Patent Application
20100307709
This invention relates generally to refining of steel. More particularly, this invention relates to processes for refinement of silicon-bearing Al-killed and Al—Si dual killed steel to be directly cast in a continuous slab caster.
In continuous slab casting, the continuous caster is comprised of a tundish and an oscillating mold, in addition to a shroud and submerged entry nozzle. The molten steel in the ladle is poured into a tundish and then poured vertically through the submerged entry nozzle into a hollow water-cooled oscillating mold, and continuously cast slabs are withdrawn horizontally from the bottom of the mold. Refractory shrouds are used to transfer the molten steel from the ladle to the tundish, and then to the submerged entry nozzle and the mold, to avoid oxidation of the molten steel through contact with air. The shroud between the tundish and the mold feeds through the submerged entry nozzle, and is regulated by a stopper rod.
The continuous slab caster produces wide rectangular strands of large cross-section, which are cut off into slabs to be hot rolled and cold rolled for use as material for sheet and plate. Thick slabs for flat-rolled products usually have an as-cast thickness of 100 to 250 mm. Thin slabs for flat-rolled products usually have an as-cast thickness of 30 to 100 mm. The slab caster is usually used in conjunction with an electric arc furnace or basic oxygen furnace, where the hot metal in produced for the caster.
Steel for continuous casting may be subjected to deoxidation treatment usually in a ladle prior to casting. Deoxidizing the molten steel in a ladle metallurgy furnace (LMF) or Vacuum Tank Degassed (VTD) to a desired oxygen level is typical.
Aluminum (or a combination of Al and Si) has been widely used as a deoxidizer and grain size controller in the manufacture of steels. Aluminum acts as a sacrificial metal which combines with oxygen to form a stable aluminum oxide, which migrates into the slag. Aluminum is a particularly desirable material for this purpose because it can be safely stored, handled and transported at ambient temperature, and, it is reactive as an oxidizing agent with steel at steelmaking temperatures.
Most thin slab casting and plating grades of steel are typically Al-killed steels. In some cases a combination of Al and Si is used to kill the steel. While this steel can be cast “as is” in large slab casters, further treatment is required in thin slab casters to avoid clogging or choking of submerged entry nozzles. One established practice in thin slab casting is to modify alumina and spinel inclusions by treatment with calcium to provide for more liquidity. With proper calcium treatment, the majority of the solid alumina (Al2O3) and/or spinel (MgAl2O4) inclusions are modified to liquid inclusions and casting is performed with acceptable surface quality to the cast slab. For continuous casting in a thin slab caster, 600 feet (182.9 m) of calcium wire has been found sufficient for a 170 ton (154 tons metric) ladle to add the calcium to avoid nozzle clogging (about 0.134 lb/ton, 0.067 kg/ton metric). 600 feet (182.9 m) of calcium wire contains about 22.5 lbs (10.2 kg) of calcium and is equivalent to about 16.8 ppm effective calcium in the refined steel. The recovery of calcium in the steel from calcium wire is less than 100% so that the effective calcium will be less than the amount added.
There are two main grades of silicon-bearing steels for sheets and plate steels made in a thin slab caster:
Problems with stopper rod wear associated with excessive Ca-addition have been observed in silicon-bearing steels where ferrosilicon and/or Silicomanganese have been added to achieve the desired silicon concentration in the finished steel. In a “Study of Casting Issues using Rapid Inclusion Identification and Analysis”, Story, et al., AISTech 2006 Proceedings, Vol. 1, pp. 879-889, it was determined that ferrosilicon can contain calcium in addition to silicon and other alloying elements. To address stopper rod wear, Story et al. discussed using high purity ferrosilicon containing about 0.024% calcium.
A method of making silicon-bearing steel comprising the steps of:
The calcium-containing silicon additive may be ferrosilicon and cheap ferrosilicon additive since the percent of calcium in the additive need not be kept low. The calcium-containing silicon additive may include additives having less than about 1.8% calcium, and further includes additives with less than about 1% calcium.
The low carbon steel may have a carbon content between about 0.003% and about 0.5% by weight. The disclosed method of refining silicon-bearing steel includes low carbon steels.
The disclosed refining of silicon-bearing steel may occur in a ladle metallurgical furnace or vacuum tank degasser.
A cast steel is made by a method comprising the steps of:
Further the silicon content may be between 0.1% and 1.5% by weight.
To understand the operation of the disclosed methods and product, a number of embodiments are described by reference to the accompanying drawings. No limitation on the scope of the claimed invention is thereby intended. Such alterations and further modifications in the illustrated embodiments, and such further applications of method and product are contemplated as would occur to one skilled in the steelmaking art.
Referring now to
The ladle 18 of unrefined molten steel 24 is routed from the EAF 12 to the LMF or VTD 14 to refine the molten steel into a form suitable for casting by the continuous slab caster apparatus 16. In general terms, as seen in
In slab casting described herein, the steel is generally subjected to aluminum deoxidization, which results in the formation of solid Al2O3 inclusions in the steel. Following in the refining process, the deoxidized molten steel in ladle 18 is desulfurized. After desulfurization, the steel is treated with calcium to modify the solid Al2O3 and/or spinet inclusions to liquid Ca-alumina inclusions. Following refining, the deoxidized, desulfurized and calcium treated molten steel in ladle 18 is transferred to the continuous steel slab casting apparatus 16.
In the disclosed method, the amount of calcium in the required ferrosilicon (silicon additive) is taken into account during the refining of the molten steel. The following will consider FeSi as the silicon additive.
