Taguchi Method. UKH Journal of Science and Engineering, 2017. 1(1): p. 53-59.
[19] Mehrabi, N., et al., Parameter optimization for nitrate removal from water using activated carbon and composite of activated carbon and Fe2O3 nanoparticles. RSC advances, 2015. 5(64): p. 51470-51482.
[20] El Moneim, N.A., I. Ismail, and N. MM, Simulation of Ammonia Production using HYSYS Software. Simulation, 2020. 62.
[21] Sousa, A.M., H.A. Matos, and M.J. Pereira, Modelling Paraffin Wax Deposition Using Aspen HYSYS and MATLAB, in Computer Aided Chemical Engineering. 2019, Elsevier. p. 973-978.
[22] Gervasi, J., L. Dubois, and D. Thomas, Simulation of the post-combustion CO2 capture with Aspen HysysTM software: study of different configurations of an absorption-regeneration process for the application to cement flue gases. Energy Procedia, 2014. 63: p. 1018-1028.
[23] Edwin, M., S. Abdulsalam, and I. Muhammad, Process simulation and optimization of crude oil stabilization scheme using Aspen-HYSYS Software. International Journal of Recent Trends in Engineering & Research. DOI, 2017. 10.
[24] Haydary, J., Chemical process design and simulation: ProMax and Aspen Hysys applications. 2019: John Wiley & Sons.
[25] Smejkal, Q. and M. Šoóš, Comparison of computer simulation of reactive distillation using PROMAX and HYSYS software. Chemical Engineering and Processing: Process Intensification, 2002. 41(5): p. 413-418.