Skip to main content
Materials logoLink to Materials
. 2024 Mar 8;17(6):1254. doi: 10.3390/ma17061254

Control of Aluminum and Titanium Contents in the Electroslag Remelting of ATI 718PlusTM Alloy

Lesong Li 1,2, Minqing Wang 1,2,3,*, Qintian Zhu 1,2,3,*, Xiaopeng Xu 1,2, Sifan Yu 1,2, Jian Zhang 3, Yang Zhou 3
Editor: Francesco Iacoviello
PMCID: PMC10972312  PMID: 38541408

Abstract

The burning loss of Al and Ti elements in superalloys during electroslag remelting has become a prevalent issue. And the existing slag system is not suitable for smelting the ATI 718PlusTM alloy. Therefore, it is imperative to develop a new slag system for smelting the ATI 718PlusTM alloy. To mitigate this issue, a thermodynamic model of the oxidation reaction of Al and Ti at the slag and alloy interface was established based on the ion and molecule coexistence theory (IMCT). The thermodynamic model was used to investigate the correlation between the equilibrium content of Al and Ti, slag composition, smelting temperature, and initial Al and Ti content of the electrode. The results indicate that while increasing the smelting temperature can effectively inhibit the burning loss of Al, it will exacerbate the burning loss of Ti. Increasing CaO and Al2O3 contents can inhibit the Al burning loss, while an increase in the TiO2 content can inhibit the Ti burning loss. Although an increase in the MgO content results in the burning loss of Al, its impact on the Al is minimal. The burning loss of Al and Ti was not affected by the change in the CaF2 content. The high Al content in ATI 718PlusTM makes it prone to burning loss of Al during the electroslag remelting. The combustion loss of Al can be reduced by increasing the Ti content in the electrode or adding a suitable amount of aluminum powder to the slag system. The accuracy of the model had been validated through experimental verification.

Keywords: ATI 718PlusTM, electroslag remelting, thermodynamic model, ion and molecule coexistence theory

1. Introduction

Superalloys refined by electroslag remelting have been widely used in aerospace, petrochemical, and other fields [1,2], so there are strict requirements on their properties. The principal components of the strengthening phase in superalloys are Al and Ti, and any alteration in the content of these elements within the alloy will have an impact on their high-temperature properties [3]. During the process of electroslag remelting, the Al and Ti elements react with unstable oxides, resulting in a loss of these elements due to burning, which has a significant impact on the quality of the electroslag ingot [4,5,6,7].

The primary approach to control the content of Al and Ti elements in superalloys during electroslag remelting is to minimize their interaction with the O element. The sources of the O element can be summarized as follows [8,9,10]: (1) the electroslag remelting is conducted in the ambient atmosphere, resulting in a reaction between oxygen and aluminum as well as titanium elements; (2) the electrode surface is not properly cleaned and contains impurities, such as FeO; (3) the slag system contains a small amount of SiO2; (4) the contents of Al2O3 and TiO2 in the slag are either excessive or insufficient. The primary factor among them is the irrational contents of Al2O3 and TiO2 in the slag. Therefore, it is imperative to investigate the impact of slag system constituents on the elements Al and Ti.

There have been reports regarding the control of Al and Ti in electroslag remelting. Pateishy [11] et al. studied the changes in Ti and Si contents during ESR and found that adding some TiO2 in slag could reduce the loss of Ti. Tan [12] et al. developed a thermodynamic model based on the ion and molecule coexistence theory, examining the impact of slag system components on the GH4065A alloy and identifying a slag system capable of inhibiting Al and Ti burning losses. Yang and Park [13] found that with increases in the reaction temperature, Ti was more easily oxidized than Al in nickel-based alloys. Therefore, more TiO2 should be added to the slag system at high temperatures. Jiang [14] et al. studied the relationship between the contents of Al, Ti, and Si in the GH8825 alloy and the content of CaO in the slag system and found that the higher the content of CaO in slag, the lower the loss of Ti via the reaction of Ti with the silica of the ESR slag. Duan [15] et al. systematically studied the effects of the slag composition and temperature on the contents of Al and Ti in the Inconel 718 alloy and found that the importance of factors for controlling the equilibrium Al content in the alloy was ordered as TiO2 > Al2O3 > CaO > CaF2 > MgO in ESR slags. In the research process, these scholars employed a methodology that integrates a thermodynamic model and experimental verification to derive effective measures for suppressing the combustion loss of Al and Ti elements.

Many scholars have established activity models suitable for different slag systems through experimental research, such as a regular solution model for molten slags [16], Temkin’s model [17], the ion and molecule coexistence theory model [18], and so on. The accuracy of the predictions made by many of these models is limited due to inherent limitations. The prerequisite for the application of the regular solution model for molten slag is to know the interaction energy between the cations of the components in the studied slag system. For a slag system with unknown interaction energy, it should be calculated based on test data [16]. The Temkin model only considers the most basic characteristics of slag, ignoring the difference in electrostatic potential when the ionic charge symbol is the same but the type and size are different, so the properties of the complete ionic solution are different from the actual slag [17]. The ion and molecule coexistence theory model obeys the law of mass action. Therefore, the known thermodynamic data, combined with the mass action law, can be used to predict the concentration of each structural unit in the slag system accurately [18]. Therefore, the ion and molecule coexistence theory model is utilized for constructing the thermodynamic model of the CaF2-CaO-MgO-Al2O3-TiO2 slag system.