First, the concentration of calcium in the source of ferrosilicon is determined. Next, the amount of ferrosilicon that is needed for addition to the molten steel to achieve the desired silicon concentration in the finished steel, and, the quantity of calcium in the required amount of ferrosilicon is calculated. If the amount of calcium is greater than the required amount (e.g., 16.8 ppm during normal non-startup operations), the required amount of ferrosilicon is divided into two portions, a early portion and a late portion. The late portion is the amount of ferrosilicon that contains the desired amount of calcium in the finished steel. The early portion is the amount of ferrosilicon containing the excess amount of calcium not wanted in the finished molten steel. In general, desired sources of ferrosilicon contain less than 1.8% calcium or less than 1% calcium; although this is desired, other concentrations, greater than 1.8%, can also be used in this disclosed method of forming and refining silicon-bearing steel.
The early ferrosilicon portion, FeSiearly is added early during steel deoxidation with Al or early during refining in the ladle metallurgical furnace (LMF) or vacuum tank degasser (VTD), typically before or during desulfurization, so that the calcium in the early added ferrosilicon can combine with sulfur and other impurities, and migrate to the slag. For example, the calcium in the early added ferrosilicon can react with sulfur forming CaS that migrates to and is removed as part of the slag that is formed during refining. The late ferrosilicon portion, FeSilate, is added late in the refining process, after desulfurization has completed, typically to less than 0.01% S by weight. The calcium added to the LMF or VTD from the FeSilate portion modifies the solid alumina inclusions into liquid inclusions and reduces the incidence of nozzle clogging or choking in the submerged entry nozzle. Since any excess calcium present in the total amount of ferrosilicon added to the LMF or VTD was removed during desulfurization by adding the excess portion, FeSiearly, during desulfurization, the incidence of excess stopper rod wear is reduced.
Where the calcium present in the required quantity of FeSi is equal to or less than the required amount of calcium in the finished steel, only one addition of ferrosilicon, FeSilate is made during refining. This single late addition of ferrosilicon is done after desulfurization. In the event that the calcium present in the required quantity of FeSi is less than the required amount, an additional amount of calcium, typically in the form of calcium wire, is added with the required quantity of FeSi.
In casting campaigns using the method of forming and refining silicon-bearing steels described, It has been found that the casting campaigns have been extended to 18 heats, which is the typical limit for the submerged entry nozzle (SEN) before replacement. Using the early processes of adding the required amount of ferrosilicon after desulfurization and followed by adding the required amount of calcium, also added after desulfurization, stopper rod wear would usually be the limiting factor and limited the casting campaign to 10 heats.
Once the concentrations of calcium and silicon in the ferrosilicon are known, the concentrations are entered into the spreadsheet at 101 and 103, respectively. The desired concentration of silicon in the finished steel is entered at 105. A total quantity 107 of required ferrosilicon is then calculated. The total quantity 107 of ferrosilicon required, FeSireq, is based on the heat size 102, multiplied by the target % silicon 105 and adjusted to account for the silicon concentration 103 in the ferrosilicon and the recovery factor 121 for ferrosilicon as follows:
The total ferrosilicon required, FeSireq, is then divided into a first or early ferrosilicon addition 111, FeSiearly, and a second or late ferrosilicon addition 109, FeSilate. The late ferrosilicon addition, FeSilate, is the amount of ferrosilicon that, is contains the target quantity Catarget, 123, of calcium from the total ferrosilicon required, FeSireq. The target quantity of calcium, Catarget, is that amount of calcium which results in 16.8 ppm calcium continuous operation, (22.4 ppm calcium startup), in the refined metal at the time of casting. If the calcium available, Caavail, in the total ferrosilicon required, FeSireq, is equal to or less than the target quantity of calcium, Catarget, then FeSilate is equal to FeSireq and there is no early addition of ferrosilicon. If the calcium available, Caavail, in the total ferrosilicon required is greater than the target quantity of calcium, Catarget, then FeSilate is that amount of FeSi that contains the target quantity of calcium, Catarget. Specifically, this amount can be calculated by dividing the target calcium, Catarget by the calcium available, Caavail, multiplied by the total ferrosilicon required, FeSireq.
In the event that the calcium, Caavail, present in the total ferrosilicon required, FeSireq, is less than the amount of calcium required, Catarget, 123, additional calcium is added, usually in the form of calcium wire with the FeSilate portion ferrosilicon. For convenience, the additional calcium required 113, Caadd, is calculated in feet of calcium wire, because a typical way of adding any additional calcium is by adding calcium wire. Other units of measurement, such as pounds, kilograms, etc. could also be used.
Caadd=Catarget−Caavail (4.0)
The disclosed methods of making silicon-bearing steel reduce the cost of making the steel by replacing calcium wire with calcium containing ferrosilicon and by extending the length of a casting campaign to about 18 heats. It has been estimated the cost savings per ton of steel using the disclosed methods is about $2 per ton, about half due to reduced calcium wire usage and about half due to extending the length of the casting campaign.
Based upon the foregoing disclosure, it should now be apparent that method of the present invention will carry out the objects set forth hereinabove. It is, therefore, to be understood that any variations evident fall within the scope of the claimed invention and thus, the selection of specific component elements can be determined without departing from the spirit of the invention herein disclosed and described.
This application is divisional application of U.S. Utility application Ser. No. 12/434,140, filed May 1, 2009, which is a continuation of International Application No. PCT/US2007/083125, filed Oct. 31, 2007, which claims priority from and the benefit of U.S. Provisional Application No. 60/863,848, filed Nov. 1, 2006. The disclosures of each application are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 60863848 | Nov 2006 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 12434140 | May 2009 | US |
| Child | 12840686 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/US2007/083125 | Oct 2007 | US |
| Child | 12434140 | US |
