Background of the Invention
[0001] The present invention relates to a free machining, deformed, solid steel product
made from molten steel containing dissolved oxygen.
[0002] Molten steel for making such products is generally prepared in a steel refining furnace
such as a basic oxygen furnace, an electric furnace and, in decreasing utilization,
an open hearth furnace. Molten steel prepared in a steel refining furnace generally
contains dissolved oxygen which is usually regarded as an undesirable impurity.
[0003] A conventional expedient for removing dissolved oxygen from molten steel is to add
elements, such as aluminium silicon, titanium or zirconium, that form stable oxides.
These metal elements are referred to hereinafter as solid deoxidising agents. A deoxidising
treatment employing a solid deoxidising agent is usually conducted outside of the
steel refining furnace, typically in a ladle into which the molten steel has been
poured from the steel refining furnace.
[0004] In certain steels, sulfur is added to the steel to improve the machinability of the
steel. Sulfur combines with manganese to form manganese sulfide inclusions in the
solidified steel, and these inclusions improve the machinability of the steel (DE-B-1608752
and DE-A-2,823,366). Manganese sulfide inclusions have a tendency to be elongated
in the direction of rolling when a solidified steel casting is rolled into a shape
(product) and elongated manganese sulfide inclusions are less desirable from a machinability
standpoint than globular manganese sulfide inclusions. Likewise, smaller manganese
sulfide inclusions are considered less desirable than larger inclusions.
[0005] An object of the invention is to provide a free machining, deformed, solid product
which has improved properties compared to such known products.
[0006] This aim is achieved by the invention as claimed.
[0007] The manganese sulfide inclusions are in a desired form of relatively globular manganese
oxysulfide inclusions which resist deformation when the solidified steel undergoes
rolling and undesirable oxide inclusions which interfere with machinability are avoided.
[0008] If 60-150 parts per million (mg/kg ppm) of dissolved oxygen is retained in the molten
steel upon solidification, the retained oxygen combines with the manganese sulfide
to form oxygen containing manganese sulfide inclusions (manganese oxysulfides) which
are more resistant to deformation or elongation during rolling than are those manganese
sulfide inclusions formed in steel containing very little dissolved oxygen. The retained
oxygen also increases the size of the inclusions. The end result of the retained oxygen
is the formation of larger, relatively globular manganese oxysulfides in the rolled
steel shape.
[0009] Although it is desirable to retain in the molten steel a limited amount of dissolved
oxygen, it is undesirable to retain in the molten steel a dissolved oxygen content
above that needed to provide relatively large, globular manganese oxysulfides. However,
if the surplus dissolved oxygen content is removed with solid deoxidising agents (DE-A-2,823,366),
this forms, in the solidified steel, oxide inclusions which can have a detrimental
affect on machinability. Accordingly, it is undesirable to control the surplus dissolved
oxygen content in a free machining steel with solid deoxidising agents.
[0010] In cases where the dissolved oxygen content is less than that required to provide
the desired globular manganese oxysulfides, the dissolved oxygen content must be increased.
[0011] Molten steel prepared in a steel refining furnace for making a product according
to the invention is conventionally poured from the furnace into a ladle from which
the molten steel is introduced into a casting mold which may be either an ingot mold
or a continuous casting mold. If the steel is flowed into a continuous casting mold,
it is first flowed from the ladle into a tundish which contains one or more outlet
openings through which the steel flows to the continuous casting mold. Some tundishes
contain internal structure in the form of baffles, dams, weirs and the like to control
or direct the movement of the molten steel through the tundish, and this, as well
as the general configuration of the tundish and its entry and exit locations, causes
the molten steel to undergo a mixing action as it flows through the tundish. Embodiments
of tundishes containing the internal structure and general configuration discussed
above are disclosed in Jackson, et al., U.S. application serial No. 808,570, filed
December 13, 1985
[0012] The bath of molten steel in the ladle is usually covered with a slag layer, and the
molten steel in the tundish can also be covered with a slag layer. Typically, the
slag layer on the molten steel in the ladle or in the tundish comprises, at least
to some extent, slag from the steel refining furnace in which the molten steel was
initially prepared.
