Metals and valuable metal compounds are important parts of our everyday lives with applications ranging from aluminum foil over circuit boards to high-performance alloys for engineering and buildings construction. Large-scale metal production processes provide access to metals contained in numerous naturally occurring ores, earths and minerals and should be considered one of the major drivers of industrialization, leading to a continuous increase in living standards. Thereby, metals are often present in the form of oxides or other compounds of low reactivity and high stability. This makes metal extraction an often energy-intensive, environmentally problematic endeavor, relying on high reaction temperatures around 1000 °C or aggressive, corrosive and toxic chemicals. A disruptive, new approach for more sustainable metal production could be ionometallurgy, i.e., metal extraction by means of ionic liquids (ILs) and deep eutectic solvents (DESs). ILs, per definition, are salts with a melting point below 100 °C, while DESs are eutectic mixtures of two or more reagents with a melting point below that of the individual components. Both classes of materials feature favorable properties, such as a good solubility for many inorganic salts. Ionometallurgy is a seemingly simple approach, dissolving metal oxides at moderate temperature in an IL or DES and subsequently either electrodepositing the respective metal or producing valuable metal compounds by downstream chemistry. This thesis elucidated the general feasibility of the direct ionometallurgical metal production from metal oxides in two betaine-based solvents, namely the IL betainium bis(trifluoromethylsulfonyl)imide ([Hbet][NTf2]) and a DES consisting of betaine hydrochloride, urea and glycerol in the molar ratio 1 : 4 : 2.5 ([Hbet]Cl/4U/2.5GLY). Initial solubility studies involved a broad screening of the reaction behavior of numerous metal oxides with different properties regarding the position of the metal in the periodic table, its oxidation state as well as the basicity of the oxide. Exploiting the Brønsted-acidic functional group of the betainium cation, metal oxide dissolution in this case follows the principle of an acid-base reaction. Correspondingly, [Hbet][NTf2] favors the dissolution of basic or amphoteric metal oxides, while acidic metal oxides remain unaffected. In-depth investigations were performed for the examples of copper, cobalt and aluminum and identified the metal oxide lattice energy, the crystal structure and the reaction temperature as well as complex stabilities of the metal ions as additional factors to influence the solubility. How additives can affect the reaction outcome in multiple ways was shown for the example of chloride. In the copper system, small amounts of chloride act catalytically, while larger concentrations not only decrease the reaction time but also exhibit a structure-directing effect. For cobalt oxides, chloride is assumed to be reaction-driving due to the high chloride affinity of cobalt(II). These results were supported by seven new crystal structures found in the course of these investigations. Thereby, for the first time, metal oxide dissolution in [Hbet][NTf2] was systematically investigated under water-poor conditions. Abstaining from aqueous IL solutions, although water was shown to promote metal oxide dissolution, enables access to several metals via electrodeposition. This is facilitated by the large electrochemical windows of [Hbet][NTf2] and [Hbet]Cl/4U/2.5GLY, amounting to −2.0–1.4 V and −2.3–0.9 V, respectively. Copper, cobalt, nickel, tin, lead, zinc, and small amounts of vanadium were shown to be electrochemically reducible, whereas manganese, molybdenum and aluminum could not be electrodeposited within the electrochemical stability range of the IL or DES. For the deposition of the noble metal copper, the chloride content, the deposition temperature and additional organic solvents were identified as crucial parameters for the deposition potential as well as the quality of the deposit. By copper-coating a steel plate, a potentially industrially relevant application was demonstrated. Compared