1. Introduction
Currently, one of the stages of aluminum production is refining, which allows the removal of metallic and non-metallic impurities from the liquid metal, including hydrogen, which causes porosity and thus deteriorates the mechanical properties of the material [
1,
2,
3]. In recent years, there has been a continuous development of techniques for introducing refining gas in the production process of high-grade aluminum. Starting with a single lance, a pile of lances with additional equipment, porous plugs, usually ended with rotors with graphite blades [
4,
5,
6]. Therefore, nowadays, the refining process is very often carried out in reactors with rotors through which refining gas is introduced, most often argon or a mixture of argon and chlorine. The essence of the process is the introduction of fine gas bubbles into the liquid metal, which simultaneously mix the metal and remove unnecessary gaseous and non-metallic impurities as a result of flotation [
7,
8,
9].
In recent years, the topic of aluminum refining has attracted many researchers. Most of the works focus on understanding the phenomena occurring during the process, which is possible thanks to the use of physical modeling [
10,
11,
12,
13,
14,
15]. More and more often, this modeling is supplemented and at the same time verified by numerical modeling [
16,
17,
18,
19,
20]. However, many studies are still based on experiments conducted directly under industrial conditions [
21,
22,
23,
24,
25]. An important topic is the durability of the rotor material. Various types of graphite are used as the material for the impeller and rotor shafts due to the ease of machining and non-wettability with metals. It is not without reason that graphite is used for elements of machines and rotors, because it is resistant to the refining gases used, i.e., chlorine, nitrogen and argon, as well as their mixtures and other aggregates. After immersion in a liquid metal bath, an element made of graphite is subjected to a rapid (fractional) temperature change from room temperature to several hundred degrees Celsius. At the same time, the rotor is exposed to cold refinery gases. Moreover, the very use of a rotor requires a high degree of strength, since the rotating gas distribution rotor heads are immersed in the melt during rotation. Therefore, one of the disadvantages of graphite as a material for rotors is its oxidation and erosion. Therefore, the paper presents test results for the same type of rotor with an impeller made of three different types of graphite. This type of research is unique, but many researchers are increasingly focusing on topics related to the durability and consumption of materials used in industry, although this type of research is not easy [
26,
27,
28].
2. Research Study and the Object
The refining process was carried out on the AlSi9Cu3(Fe) alloy using an FDU unit with a rotor. The AlSi9Cu3(Fe) alloy was obtained from secondary materials (scrap); therefore, after each series of experiments, the chemical composition was determined with using optical emission spectrometry—the average chemical composition within the standards is presented in
Table 1.
The research focused on the assessment of the refining efficiency at the FDU stand, as shown in
Figure 1a, with different degrees of wear of various types of graphite rotor, the scheme of which is shown in
Figure 1b with the characteristic dimensions marked.
Table 2 presents the processing parameters; additionally, three types of tested rotors, which differed in the material from which the rotor was made, are marked in it.
In the first case, it was classic graphite, in the second, it was fine-grained graphite, and in the third, it was classic graphite with SiC spraying.
Table 3 presents the basic parameters of these rotors, such as density, flexural strength and porosity. Rotors A1 and A2 are additionally impregnated with refractory material. This impregnation is to prevent the oxidation of the graphite, which should extend the service life of the FDU rotor. In the case of the A3 rotor, SiC refractory spraying was used instead of impregnation. The spray was applied to the entire surface of the shaft and impeller. Spraying is to prevent abrasive wear and oxidation of the graphite, which can extend the life of the FDU impeller.
The course of refining and the life of the rotors were assessed on the basis of the number of cycles at which a certain percentage of rotor wear is achieved. The achievement of individual stages or a specific degree of rotor wear was determined after consultation with the suppliers of individual rotors together with one of the local die-casting foundry company (for automotive), based on experience and internal regulations. Therefore, as part of the experiments, a series of tests was carried out for five cases (0% to 100% of consumption every 25%) corresponding to the cycles of the refining process. One cycle is 3 min of rotor operation. The wear values assigned to the respective cycles are summarized in
Table 4. The number of cycles corresponding to 100% wear of each rotor was determined by the manufacturer as 1,200. The number of cycles corresponding to the individual stages of rotor wear was derived from this value. However, due to the production possibilities, it was not feasible to adhere exactly to the specified number of cycles. Due to the loss of A1 rotor material and the operational safety, the tests were completed before 1200 cycles. Therefore, 100% wear of the A1 rotor corresponds to 1112 cycles.