[0013] In both the ladle and the tundish there is an interface between the bath of molten
steel and the slag layer. In the tundish, the area of this interface per unit mass
of molten steel is relatively large while in the ladle the area of this interface
per unit mass of molten steel is relatively small. In the tundish it is several times
greater than in the ladle.
[0014] The bath of molten steel in the ladle can be stirred by bubbling gases, such as argon,
through the bath in the ladle, by electromagnetic stirring, by alloy injection, etc.
As a result, there is a substantial turnover of molten steel at the interface between
the bath of molten steel and the slag layer in a ladle in which the bath of molten
steel undergoes stirring.
[0015] Typically, there is dissolved oxygen in the bath of molten steel, and in the covering
slag layer there are oxides, such as manganese oxide (MnO) and iron oxide (FeO), having
a cation corresponding to one of the metallic elements (Mn, Fe) in the bath of molten
steel. The dissolved oxygen in the molten steel and the oxides in the slag layer usually
move toward equilibrium with each other, i.e. the relative proportions of each move
toward stable values absent some external disruption. There is movement toward equilibrium
because of the natural tendency for chemical reactions to occur and to continue until
they produce a state of equilibrium. The respective amounts of dissolved oxygen and
slag layer oxides which are in equilibrium can be calculated from available thermodynamic
data.
[0016] For a bath of molten steel made in a basic oxygen furnace and which is covered in
the ladle with a layer of slag from the same furnace and to which ferromanganese has
been added at the ladle, the movement toward equilibrium is typically in the direction
whereby oxygen from the slag oxides enters the molten steel to increase the dissolved
oxygen content thereof. As the temperature of the molten steel bath drops, the amount
of dissolved oxygen which the molten steel will hold in equilibrium also drops.
[0017] As noted above, a molten steel bath in a ladle may be stirred with an inert gas such
as argon. The stirring gas may also contain, in addition to argon, carbon monoxide.
For a given carbon content in the molten steel, there is an equilibrium between the
carbon monoxide in the stirring gas and the carbon and oxygen in the bath of molten
steel through which the carbon monoxide gas flows. The respective amounts of each
which are in equilibrium can be readily calculated from available thermodynamic data.
[0018] A method for making a steel product according to the invention is performed outside
of the steel refining furnace, typically in a ladle, although some procedures may
be performed in a tundish. The method is performed with a steel containing carbon,
manganese and iron.
[0019] In a procedure performed in a ladle, untreated molten steel is first prepared in
a steel refining furnace and then poured into the ladle to form therein a bath of
molten steel. The bath of molten steel contains dissolved oxygen. In the ladle, the
bath of molten steel is covered with a slag layer comprising an undiluted slag containing
an oxide which, in the percentage thereof existing in the undiluted slag, initially
moves toward equilibrium with dissolved oxygen in the bath. Typically, the undiluted
slag is the slag from the steel refining furnace, and the oxide moving toward equilibrium
is MnO or FeO or both. The slag also contains other compounds conventionally found
in slag resulting from steel making operations.
[0020] It may be necessary to reduce (or increase) the amount of dissolved oxygen in the
molten steel bath, e.g. a reduction may be required if the dissolved oxygen content
is greater than that required to impart the necessary globularity to the manganese
sulfide inclusions upon solidification and rolling of the steel.
[0021] The dissolved oxygen content of the bath may be decreased by diluting the slag in
the slag layer. More particularly, the percentage of slag layer oxide (MnO, FeO) which
was moving toward equilibrium with the dissolved oxygen in the steel is decreased
by adding to the slag layer a diluent oxide, e.g. calcium oxide (lime) (CaO).
[0022] Diluting the slag disrupts the initial movement toward equilibrium between the oxide
in the slag layer and the dissolved oxygen in the bath of molten steel. Assuming that,
before disruption, the movement toward equilibrium was in the direction whereby oxygen
from the slag oxides enters the molten steel, the disruption reverses the direction
of that movement. If the oxides in the slag were in equilibrium with the dissolved
oxygen in the steel, the disruption caused by diluting the slag produces movement
in the desired direction whereby dissolved oxygen from the molten steel enters the
slag as oxide. If the initial movement toward equilibrium were in the desired direction,
but the movement was relatively insubstantial or otherwise insufficient, the disruption
caused by diluting the slag will increase the movement in the desired direction.