The ATI 718PlusTM alloy possesses a specific Al/Ti, setting it apart from other alloys. A slight modification in the composition of Al + Ti and Al/Ti has a significant impact on the type and quantity of precipitated phases as well as the mechanical properties of the alloy. The endurance life and thermal stability of the alloy increase significantly when n(Al + Ti) = 4at%, with an n(Al)/n(Ti) increase from 1 to 4. The maximum value is attained when the Al/Ti equals 4 [19]. Therefore, it is crucial to control the Al and Ti contents during the ESR of the ATI 718PlusTM alloy. However, it is difficult to control the Al and Ti contents within a narrow range efficiently enough to meet the specific requirements for Al/Ti.

A thermodynamic model was developed based on the IMCT to describe the burning losses of Al and Ti elements in the ATI 718PlusTM alloy during electroslag remelting. The influence of the slag system components, smelting temperature, and electrode element content on the Al and Ti contents of the ATI 718PlusTM alloy were analyzed. The optimal slag system ratio for inhibiting the burning losses of Al and Ti elements has been determined. The model’s results have been validated through experimental verification.

2. Experimental

2.1. The Creation of a Thermodynamic Model

Firstly, the structural units of the slag system are determined by consulting the phase diagrams of the slag system. The relevant equations are then listed based on the principles of chemical equilibrium and mass conservation, followed by establishing a calculation model to determine the activity of each structural unit in the slag system. The activity of each structural unit of the slag system under different compositions and temperatures can be calculated by solving the equation with Matlab 2020a [20].

2.2. The Experiment on the Balance of Slag Alloy

The ATI 718PlusTM alloy produced via vacuum induction melting was used in this experiment. The composition of the remelting slag was CaF2-CaO-MgO-Al2O3-TiO2. The schematic diagram of the experimental resistance furnace is depicted in Figure 1.

Figure 1.

Figure 1

Schematic diagram of a resistance furnace.

The first step involves placing 500 g of the alloy and 60 g of slag into a ZrO2 crucible, which is lined with a 0.2 mm thick molybdenum sheet. Then, the ZrO2 crucible should be placed inside the graphite crucible to prevent the liquid metal leakage under elevated temperature conditions. After placing the graphite crucible inside the resistance furnace, initiate the power supply of the resistance furnace and increase the temperature to 1873 K at a rate of 10 K/min. Maintain this temperature for a duration of 60 min, subsequent to which, turn off the power and permit the furnace to cool down to the ambient temperature. During the whole experiment, the resistance furnace is injected with argon gas at a flow rate of 5 L/min to prevent the reaction between oxygen and the liquid metal.

After the reaction between slag and the alloy, the electroslag ingot was axially sampled using the wire cutting method. Then, the Al and Ti element contents in the electroslag ingot were determined using inductively coupled plasma atomic emission spectrometry (ICP-AES).

3. Thermodynamic Model

During the electroslag remelting of the ATI 718PlusTM alloy, when the electrode is in contact with the slag pool, the Al in the alloy reacts with the unstable TiO2 in the slag. The reaction is represented as Equation (1) [11].

4[Al] + 3[TiO2] ⇋ 3[Ti] + 2[Al2O3] (1)
log10Ki=log10aAl2O32aTi3aTiO23aAl4=log10aAl2O32aTiO23+log10fTi3w([Ti])3fAl4w([Al])4=35,300T9.94 (2)

In the above Equation (2), Ki is the equilibrium constant for the reaction shown in Equation (1); aAl2O3 and aTiO2 are the activities of Al2O3 and TiO2 in the slag; aAl and aTi are the activities of Al and Ti; fAl and fTi are the Henrian activity coefficients for Al and Ti; wi is the mass fraction of element i in the metal; and T is the absolute temperature.

The activity of alloying elements is calculated as follows:

log10fi=(eijwj) (3)
ai=fiwi (4)

In the above Equation (3), eij is the activity coefficient of the alloying component element j on element i.

Table 1 shows the chemical composition of the ATI 718PlusTM alloy used for developing the model. The S2059 slag system is selected as the base slag system, the composition of which is listed in Table 2. And Table 3 shows the activity interaction coefficient.

Table 1.

Chemical composition of ATI 718PlusTM alloy (mass fraction).

Nb Cr Ni Al Ti Mo
5.50 18.00 51.93 1.59 0.81 2.69

Table 2.

Composition of base slag system (mass fraction).

Slag CaF2 CaO Al2O3 MgO TiO2
S2059 50 20 22 5 3

Table 3.

