Electrolysis of Converter Matte in Molten CaCl2-NaCl

The electrolytic production of nickel-copper alloy by electrochemical reduction of converter matte in molten salt has been investigated. The sintered solid porous pellets of Ni 3 S 2 , Cu 2 S and converter matte were electrolyzed at a voltage of 3.0 V in molten CaCl 2 -NaCl under the protection of argon gas at 700˚C, respectively. The electro-reduction processes were investigated and the products were characterized. The results show that the molten salt electro-reduction process can be used to produce nickel, copper and nickel-copper alloy directly from Ni 3 S 2 , Cu 2 S and converter matte precursors in molten CaCl 2 -NaCl, respectively. CaS would be formed as the intermediate com-pound during the electro-reduction process, and then the formed CaS can be gradually decomposed and removed with the increase of the electrolysis time. The experimental results show that the molten salt electro-reduction process has the potential to be used for the reduction of sulfide minerals in molten CaCl 2 -NaCl.


Introduction
Nickel-copper alloy is a high-quality corrosion-resistant alloy with good corrosion resistance in seawater, acid, alkali and reducing gas atmosphere [1] [2] [3] [4] [5]. Nickel-copper alloy has high commercial value due to its excellent manufacturability and mechanical property. In the conventional smelting process for nickel-copper alloy production, pure nickel and copper metals should be processes.
So far, over 90% of the world's primary copper on the earth's crust is present in the form of copper sulfide minerals, and about 50% of the world's primary nickel production starts from nickel sulfide ores [6] [7] [8]. Meanwhile, most of the nickel sulfide ores are inevitably associated with copper sulfides [9] [10] [11]. In the traditional pyrometallurgical process, the sulfide ores are mined, reduced in size, and floated to produce nickel-and copper-rich concentrates. Then, the concentrates are smelted in flash smelter or electric furnace to produce nickel-copper matte. Subsequently, the nickel-copper matte is smelted and converted into converter matte, the converter matte is commonly dominated by nickel and copper sulfides with a small amount of iron sulfide. After that, the converter matte is separated into nickel concentrate and copper concentrate by flotation. Then, the nickel and copper concentrates are fabricated into Ni 3 S 2 and Cu 2 S anodes for the electrolysis in aqueous electrolyte to produce Ni and Cu, respectively [12] [13] [14]. It is obvious that the traditional process is complex. In addition, this process may also be suffered from the limited electrochemical window of the aqueous electrolyte and the large ohmic polarisation caused by the non-conducting sulfur deposited on the anode [15].
In recent years, a generic process for producing metals and alloys by direct electrochemical reduction of metal oxides or their mixtures has attracted worldwide attention [16]. Many efforts have been devoted to the direct reduction of metal oxides [17]- [25]. Actually, many metal sulfides are thermodynamically less stable than their oxide compounds [26]. Recently, some researchers have investigated the electro-reduction of sulfides in molten salts [6] [15] [27] [28]. Li et al. [27] investigated the electrolysis of MoS 2 in molten CaCl 2 . Chen et al. [28] examined the removal of S in liquid copper. Ge et al. [6] studied the electrochemical extraction of copper from copper sulfide in molten CaCl 2 -NaCl. Wang et al. [15] investigated the electrolysis of WS 2 to metal W in molten NaCl-KCl. However, these previous work generally focused on pure metal sulfides, the direct electrochemical reduction of sulfide minerals in molten salts needs more investigation.
In the present work, the electro-reduction process has been used to directly extract nickel-copper alloy from converter matte in molten CaCl 2 -NaCl at 700˚C. This work will show that the converter matte can be reduced to nickel-copper alloy in molten salts. The results generally suggest that the molten salt electro-reduction process is a promising process for the facile reduction of sulfide minerals in molten CaCl 2 -NaCl.   and Figure 1(f), respectively. It is observed that the phase with mazarine is determined as Cu 2 S and the phase with watchet is confirmed to be Ni 3 S 2 . In addition, the Ni 3 S 2 and Cu 2 S separated from the converter matte were also used as the starting cathode materials for comparison. The phase compositions of the Ni 3 S 2 and Cu 2 S are shown in Figure 1(c) and Figure 1(d), respectively. As shown in Figure 1(d), the Cu 2 S sample contains a small amount of Ni 3 S 2 and Cu 5 FeS 4 . The chemical compositions of these initial samples (Ni 3 S 2 , Cu 2 S and converter matte) used in the present study are listed in Table 1. The schematic diagram of the electrolytic cell used for the electro-reduction experiment is shown in Figure 2. The anhydrous CaCl 2 and NaCl were weighed and mixed at the molar ratio of 1:1. The CaCl 2 -NaCl mixture was filled in an alumina crucible (55 mm in diameter, 120 mm in height) and served as electrolyte. The converter matte was firstly ball-milled and screened to obtain homogenous powders with particle size below 75 μm. Then, about 1.0 g of the converter matte powder was pressed into pellet with a diameter 8 mm under a pressure of 10 MPa, the pressed pellet was sintered in argon gas at 400˚C for 2 h. Similar procedures were also used to fabricate the Ni 3 S 2 and Cu 2 S pellets. The sintered pellet was wrapped with thin stainless steel nets (pore size of 75 μm) and then attached to a Fe-Cr-Al wire (2 mm diameter) to form a cathode. A graphite rod (12 mm diameter) was used as an anode. The electrochemical experiments were controlled by using a BioLogic HCP-803 electrochemical workstation. Argon gas (99.99%) was used to maintain an inert atmosphere during electrolysis process.

