Hendrik Setiawan, Himawan Tri Bayu Murti Petrus, and Indra Perdana, Reaction kinetics modeling for lithium and cobalt recovery from spent lithium-ion batteries using acetic acid, Int. J. Miner. Metall. Mater., 26(2019), No. 1, pp. 98-107. https://doi.org/10.1007/s12613-019-1713-0
Cite this article as:
Hendrik Setiawan, Himawan Tri Bayu Murti Petrus, and Indra Perdana, Reaction kinetics modeling for lithium and cobalt recovery from spent lithium-ion batteries using acetic acid, Int. J. Miner. Metall. Mater., 26(2019), No. 1, pp. 98-107. https://doi.org/10.1007/s12613-019-1713-0
Research Article

Reaction kinetics modeling for lithium and cobalt recovery from spent lithium-ion batteries using acetic acid

+ Author Affiliations
  • Corresponding author:

    Indra Perdana    E-mail: iperdana@ugm.ac.id

  • Received: 9 April 2018Revised: 30 May 2018Accepted: 30 June 2018
  • Lithium and cobalt recovery from spent lithium-ion batteries (LIBs) is a major focus because of their increased production and usage. The conventional method for recycling spent LIBs using inorganic acids produces harmful byproducts. In this work, the leaching agent was substituted with a less expensive and more environmentally friendly alternative-acetic acid-and a mathematical model was developed to describe the kinetics of the recovery process. The variables used were the pH value, temperature, H2O2 concentration, and the solid-to-liquid (S/L) ratio. The mathematical model used was the shrinking core model, which was modified to accommodate an equilibrium reaction. The experimental results show that the rate of recovery of Li and Co over time was only affected by temperature. The leaching behaviors of Li and Co were found to oppose each other. An increase in temperature resulted in increased recovery of Li but decreased recovery of Co because of the product-favoring endothermic reaction of Li and the reactant-favoring exothermic reaction of Co. The product of Li has a lower entropy value than the reactant as a free-moving ion, whereas the product of Co leaching has a higher entropy value as a stiff crystal complex. Thus, temperature conditioning is a pivotal factor in the leaching of spent LIBs.
  • loading
  • [1]
    M. Broussely and G. Archdale, Li-ion batteries and portable power source prospects for the next 5-10 years, J. Power Sources, 136(2004), No. 2, p. 386.
    [2]
    L. Li, J. Ge, F. Wu, R.J. Chen, S. Chen, and B.R. Wu, Recovery of cobalt and lithium from spent lithium ion batteries using organic citric acid as leachant, J. Hazard. Mater., 176(2010), No. 13, p. 288.
    [3]
    C. K. Lee and K. I. Rhee, Reductive leaching of cathodic active materials from lithium ion battery wastes, Hydrometallurgy, 68(2003), No. 1-3, p. 5.
    [4]
    S.M. Shin, N.H. Kim, J.S. Sohn, D.H. Yang, and Y.H. Kim, Development of a metal recovery process from Li-ion battery wastes, Hydrometallurgy, 79(2005), No. 3-4, p. 172.
    [5]
    A.L. Salgado, A.M.O. Veloso, D.D. Pereira, G.S. Gontijo, A. Salum, and M.B. Mansur, Recovery of zinc and manganese from spent alkaline batteries by liquid-liquid extraction with Cyanex 272, J. Power Sources, 115(2003), No. 2, p. 367.
    [6]
    W.G. Lv, Z.H. Wang, H.B. Cao, Y. Sun, Y. Zhang, and Z. Sun, A critical review and analysis on the recycling of spent lithium-ion batteries, ACS Sustainable Chem. Eng., 6(2018), No. 2, p. 1504.
    [7]
    X.H. Zheng, Z.W. Zhu, X. Lin, Y. Zhang, Y. He, H.B. Cao, and Z. Sun, A mini-review on metal recycling from spent lithium ion batteries, Engineering, 4(2018), No. 3, p. 361.
    [8]
    Y. Shi, G. Chen, and Z. Chen, Effective regeneration of Li-CoO2 from spent lithium-ion batteries:a direct approach towards high-performance active particles, Green Chem., 20(2018), No. 4, p. 851.
    [9]
    M.K. Jha, A. Kumari, A.K. Jha, V. Kumar, J. Hait, and B.D. Pandey, Recovery of lithium and cobalt from waste lithium ion batteries of mobile phone, Waste Manage., 33(2013), No. 9, p. 1890.
    [10]
    R.C. Wang, Y.C. Lin, and S.H. Wu, A novel recovery process of metal values from the cathode active materials of the lithium-ion secondary batteries, Hydrometallurgy, 99(2009), No. 3-4, p. 194.
    [11]
    S.G. Zhu, W.Z. He, G.M. Li, X. Zhou, X.J. Zhang, and J.W. Huang, Recovery of Co and Li from spent lithium-ion batteries by combination method of acid leaching and chemical precipitation, Trans. Nonferrous Met. Soc. China, 22(2012), No. 9, p. 2274.
    [12]
    S. Saeki, J. Lee, Q. Zhang, and F. Saito, Co-grinding LiCoO2 with PVC and water leaching of metal chlorides formed in ground product, Int. J. Miner. Process., 74(2004), Suppl., p. S373.
    [13]