Activity interaction coefficients in nickel-based alloy melts in the present work [21,22,23].

eji Mn Cr Ni Al Ti Mo
Al 0.034 0.045 −0.0376 0.0800
Ti −0.12 0.025 −0.0166 0.0561 0.016

A phase diagram of the CaF2-CaO-MgO-Al2O3-TiO2 slag system reveals its 21 structural units, including four ions (Ca2+, Mg2+, F2−, and O2−), two simple molecules (Al2O3 and TiO2), and 15 complex molecules, such as 11CaO·7Al2O3·CaF2. Table 4 lists their molar number and mass action concentration, while Table 5 shows the chemical equations regarding the formation of complex molecules and their Gibbs free energies.

Table 4.

Molar number and mass action concentration of structural units in 100 g CaF2-CaO-MgO-Al2O3-TiO2 slag system based on IMCT [24,25].

Items Structural Unit Serial Number Moles of Structural Units n/mol Mass Action Concentration of Structural Units Ni
Ions Ca2++2F2 1 n1=nCa2+,CaF2=2nF,CaF2 N1=3n1niNCaF2
Ca2++O2 2 n2=nCa2+,CaO=nO2,CaO N2=2n2niNCaO
Mg2++O2 3 n3=nMg2+,MgO=nO2,MgO N3=2n3niNMgO
Molecules, composite molecules Al2O3 4 n4=nAl2O3 N4=n4niNAl2O3
TiO2 5 n5=nTiO2 N5=n5niNTiO2
CaO·Al2O3 c1 nc1=nCaO·Al2O3 Nc1=nc1niNCaO·Al2O3
MgO·Al2O3 c2 nc2=nMgO·Al2O3 Nc2=nc2niNMgO·Al2O3
3CaO·Al2O3 c3 nc3=n3CaO·Al2O3 Nc3=nc3niN3CaO·Al2O3
12CaO·7Al2O3 c4 nc4=n12CaO·7Al2O3 Nc4=nc4niN12CaO·7Al2O3
CaO·2Al2O3 c5 nc5=nCaO·2Al2O3 Nc5=nc5niNCaO·2Al2O3
CaO·6Al2O3 c6 nc6=nCaO·6Al2O3 Nc6=nc6niNCaO·6Al2O3
CaO·TiO2 c7 nc7=nCaO·TiO2 Nc7=nc7niNCaO·TiO2
3CaO·2TiO2 c8 nc8=n3CaO·2TiO2 Nc8=nc8niN3CaO·2TiO2
4CaO·3TiO2 c9 nc9=n4CaO·3TiO2 Nc9=nc9niN4CaO·3TiO2
Al2O3·TiO2 c10 nc10=nAl2O3·TiO2 Nc10=nc10niNAl2O3·TiO2
MgO·TiO2 c11 nc11=nMgO·TiO2 Nc11=nc11niNMgO·TiO2
MgO·2TiO2 c12 nc12=nMgO·2TiO2 Nc12=nc12niNMgO·2TiO2
2MgO·TiO2 c13 nc13=n2MgO·TiO2 Nc13=nc13niN2MgO·TiO2
3CaO·3Al2O3·CaF2 c14 nc14=n3CaO·3Al2O3·CaF2 Nc14=nc14niN3CaO·3Al2O3·CaF2
11CaO·7Al2O3·CaF2 c15 nc15=n11CaO·7Al2O3·CaF2 Nc15=nc15niN11CaO·7Al2O3·CaF2

Table 5.

Chemical reaction formulae of possible composite molecules formed in 100 g CaF2-CaO-MgO-Al2O3-TiO2 five-membered slag system [26,27].

Chemical Equation Giθ/J·mol1 Ni
Ca2++O2+Al2O3=CaO·Al2O3 5941359.413T Nc1=Kc1N2N4
Mg2++O2+Al2O3=MgO·Al2O3 188286.276T Nc2=Kc2N3N4
3Ca2++O2+Al2O3=3CaO·Al2O3 2175729.288T Nc3=Kc3N23N4
12Ca2++O2+7Al2O3=12CaO·7Al2O3 617977612.119T Nc4=Kc4N212N47
Ca2++O2+2Al2O3=CaO·2Al2O3 1673625.522T Nc5=Kc5N2N42
Ca2++O2+6Al2O3=CaO·6Al2O3 2259431.798T Nc6=Kc6N2N46
Ca2++O2+TiO2=CaO·TiO2 799003.35T Nc7=Kc7N2N5
3Ca2++O2+2TiO2=3CaO·2TiO2 20710011.35T Nc8=Kc8N23N52
4Ca2++O2+3TiO2=4CaO·3TiO2 29288017.573T Nc9=Kc9N24N53
Al2O3+TiO2=Al2O3·TiO2 25270+3.924T Nc10=Kc10N4N5
Mg2++O2+TiO2=MgO·TiO2 26400+3.14T Nc11=Kc11N3N5
Mg2++O2+2TiO2=MgO·2TiO2 27600+0.63T Nc12=Kc12N52N3
2Mg2++O2+TiO2=2MgO·TiO2 25500+1.26T Nc13=Kc13N5N32
3Ca2++O2+3Al2O3+Ca2++2F=3CaO·3Al2O3·CaF2 4449273.15T Nc14=Kc14N1N23N43
11Ca2++O2+7Al2O3+Ca2++2F=11CaO·7Al2O3·CaF2 228760155.8T Nc15=Kc15N1N211N47