Experimental
During the electrolysis process, sulphur in cathode may get ionized and transport to the anode, which may cause the precipitation of CaS [6].

Results and Discussion
The typical current-time curve recorded during the electrolysis process of Cu 2 S is presented in Figure 3  The XRD patterns of the Cu 2 S pellets after being reduced at 3.0 V and 700˚C for different times in molten CaCl 2 -NaCl are shown in Figure 3(b). It is seen that the phases of the sample obtained at 1 h include Cu, CaS and FeNi 3 . Moreover, with the increase of electrolysis time, the peak intensity of CaS decreases evidently. According to the XRD patterns shown in Figure 3(b), copper with a small amount of FeNi 3 obtained after being electrolyzed for more than 2 h at 3.0 V. According to the previous work [6], CaS has a low solubility in the salt melt and it will decompose into Ca 2+ and S 2− as electrolysis proceeds further. S 2− will transport to the anode and then oxidize to form elemental sulphur. The electrode reactions for Cu 2 S may be reasonably considered as: Anodic reaction: Cathodic reaction: Cu + + e -→ Cu (2) Figure 4 shows the SEM images of the Cu 2 S pellets after being electrolyzed for 5 h.   The products obtained at different electrolysis stages were characterized by using XRD. Figure 5(b) shows the XRD patterns of the Ni 3 S 2 pellets after being reduced at 3.0 V and 700˚C for different times in molten CaCl 2 -NaCl. The phases of the sample obtained at 1 h include Ni and CaS. Moreover, with the increase of electrolysis time, the peak intensity of CaS decreases evidently. Based on the result of the XRD analysis ( Figure 5(b)), it is suggested that the electrolysis process of Ni 3 S 2 is similar to the electrolysis process of Cu 2 S, and the reactions may be expressed as: Anodic reaction: S 2-→ 1/2S 2 (g) + 2e - Cathodic reaction: Ni 2+ + 2e -→ Ni (4) Figure 6 shows the SEM images of the Ni 3 S 2 pellet after being electrolyzed for 5 h. Figure 6(b) is the partial enlarged detail showing the particles of Figure   6(a). Obviously, after 5 h electrolysis, the particles presents a complicated structure. Although most of the particles are irregular strips, the dendritic crystals can also be found in Figure 6. The particle size of the obtained nickel is significantly larger than that of the copper obtained under the same electrolysis conditions. The current-time curve of the electrolysis process of converter matte is shown in Figure 7(a). Obviously, the current sharply drops within the first 20 min.
Then, the current decreases and reaches to a steady value at 2 h. In comparison with the current-time curves shown in Figure 3(a) and Figure 5(a), it can be seen that the current-time curve of the electrolysis of converter matte is different. In the initial reaction period, the shape of the current-time curve shown in Figure 7(a) is similar to that of the current-time curve shown in Figure 5(a).
The electrolysis process for the converter matte is mainly involved with the electro-reduction of Ni 3 S 2 and Cu 2 S. Therefore, after 1 h electrolysis, the shape of the    Anodic reaction: S 2-→ 1/2S 2 (g) + 2e - Cathodic reactions: Cu + + e -→ Cu (6) Ni 2+ + 2e -→ Ni (7) Ni + Cu → NiCu (8) Figure 8 shows the SEM images of converter matte pellet after being electrolyzed at 3.0 V and 700˚C for 5 h. Figure 8(b) is the partial enlarged detail showing the particles of Figure 8(a). After 5 h electrolysis, the pellet contains large interconnected particles. In comparison with the pure nickel and copper particles produced from Ni 3 S 2 and Cu 2 S pellets, the NiCu alloy particles are more uniform and dense ( Figure 8).
It should be noted that the electro-reduction process can produce sulphur element and NiCu alloy simultaneously. Considering there are several kinds of metals on the earth are present in the form of sulfides minerals, and the traditional extraction processes are complex. In addition, emission of SO 2 is also a difficult problem due to the increased environmental restrictions. Therefore, the molten salt electro-reduction process may provide a promising strategy for the sustainable reduction of sulfides minerals.

Conclusion
The molten salt electro-reduction process has been used to extract nickel-copper alloy from converter matte in molten CaCl 2 -NaCl. The results show that the sintered solid porous Cu 2 S, Ni 3 S 2 and converter matte pellets can be electrolyzed to copper, nickel and nickel-copper alloy under a voltage of 3.0 V at low temperature (approximately 700˚C), respectively. CaS would be formed as the intermediate product in the early electrolysis stage, and then CaS would be gradually