• International Journal of Technology (IJTech)
  • Vol 13, No 2 (2022)

Product Diffusion-Controlled Leaching of Nickel Laterite using Low Concentration Citric Acid Leachant at Atmospheric Condition

Product Diffusion-Controlled Leaching of Nickel Laterite using Low Concentration Citric Acid Leachant at Atmospheric Condition

Title: Product Diffusion-Controlled Leaching of Nickel Laterite using Low Concentration Citric Acid Leachant at Atmospheric Condition
Kevin Cleary Wanta, Widi Astuti, Himawan Tri Bayu Murti Petrus, Indra Perdana

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Wanta, K.C., Astuti, W., Petrus, H.T.B.M., Perdana, I., 2022. Product Diffusion-Controlled Leaching of Nickel Laterite using Low Concentration Citric Acid Leachant at Atmospheric Condition. International Journal of Technology. Volume 13(2), pp. 410-421

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Kevin Cleary Wanta -Department of Chemical Engineering, Faculty of Industrial Technology, Parahyangan Catholic University, Jl. Ciumbuleuit 94, Bandung, 40141, Indonesia - Department of Chemical Engineering, Faculty of
Widi Astuti Research Unit for Mineral Technology, National Research and Innovation Agency (BRIN), Jl. Ir. Sutami Km. 15, Tanjung Bintang, 35361, Indonesia
Himawan Tri Bayu Murti Petrus Department of Chemical Engineering, Faculty of Engineering, Universitas Gadjah Mada, Jl. Grafika 2, Bulaksumur, Yogyakarta, 55281, Indonesia
Indra Perdana Department of Chemical Engineering, Faculty of Engineering, Universitas Gadjah Mada, Jl. Grafika 2, Bulaksumur, Yogyakarta, 55281, Indonesia
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Abstract
Product Diffusion-Controlled Leaching of Nickel Laterite using Low Concentration Citric Acid Leachant at Atmospheric Condition

This work studies the leaching kinetics of nickel laterite in a citric acid solution. A new kinetics model that considers a reversible chemical reaction and internal diffusion of a product is proposed. The experiment was conducted at various temperatures (303, 333, and 358 K) and particle sizes (< 70 to 250 ?m). Whereas acid concentration, pulp density, and leaching time were constant at 0.1 M, 20% w/v, and 120 min, respectively. The experimental results showed that the leaching process was dependent on temperature and particle size. In the case of Ni, Al, and Fe leachings, the formation of complex molecules might lead to a steric hindrance of product diffusion; however, this was not observable for Mg. The proposed model was found to be much better than the conventional shrinking core models (SCM). Using the proposed model, the activation energy for nickel was found to be 121.38 ± 0.0324 kJ/mol, 78.98 ± 0.4157 kJ/mol, 1,022.62 ± 9.6507 J/mol for forward reaction, backward reaction, and diffusion, respectively.

Citric acid; Diffusion model; Leaching kinetics; Nickel laterite; Shrinking core model

Introduction

In extractive metallurgy, atmospheric pressure acid leaching (APAL) and bioleaching have been highlighted as options for recovering valuable metals, such as base metals and rare earth elements (Mirwan et al., 2017; Basuki et al., 2020; Trisnawati et al., 2020). These methods have been established and are ready for application on an industrial scale, especially if an intermediate product is preferable for further downstream applications (Rao et al., 2012; Ash et al., 2020). An in-depth study of leaching kinetics is essential to design process equipment for a better industrial-scale application.