The chemical reaction of each component in the slag system follows the law of the conservation of mass. The molar fractions of each oxide in the slag system are denoted as b1 = nCaF2, b2 = nCaO, b3 = nMgO, b4 = nAl2O3, and b5 = nTiO2, and the total molar fraction is Σni. The ratio of the amount of substance ni of each structural unit in the slag system at reaction equilibrium to the total amount of substance Σni yields the mass action concentration Ni of each structural unit in the slag system. The mass action concentration refers to the concentration of a structural unit in a metallurgical melt that is subject to the law of mass action. The mass action concentration and activity are the same for pure matter as the standard state [28]. Therefore, as a description of the ion and molecule coexistence theory, the mass conservation equation was established in Equations (5)–(10); the nonlinear equations were then solved using MATLAB 2020a to obtain the mass action concentration of each structural unit.

N1+N2+N3+N4+N5+Nc1+Nc2+Nc3+Nc4+Nc5+Nc6+Nc7+Nc8+Nc9+Nc10+Nc11+Nc12+Nc13+Nc14+Nc15=Ni=1 (5)
b1=13N1+Nc14+Nc15ni=nCaF2 (6)
b2=0.5N2+Nc1+3Nc3+12Nc4+Nc5+Nc6+Nc7+3Nc8+4Nc9+3Nc14+11Nc15ni=nCaO (7)
b3=0.5N3+Nc2+Nc11+Nc12+2Nc13ni=nMgO (8)
b4=N4+Nc1+Nc2+Nc3+7Nc4+2Nc5+6Nc6+Nc10+3Nc14+7Nc15ni=nAl2O3 (9)
b5=N5+Nc7+2Nc8+3Nc9+Nc10+Nc11+2Nc12+Nc13ni=nTiO2 (10)

The relation between the equilibrium contents of Al and Ti in the ATI 718PlusTM alloy and the slag system components, smelting temperature, and initial alloying elemental contents is obtained from Equation (2); this relation is shown for Al and Ti as Equations (11) and (12), respectively.

Log10wAl=14log10aAl2O32aTiO234log10fAl+3log10fTi+3log10wTi35300T9.94 (11)
log10wTi=13log10aTiO23aAl2O32+4log10fAl3log10fTi+4log10wAl+35300T9.94 (12)

The equilibrium Al and Ti contents are directly related to the activity of Al2O3 and TiO2, the smelting temperature, the initial Al and Ti contents of the alloy, and the activity in the slag. However, the equation does not depict the relationship between them and CaF2, CaO, and MgO in the slag. Therefore, it is necessary to analyze the influence of other components on the equilibrium content of Al and Ti elements in the slag system through theoretical calculations.

4. Results and Discussion

4.1. The Influence of Smelting Temperature on the Equilibrium Contents of Al and Ti

The temperatures at the electroslag remelting electrode, droplet, and molten bath are believed to be 1750 K, 1948 K, and 1948 K, respectively; the temperature of the slag–alloy interface is 1950 K, according to Mitchell [29]. Therefore, this paper selects five temperatures for research: 1773 K, 1823 K, 1873 K, 1923 K, and 1973 K.

The influence of the smelting temperature on the equilibrium contents of Al and Ti when the composition of slag system components remains constant is illustrated in Figure 2. The figure demonstrates that an increase in the smelting temperature impedes the burning loss of Al, while a decrease in the smelting temperature hampers the burning loss of Ti. This phenomenon is consistent with the results of Shen et al. [30]. They point out that with temperature increases in a constant slag composition, the Ti content decreases drastically and the Al content increases.

Figure 2.

Figure 2

Relationship between equilibrium Al and Ti content and smelting temperature.

The activity of Al2O3 and TiO2 increases with the rise in smelting temperature, while lgaAl2O32/aTiO23 exhibits a continuous decrease. This indicates that the content of TiO2 in the slag system increases after the chemical reaction. The reverse reaction of Equation (1) occurs at elevated temperatures, leading to an enhanced generation of Al elements and consequently an increase in the equilibrium Al content. A reduction in the smelting temperature, on the contrary, promotes the forward reaction in Equation (1) to enhance the production of Ti elements.

The minimum Al content of the ATI 718PlusTM alloy is 1.2. According to the theoretical calculation results, when the melting temperature is lower than 1873 K, the burning loss of the Al element occurs easily. In order to ensure the properties of the alloy, the set temperature of electroslag remelting should not be lower than 1923 K.