    F. He, R.L. Man, Q. Liu, Z.M. Sun, J. Xu, and J. Zhang, Kinetics of acid leaching cobalt from waste lithium-ion batteries using oat straw, Chin. J. Nonferrous Met., 25(2015), No. 4, p. 1103.
    [14]
    L. Chen, X.C. Tang, Y. Zhang, L.X. Li, Z.W. Zeng, and Y. Zhang, Process for the recovery of cobalt oxalate from spent lithium-ion batteries, Hydrometallurgy, 108(2011), No. 1-2, p. 80.
    [15]
    Y.X. Yan, J.L. Gao, J.P. Wu, and B. Li, Effects of inorganic and organic acids on heavy metals leaching in contaminated sediment,[in] Interdisciplinary Response to Mine Water Challenges, Sui, Sun & Wang, eds., China University of Mining and Technology Press, Xuzhou, 2014, p. 406.
    [16]
    M. Humar, F. Pohleven, and M. Šentjurc, Effect of oxalic, acetic acid, and ammonia on leaching of Cr and Cu from preserved wood, Wood Sci. Technol., 37(2004), No. 6, p. 463.
    [17]
    S. Yagi and D. Kunii, Studies on combustion of carbon particles in flames and fluidized beds, Symp. (Int.) Combust., 27(1955), No. 1, p. 231.
    [18]
    O. Levenspiel, Chemical Reaction Engineering, John Wiley & Sons, New Jersey, 1999.
    [19]
    C.H. Sun, L.P. Xu, X.P. Chen, T.Y. Qiu, and T. Zhou, Sustainable recovery of valuable metals from spent lithium-ion batteries using DL-malic acid:Leaching and kinetics aspect, Waste Manage. Res., 36(2018), No. 2, p. 113.
    [20]
    N. Othusitse and E. Muzenda, Predictive models of leaching processes:A critical review,[in] The 7th International Conference on Latest Trends in Engineering & Technology, Irene, Pretoria (South Africa), 2015, p. 136.
    [21]
    S.C. Bouffard and D.G. Dixon, Evaluation of kinetic and diffusion phenomena in cyanide leaching of crushed and run-of-mine gold ores, Hydrometallurgy, 86(2007), No. 1-2, p. 63.
    [22]
    F. Beolchini, M.P. Papini, L. Toro, M. Trifoni, and F. Vegliò, Acid leaching of manganiferous ores by sucrose:Kinetic modelling and related statistical analysis, Miner. Eng., 14(2001), No. 2, p. 175.
    [23]
    F.K. Crundwell and S.A. Godorr, A mathematical model of the leaching of gold in cyanide solutions, Hydrometallurgy, 44(1997), No. 1-2, p. 147.
    [24]
    K.C. Wanta, I. Perdana, and H.T.B.M. Petrus, Evaluation of shrinking core model in leaching process of Pomalaa nickel laterite using citric acid as leachant at atmospheric conditions, IOP Conf. Ser. Mater. Sci. Eng., 162(2016), No. 1, art. No. 012018.
    [25]
    W. Astuti, T. Hirajima, K. Sasaki, and N. Okibe, Kinetics of nickel extraction from Indonesian saprolitic ore by citric acid leaching under atmospheric pressure, Miner. Metall. Process., 32(2015), No. 3, p. 176.
    [26]
    N.S. Panina, A.N. Belyaev, and S.A. Simanova, Carboxylic acids and their anions. Acid and ligand properties, Russ. J. Gen. Chem., 72(2002), No. 1, p. 91.
    [27]
    J.N. van Niekerk and F.R.L. Schoening, The crystal structures of nickel acetate, Ni(CH3COO)2.4H2O, and cobalt acetate, Co(CH3COO)2.4H2O, Acta Crystallogr., 6(1953), No. 7, p. 609.
    [28]
    J.D. Donaldson and D. Beyersmann, Cobalt and cobalt compounds,[in] Ullmann's Encyclopedia of Industrial Chemistry, Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim, 2012, p. 467.
    [29]
    M. Eigen and R.G. Wilkins, The kinetics and mechanism of formation of metal complexes,[in] Mechanisms of Inorganic Reactions, Kleinberg et al., eds., American Chemical Society, Washington DC, 1965, p. 55.
    [30]
    H.S. Fogler, Elements of Reaction Engineering, Pearson Education Inc., New Jersey, 2006.
    [31]
    J.M. Smith, H.C. Van Ness, and M.M. Abbott, Introduction to Chemical Engineering Thermodynamics, Mc Graw-Hill, New York, 2005.
    [32]
    J.H. Li, P.X. Shi, Z.F. Wang, Y. Chen, and C.C. Chang, A combined recovery process of metals in spent lithium-ion batteries, Chemosphere, 77(2009), No. 8, p. 1132.
    [33]
    Don W. Green and Robert H. Perry, Perry's Chemical Engineers' Handbook, 8th ed., Mc Graw-Hill, New York, 2008.
    [34]
    M.J. Wang and A. Navrotsky, Enthalpy of formation of Li-NiO2, LiCoO2 and their solid solution, LiNi1-xCoxO2, Solid State Ionics, 166(2004), No. 1-2, p. 167.
    [35]
    G. Glockler, Bond energies and bond distances of hydrocarbons, J. Chem. Phys., 21(1953), No. 7, p. 1242.
    [36]
    J.P. Cyr, J. Dellacherie, and D. Balesdent, Standard data for the formation of solid cobaltous oxide, J. Chem. Eng. Data, 26(1981), No. 3, p. 319.
  • 加载中

Catalog

    通讯作者: 陈斌, bchen63@163.com
    • 1. 

      沈阳化工大学材料科学与工程学院 沈阳 110142

    1. 本站搜索
    2. 百度学术搜索
    3. 万方数据库搜索
    4. CNKI搜索

    Share Article

    Article Metrics

    Article Views(957) PDF Downloads(82) Cited by()
    Proportional views

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return