Technical Field
[0001] The present invention relates to an estimation method of the depositional shape of
the charged material inside a blast furnace and a replacement method of the coke inside
the blast furnace.
Background Art
[0002] A blast furnace is operated as follows. Iron ore and coke are charged from a furnace
top, high-temperature air is blown in through tuyeres provided in a furnace lower
part, and molten pig iron and slag are discharged through tap holes. In a process
of the upward movement, inside the furnace, of high-temperature reducing gases such
as CO and H
2 generated in regions ahead of the tuyeres, molten pig iron is produced by heating,
reducing, and melting the iron ore that moves downward inside the furnace. The high-temperature
air continues to be blown into the furnace during a steady operation; however, there
may be taken a measure referred to as blowing down under which air-blowing into the
blast furnace is temporarily stopped due to non-steady events such as a repair of
a furnace body and addressing an operational trouble. In such a case, the temperature
of the charged material inside the furnace is decreased due to heat removal from the
furnace body and air suction from the tuyeres.
[0003] When the temperature inside the furnace is decreased, the molten material inside
the furnace is increased in viscosity and further solidifies, thereby becoming difficult
to be discharged through the tap holes. When air-blowing is performed through the
tuyeres in such a situation, the molten pig iron and slag subjected to reduction melting
are not discharged, and the build-up amount of the molten pig iron and slag in the
furnace lower part is thereby increased. There is also a case in which the molten
pig iron and slag that have built up in the furnace lower part become able to be discharged
with the heating of the furnace lower part by dripping molten pig iron and slag. However,
when the temperature increase of the furnace lower part is insufficient, the situation
in which there is a difficulty in discharging the molten pig iron and slag continues,
and the build-up amount of the molten pig iron and slag further increases. When the
level of the molten pig iron and slag (the height of a surface of the molten pig iron
and slag) reaches a tuyere due to a remarkable increase in the build-up amount, troubles
such as erosion of a tuyere and blockage of a blast pipe will be caused. In such a
case, air-blowing into the furnace cannot be performed; thus, heat input into the
furnace ceases, which leads to a hearth chilling accident.
[0004] The hearth chilling accident here refers to an event in which the molten pig iron
and slag cannot be discharged through the tap holes due to a remarkable decrease of
the heat level inside the blast furnace, and a steady operation becomes difficult
to be continued. When such an accident occurs, the following measures are taken to
recover the furnace condition. That is, a solidified material positioned between one
tap hole and tuyeres just above the tap hole is melted by a technique, such as oxygen-blowing,
and is discharged to ensure an outlet for the molten material. Subsequently, air-blowing
is performed through the tap hole and the two to three tuyeres just above the tap
hole, and, while a solidified layer therearound is melted gradually by using the generated
molten material, the numbers of tap holes and tuyeres in use are raised nearly to
those in the steady operation. Because a recovery from the hearth chilling accident
to the steady operation usually takes two to three months, the production amount of
molten pig iron is understandably remarkably decreased during the recovery. In addition
to that, there is a great danger that an operator is exposed to a high-temperature
molten material and a poisonous gas in the process of the recovery work. Thus, such
a hearth chilling accident can be considered as an operational trouble that entails
huge loss and risk in economic and safety terms.
[0005] As described above, because the heat level inside the furnace is low at the time
of a startup operation after the blowing down, the risk of the hearth chilling accident
is increased. Thus, in the existing art, the coke ratio is increased to increase the
heat level inside the furnace before the blowing down, and the risk of a hearth chilling
accident is reduced. However, with an increase in the time period of the blowing down,
the heat level inside the furnace gradually becomes unable to be maintained by such
heat compensation due to the increase in the coke ratio. In such a case, as Fig. 1
illustrates, there is used a method in which air-blowing is suspended after the charged
material inside the furnace is reduced in volume from the upper end of a bosh part
of the blast furnace to the level of the tuyeres on condition of the high coke ratio,
a raw material is charged, again on condition of the high coke ratio before the startup
from the blowing down, and air-blowing into the furnace is then resumed. Such an blowing
down is referred to as blowing down with lowering stock level. Such a blowing down
with lowering stock level, which is conducted in the case of a large-scale facility
repair or a long-term suspension of a blast furnace operation, is an blowing down
continuing over a time period longer than a usual blowing down, thereby having a further
increased risk of furnace cooling at the time of startup.