4.2. The Influence of Components in the Slag System on the Equilibrium Contents of Al and Ti

The relationship between the components of the slag system and the equilibrium contents of Al and Ti is investigated at a smelting temperature of 1973 K. The relationship between the content of Al and slag system components is illustrated in Figure 3. Similarly, Figure 4 illustrates the relationship between the content of Ti and slag system components. It is necessary to keep the proportional fractions of the contents of several other components in the slag constant when calculating the effect of one component of the slag system on the equilibrium Al and Ti contents. Take CaO as an example: when exploring the effect of CaO on the equilibrium Al and Ti content, the slag system group element mass fraction changes to CaF2:CaO:Al2O3:MgO:TiO2 = 50:XCaO:22:5:3, i.e., when the CaO mass fraction changes to 21%, the CaF2 mass fraction subsequently changes to 79 × 50/80 = 49.375%, and the other group element changes are also the same.

Figure 3.

Figure 3

Figure 3

Relationship between equilibrium Al content and slag system component content.

Figure 4.

Figure 4

Figure 4

Relationship between equilibrium Ti content and slag system component content.

An increase in Al2O3 content, as depicted in Figure 3, leads to a significant rise in the equilibrium Al content. This can be attributed to the fact that Al2O3 consumes a substantial amount of Ti in the electrode, resulting in an increased generation of Al. Although excessive amounts of Al2O3 can increase the Al content in the electroslag ingot, it will result in the burning of Ti.

The content of the Al element increases with increases in the CaO content. This phenomenon can be attributed to the formation of complex molecules, such as CaO·TiO2, 3CaO·2TiO2, and 4CaO·3TiO2, due to the increased content of CaO. Consequently, the reaction between TiO2 and Al is reduced. However, when the CaO content is increased from 1% to 30%, the ratio of Al2O3 and TiO2 activities in the slag initially increases and then decreases. Moreover, when the mass fraction of CaO is 30%, the ratio of activities between Al2O3 and TiO2 is higher than that at a CaO mass fraction of 1%, indicating an increased degree of reaction between Ti and Al2O3, which results in an increase in the Al content in the electroslag ingot. Similarly, in Figure 4, the equilibrium Ti content decreases as the CaO and Al2O3 contents increase. This phenomenon is consistent with the results of Jiang et al. [14]. Their study concluded that the high CaO content in CaF2-CaO-Al2O3-MgO-TiO2-SiO2 slag can prevent the oxidation of Al in the GH8825 alloy.

The equilibrium Al content decreases with increases in the TiO2 content. However, the equilibrium Ti content increases with an increasing TiO2 content. This is because Equation (1) proceeds to the left of the reaction, increasing the Ti content by consuming more Al. However, an excessive TiO2 content will increase the Ti content and cause burning of Al.

As the MgO content increases, the equilibrium Al content decreases but remains higher than that of the initial electrode at a temperature of 1973 K. This is because Al reacts with MgO at high temperatures [31]: 2Al + 3MgO ⇋ 3Mg + Al2O3. However, the amount of the Al element consumed by MgO is little. Consequently, adjusting the MgO content allows for control over the Mg content in electroslag ingots. Similarly, increases in the MgO content result in a continuous rise in log10aTiO23aAl2O32, which promotes the forward reaction 4Al + 3TiO2 ⇋ 3Ti + 2Al2O3 and consequently enhances the equilibrium Ti content. The inhibitory effect of the MgO content on the combustion of Al and Ti is the same as that obtained by Duan [15] et al.

CaF2 has little effect on the equilibrium Al content and does not cause any burning loss of Al when changing the slag composition. And CaF2 has very little impact on Ti.

Thus, adjusting the contents of MgO and CaF2 can modify the physical properties of a slag system. And the Mg content in an electroslag ingot can be adjusted by adjusting the MgO content.

4.3. The Influence of the Initial Al and Ti Content in the Electrode on the Equilibrium Al and Ti Content of the Alloy

The content of Al and Ti elements in the initial electrode will also have an impact on the Al and Ti element contents of the electroslag ingot, in addition to factors such as slag system components and the smelting temperature. Therefore, the influence of the Al and Ti contents of the ATI 718PlusTM alloy electrode on the equilibrium contents of Al and Ti in the electroslag ingot was studied.

Six different initial contents within the specified range of the Al and Ti elements of the ATI 718PlusTM alloy were selected for this analysis at 1973 K. The effect of the slag system composition on the equilibrium Al content at varying initial Ti contents is shown in Figure 5. When the content of slag system components is constant, the equilibrium Al content increases with an increasing initial Ti content. This is because as the Ti content increases, its activity in the alloy strengthens, leading to a stronger reaction with Al2O3 in the slag and generating more Al contents. Thus, the burning loss of the Al element is inhibited. Similarly, as shown in Figure 6, the equilibrium Ti content increases with an increasing Al content in the alloy. The comparison of Figure 5 and Figure 6 reveals that the initial Ti content has a more significant influence on the equilibrium Al content of the alloy.

Figure 5.

Figure 5

Relationship between equilibrium Al with different initial Ti contents.