All samples of experiments series 1/VT to 5/VT (0% to 100% wear) were selected to give an idea of the course and nature of refining efficiency. Selected series of experiments represent 144 melts, where we focused on the efficiency of melt refining during production within the following technological flow: AlSi9Cu3(Fe) alloy → STRIKO shaft furnace → FDU → UP maintenance furnace → die casting → ROCKER COVER.
In order to assess the efficiency of refining, alloy samples for the density index test were taken before (FDUs) and after refining (FDUe)—it gives possibility to evaluate visual stages of degassing—Dichte Index test (80 mbar).
Gasification is usually referred to as double weighing. The principle of the method is to compare the density of an alloy sample solidifying under atmospheric pressure with a sample solidifying under reduced pressure. The Sieverts law is applied here, according to which the solubility of hydrogen in the metal is lower under reduced pressure, and thus, more hydrogen bubbles are removed during solidification than at atmospheric pressure. The bubbles remain enclosed in the metal and thus reduce its density. A sample of the alloy to be assessed is taken from the melting furnace and poured into two test crucibles (metal, ceramic or sand mix—according to the manufacturer) with a volume of about 40–80 mL. One sample is allowed to solidify at atmospheric pressure, while the other is allowed to solidify under a defined vacuum in a vacuum chamber. The density of the sample solidified under atmospheric pressure
ρs atm and the sample solidified in vacuum
ρs vak is determined by weighing in air and after immersion in a beaker with water, using the principle of Archimedes’ law. The sample densities are calculated according to the general formula:
From the densities
ρs atm and
ρs vak, the density index known as Dichte Index (DI) is determined according to the formula:
The double weighing method is probably the most common and relatively accurate method in foundries today. The value of the DI in conventional castings is usually around a few percent. Modern instruments designed for this method only require weighing of the sample in air and immersed in water. The density is calculated automatically. The DI expresses the overall effect of the content of gases and oxide inclusions—that is, the actual tendency of an alloy to form bubbles.
3. Research Results and Discussion
Table 5 shows the results of rotor wear profile for all graphite types after the cycles listed in
Table 4. The wear of the A1 rotor after 25% of refining cycles is not high. Droplets of material appear on the rotor shaft but also on the impeller, but no reduction in the rotor material has been observed. After 50% of refining cycles, the dripping of the material is significantly greater, and the lower edge of the impeller has also decreased. After 75% of refining cycles, the material drips are significant, and the lower edge of the impeller has decreased significantly from the baseline. Throughout 100% of the refining cycles, the rotor is still operational, but the bottom edge is very negligible. Significant material infiltration was also observed on the shaft and baffle as well as on the impeller.
The wear of the A2 rotor after 25% of refining cycles is high compared to the A1rotor. Significant infiltration on the shaft and the impeller have been found; moreover, the lower edge of the impeller is significantly damaged and worn. After 50% of refining cycles, the rotor wear is close to 25% of refining cycles; only a reduction in the lower edge of the impeller was observed. After 75% of refining cycles, the material wear is significant, a significant material drip on the shaft and the rotor itself has been observed, and the lower edge of the impeller is already significantly worn. Unfortunately, the rotor did not survive the 100% refining cycles.
In the case of the A3 rotor, after 25% of refining cycles, a very high wear of the rotor material was observed, and the lower edge of the rotor is very worn (very thin), which proves its fast wear. The rotor made of this material did not withstand up to 50% of the refining cycles. This material was worn much faster than the A1 and even the A2 rotors.