[0023] The discussion in the preceding paragraph assumes that the slag is diluted to decrease
the dissolved oxygen content of the molten steel. If the dissolved oxygen content
of the molten steel were to be increased, one would add MnO and/or FeO to the slag
layer.
[0024] Referring again to the procedure in which the slag is diluted with lime, the result
thereof is to form, at the molten steel bath-slag layer interface, additional amounts
of the diluted oxide (e.g. MnO and/or FeO), and these additional amounts are absorbed
into the slag layer as a result of the natural tendency to reestablish an equilibrium
between that oxide in the slag layer and the dissolved oxygen in the bath of molten
steel.
[0025] Oxide formation within the bath of molten steel is avoided because essentially all
of the oxides which form as a result of the above-described disruption of the equilibrium
will form at the interface between the bath of molten steel and the slag layer. Oxides
which form at the interface are readily absorbed by the slag, thereby avoiding the
formation of oxides within the steel. The manganese, the iron and the dissolved oxygen
which combine to form oxides come from the molten steel at the interface.
[0026] The mixing action which the bath of molten steel undergoes as a result of the stirring
thereof, replenishes the manganese, iron and dissolved oxygen removed from the molten
steel at the interface, and the reaction at the interface which causes the formation
of oxides continues until the dissolved oxygen content in the bath of molten steel
is in equilibrium with the oxides in the slag layer. If the formation of oxides at
the interface ceases before the dissolved oxygen content is decreased to the desired
level, formation of additional oxide at the interface can be reinitiated by adding
more diluent oxide to the slag layer, and this procedure is continued until the dissolved
oxygen content is decreased to the desired level.
[0027] The procedure described above can be employed in the tundish as well as in the ladle.
In the tundish, the increased area of the molten steel-slag interface per unit mass
of molten steel compensates for the absence in the tundish of external stirring forces,
such as a stirring gas or electro-magnetic stirring, which are employed when the procedure
is performed in the ladle. The procedure, however, does not exclude the use of external
stirring forces (e.g. a stirring gas) in the tundish.
[0028] If the dissolved oxygen content in the molten steel is less than that desired, e.g.
less than that required to provide the desired size and globularity to the manganese
sulfide inclusions, the dissolved oxygen content can be increased by employing another
expedient in accordance with the present invention. The procedure employing this expedient
is performed in the ladle and involves bubbling through the ladle a stirring gas composed
of argon and carbon monoxide. The percentage of carbon monoxide in the stirring gas
is greater than that which is in equilibrium with the carbon and dissolved oxygen
content in the steel. As a result, the proportion of carbon monoxide in the stirring
gas decreases producing an increase in the proportion of dissolved oxygen and carbon
in the molten steel. This change in proportions will continue for so long as the gaseous
mixture containing carbon monoxide in excess of that in equilibrium with carbon and
oxygen in the molten steel is continued.
[0029] A gaseous mixture of argon and carbon monoxide can also be used to decrease the dissolved
oxygen content of the molten steel, if the percentage of carbon monoxide in the gas
is less than that which is in equilibrium with the carbon and dissolved oxygen in
the steel. Decreasing the dissolved oxygen content in the steel in this manner can
be used as a supplement to the first method described above, which dilutes the FeO
and/or MnO content of the slag layer. The first-described method can be employed without
changing the carbon content of the steel. The later-described method can be employed
without substantially changing the manganese content of the steel.
[0030] The later-described method can also be employed as a supplement to the first-described
method, in cases where the dissolved oxygen content is reduced too much, in which
case the later-described method would be employed to produce a slight increase in
the dissolved oxygen content.
[0031] Other features and advantages are inherent in the products claimed and disclosed
or will become apparent to those skilled in the art from the following detailed description.
Detailed Description
[0032] The present invention will be described in the context of producing free machining
steel products containing relatively large, globular manganese oxysulfides.
[0033] In a typical method for making a product embodying the invention, molten steel from
a basic oxygen furnace is poured into a ladle. Certain alloying ingredients may be
added to the molten steel at the ladle during the tapping operation. These include
manganese (added as ferro-manganese), carbon (added as coke) and sulfur. A typical
heat of steel poured into the ladle has a mass of about 200,000 kg. The bath of molten
steel in the ladle is covered with a layer of slag. The slag layer is composed principally
of slag from the basic oxygen furnace. Typically, the proportion of FeO and MnO in
the slag relative to the dissolved oxygen content of the steel are such that there
would be a movement toward equilibrium in the direction whereby oxygen from the oxides
in the slag enters the bath of molten steel.