Figure 6.

Figure 6

Relationship between equilibrium Ti with different initial Al contents.

The ATI 718PlusTM alloy is a high-Al and low-Ti superalloy that is more likely to produce the “burning Al increases Ti” phenomenon in the ESR. Therefore, for ensuring alloy performance stability and reducing the Al burning loss, either the Ti content in the electrode can be appropriately increased or an appropriate amount of Al powder can be added to the slag system.

4.4. Validation of Thermodynamic Model

Based on the theoretical calculations, the smelting temperature was elevated and adjustments were made to the content of each component in the slag system. The slag–alloy balance experiment was conducted using the adjusted slag system, and the smelting outcome was compared to that of the S2059 slag system. The electroslag ingot was sampled and analyzed after the experiment. The sampling diagram of the electroslag ingot is shown in Figure 7.

Figure 7.

Figure 7

The sampling diagram of electroslag ingot.

In order to verify whether the thermodynamic model is consistent with the experimental results, Equation (2) could be changed to Equation (13). The relationship between log10(XTiO23/XAl2O32) and log10(wTi3/w[Al]4) can be obtained from the slag–alloy equilibrium test results and the interaction concentration of the slag system components calculated by the model. As shown in Figure 8, the experimental results are in good agreement with the model calculation, indicating that the established thermodynamic model is reasonable.

log10XTiO23XAl2O32=log10wTi3w[Al]4+log10fTi3*γAl2O32fAl4*γTiO2335,300T+9.94 (13)
γi=NiXi (14)

Figure 8.

Figure 8

Dependence of the log10(XTiO23/XAl2O32) on log10([Ti]3/[Al]4).

In the above Equations (13) and (14), γTiO2 and γAl2O3 express the activity coefficients of TiO2 and Al2O3 in slag and XTiO2 and XAl2O3 express the mole fractions of TiO2 and Al2O3 in slag.

The distribution of Al and Ti elements in the electroslag ingot is illustrated in Figure 9 shows that the fluctuation ranges of Ti and Al contents are 0.01% and 0.02%, respectively, indicating that the precise control of Al and Ti contents has been preliminarily achieved in the ESR of the ATI 718PlusTM alloy. Compared with the smelting results of the S2059 slag system, the distribution of Al and Ti elements along the axial direction of the electroslag ingot is uniform. In the beginning of smelting with the S2059 slag, the occurrence of “burning Al increases Ti” is observed. Due to the high TiO2 content in the S2059 slag system, a significant consumption of aluminum takes place during the initial smelting phase, resulting in an increased production of titanium. As smelting progresses and a portion of TiO2 in the slag becomes depleted, Equation (1) reaches a dynamic state.

Figure 9.

Figure 9

Distribution of elemental contents of Al and Ti in axial direction in electroslag ingot of ATI 718PlusTM alloy: (a) w(Al)/%; (b) w(Ti)/%.

5. Conclusions

Herein, the influence of the slag system components, smelting temperature, and electrode element content on the Al and Ti contents of the ATI 718PlusTM alloy were analyzed by developing a thermodynamic model. The main conclusions obtained from the study are as follows:

  1. Increases in the smelting temperature can effectively inhibit the burning loss of the Al element, while decreases in the smelting temperature can effectively inhibit the burning loss of the Ti element. In the electroslag remelting of the ATI 718PlusTM alloy, it is necessary to appropriately increase the smelting temperature. The set temperature of electroslag remelting should not be lower than 1923 K.

  2. Increasing the Al2O3 and CaO contents and decreasing the TiO2 and MgO contents in slag can inhibit the burning loss of Al; on the contrary, it can inhibit the burning loss of Ti. Varying CaF2 contents had little effect on the equilibrium content of Al and Ti contents; varying the MgO content could adjust the Mg content in the ATI 718PlusTM alloy.

  3. The initial Ti content of the electrode has a more significant influence on the equilibrium Al content of the alloy. Appropriately increasing the Ti content in the ATI 718PlusTM alloy or adding Al powder to the slag can inhibit the burning loss of Al.

Author Contributions

Conceptualization, L.L., M.W. and Q.Z.; Methodology, L.L., M.W. and Q.Z.; Software, L.L. and Q.Z.; Validation, L.L. and Q.Z.; Writing—original draft, L.L.; Writing—review & editing, L.L., M.W., Q.Z., X.X., S.Y., J.Z. and Y.Z.; Funding acquisition, M.W. and Q.Z. All authors have read and agreed to the published version of the manuscript.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

Data are contained within the article.

Conflicts of Interest

Authors Lesong Li, Minqing Wang, Qintian Zhu, Xiaopeng Xu and Sifan Yu were employed by the company Gaona Aero Material Co., Ltd.; Authors Jian Zhang and Yang Zhou were employed by the company Chengdu Advanced Metal Materials Industry Technology Research Institute Co., Ltd. The remaining authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.

Funding Statement

This research was funded by Postdoctoral Fund (Grant number 2023P4C2T02H).