to the conventional industrial process for copper production, this ionometallurgical approach could imply a significant simplification and proceed at much lower reaction temperatures. Starting from tenorite or oxidic copper waste, copper coatings could directly be producible avoiding multiple process steps. Furthermore, the cobalt system revealed, that the thorough understanding of the complex equilibria present in solution is crucial for the successful electrodeposition of the metal. Thus, no deposits were obtained when anionic [CoCl4]2– was the predominant cobalt complex species. The adjustment of the cobalt-to-chloride ratio is a suitable method to generate sufficient amounts of cationic cobalt complexes, allowing for the deposition of the metal. Overall, several metals were directly produced from their oxides by the ionometallurgical approach at temperatures below 175 ℃. This means a significant temperature reduction compared to the conventional processes. Encouragingly, [Hbet][NTf2] already showed first promising results when applied to industrially relevant starting materials, such as black mass for the recycling of lithium ion batteries or bauxite as a highly relevant, naturally occurring aluminum resource. While this qualifies ionometallurgy in principle as a considerable improvement regarding process sustainability, the impact of [Hbet][NTf2] and [Hbet]Cl/4U/2.5GLY was analyzed in more depth. Thereby, the recyclability of the solvents is considered a very important factor for the efficient implementation of ionometallurgy in larger scale. First experiments in a two-compartment electrochemical cell showed that metals can be electrodeposited cathodically with a tailorable anode reaction. The oxygen evolution reaction in an aqueous electrolyte proved as suitable benign oxidation reaction in the anode half cell. The intactness of [Hbet][NTf2] after metal electrodeposition in this set-up was evidenced by NMR spectroscopy, qualifying the IL for reuse in principle. As opposed to this, decomposition reactions were identified to take place in both the IL and the DES. At 175 °C, [Hbet][NTf2] undergoes the chloride-induced decomposition via a Hunsdieker and a Deacon reaction, which is avoidable by a lower reaction temperature of 150 °C. NMR studies suggest that [Hbet][NTf2] does not decompose during the ionometallurgical process at this temperature. However, in the case of [Hbet]Cl/4U/2.5GLY, NMR and mass spectrometric studies proved the degradation via several decomposition pathways at 60 °C already. These decomposition reactions change the composition of the DES, which also affects the solubility of metal oxides. The thermal and chemical stability of [Hbet][NTf2] and [Hbet]Cl/4U/2.5GLY, besides other factors, have direct implications for their consideration as green solvents. Thus, [Hbet][NTf2] should only be used at reaction temperatures below 150 °C. Furthermore, its industrial application might be impeded by the expensive and toxic [NTf2]– anion. While betaine-based solvents can be easily accessible due to the natural abundance of betaine, the synthesis effort of the [NTf2]– anion makes [Hbet][NTf2] a considerably expensive IL. [Hbet]Cl/4U/2.5GLY is cheaper and easier to be synthesized from naturally abundant substances, yet not a considerable option due to its decomposition at low temperature already. Its thermal and chemical instability pose hardly surmountable obstacles regarding the recycling and the toxicity of [Hbet]Cl/4U/2.5GLY. Thus, both [Hbet][NTf2] and [Hbet]Cl/4U/2.5GLY do not qualify as green solvents and more benign alternatives should be found in the future. Altogether, this thesis showed that the ionometallurgical production of metals from their oxides is possible and, moreover, could be a sustainable alternative to conventional processes. The presented investigations extend our understanding of metal oxide chemistry in ILs or DESs and provide proofs of concept, laying a foundation for further work that leaves numerous opportunities for ongoing exploration and optimization. Hence, ionometallurgy could be one step to face the urgent challenge of climate change.