[0006] As a measure to reduce the furnace-cooling risk during such an blowing down or a
blowing down with lowering stock level, there is proposed a method in which, as Fig.
1 illustrates, before air-blowing, a burner is inserted into a tap hole and is caused
to blow in oxygen and fuel, the heat level in a region from the tuyere to the tap
hole is raised sufficiently, and air-blowing is then started (Patent Literature 1).
In addition, to improve the gas and molten-material permeability in the furnace lower
part, there is proposed a method in which a portion of the coke, in the furnace lower
part, pulverized and decreased in strength (deteriorated coke) is removed and replaced
by new coke (Patent Literature 2).
Citation List
Patent Literature
Non Patent Literature
Summary of Invention
Technical Problem
[0009] The approach described in Patent Literature 1 is effective for improving the heat
level in the furnace lower part of the blast furnace. In view of the purpose of reducing
the risk of a hearth chilling accident, it is considered that simultaneously adopting,
in combination, an approach of replacing deteriorated coke that is pulverized and
decreased in strength with new coke, as in Patent Literature 2, can ensure far better
gas and molten-material permeability in the furnace lower part and can thus reduce
the risk of a hearth chilling accident. However, by partially removing the coke in
the furnace lower part by half measures, the charged material above the consumed portion
locally moves down, and the layering structure of the raw material to be subsequently
charged will become nonuniform; thus, there is concern about a manifestation of adverse
effects on the operation, such as lowered gas permeability in the furnace upper part
and reduction failure of the raw material.
[0010] The present invention provides, in a blast furnace in a blowing down with lowering
stock level, an estimation method of a depositional shape of a charged material inside
the blast furnace formed after coke inside the blast furnace is consumed by using
a burner when the blast furnace is caused to start up.
[0011] The present invention further provides a replacement method of coke inside the blast
furnace using the estimation method.
Solution to Problem
[0012] The subject matter of the present invention is as follows.
- [1] An estimation method of a depositional shape of a charged material inside a blast
furnace, in which, when a blast furnace in a blowing down with lowering stock level
is caused to start up, there is estimated a depositional shape of a charged material
inside the blast furnace formed after a burner is inserted into the blast furnace
through a tap hole of the blast furnace and is used to consume coke inside the blast
furnace, the estimation method including the steps of:
estimating a depositional shape of a charged material inside a blast furnace in a
blowing down with lowering stock level;
estimating a charged region of coke inside the blast furnace from the depositional
shape of the charged material inside the blast furnace estimated through the previous
step and from a shape of a solidified layer on a bottom part inside the blast furnace;
estimating an amount of coke inside the blast furnace that is consumed by using the
burner; and
estimating, from the amount of the coke inside the blast furnace, a depositional shape
of a charged material inside the blast furnace formed after consumption of the coke
inside the blast furnace.
- [2] A replacement method of coke inside a blast furnace using the estimation method
of the depositional shape of the charged material inside the blast furnace according
to the previous article [1], the replacement method including:
charging coke into the blast furnace so as to reduce a change between the depositional
shape of the charged material inside the blast furnace in the blowing down with lowering
stock level and the depositional shape of the charged material inside the blast furnace
formed after the consumption of the coke inside the blast furnace.
Advantageous Effects of Invention
[0013] According to the present invention, in the blast furnace in the blowing down with
lowering stock level, it is possible to estimate the depositional shape of the charged
material inside the blast furnace formed after the coke inside the blast furnace (deteriorated
coke) is consumed by using the burner when the blast furnace is caused to start up.