[0034] However, the dissolved oxygen content in the molten steel is typically above that
needed for producing the desired size and globularity in the manganese sulfide inclusions.
Accordingly, some lime (CaO) is added to the slag from the basic oxygen furnace during
the tapping operation. This has a diluting effect on the slag in the slag layer in
the ladle, decreasing the percentages of MnO and FeO in the slag layer with the intent
of producing a decrease in the dissolved oxygen content in the molten steel bath covered
by the slag layer.
[0035] The slag layer in the ladle has a mass of about 1000-3000 kg and is typically between
75 and 150 mm in depth. If the slag layer is too deep, some deslagging may be required.
The minimum depth of the slag is determined by factors such as the need to cover exposed
upper portions of the ladle lining.
[0036] Typical compositions for the molten steel bath in the ladle are set forth below,
with iron being the balance:
TABLE I
Sample |
Wt.% |
|
C |
Mn |
P |
S |
Si |
A |
0.076 |
0.85 |
0.066 |
0.29 |
0.017 |
B |
0.073 |
0.93 |
0.080 |
0.27 |
0.001 |
C |
0.080 |
1.09 |
0.078 |
0.31 |
0.001 |
[0037] Typical approximate amounts for the principal components of the slag layer covering
the bath of molten steel in the ladle, following the tapping operation, are set forth
below:
TABLE II
Example |
Wt.% |
|
SiO₂ |
Al₂O₃ |
S |
CaO |
FeO |
MnO |
1 |
14 |
5 |
1.5 |
44 |
12 |
17 |
2 |
5 |
5 |
4 |
26 |
13 |
29 |
3 |
5 |
5 |
5 |
39 |
8 |
24 |
[0038] The aim temperature in the ladle after the tapping operation is about 1590°C.
[0039] For purposes of producing globular manganese oxysulfides, it is usually desirable
for the bath of molten steel to contain a dissolved oxygen content in the range 60-150
mg/kg (ppm). The particular amount in this range depends upon the manganese and sulfur
content of the steel.
[0040] If the diluting oxide added to the slag during tapping did not produce a sufficient
decrease in the molten steel's dissolved oxygen content, that content may be further
decreased during a procedure known as ladle metallurgy treatment, a procedure in which
other adjustments can be made to the composition of the steel. Ladle metallurgy treatment
is typically conducted in a ladle metallurgy furnace which is a heated compartment
having a removable roof or cover into which is placed the ladle containing the bath
of molten steel with a slag layer thereon. The slag layer should have a minimum depth
sufficient to render unexposed the upper portions of the ladle lining, to protect
those ladle portions from the electric arcs with which the ladle metallurgy furnace
is heated.
[0041] An example of one approximate aim slag composition during ladle metallurgy treatment
is as follows:
TABLE III
Ingredient |
Wt.% |
CaO |
36 |
SiO₂ |
5 |
Al₂O₃ |
6 |
MgO |
2.5 |
MnO |
30 |
FeO |
10 |
S |
5 |
P₂O₅ |
1 |
[0042] In one embodiment, a typical aim dissolved oxygen content in the molten steel is
an amount no greater than 130 mg/kg (ppm). If the oxygen content of the steel in the
ladle is greater than the aim amount, the slag in the ladle is further diluted with
lime, e.g. about 400-500 kg at a time. The oxygen content is then monitored periodically
after the slag has been diluted with lime, and further dilutions with lime are made
if necessary.
[0043] Set forth below in Table IV is an example showing the effect on the dissolved oxygen
content of further diluting the slag layer with lime. In this particular example,
the composition of the molten steel in the ladle was, in wt.%: about 0.08 carbon,
about 1 manganese, less than 0.002 silicon, nil aluminum, about 0.3 sulfur and less
than about 0.08 phosphorous. Before further dilution, the slag layer had an approximate
composition, in wt.%, of about: 40 CaO, 5 SiO₂, 5 Al₂O₃, 2.5 MgO, 30 MnO, 12 FeO and
5.5 S. The aim dissolved oxygen content for this example was about 120 mg/kg (ppm).
The bath of molten steel was stirred electromagnetically.
