1. Introduction
The increasing demand for iron ore in the world causes the continuous exhaustion of mineral resources [
1]. High-grade iron ore resources are decreasing [
2]. Accordingly, many researchers are focused on the use of secondary sources of iron [
3,
4].
According to incomplete statistics, the annual discharge of cyanide tailings from Chinese gold smelting enterprises has exceeded 20 million tons [
5]. Based on the different cyanide leaching processes, cyanide tailings can be divided into heap leaching tailings, full mud cyanide tailings, concentrate cyanide tailings, oxidation roasting-cyanide tailings, etc. [
6]. Cyanide tailings often contain harmful substances such as cyanide and arsenic, which are harmful to the environment [
7,
8,
9]. Some scholars have conducted research on the harmlessness of cyanide tailings and achieved good results [
10,
11,
12,
13]. In addition, the proportion of oxidation roasting-cyanide tailings is relatively large, reaching more than 30% of the cyanide tailings. Chemical analysis shows that there is a large quantity of iron minerals in oxidation roasting-cyanide tailings (hereinafter referred to as “cyanide tailings”). The iron grade is often higher than 30%, and some are even higher than 45% [
14]. Therefore, cyanide tailings have great potential as an available secondary resource in iron recovery [
15,
16]. However, for technical and economic reasons, cyanide tailings are still mainly stored and currently only used as ingredients [
17,
18]. The storage of a large amount of cyanide tailings causes a great waste of resources [
19].
Phase analysis indicated that iron minerals in the cyanide tailings were mainly hematite. There was often more than 0.8% sulfur in the cyanide tailings, and sulfur was mainly in the form of sulfide. Studies have shown that the reduction roasting-magnetic separation technique is an effective method for treating cyanide tailings to recover iron [
20,
21,
22,
23,
24]. According to the different degree of reduction of iron minerals, the magnetic separation product can be divided into iron concentrate and reduced iron [
25,
26]. Some researchers have used the reduction roasting-magnetic separation process to treat the cyanide tailings and obtained iron concentrate with higher iron grades under optimal conditions [
27,
28,
29]. The thermodynamic reaction law of the iron-containing compound in the reduction roasting process of cyanide tailings was also revealed [
30]. Some scholars have obtained reduced iron products with an iron grade greater than 90% by the reduction roasting-magnetic separation process [
31,
32,
33,
34,
35]. However, the common problem is that the reduced iron products often contain higher sulfur. When reduced iron is used as a raw material for blast furnace ironmaking, almost all the sulfur will be concentrated in molten iron. Therefore, desulfurization is important for the effective utilization of high-sulfur cyanide tailings.
Researchers used calcium oxide or calcium carbonate as additives to carry out the study of iron extraction and sulfur reduction in cyanide tailings and found that adding CaO effectively improved iron reduction and decreased the sulfur content in reduced iron products [
36,
37,
38]. However, how CaO affects the gasification rate of the reducing agent has not been reported yet. Moreover, the phase transition law of sulfur during the reduction roasting of cyanide tailings remains unknown.
Therefore, in this work, the mechanism of CaO in reduction roasting was investigated using the CO and CO2 gas composition produced by the reaction, total reaction gasification rate, mineral composition and microstructure, distribution characteristics of sulfur, and intercalation relationship between iron particles and gangue minerals, for which the roasting temperature and time were 1150 °C and 40 min, and bituminous coal was 20 wt%. It is expected that the present research will provide theoretical guidance for desulfurization in treating high-sulfur cyanide tailings.
2. Materials and Methods
2.1. Cyanide Tailings
The cyanide tailings used in this study were sampled from a gold smelter (Shandong Province, China). The results of main chemical element/oxide analysis are shown in
Table 1. The total iron grade and sulfur grade of cyanide tailings are 48.05% and 1.05%, respectively. Cyanide tailings contain SiO
2 (20%), Al
2O
3 (5.38%), and Na
2O (3.48%), respectively. Iron is the main recycling valuable element. Sulfur may affect the quality of iron products. The results of X-ray diffraction (XRD) analysis (Rigaku Corporation, Akishima-shi, Japan) are presented in
Figure 1. Combined with microscope observation results and
Figure 1, cyanide tailings were mainly composed of hematite, magnetite, quartz, albite, potassium feldspar, and pyrite.