Footnotes

Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

References

  • 1.Du J.H., Lv X.D., Dong J.X., Sun W.R., Bi Z.N., Zhao G.P., Deng Q., Cui C.Y., Ma H.P., Zhang B.J. Research Progress of Wrought Superalloys in China. Acta Metall. Sin. 2019;55:1115–1132. doi: 10.11900/0412.1961.2019.00142. [DOI] [Google Scholar]
  • 2.Kracke A. Superalloys, the Most Successful Alloy System of Modern Times-Past, Present, and Future; Proceedings of the 7th International Symposium on Superalloy 718 and Derivatives; Pittsburgh, PA, USA. 10–13 October 2012. [Google Scholar]
  • 3.Ju J.T., Zhu Z.H., Yang K.S., Ji G.H., An J.L., Shi C.B. Control of Al and Ti Contents During Electroslag Remelting of High-Temperature Ni-based Alloys. Rare Met. Mater. Eng. 2021;50:3550–3561. [Google Scholar]
  • 4.Chen G.S., Cao M.H., Zhou D.H., Jin X. Metallurgical quality of super alloy GH4169 melted in the 5t electroslag furnace under protective Ar gas. J. Aeronaut. Mater. 2003;23:88–91. [Google Scholar]
  • 5.Li S.J., Cheng G.G., Yang L., Chen L., Yan Q.Z., Li C.W. A Thermodynamic Model to Design the Equilibrium Slag Compositions during Electroslag Remelting Process: Description and Verification. ISIJ Int. 2017;57:713–722. doi: 10.2355/isijinternational.ISIJINT-2016-655. [DOI] [Google Scholar]
  • 6.Li X., Geng X., Jiang Z.H., Li H.B., Xu F.H., Wang L.X. Influences of slag system on metallurgical quality for high temperature alloy by electroslag remelting. Iron Steel. 2015;50:41–46. doi: 10.1179/1743281214Y.0000000197. [DOI] [Google Scholar]
  • 7.Bin Y., Wanming L., Shaopeng W., Ximin Z., Haocen Y. Thermodynamic analysis of Al and Ti element loss in electroslag remelting Inconel 718 superalloy. Iron Steel. 2019;54:86–94. doi: 10.13228/j.boyuan.issn0449-749x.20180378. [DOI] [Google Scholar]
  • 8.Morscheiser J., Thönnessen L., Gehrmann B., Friedrich B., Recycling M. The Influence of the Slag Composition on the Desulfurization of Ni-Based Superalloys; Proceedings of the 2011 International Symposium on Liquid Metal Processing and Casting; Nancy, France. 25–28 September 2011. [Google Scholar]
  • 9.Wang X.C. Analysis on Control of Ai and Ti Content in ESR Ingot of GH3030. Spec. Steel Technol. 2006;11:7–9. doi: 10.16683/j.cnki.issn1674-0971.2006.02.002. [DOI] [Google Scholar]
  • 10.Melgaard D.K., Williamson R.L., Beaman J.J. Controlling remelting processes for superalloys and aerospace Ti alloys. JOM. 1998;50:13–17. doi: 10.1007/s11837-998-0372-9. [DOI] [Google Scholar]
  • 11.Pateisky G., Biele H., Fleischer H.J. The Reactions of Titanium and Silicon with Al2O3-CaO-CaF2 Slags in the ESR Process. J. Vac. Sci. Technol. 1972;9:1318–1321. doi: 10.1116/1.1317029. [DOI] [Google Scholar]
  • 12.Tan J.P., Wang F., Liu Z.Q., Baleta J., Li B.K., Zhang B.J. A thermodynamic model for predicting Ti and Al element of SiO2-Al2O3-FeO-TiO2-CaO-MgO-CaF2 slag in electroslag remelting process. J. Mater. Res. Technol. 2023;23:4702–4715. doi: 10.1016/j.jmrt.2023.02.087. [DOI] [Google Scholar]
  • 13.Yang J.G., Park J.H. Distribution Behavior of Aluminum and Titanium Between Nickel-Based Alloys and Molten Slags in the Electro Slag Remelting (ESR) Process. Metall. Mater. Trans. B-Process Metall. Mater. Process. Sci. 2017;48:2147–2156. doi: 10.1007/s11663-017-0994-9. [DOI] [Google Scholar]
  • 14.Jiang Z.H., Hou D., Dong Y.W., Cao Y.L., Cao H.B., Gong W. Effect of Slag on Titanium, Silicon, and Aluminum Contents in Superalloy During Electroslag Remelting. Metall. Mater. Trans. B-Process Metall. Mater. Process. Sci. 2016;47:1465–1474. doi: 10.1007/s11663-015-0530-8. [DOI] [Google Scholar]
  • 15.Duan S.C., Shi X., Mao M.T., Yang W.S., Han S.W., Guo H.J., Guo J. Investigation of the Oxidation Behaviour of Ti and Al in Inconel 718 Superalloy During Electroslag Remelting. Sci. Rep. 2018;8:5232. doi: 10.1038/s41598-018-23556-3. [DOI] [PMC free article] [PubMed] [Google Scholar]