[0014] According to the present invention, a change in the depositional shape of the charged
material inside the blast furnace with the consumption of the deteriorated coke is
estimated, and coke is charged into the blast furnace with reference to the estimation
result. Thus, while a change in the depositional shape of the charged material inside
the blast furnace with the replacement of the coke inside the blast furnace is reduced,
the coke inside the blast furnace in the blowing down with lowering stock level (deteriorated
coke) is replaced by new coke, and the gas and molten-material permeability in the
furnace lower part can thereby be improved. As a result, the blast furnace in a state
of blowing down can be caused to start up stably to reach a state of steady operation.
Brief Description of Drawings
[0015]
[Fig. 1] Fig. 1 is a schematic view illustrating an example of a depositional shape
of charged material inside a blast furnace in a blowing down with lowering stock level
and a state in which a burner is inserted into the furnace through a tap hole of the
blast furnace.
[Fig. 2] Fig. 2 illustrates a charged region of the coke inside the furnace that is
estimated in the present example.
[Fig. 3] Fig. 3 illustrates the depositional shape of the charged material inside
the furnace formed after consumption of the coke inside the furnace that is estimated
in the present example.
Description of Embodiments
[0016] The present invention is implemented for a blast furnace. The blast furnace refers
to an industrial furnace for producing molten pig iron by using a main raw material
such as iron ore and sintered ore, including iron oxide and a reducing material such
as coke, including carbon or hydrogen. The main raw material and the reducing material
are charged, in layers, from a furnace top, and a blast of hot air containing oxygen
and the reducing material such as powdered coal are delivered into the furnace through
tuyere parts. Through a process in which CO and H
2 generated through gasification of the reducing material in the vicinity of each of
the tuyeres flow to a furnace upper part, the main raw material charged from the furnace
top is heated, reduced, and melted, and molten pig iron is thus generated. Inside
the furnace, the generated molten pig iron drips to be collected on a furnace hearth
part and is discharged through tap holes provided in a side face of the lower part
of the blast furnace. Although the facility design of a blast furnace including, for
example, the inner capacity of a blast furnace, a raw material charging mechanism,
and the number of tuyeres often varies from one furnace body to another, the present
invention is applicable regardless of such differences in the facility design.
[0017] In addition, in the operation of the blast furnace, various materials are used as
the main raw material and the reducing material that are charged from the furnace
top and as the reducing material that is blown into through the tuyere parts. Examples
of the main raw material include iron ore, sintered ore, pellet, scrap, and reduced
iron. Examples of the reducing material that is charged from the furnace top include
lump coke, and smaller coke such as coke granules and ferrocoke. Examples of the reducing
material that is blown into through the tuyere parts include: powdered coal; coke
breeze; plastic; a combustible gas, such as a natural gas, including at least one
kind of carbon atoms and hydrogen atoms; and liquid fossil fuel. The present invention
is applicable regardless of types of the raw material and the reducing material to
be used.
[0018] In the present invention, it is found that a change in the depositional shape of
the charged material inside the furnace before and after the consumption of deteriorated
coke can be estimated by estimating the depositional shape of the charged material
inside the blast furnace in a blowing down with lowering stock level (hereinafter,
referred to also as an initial depositional shape), the shape of a solidified layer
on a bottom part inside the furnace (solidified layer shape), the consumption behavior
of the coke inside the furnace (deteriorated coke), and the depositional shape of
the charged material inside the furnace formed after the consumption of the deteriorated
coke. It is also found that, by appropriately determining, for example, the amount
and a charging position of the coke to be charged anew based on the estimation result
of the depositional shape change, there can be reduced a change in the depositional
shape of the charged material inside the furnace before and after the charged coke
inside the furnace under the blowing down with lowering stock level is replaced by
the coke to be charged anew when the furnace is caused to start up from the blowing
down with lowering stock level.