        Most studies have shown that leaching or bioleaching process kinetics can be approached using the shrinking core model (SCM) (Ayanda et al., 2011; Abilash et al., 2013; Dong et al., 2017; Wang et al., 2017). The SCM is a kinetics model that explains the mechanism of heterogeneous processes, especially for solid-gas reactions (Amiri et al., 2014). The development of this model was mainly based on a single step that controls the process (Wanta et al., 2016). As a heterogeneous process, the leaching process might consist of a sequence of simultaneous steps. A different assumption might result in a different model, which generates the question of whether the model could explain the actual physical phenomenon. The most common models are derived on the assumption that the kinetics are controlled by the reaction and/or diffusion of the reactant entity (Su et al., 2010; Ayanda et al., 2011; Gharabaghi et al., 2012; Astuti et al., 2016; Mashifana et al., 2019); meanwhile, the limitation of the product entity is rarely explained. Some studies on the leaching process have used inorganic and organic leachates and shown inconsistent results, proving that SCMs would be insufficient to describe the corresponding physical phenomena (Mirwan et al., 2017; Setiawan et al., 2019; Wanta et al., 2020).
        The kinetics model of the leaching process has become of interest, as the resulting information can be used for further process development and scale-up purposes. In a leaching process that involves organic acid leachates, there are two unique and different conditions: (1) the formation of metal-organic complex compounds (ligand) (Zelenin, 2007; Jean–Soro et al., 2012; Guilpain et al., 2018), which have a larger molecule size than that of inorganic acid leachates, and (2) reversible reactions associated with acid dissociation and product formation (see Equations 1 and 4) (Zelenin, 2007; Simate et al., 2010; Behera et al., 2011; Horeh et al., 2016). These two conditions can cause the failure of the existing SCM to explain the kinetics of the leaching process, which involves organic acid leachates. This study focuses on developing an alternative and novel mathematical model to describe the kinetics of the leaching process in which organic acid (citric acid solution) is used as a leachate. This model involves the steps that most probably control the leaching process with organic acid leachates: 1) product molecule internal diffusion and 2) reversible chemical reactions. This model is called the product diffusion-controlled model.


Figure 1 Illustration of the leaching mechanism controlled by the chemical reaction and diffusion of product molecules

 

The product diffusion-controlled model is arranged according to the mechanism of the leaching process using organic acid (citric acid in this work), as illustrated in Figure 1. Reactant molecules (white spheres in Figure 1a) diffuse through particle pores from the main liquid body. Since the pore size is much larger compared to the reactant molecule diameter, molecular diffusion-type transport is assumed to prevail in the pores. Reactant molecules are then adsorbed into the interior surface to form the adsorbed species (black spheres in Figure 1b), which are always assumed to be in an equilibrium phase. Chemical reactions occur on the solid surface (Figure 1c), as shown in Equations 1–4 (Simate et al., 2010; Behera et al., 2011; Prihutami et al., 2021):


Element M in Equation 3 consists of other metal elements, such as Fe, Mg, Al, and so on.

In the case of complex compounds formed as products (black parallelograms in Figure 1c), the adsorbed product molecules will desorb to produce liquid-like free molecules in the pore system (Figure 1d). The concentration of the free molecules is assumed to always be in equilibrium with that of the adsorbed molecules. The equilibrium can be expressed as follows Equations 5:

                        

where H is a constant, xp is the concentration of the adsorbed product molecules (ppm), and Cp is the concentration of the free product molecules (ppm). The last step is the movement of product molecules (white parallelograms in Figure 1e) through the pores to the main liquid body. The movement is assumed to be due mainly to molecular diffusion.

In the present work, the proposed model was verified for the leaching of nickel laterite in a low concentration of citric acid. The leaching product of interest is a nickel compound. The development of the material balance for the leached nickel compound inside the solid particle results in Equations 6–8:

        where Cp is the concentration of a liquid-like nickel citrate in the pore channel, De is effective diffusivity, ? is porosity, xm is the concentration of the nickel in a solid phase, kr,1 is the reaction rate constant of the product side, kr,2 is the reaction rate constant of the reactant side, Nb is the amount of the particle, V is the volume of the solution, Rp is the particle radius, and Cp,l is the concentration of the nickel citrate in the liquid body. The equation is numerically solved with the initial and boundary conditions, as shown in the following Equations 9–11:


where xmo is the initial concentration of nickel in the solid phase. The low concentration of the citric acid solution used in this work allows the proposed model to be used for further application in the bioleaching process. The proposed model is expected to be more accurate for determining the kinetics parameters needed for further designing the scaled-up extractor.


Conclusion

This work presented a study to experimentally prove that the diffusion of products determines the rate of the leaching process of nickel laterite. In the case of leaching Ni, Al, and Fe from the mineral, the resulting products consisted of relatively large molecules, whose transport was sterically hindered in the pore channels. Meanwhile, leached Mg was present in ionic forms; hence, its transport through the pores did not determine the leaching process. The proposed mathematical model, considering the steps of reaction and transport of product molecules, was suitable for describing the Ni leaching process phenomenon. The model will be applicable to a similar process that incorporates large product molecules.

Acknowledgement

    The authors gratefully acknowledge the Department of Chemical Engineering, Universitas Gadjah Mada, for assistance with the sample analysis. In addition, the authors acknowledge Research Unit for Mineral Technology, National Research and Innovation Agency (BRIN) for providing samples and chemical analysis.