TABLE IV
Elapsed Time, min. |
Event |
Temp., °C |
Dissolved oxygen, mg/kg |
Start |
cover on at ladle metallurgy furnace |
-- |
-- |
7 |
-- |
1573 |
151 |
16 |
add alloying ingredients to molten steel |
-- |
-- |
23 |
add alloying ingredients to molten steel |
-- |
-- |
28 |
add 400 kg lime to slag |
-- |
-- |
38 |
-- |
1573 |
138 |
44 |
-- |
1577 |
123 |
54 |
add 393 kg lime to slag |
-- |
-- |
59 |
-- |
1583 |
121 |
69 |
-- |
1580 |
121 |
76 |
-- |
1579 |
121 |
79 |
remove ladle from ladle metallurgy furnace |
-- |
-- |
[0044] In the ladle, diluting the slag layer with lime must be accompanied by a stirring
of the molten steel bath. Merely adding lime to the slag layer as a diluent oxide
is not enough. Stirring produces a turnover of molten steel at the interface between
the molten steel bath and the slag layer to produce continued oxide formation there
and absorption of the oxide thus formed into the slag layer.
[0045] As noted above, in the ladle, stirring is accomplished in one procedure by bubbling
a gas upwardly through the bath of molten steel. The gas is preferably an inert gas
such as argon. The stirring gas may also be a mixture of argon and carbon monoxide,
and this will be discussed more fully below.
[0046] Stirring may also be accomplished electromagnetically or by other expedients heretofore
utilized to obtain a mixing action in a ladle containing a bath of molten steel.
[0047] The diluent oxide or lime may be added to the slag during tapping, during ladle metallurgy
treatment or during both. It is necessary to dilute the slag layer because, before
dilution, the iron oxide and manganese oxide percentages in the slag relative to the
dissolved oxygen content in the molten steel are such that there would be a movement
toward equilibrium in the direction of oxygen from the slag oxides entering the bath
of molten steel. This is the condition which existed when the molten steel and the
slag were still in the steel refining furnace. In other words, the slag which covered
the molten steel in the steel refining furnace had MnO and FeO contents which resulted
in the equilibrium movement described in the preceding part of this paragraph. In
order to reduce the dissolved oxygen content of the molten steel, it is necessary
to dilute the slag with lime, thereby reducing the percentages of MnO and FeO in the
slag layer and causing the formation of additional MnO and FeO at the interface between
the molten steel and the slag layer, in the manner previously described.
[0048] Although the preferred slag diluent is lime, other diluent oxides may be employed.
These comprise aluminum oxide (Al₂O₃), magnesium oxide (MgO), zirconium oxide (ZrO)
and dolomite (CaMgO₂). Silica (SiO₂) should be avoided as a diluent oxide.
[0049] The dissolved oxygen content of the molten steel bath is decreased without the need
to employ solid deoxidizing agents, which are excluded from the bath of molten steel.
As a result, the solidified steel does not contain any additional undesirable oxides
which could impair the machinability of the steel.
[0050] In conventional steel-making operations, the molten steel in the ladle is introduced
from the ladle either into ingot molds or into a tundish when a continuous casting
operation is employed to solidify the steel. When the molten steel is introduced into
a tundish, the treatment for reducing the dissolved oxygen content in the molten steel
can be performed at the tundish in lieu of performing the treatment in the ladle.
In the tundish, the molten steel would be covered with the same slag layer described
above in connection with performing the treatment in the ladle, and the slag layer
is diluted with the same diluent oxide (e.g. lime) as is employed in that embodiment
of the method performed at the ladle.
[0051] Unlike the ladle, however, external mixing forces, such as gas-induced stirring,
or electromagnetic stirring, are usually not available at the tundish. However, in
the tundish the area of the interface between the bath of molten steel in the tundish
and the slag layer, per unit mass of molten steel, is several times greater than the
area of that interface in a ladle. Accordingly, less stirring is required to accomplish
the treatment than is necessary when the treatment is performed in a ladle. In addition,
there is an internal mixing force at the tundish resulting from the action of the
ladle stream entering the tundish. Moreover, a tundish can contain internal structural
elements, such as baffles, dams and weirs, which direct the movement of the molten
steel as it flows through the tundish, and this, plus the mixing action due to the
ladle stream as well as the general configuration of a tundish and its entry and exit
locations, produces sufficient mixing to enable satisfactory performance of the treatment
in the tundish.