<Estimation Method of Depositional Shape of Charged Material Inside Blast Furnace>
[0019] An estimation method of a depositional shape of a charged material inside a blast
furnace of the present invention includes the steps of: estimating a depositional
shape of a charged material inside a blast furnace in a blowing down with lowering
stock level; estimating a charged region of coke inside the blast furnace from the
depositional shape of the charged material inside the blast furnace estimated through
the previous step and from a shape of a solidified layer on a bottom part inside the
blast furnace; estimating an amount of coke inside the blast furnace that is consumed
by using a burner; and estimating, from the amount of the coke inside the blast furnace,
a depositional shape of a charged material inside the blast furnace formed after consumption
of the coke inside the blast furnace.
(Step of Estimating Depositional Shape of Charged Material Inside Blast Furnace in
Blowing Down with Lowering Stock Level)
[0020] In the step of estimating a depositional shape of a charged material inside a blast
furnace in a blowing down with lowering stock level, the depositional shape (initial
depositional shape) of the charged material inside the blast furnace in a blowing
down with lowering stock level is estimated. Examples of the estimation method of
the initial depositional shape include a method in which the initial depositional
shape is estimated from the results obtained by measuring, with a rangefinder, distances
from the furnace top of the blast furnace in a blowing down with lowering stock level
to several spots on the surface of the charged material inside the furnace. Examples
of the rangefinder include, but not particularly limited to, a noncontact rangefinder
such as a laser rangefinder. The depositional shape can be estimated three-dimensionally
by measuring, with the rangefinder, the distances to several spots on the surface
of the charged material inside the furnace.
However, the estimation method of the initial depositional shape is not limited thereto,
and the technique of the present invention can be implemented regardless of the estimation
method of the initial depositional shape.
(Step of Estimating Charged Region of Coke Inside Blast Furnace)
[0021] In the step of estimating a charged region of coke inside the blast furnace, a charged
region of the coke inside the blast furnace is estimated from the depositional shape
(initial depositional shape) of the charged material inside the furnace estimated
by the step of estimating the initial depositional shape described above and from
the shape of a solidified layer on the bottom part inside the furnace. The blast furnace
in a blowing down with lowering stock level includes a solidified layer that has increased
in size on the bottom part inside the furnace. In the present step, the shape of the
solidified layer on the bottom part inside the furnace is estimated. Examples of the
estimation method of the shape of the solidified layer on the bottom part inside the
furnace include an approach using the boundary element method, such as an approach
described in Non Patent Literature 1. In the approach described in Non Patent Literature
1, a heat transfer calculation using the boundary element method is performed on the
assumption that the interface of the solidified layer coincides with the isotherm
of the solidification temperature (1150° C) of pig iron. This approach is a method
in which sequential calculation is performed to determine the solidification interface
such that the error between the value of a temperature of the furnace bottom in an
actual furnace actually measured by a thermocouple and the calculation result of a
temperature obtained by using the boundary element method is minimized. The shape
of the solidified layer on the bottom part inside the furnace can be estimated from
the solidification interface determined as described above. Note that thermocouples
are usually provided in the furnace bottom part of the blast furnace below the tuyeres,
at plural positions in the circumferential direction and the height direction of the
blast furnace.
[0022] After the shape of the solidified layer on the bottom part inside the furnace is
estimated as described above, a charged region of the coke inside the furnace is estimated.
As for the estimation method of the charged region of the coke inside the furnace,
by using the initial depositional shape and the shape of the solidified layer on the
bottom part inside the furnace that are estimated as described above, a region other
than the region of the shape of the solidified layer can be estimated as the charged
region of the coke inside the furnace.
