


Vol 48, No 1 (2018)
- Year: 2018
- Articles: 13
- URL: https://journals.rcsi.science/0967-0912/issue/view/11196
Article
Behavior of Conducting Liquid within an Arc Furnace in a Vertical Magnetic Field
Abstract
In a vertical magnetic field, bulk electromagnetic forces arise in conducting melt within the bath of a dc arc furnace. As a result, the melt is set in motion. The flow of slag and metal in the furnace bath may lead to effective mixing but may also have negative consequences, such as increased lining wear in the region of the hearth electrode. There has been little research on conductive mixing in the bath of a dc arc furnace. Theoretical concerns include the character of the flow in the bath under the action of magnetic fields of specific magnitude; practical considerations include the lack of simple and reliable sources of magnetic fields. In the present work, the utility of a transparent physical model in studying the flow of conducting liquid in an external vertical magnetic field is investigated. The applicability of the modeling results to processes in the 5-t bath of an industrial dc arc furnace is analyzed. It proves possible in principle to study the flow of conducting melt in external vertical magnetic fields on models based on transparent nonmetallic conducting liquids. The use of an aqueous solution of table salt permits assessment of the liquid velocity at its free surface and close to the hearth electrode by video recording. By physical modeling of the flow of conducting fluid in the bath under the action of an external vertical magnetic field, with different switching sequences of the hearth electrode and different currents in the bath, it is possible to establish the character of the liquid flow when the hearth electrode is at the center of the bath or somewhat displaced. The mean rate of liquid rotation in the horizontal plane is increased when the hearth electrode is at some distance from the bath axis. The strength of the vertical magnetic field producing conductive motion in the metal bath of a 5-t dc arc furnace is estimated: around 5 kA/m.



Manganese Capacity and Optical Basicity of Metallurgical Slag
Abstract
In practice, the concept of slag capacity is used to assess the distribution of elements between condensed phases. In particular, researchers determine the sulfide, phosphate, chromate, and nitride capacity of slags. In the present work, a mathematical model of the manganese capacity is derived. To that end, two equivalent forms of the manganese capacity are derived from the equilibrium constants of the redox reaction of manganese [Mn] + (1/2)O2 = (MnO). These indices reflect the manganese distribution between the metal and the slag and do not depend on the composition of the metal and the gas phase. One version takes the form CMn = KMn/γ(MnO). If we take logarithms and use the known equilibrium constant KMn of the redox reaction, we may write logCMn = 21122/T–logγ(MnO)–4.5509. To find the activity coefficient of manganese oxide, equilibrium between hot metal, cast iron, ferrosilicon, ferromanganese, and the corresponding slags is studied experimentally at various temperatures, on circulatory apparatus permitting the study of heterogeneous equilibria involving the gas phase. Using the apparatus, the change in gas volume in the reactions is monitored and automatically recorded and constant pressure is automatically maintained in the system. The attainment of equilibrium is also judged from the constancy of chemical composition of the condensed phases over time. If numerical values of γ(MnO) are available, they may be used to calculate the manganese capacity of all the slags from the equation already given. For the sake of practical convenience, the manganese capacity is written in terms of the temperature and the optical basicity λed calculated from the electron density known for elements in the periodic table: logCMn =–1.866λed + 21049/T–3.131 (R2 = 0.997). According to this equation, the manganese capacity depends only on λed and the temperature and may be used for metals and slags of practically any composition.