Supplementary Material
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R1-CE-4641-20211004093548.docx Docs File of Manuscript with Highlights and Annotations
References

Abilash, Mehta, K.D., Pandey, B.D., 2013. Bacterial Leaching Kinetics for Copper Dissolution from a Low-Grade Indian Chalcopyrite Ore. Metalurgia e Materials (Metallurgy and Materials), Volume 66(2), pp. 245–250

Agacayak, T., Zedef, V., Aras, A., 2016. Kinetic Study on Leaching of Nickel from Turkish Lateritic Ore in Nitric Acid Solution. Journal of Central South University, Volume 23, pp. 39–43

Amiri, A., Ingram, G.D., Maynard, N.E., Livk, I., Bekker, A.V., 2014. An Unreacted Shrinking Core Model for Calcination and Similar Solid–to–Gas Reactions. Chemical Engineering Communications, Volume 202(9), pp. 1161–1175

Ash, B., Nalajala, V.S., Popuri, A.K., Subbaiah, T., Minakshi, M., 2020. Perspectives on Nickel Hydroxide Electrodes Suitable for Rechargeable Batteries: Electrolytic vs. Chemical Synthesis Route. Nanomaterials, Volume 10(9), pp. 1–22

Astuti, W., Hirajima, T., Sasaki, K., Okibe, N., 2016. Comparison of Atmospheric Citric Acid Leaching Kinetics of Nickel from Different Indonesian Saprolitics Ores. Hydrometallurgy, Volume 161, pp. 138–151

Ayanda, O.S., Adekola, F.A., Baba, A.A., Fatoki, O.S., Ximba, B.J., 2011. Comparative Study of the Kinetics of Dissolution of Laterite in Some Acidic Media. Journal of Minerals & Materials Characterization & Engineering, Volume 10(15), pp. 1457–1472

Basuki, K.T., Rohmaniyyah, A., Pusparini, W.R., Saputra, A., 2020. Extraction Development for the Separation of Gadolinium from Yttrium and Dysprosium Concentrate in Nitric Acid Using Cyanex 572. International Journal of Technology, Volume 11(3), pp. 450–460

Behera, S.K., Panda, P.P., Singh, S., Pradhan, N., Sukla, L.B., Mishra, B.K., 2011. Study on Reaction Mechanism of Bioleaching of Nickel and Cobalt from Lateritic Chromite Overburdens. International Biodeterioration & Biodegradation, Volume 65, pp. 1035–1042

Callister, W.D., Rethwisch, D.G., 2015. Materials Science and Engineering. 9th Edition. USA: John Wiley & Sons

Dong, Y.-b., Li, H., Lin, H., Zhang, Y., 2017. Dissolution Characteristics of Sericite in Chalcopyrite Bioleaching and Its Effect on Copper Extraction. International Journal of Minerals, Metallurgy, and Materials, Volume 24(4), pp. 369–376

Gharabaghi, M., Irannajad, M., Azadmehr, A.R., 2012. Leaching Behavior of Cadmium from Hazardous Waste. Separation and Purification Technology, Volume 86, pp. 9–18

Girgin, ?., Obut, A., Üçyildiz, A., 2011. Dissolution Behaviour of a Turkish Lateritic Nickel Ore. Minerals Engineering, Volume 24(7), pp. 603–609

Guilpain M., Laubie, B., Zhang, X., Lorel J.L., Simonnot, M.-O., 2018. Speciation of Nickel Extracted from Hyperaccumulator Plants by Water Leaching. Hydrometallurgy, Volume 180, pp. 192–200

Horeh, N.B., Mousavi, S.M., Shojaosadati, S.A., 2016. Bioleaching of Valuable Metals from Spent Lithium-Ion Mobile Phone Batteries using Aspergillus niger. Journal of Power Sources, Volume 320, pp. 257–266

Ismail, S., Hussin, H., Hashi, S.F.S., Abdullah, N.S., 2016. Leaching and Kinetic Modeling of Malaysian Low-Grade Manganese Ore in Sulfuric Acids. Advanced Materials Research, Volume 1133, pp. 629–633

Jean–Soro, L., Bordas. F., Bollinger, J.-C., 2012. Column Leaching of Chromium and Nickel from a Contaminated Soil Using EDTA and Citric Acid. Environmental Pollution, Volume 164, pp. 175–181