(Step of Estimating Amount of Coke Inside Blast Furnace That IS Consumed by Using
Burner and Estimating, From the Amount of Coke Inside Blast Furnace, Depositional
Shape of Charged Material Inside Blast Furnace Formed After Consumption of Coke Inside
Blast Furnace)
[0023] In the step of estimating an amount of coke inside the blast furnace that is consumed
by using a burner, there is estimated the amount of the coke inside the blast furnace
that is consumed by using a burner inserted into the furnace through a tap hole of
the blast furnace. Examples of this estimation method include a method in which estimation
is performed by using: a flow passage, in a coke-charged layer (the charged region
of the coke inside the furnace), of a combustion gas that is blown into the furnace
from the burner; and the composition of the combustion gas, on the assumption that
all of the combustion gas blown from the burner reacts with coke. However, the temperature
of the combustion gas decreases gradually while the combustion gas moves upward inside
the furnace, thereby there is a probability of becoming lower than a temperature at
which a reaction proceeds in the coke-charged layer. In addition, even if the temperature
of the combustion gas is a temperature at which a reaction proceeds, the reaction
speed varies depending on the temperature. Thus, it is preferable that the consumption
behavior of the coke inside the furnace (deteriorated coke) is estimated in consideration
of the heat transfer between the combustion gas and the coke inside the furnace and
the temperature dependence of the reaction speeds of various reactions.
[0024] As for the gas used for the burner inserted through a tap hole, a gas as it is or
after its burning that reacts with and consumes the coke inside the furnace may be
used. Although the inventors of the present invention used LNG and oxygen as the gas,
the type of the gas usable in the technique described in the present invention is
not limited thereto.
[0025] After the amount of the coke inside the furnace that is consumed by using the burner
(a consumption region of the coke inside the furnace) is estimated as described above,
and, in the step of estimating a depositional shape of a charged material inside the
blast furnace formed after consumption of the coke inside the blast furnace, the depositional
shape of the charged material inside the blast furnace formed after consumption of
the coke inside the blast furnace is estimated based on the estimated amount of the
coke inside the furnace. Regarding the depositional shape formed after the consumption
of the coke inside the furnace, as Fig. 3 illustrates, based on hollow regions generated
by consuming the coke inside the furnace (deteriorated coke) with the combustion gas,
a region other than the hollow regions can be estimated as the depositional shape
of the charged material inside the furnace formed after the consumption of the coke
inside the furnace.
<Replacement Method of Coke Inside Blast Furnace>
[0026] For a replacement method of coke inside a blast furnace of the present invention,
the above-described estimation method of the depositional shape of the charged material
inside the blast furnace is used. Specifically, based on the depositional shape (initial
depositional shape) of the charged material inside the furnace in the blowing down
with lowering stock level and the depositional shape of the charged material inside
the furnace formed after the consumption of the coke inside the furnace, new coke
is charged into the blast furnace so as to reduce a change between the depositional
shapes, and the coke inside the furnace in the blowing down with lowering stock level
is thus replaced by the new coke. That is, regarding the amount of the coke to be
charged anew and a position at which the coke is charged, it is desirable that the
coke is charged so as to reproduce the initial depositional shape of the charged material
inside the furnace. Examples of the method for charging coke anew include a method
in which coke is charged from the furnace top as in a normal operation and a method
in which a conveyor belt is inserted into the furnace through a tuyere part, and charging
is performed by using the conveyor belt. The larger the difference in height between
a position at which new coke is charged and the charged material inside the furnace,
the higher the possibility that the charged new coke increasingly becomes granular.
Thus, new coke is preferably charged into the furnace at a position whose difference
in height from the charged material inside the furnace is minimized.
[0027] As described above, with the approach of the present invention, a change in the depositional
shape with the consumption of the coke inside the blast furnace in a blowing down
with lowering stock level (deteriorated coke) is estimated, and coke is charged into
the blast furnace with reference to the estimation result. Thus, while a change in
the depositional shape of the charged material inside the blast furnace with the replacement
of the coke inside the furnace is reduced, the deteriorated coke is replaced by new
coke, and the gas and molten-material permeability of the furnace lower part can thereby
be improved. As a result, the blast furnace in a state of blowing down can be caused
to start up further stably to reach a state of steady operation.