A comparison of the CAD models of new rotors and 3D scans of the rotors in the final stage of operation revealed material losses during operational tests. The dimensional deviations from the original shape of the rotors are shown in
Figure 2. The rotor A1 shows a material loss of 36.9%. The maximum dimensional deviations of the rotor A1 reached the values of about 10 mm and are located on the underside of the impeller. Rotor A2 shows a material loss of 45.7%. The maximum deviations were around 25 mm and mainly occurred in the area of the blade recesses on the underside of the impeller. In the case of the A3 rotor, the material loss reached 28.8%. The maximum deviations from the original shape were about 25 mm and occurred in the area of the blade recess on one side of the impeller.
The Dichte Index (DI) values, as well as the density of samples solidified in vacuum, were determined from the results of the vacuum test of individual melts. Within the results, a comparison of the values of the Dichte Index (DI) at the beginning of the refining process (FDUstart) and at the end of the process (FDUend) is presented in
Figure 3 for rotors A1, A2 and A3.
The achieved results of the Dichte Index (DI) show that before the refining process, the melt shows an increased gas content for A1 rotor
and
for both series 1/VT and 5/VT (0% and 100% wear;
Figure 3a). As part of the refining process carried out in the FDU device, we observed a significant reduction in DI, which is evident from the achieved values:
and
, for both series 1/VT and 5/VT (0% and 100% wear;
Figure 3b). A similar behavior of the Dichte Index is observed for the A2 and A3 rotors. For the A2 rotor Dichte Index at the beginning of the refining, the following level is observed:
and
for series 1/VT and 4/VT (0% and 75% wear). At the end of refining, the Dichte Index values were the following:
and
for series 1/VT and 4/VT (0% and 75% wear). Whereas for the A3 rotor, the Dichte Index at the beginning of the refining was:
and
for series 1/VT and 2/VT (0% and 25% wear), and at the end of refining:
and
for series 1/VT and 2/VT (0% and 25% wear).
The results of the DI after the FDU treatment show a significant difference between the rotor showing 0% and 100% wear. With 0% wear of the rotor (series 1/VT), it can be concluded that the rotor contains moisture which is gradually released. With a 100% rotor wear (series 5/VT), it can be stated that even with such a high wear, the rotor achieves the lowest DI not only within the average values but also within the individual melts. These trends for DI are also seen in the density results of vacuum-solidified samples.
Figure 4 presents a summary of changes in the alloy density for the beginning and end of refining for the three tested rotors A1, A2 and A3.
In addition to determining the Dichte Index (DI) and the density of the vacuum solidified samples, the evaluation of the vacuum solidification tests was performed by visual cross-section evaluation. The most interesting series of heats were selected for testing, which always contained samples from the two heats that had the largest initial DI difference. For series 1/VT (rotor wear 0%) and 5/VT (rotor wear 100%), images of individual samples for the Dichte Index for rotor A1 are shown in
Figure 5; whereas for rotors A2 and A3, respectively, these images are shown in
Figure 6 and
Figure 7. The sampling point and the achieved Dichte Index are indicated in each image.
In the case of rotor A1, at the beginning of the refining process, significant porosity is observed in the entire sample volume. At the end of the refining cycle, the porosity is much less, but some gas bubble residues are still visible in some places in the sample (see
Figure 5a). Much better results are observed for 100% rotor wear, especially after completion of the refining cycle. There is practically no porosity in the sample volume; perhaps only a few tiny residual gas bubbles can be seen in the selected samples (see
Figure 5b). Similar conclusions can be applied to rotors A2 and A3.
As part of individual series of experiments, the melting point was also measured at the following technological sites: AM (After Melting), FDU
start, FDU
end and AR (After Refining). An evolution of temperature drop during die casting for each rotor is summarized in
Figure 8. The achieved temperature drops show the same trend, including places with the greatest heat loss, during processing at the FDU unit, when the melt temperature decreases by an average of 15.5 °C to 23.4 °C. The total temperature drop of AlSi9Cu3(Fe) during processing before casting into the holding furnace was 25.3 to 33.6 °C.