  • 16.Yan X., Guo Z., Yu X., Wang D. A Review on the Development of Regular Solution Model for Molten Slags and Its Application on the Metallurgical Physico-Chemistry (Part II) Shanghai Met. 1995;17:1–6. [Google Scholar]
  • 17.Ji C., Che Y., Xu K. Temkin’s Model. In: Xu K., editor. The ECPH Encyclopedia of Mining and Metallurgy. Springer Nature; Singapore: 2022. p. 1. [Google Scholar]
  • 18.Jiang Z. Electroslag Metallurgy. China Science Publishing & Media Ltd.; Beijing, China: 2015. [Google Scholar]
  • 19.Kennedy R.L. Allvac® 718Plus™, superalloy for the next forty years; Proceedings of the 6th International Symposium on Superalloys 718, 625, 706 and Derivatives; Pittsburgh, PA, USA. 2–5 October 2005; pp. 1–14. [Google Scholar]
  • 20.The Math Works, Inc. MATLAB. The Math Works, Inc.; Natick, MA, USA: 2020. [Google Scholar]
  • 21.Hou D., Wang D.Y., Zhou X.Z., Hu S.Y., Wang H.H., Qu T.P. Study on Physical and Chemical Properties of Slag Used for Electroslag Remelting of Superalloy Containing Titanium and Aluminum. Metall. Mater. Trans. B-Process Metall. Mater. Process. Sci. 2022;53:2972–2990. doi: 10.1007/s11663-022-02579-2. [DOI] [Google Scholar]
  • 22.Liu F.B., Gao J.Z., Cao H.B., Li H.B., Jiang Z.H., Geng X., Kang C.P., Chen K., An R.D. Effect of slag composition on elements oxidation behavior of GH984G superalloy for electroslag remelting withdrawal process. J. Iron Steel Res. Int. 2022;29:761–771. doi: 10.1007/s42243-021-00602-5. [DOI] [Google Scholar]
  • 23.Gong W., Zhou R.A., Wang P.F., Jiang Z.H., Geng X. Effect of Al2O3 and TiO2 Contents in the Refining Slag on Al and Ti Contents of Incoloy825 Alloy. ISIJ Int. 2022;62:2255–2265. doi: 10.2355/isijinternational.ISIJINT-2022-158. [DOI] [Google Scholar]
  • 24.Hou D., Jiang Z.H., Dong Y.W., Cao Y., Cao H., Gong W. Thermodynamic design of electroslag remelting slag for high titanium and low aluminium stainless steel based on IMCT. Ironmak. Steelmak. 2016;43:517–525. doi: 10.1080/03019233.2015.1110920. [DOI] [Google Scholar]
  • 25.Duan S.C., Guo H.J., Shi X., Guo J., Li B., Han S.W., Yang W.S. Thermodynamic analysis of the smelting of Inconel 718 superalloy during electroslag remelting process. Chin. J. Eng. 2018;40:53–64. doi: 10.13374/j.issn2095-9389.2018.s1.009. [DOI] [Google Scholar]
  • 26.Yang X.M., Shi C.B., Zhang M., Zhang J. A Thermodynamic Model for Prediction of Iron Oxide Activity in Some FeO-Containing Slag Systems. Steel Res. Int. 2012;83:244–258. doi: 10.1002/srin.201100233. [DOI] [Google Scholar]
  • 27.Li Z., Geng X., Jiang Z., Fubin L. Deoxidation thermodynamic of electroslag remelting 304NG stainless steel. J. Cent. South Univ. (Sci. Technol.) 2023;54:4273–4282. [Google Scholar]
  • 28.Jian Z. Computational Thermodynamics of Metallurgical Melts and Solutions. Metallurgical Industry Press; Beijing, China: 2007. [Google Scholar]
  • 29.Bacon W.G., Fraser M., Mitchell A. The application of electroslag melting and welding to the manufacture of large steel components. Can. Metall. Q. 1975;14:161–167. doi: 10.1179/000844375795050300. [DOI] [Google Scholar]
  • 30.Shen Z., Guo J., Duan S., Guo H., Duan R., Huang S. Thermodynamics and Optimization of a Slag System for Al and Ti Burning Loss Control of a Φ1100-mm Ni-Based Superalloy Ingot During the Electroslag Remelting Process. JOM. 2023;75:2636–2645. doi: 10.1007/s11837-023-05807-5. [DOI] [Google Scholar]
  • 31.Chen C., Zhao W., Dong D. Control of Mg Content during Electroslag Remelting of GH99 Alloy. Beijing Iron and Steel Institute; Beijing, China: 1985. p. 14. [Google Scholar]

Associated Data

This section collects any data citations, data availability statements, or supplementary materials included in this article.

Data Availability Statement

Data are contained within the article.


Articles from Materials are provided here courtesy of Multidisciplinary Digital Publishing Institute (MDPI)

RESOURCES