EXAMPLE
[0028] Hereinafter, the present invention will specifically be described with an example.
However, the present invention is not limited to the example below.
[0029] In the present example, in a commercial blast furnace in a long-term blowing down
with lowering stock level, after the depositional shape of the charged material inside
the furnace formed after consumption of deteriorated coke was estimated based on the
above-described embodiment, new coke was charged, air-blowing through tuyeres was
then started, and a startup operation of the blast furnace was performed.
[0030] First, the initial depositional shape of the charged material inside the furnace
was estimated from the data of distances from the furnace top of the blast furnace
in the blowing down with lowering stock level to the charged material inside the furnace
measured by using a noncontact rangefinder (in the present example, a laser rangefinder).
Further, by using the data given by thermometers provided in the furnace bottom part
of the blast furnace, a solidified layer shape on the bottom part inside the blast
furnace was estimated by the approach described in the embodiment using the boundary
element method. The result of estimating a charged region of the coke inside the furnace
through such approaches is illustrated in Fig. 2. Note that Fig. 2(a) illustrates,
from diagonally above, the estimated charged region of the coke inside the furnace,
and Fig. 2(b) is a vertical sectional view (schematic view) of a tap hole (2th) in
Fig. 2(a).
[0031] Subsequently, on the assumption that a burner is inserted through a tap hole of the
furnace bottom part of the blast furnace and is caused to blow a combustion gas into
the furnace, a change in the depositional shape of the charged material inside the
furnace with the consumption of the coke inside the furnace (deteriorated coke) by
the blowing-in of the combustion gas was estimated by the approach described in the
above-described embodiment. The estimation result of the depositional shape of the
charged material inside the furnace formed after the consumption of the deteriorated
coke is illustrated in Fig. 3. Note that Fig. 3(a) illustrates, from diagonally above,
the estimated depositional shape of the charged material inside the furnace formed
after the consumption of the deteriorated coke, and Fig. 3(b) is a vertical sectional
view (schematic view) of the tap hole (2th) in Fig. 3(a). The comparison between Fig.
2 and Fig. 3 reveals that, from the vicinity of a tap hole toward the upper side,
the deteriorated coke was consumed, and cone-shaped hollows were formed. In addition,
the weight of new coke required to be charged in the hollows was calculated from the
volume of the hollows obtained through the comparison between the estimation results
of Fig. 2 and Fig. 3.
[0032] Based on the calculation result of the weight described above, the burner was inserted
through a tap hole, the deteriorated coke inside the furnace was consumed, the new
coke was charged into the hollows though tuyeres, and coke and a main raw material
were then charged from the furnace top to an upper part relative to the tuyere level.
Subsequently, when air-blowing was started through the tuyeres to perform the startup
operation, molten pig iron and slag were smoothly discharged through the tap holes,
and the blast furnace was able to be returned to the state of steady operation, without
a serious trouble such as a trouble that the molten pig iron and slag are prevented
from being discharged, and the remaining pig iron and slag inside the furnace thus
build up to the tuyere level (the height of the tuyeres).
[0033] The above-described result has revealed that, with the present invention, while a
change in the depositional shape of the charged material inside the blast furnace
with the replacement of the coke inside the furnace is reduced, the gas and molten-material
permeability of the furnace lower part can be improved by replacing deteriorated coke
with new coke, and the blast furnace in the state of blowing down with lowering stock
level can be caused to start up stably to reach the state of steady operation.
Reference Signs List
[0034]
- 1
- blast furnace body
- 2
- tuyere (air-blowing tuyere)
- 3
- tap hole
- 4
- coke
- 5
- solidified layer
- 6
- burner