Oxygen Solubility in Fe–Co Melts Containing Carbon
Abstract
In thermodynamic analysis of solutions of oxygen in Fe–Co melts containing carbon, the equilibrium constants of reactions between carbon and oxygen are determined, as well as the activity coefficients at infinite dilution and the interaction parameters in melts of different composition at 1873 K. The dependence of oxygen solubility in such melts on the cobalt and carbon content is calculated. In iron–cobalt melts, carbon has high oxygen affinity. The deoxidizing ability of carbon increase significantly with increase in cobalt content in the melt. In pure cobalt, it is more than an order of magnitude greater than in pure iron. Deoxidation by carbon produces gaseous oxides: carbon monoxide (CO) and dioxide (CO2). The reaction of carbon and oxygen dissolved in the melt and hence the deoxidizing ability of carbon depend on the total gas pressure above the melt. Decrease in gas pressure significantly improves the reducing properties of carbon. The minimum oxygen concentration for alloys of the same composition is reduced by practically an order of magnitude with tenfold decrease in the total gas pressure. The gas composition above Fe–Co melts and the equilibrium carbon and oxygen concentrations in the melt are calculated with total gas pressures of 1.0, 0.1, and 0.01 atm. The optimal oxygen concentration (1–10 ppm) in Fe–Co melts is reached at carbon concentrations between 0.01 and 1% depending on the total gas pressure (0.01–1 atm). The solubility of oxygen in iron–cobalt melts containing carbon passes through a minimum, which is shifted to lower carbon content with increase in the melt’s cobalt content. Further additions of carbon increase the oxygen concentrations in the melt. With increase in cobalt content, this increase will be sharper.



Composition and Mobility of Ionic Ensembles in Slags for Steel Refining in the Ladle–Furnace Unit
Abstract
High-lime synthetic slags for refining steels in the ladle–furnace unit are investigated. The content of the slag mixtures is as follows: 60 wt % CaO, 7 and 8 wt % MgO, 7–23 wt % Al2O3, and 9–18 wt % SiO2, with additions of 8 wt % CaF3 and 5–15 wt % Na2O. Polymer theory is used to calculate the composition of the anionic subsystem in the slag melts. The log-mean polymerization constants Kp* for multicomponent melts are calculated from the known polymerization constants in binary systems. It is found that Kp* ≈ 10–3–10–2 in the range 1500–1600°C. In that range, the melt’s degree of polymerization is 3 × 10–4–8 × 10–3. In the most polymerized melt, the ionic content of the dimers Si2O76- and Al2O78- is no more than 0.1 and 1.5% of the values for the corresponding monomers. Therefore, we assume, with an error of about 2%, that the structural units of the anionic subsystem are monomers AlO45- and SiO44- simple O2– and F– ions (slag 7). The cationic subsystem consists of Ca2+, Mg2+, Na+, and Al3+ ions in octahedral coordination with oxygen (less than 3% of all the Al atoms). In all the melts, the concentrations of free oxygen ions O2– and Ca2+ ions are similar. In half the cases, the content of O2– ions is greater than the content of Ca2+ ions. The mean mobility U and self-diffusion coefficient D for all the cations are calculated from data for the electrical conductivity and the density. With increase in temperature from 1500 to 1600°C, U and D increase by 50 and 60%, respectively, in all the slags. With increase in the mutual substitution of the components in the slag mixtures M = n(Na2O, CaF2)/n(Al2O3 + SiO2), mol/mol, at 1600°C, U increases from 1.14 × 10–8 to 1.46 × 10–8 m2/(V s) for slags 1–6 (0 ≤ M ≤ 1.1) and from 1.01 × 10–8 to 1.66 × 10–8 m2/(V s) for slags 7–10 (0.25 ≤ M ≤ 0.65). Correspondingly, D increases from 9.2 × 10–10 to 12.8 × 10–10 m2/s for slags 1–6 and from 8.2 × 10–10 to 14.3 × 10–10 m2/s for slags 7–10. The temperature dependence of U and D may be approximated by an Arrhenius equation with activation energies EU and ED. With increase in M in the given ranges, EU declines from 146 to 100 kJ/mol (slags 1–6) and from 124.5 to 109 kJ/mol (slags 7–10). Likewise, ED declines from 159 to 116.5 kJ/mol (slags 1–6) and from 139.5 to 124 kJ/mol (slags 7–10). The mean values of EU and ED correlate with the mean distance between the cations in the melts. On the basis of the proposed alternative model of the conductivity, the O2– ions may also transfer electric charge. Preliminary estimates show that the oxygen transport number at 1600°C may exceed 0.1 in some slags.