The results of a chemical-phase analysis of iron are shown in
Table 2. From
Table 2, iron mainly existed in the form of hematite and magnetite, with distributions of 92.48% and 3.27%, respectively. Iron in iron oxide was mainly recovered by reduction roasting-magnetic separation. The results of chemical-phase analysis of sulfur are shown in
Table 3. As shown in
Table 3, sulfur mainly existed in the form of pyrite, with a distribution of 96.23%.
2.2. Reductant and Additive
Bituminous coal was chosen as the reductant. The results of a bituminous coal industry analysis are presented in
Table 4. The additive calcium oxide (CaO) is chemically reagent grade from Sinopharm Group Chemical Reagent Co., Ltd (Shanghai, China).
2.3. Testing Method
The steps of reduction roasting-magnetic separation tests of cyanide tailings were as follows: (1) mixing; (2) reduction roasting; (3) grinding and magnetic separation; and (4) analysis. The process flowsheet is shown in
Figure 2. The specific operation process was as follows.
(1) Mixing. Cyanide tailings (40 g), bituminous coal (20 wt%), and a certain proportion of CaO were accurately weighed. The samples were fully mixed.
(2) Reduction roasting. The samples were loaded into the corundum crucibles (height of 80 mm and internal diameter of 77mm). The reduction roasting tests were carried out in the shaft furnace. When the furnace temperature rose to the preset reduction temperature of 1150 °C, 5 L·min−1 of N2 was introduced to remove the air in the shaft furnace. When the flue gas analyzer showed that the O2 in the furnace was zero, the corundum crucible was hung into the shaft furnace. Then, the N2 flow rate was reduced to 3 L·min−1. The volumetric concentration of CO and CO2 gas produced by the reaction was measured and recorded in real time by the flue gas analyzer. When the set reduction time was reached, the hanging corundum crucible was taken out, and the roasted products were cooled to room temperature.
(3) Grinding and magnetic separation. The grinding and magnetic separation process was two-stage grinding and two-stage magnetic separation. The first-stage grinding fineness was −0.074 mm 85% and the strength of magnetic field was 112 kA·m−1. The second-stage grinding fineness was −0.043 mm 80%, and the magnetic field strength was 96 kA·m−1. The main grinding and magnetic separation equipment used were a RK/BK three-roll four-tube smart rod mill and a CXG-99 magnetic separator (Tianjin Hualian Mining Instrument Co. Ltd., Tianjin, China). The resulting magnetic product was called powder direct reduced iron product, or “reduced iron” for short.
(4) Analyses. S and Fe grade in the roasted products and the reduced irons were examined by infrared absorption method and titrimetric method, respectively. The iron metallization degree was calculated according to Equation (1):
where η is the iron metallization degree (%), MFe is the mass content of metallic iron of the roasted products (%), and TFe is the total iron grade of the roasted products (%). A part of the roasted products was pulverized to −0.074 mm and analyzed by XRD (Rigaku D/Max 2500, Rigaku Corporation, Akishima-shi, Japan) and phase analysis of sulfur. The other part of the roasted products was made into polished sections for observing microstructure by SEM-EDS (Vega 3 XHU, Tescan Co. Ltd., Brno, Czech Republic). The microstructure of the reduced irons was also observed by SEM.
4. Conclusions
(1) The direct reduction reaction of cyanide tailings first produced CO2 gas and then started to produce CO. With the acceleration of the gasification reaction, the amount of CO produced was much greater than that of CO2. CaO increased the gasification rate of bituminous coal and promoted the reduction of iron minerals as well as the metallization rate of iron.
(2) In the absence of CaO, the sulfur minerals in the cyanide tailings were transformed into troilite, which were closely connected with iron particles and were difficult to remove by grinding and magnetic separation. With the addition of CaO, CaO preferentially reacted with active sulfur to form oldhamite, which inhibited the formation of troilite. There was a clear boundary between oldhamite and iron particles. Oldhamite was removed by grinding and magnetic separation.
(3) The addition of CaO improved the effect of reduction roasting-magnetic separation of cyanide tailings. Under the conditions of 20 wt% bituminous coal, 15 wt% CaO, 1150 °C reduction temperature, and 40 min reduction time, the reduced iron index of 90.68% iron grade, 0.06% sulfur grade, and 92.71% iron recovery rate was obtained. The reduced iron product can be used for subsequent steelmaking.