[0052] In other words, the movement of the molten steel through the tundish subjects the
molten steel to sufficient mixing action, in the context of the relatively large area
of the slag layer-molten steel interface, per unit mass of molten steel, in the tundish.
[0053] Tundish treatment can be performed in those situations where, for one reason or another,
expedients for stirring or agitating the molten steel in the ladle are unavailable.
[0054] As noted above, when the bath of molten steel undergoes treatment in a ladle, the
bath can be stirred by bubbling upwardly through the bath a stirring gas composed
of argon and carbon monoxide. For a given carbon content, there is a percentage of
carbon monoxide in the stirring gas which is an equilibrium with carbon and oxygen
in the bath of molten steel. This characteristic can be employed to change the dissolved
oxygen content in the steel. It will also change the carbon content of the steel,
but it will not substantially change the manganese (or iron) content of the steel
as does the method wherein the slag is diluted with lime.
[0055] In that procedure wherein the oxygen content of the molten steel bath is changed
by bubbling through the bath a gaseous mixture comprising argon and carbon monoxide,
the oxygen content may be either increased or decreased. For example, for a steel
with a carbon content of 0.08 wt.%, if there are 100 mg/kg (ppm) of dissolved oxygen
in the steel, this amount of oxygen is in equilibrium with a gas containing 40% carbon
monoxide. If the carbon monoxide content of the gas is below 40% it will remove oxygen
(and carbon) from the steel to form additional carbon monoxide. If the carbon monoxide
content of the gas is above 40%, oxygen (and carbon) from the carbon monoxide will
go into the molten steel. Thus by controlling the carbon monoxide content of the stirring
gas bubbled through the steel, oxygen can either be added or withdrawn from the molten
steel.
[0056] This method, employing carbon monoxide in the stirring gas, may be utilized in connection
with the same steels described above in connection with the method wherein a diluent
oxide is added to the slag. Both methods are employed with a steel typically containing
about 0.06-0.09 wt.% carbon, and the oxygen content is controlled by both methods
so that it is at a desired amount in the range of about 60-150 mg/kg (ppm) at the
time the steel undergoes solidification. In both methods, solid deoxidizing agents
are excluded from the steel.
[0057] Hydrogen can cause problems in the steels described above, and in the method employing
carbon monoxide in the stirring gas, hydrocarbon reducing agents are excluded from
the bath of molten steel during the performance of the method.
[0058] For a given carbon content and a given dissolved oxygen content in the molten steel,
the percentage of carbon monoxide in the stirring gas which is in equilibrium therewith
is information which is either available in handbooks, or its determination is within
the ordinary skill of steel-making metallurgists. Similarly for a given dissolved
oxygen content in molten steel, the percentage of MnO or FeO in a covering slag layer
which is in equilibrium with that amount of dissolved oxygen is information which
is available or determinable.
[0059] The amount of diluent oxide necessary to add to the slag layer in order to reduce
the dissolved oxygen content to the desired level, is something which can be calculated
theoretically, at least initially, but it can also be determined empirically by adding
the diluent oxide to the slag layer in batches and thereafter periodically monitoring
the dissolved oxygen content of the molten steel. If the oxygen content is not reduced
sufficiently after adding a given amount of diluent oxide (e.g. 400-500 kg of lime),
an additional amount of diluent oxide can be added until the periodic monitoring of
the dissolved oxygen content of the molten steel shows that the desired level has
been reached.
[0060] With respect to the method employing carbon monoxide in the stirring gas, the amount
of gas required to change the oxygen content to the desired level can be theoretically
calculated, initially, but it can also be determined empirically by continuously or
periodically introducing the gas into the bath of molten steel and periodically monitoring
the dissolved oxygen content of the molten steel and eventually discontinuing the
introduction of the gas into the steel when the oxygen content has changed to the
desired level.
[0061] The foregoing detailed description has been given for clearness of understanding
only, and no unnecessary limitations should be understood therefrom, as modification
will be obvious to those skilled in the art.