Redox Properties of Gas Phases
Abstract
In the H2–O2–C system, in the general case, two reversible reactions of carbon gasification and the water gas reaction, the gas mixture H2–H2O–CO–CO2 is formed at high temperatures. In this mixture, the very low content of oxygen formed by the dissociation of H2O and CO2 is represented by the oxygen potential log (\({p_{{O_2}}}\), atm). Thus, the redox properties may be assessed in terms of the oxygen potential. In any gas mixture containing H2O and/or CO2, it may be calculated from the equations



Magnesia Sinter with Flux Based on Magnesium Silicate
Abstract
The experimental production of sinter with the addition of a byproduct of magnesite production— serpentinite–magnesite—is considered. This additive improves the strength of the sinter produced. Recommendations are made regarding the best use of serpentinite–magnesite in the sintering shop at Ural Steel.



Improvement in Blast-Furnace Performance by Using a New Form of Iron Ore
Abstract
The effective blast-furnace smelting of iron requires the use of uniform fluxed iron ore in sintered form—local cakes produced by the production of pellets with a high content of iron and residual carbon, minimal content of silica, high cold strength, and high strength in the blast furnace. The proposed new material combines the best metallurgical properties of sinter and pellets.



Stabilization of Ladle-Treatment Slags in Steel Production
Abstract
Ladle-treatment slags are primary wastes from steel production. Slag utilization is prevented by its spontaneous decomposition as a result of polymorphic transformation of dicalcium silicate with decrease in slag temperature. At OOO NLMK-Kaluga, the slag is stabilized by the introduction of boron oxide in the high–magnesia flux during ladle treatment. Industrial tests indicate stabilization of the slag and the formation of a protective layer on the lining, preventing slag corrosion.



Ensuring Specified Surface Roughness in the Production of Thin Cold-Rolled Steel Sheet
Abstract
The formation of surface microrelief on rolled strip is considered. The influence of the surface state of the rolls, the strip reduction, the rate of reduction, the mechanical properties of the metal, the lubricant employed, and other rolling and tempering parameters on the roughness of cold-rolled steel strip is analyzed. Practical means of ensuring compliance with the surface-roughness standards for thin sheet are proposed.



Improving Pipe Production on the TPA 220 Piercing Mill
Abstract
The introduction of pipe rolling from continuous-cast bullet on the TPA 220 piercing mill, with an expanded range (up to a diameter of 245 mm, as against the previous limit of 219 mm) and increase in pipe length, is described. The mechanical parameters of the mill are measured and assessed. Options for further modernization of the mill and the production of thin-walled pipe with a diameter/wall ratio of more than 30 are outlined.



Influence of Microalloying on the Strength and Corrosion of Low-Carbon Stainless Steel
Abstract
Attention focuses on how nitrogen and rare-earth metals modify the mechanical properties and corrosion characteristics of unstabilized low-carbon Fe–Cr–Ni stainless steel, additionally alloyed with silicon and molybdenum. The influence of the selected microalloying method on the mechanical properties of unstabilized low-carbon chromonickel stainless steel and its resistance to local corrosion is studied experimentally. Nitrogen-bearing 03X17H9AC2, 03X17H9AM3, and 03X18H15AM3 stainless steel microalloyed with rare-earth metals is investigated.



Cybernetic Applications of New Precision Alloys
Abstract
The operation of precision alloys in cybernetic circuits is considered. Principles that may be used to standardize the physical properties of precision alloys in complex operating conditions are outlined. Means are proposed for regulating the basic properties of alloys, including their reliability, their performance, and the structure of the life cycle.



Adjusting the Load Graph by Coordinating Major Power Consumers
Abstract
Under the current energy strategy, the Russian Ministry of Power is increasing the role of consumers in regulating the load on the power system at peak hours, by measures such as peak pricing. Analysis of the steel industry indicates rising competition on account of China’s enormous production capacity. Improvements in energy efficiency now confer competitive advantage. Methods are proposed for coordinating the operation of arc furnaces and ladle—furnace units so as to reduce the maximum load. The economic benefits of this approach are analyzed.