Mashifana, T., Ntuli, F., Okonta, F., 2019. Leaching Kinetics on the Removal of Phosphorus from Waste Phosphogypsum by Application of Shrinking Core Model. South African Journal of Chemical Engineering, Volume 27, pp. 1–6

Mirwan, A., Susianto, Altway, A., Handogo, R., 2017. A Modified Shrinking Core Model for Leaching of Aluminum from Sludge Solid Waste of Drinking Water Treatment. International Journal of Technology, Volume 8(1), pp. 19–26

National Library of Medicine—National Center for Biotechnology Information, 2020. Nickel Citrate, Aluminium Citrate, Iron Citrate, Citric Acid. Available Online at https://pubchem.ncbi.nlm.nih.gov/, Accessed on May 5, 2020

Prihutami, P., Prasetya, A., Sediawan, W.B., Petrus, H.T.B.M., Anggara, F., 2021. Study on Rare Earth Elements Leaching from Magnetic Coal Fly Ash by Citric Acid. Journal of Sustainable Metallurgy, Volume 7, pp. 1241–1253

Rao, S.V., Dong, H.Y., Jeong, S.S., Kim, S.-K., 2012. Purification of Sulphate Leach Liquor of Spent Raneynickel Catalyst Containing Al and Ni by Solvent Extraction with Organophosphorus–Based Extractants. The Scientific World Journal, Volume 2012, pp. 1–5

Rezki, A.S., Sumardi, S., Astuti, W., Bendiyasa, I.M., Petrus, H.T.B.M, 2021. Molybdenum Extraction from Spent Catalyst Using Citric Acid: Characteristic and Kinetics Study. IOP Conf. Series: Earth and Environmental Science, Volume 830, pp. 1–10

Sahu, S., Kavuri, N.C., Kundu, M., 2011. Dissolution Kinetics of Nickel Laterite Ore using Different Secondary Metabolic Acids. Brazilian Journal of Chemical Engineering, Volume 28(2), pp. 251–258

Setiawan, H., Petrus, H.T.B.M., Perdana, I., 2019. Reaction Kinetics for Lithium and Cobalt Recovery from Spent Lithium-Ion Batteries using Acetic Acid. International Journal of Minerals, Metallurgy, and Materials, Volume 26(1), pp. 98–107

Simate, G.S., Ndlovu, S., Walubita, L.F., 2010. The Fungal and Chemolithotrophic Leaching of Nickel Laterites—Challenges and Opportunities. Hydrometallurgy, Volume 103, pp. 150–157

Su, H., Liu, H., Wang, F., Lü, X., Wen, Y., 2010. Kinetics of Reductive Leaching of Low–Grade Pyrolusite with Molasses Alcohol Wastewater in H2SO4. Chinese Journal of Chemical Engineering, Volume 18(5), pp. 730–735

Thubakgale, C.K., Mbaya, R.K.K., Kabongo, K., 2012. Leaching Behaviour of a Low–Grade South African Nickel Laterite. International Journal of Materials and Metallurgical Engineering, Volume 6(8), pp. 761–765

Trisnawati, I., Prameswara, G., Mulyono, P., Prasetya, A., Petrus, H.T.B.M., 2020. Sulfuric Acid Leaching of Heavy Rare Earth Elements (HREEs) from Indonesian Zircon Tailing. International Journal of Technology, Volume 11(4), pp. 804–816

Wang, Y., Jin, S., Lv, Y., Zhang, Y., Su, H., 2017. Hydrometallurgical Process and Kinetics of Leaching Manganese from Semi–Oxidized Manganese Ores with Sucrose. Minerals, Volume 7(27), pp. 1–13

Wanta, K.C., Astuti, W., Perdana, I., Petrus, H.T.B.M., 2020. Kinetic Study in Atmospheric Pressure Organic Acid Leaching: Shrinking Core Model. Minerals, Volume 10(7) pp. 1–10

Wanta, K.C., Perdana, I., Petrus, H.T.B.M., 2016. Evaluation of Shrinking Core Model in Leaching Process of Pomalaa Nickel Laterite Using Citric Acid as Leachate at Atmospheric Conditions. In: IOP Conference Series: Materials Science and Engineering, Volume 162, pp. 1–5

Zelenin, O.Y., 2007. Interaction of the Ni2+ Ion with Citric Acid in an Aqueous Solution. Russian Journal of Coordination Chemistry, Volume 33(5), pp. 346–350