Ionometallurgy is a new trend to utilise ionic liquids as alternative green solvents for oxidic and sulfidic copper minerals. It has broad potential for traditional pyrometallurgy and hydrometallurgy. Ionometallurgy utilises ionic liquids (ILs), highly potent complexing ligands (chloride), to process oxide and copper sulfide minerals. This work focused on using the deep eutectic solvents (DES) of ionic liquids, which and provide alternative options for processing various metals, alloys, and concentrates. For this job, various analytical methods were used to determine the copper concentrate and its residue after leaching (MLA-SEM and XRPD), quantify the elements in the solution (IC and ICP-OES/MS) and explain the oxidation behaviour (CV and UV-Vis spectroscopy). Combining the analytical and electrochemical methods to the leaching experiment provided the control to improve the results and understand its oxidation behaviour. Chosen DES, Oxaline (ChCl + oxalic acid, 1:1), and Ethaline (ChCl + ethylene glycol, 1:2) were tested and enhanced on the actual copper concentrates with and without oxidative additives (FeCl3 and I2). Those oxidative additives are selected for leaching experiments by their redox potential in Ethaline. However, there are many acceptable values; the most exciting result related to Ethaline plus iodine was the potential leaching system for chalcopyrite and copper-gold concentrates leaching. Because ion chromatography (IC) and UV-Vis’s analysis confirm iodine oxidizes the Cu+ species quickly in Ethaline. Whilst identical results and oxidation behaviour appeared in chalcocite (Cu2S), chalcopyrite (CuFeS2) and copper-gold concentrates leaching. During the iodine reduction to iodide in the system, IC proved that chalcopyrite releases the Fe3+, oxidizing the chalcopyrite particles. Also, iodine oxidized the natural gold in copper-gold concentrate successfully, and gold concentration quantified ICP-MS and MLA-SEM proved there is no visible gold in the leaching residue. Based on the optimal Ethaline + I2 leaching condition, the copper concentrate was carried out with the bottle roller leaching to represent the tank leaching. Thus, DES shows that it has a high potential to be continued to scale up the experiment. Also, water was given to the Ethaline leaching system, and water had a good influence on the leaching due to reducing the viscosity and saving the Ethaline amount. Hence Ethaline plus water is used for the copper ore leaching in the column, and it can be seen that Ethaline + I2 with water (up to 20%) has a high potential to process the low-grade copper sulfide ores.:Acknowledgements Abstract Abbreviations TABLE OF CONTENTS CHAPTER ONE – INTRODUCTION OF COPPER PROCESSING TECHNOLOGIES 1.1. Overview 1.2. Copper 1.3. Gold 1.4. Hydrometallurgy and pyrometallurgy of copper and gold 1.5. Current copper and gold concentrate processing methods 1.6. An alternative copper concentrate processing method Summary of chapter 1 CHAPTER TWO – FUNDAMENTALS FOR PROCESS DEVELOPING 2.1. Introduction 2.2. Effect of temperature and stirring in leaching 2.3. Analytical methods and experimental 2.4. Experimental for leaching 2.5. Discussion of experimental errors CHAPTER THREE: ANALYTICAL EXPERIMENTS FOR LEACHING 3.1. Introduction 3.2. Analysis of copper concentrate 3.3. Cyclic voltammetry 3.4. UV-Vis spectroscopy analysis of target metals 3.5. Metals solubility in DES 3.6. Summary and conclusions CHAPTER FOUR: FUNDAMENTAL LEACHING EXPERIMENT AND INITIAL INVESTIGATION 4.1. Introduction 4.2. Initial study and fundamental leaching experiments 4.3. Study of mineral oxidation 4.4. Deep eutectic solvents leaching 4.5. Chapter summary and conclusion CHAPTER FIVE: LEACHING OF MODEL SYSTEMS IN ETHALINE WITH OXIDATIVE ADDITIVES 5.1. Introduction 5.2. Iodine effect on Cu2S and CuS leaching in Ethaline 5.3. Ferric chloride effect on CuS and Cu2S leaching 5.4. Leaching of natural gold in Ethaline with the presence of iodine 5.5. Cyclic voltammetry investigation of Cu+/2+ sulfides in DES 5.6. Chapter summary and conclusion CHAPTER SIX: LEACHING OF COPPER-GOLD CONCENTRATES IN DES AND WITH OXIDATIVE ADDITIVES 6.1. Introduction 6.2. Effect of ferric chloride (FeCl3) 6.3. Effect of iodine (I2) 6.4. Electrochemical and spectroscopic analysis of copper-gold concentrate leachates 6.6. Chapter summary and conclusion CHAPTER SEVEN: OVERALL CONCLUSION AND FUTURE WORK 7.1. Overall conclusions 7.2. Recommendations for future research CHAPTER EIGHT: APPENDIX 8.1. Chemicals and materials 8.2. Appendix References