JP2005281756A - Method for controlling tapped molten pig iron and slag in blast furnace - Google Patents
Method for controlling tapped molten pig iron and slag in blast furnace Download PDFInfo
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- JP2005281756A JP2005281756A JP2004096415A JP2004096415A JP2005281756A JP 2005281756 A JP2005281756 A JP 2005281756A JP 2004096415 A JP2004096415 A JP 2004096415A JP 2004096415 A JP2004096415 A JP 2004096415A JP 2005281756 A JP2005281756 A JP 2005281756A
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- pig iron
- molten pig
- blast furnace
- tuyere
- slag
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- 238000000034 method Methods 0.000 title claims abstract description 14
- 239000002893 slag Substances 0.000 title abstract description 5
- 229910000805 Pig iron Inorganic materials 0.000 title abstract 10
- 238000007599 discharging Methods 0.000 claims abstract description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 7
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 239000000571 coke Substances 0.000 abstract description 24
- 238000010079 rubber tapping Methods 0.000 abstract description 19
- 239000003245 coal Substances 0.000 abstract description 16
- 239000002184 metal Substances 0.000 description 15
- 229910052751 metal Inorganic materials 0.000 description 15
- 230000008021 deposition Effects 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
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- Manufacture Of Iron (AREA)
Abstract
Description
本発明は、高炉内の溶銑を溶滓ごと出銑孔から出銑滓として排出する際の高炉の出銑滓制御方法に関するものである。 The present invention relates to a blast furnace discharge control method when discharging the hot metal in the blast furnace together with the hot metal from the discharge hole.
高炉では、一般的に、コークスや鉱石等を上方から投入し、炉の下部に設けられた羽口から熱風を送風することにより、当該羽口前方の所謂レースウエイで燃焼に類似した温度上昇が発生し、これによって鉱石が溶融し、溶銑と溶滓として炉床に流下する。このように高炉の炉床部に貯留された溶銑及び溶滓(以下、単に溶銑滓とも記す)は、炉壁下端部に形成された出銑孔から出銑滓として排出される。 Generally, in a blast furnace, coke, ore, etc. are introduced from above, and hot air is blown from a tuyere provided at the lower part of the kiln, so that a temperature rise similar to combustion occurs in a so-called raceway in front of the tuyere. This causes the ore to melt and flow down to the hearth as hot metal and hot metal. Thus, the hot metal and hot metal (hereinafter also simply referred to as hot metal) stored in the hearth part of the blast furnace are discharged as the hot metal from the tap hole formed at the lower end of the furnace wall.
この出銑滓排出の際の従来の制御方法としては、例えば出銑孔からの出銑滓の状態、具体的には出銑と出滓との比率に基づいて、出銑孔から高炉内に押し込むマッドの押量と出銑孔深度との比率、即ち深度指数を調整することにより、出銑孔前の空間、所謂フリースペースの形態を制御して良好な出銑滓を確保するものがある(例えば特許文献1)。
しかしながら、前記従来の出銑滓制御方法では、まず出銑孔から排出される出銑滓の状態を検出し、その後、マッド押量と出銑孔深度との比率からなる深度指数を調整し、然る後、出銑孔前空間の形態が調整されて出銑滓量を確保できるというものであるため、出銑孔前空間の形態の調整までに手間と時間がかかるという問題がある。
本発明は、良好な出銑量を確保するために出銑孔前空間の形態の調整が容易な高炉の出銑滓制御方法を提供することを目的とするものである。
However, in the conventional tapping control method, first, the state of tapping discharged from the tapping hole is detected, and then the depth index consisting of the ratio between the mud pressing amount and the tapping depth is adjusted, After that, since the form of the space before the tap hole is adjusted to secure the amount of the tap, there is a problem that it takes time and effort to adjust the form of the space before the tap hole.
An object of the present invention is to provide a method for controlling the output of a blast furnace in which the form of the space before the tap hole is easily adjusted in order to ensure a good amount of tap.
上記課題を解決するために、本発明の高炉の出銑滓制御方法は、高炉内の溶銑を溶滓ごと出銑孔から出銑滓として排出する際の高炉の出銑滓制御方法であって、前記出銑孔の上方の羽口から投入する微粉状燃料を、他の羽口から投入する微粉状燃料より少なくするか、又は零とすることを特徴とするものである。 In order to solve the above problems, the blast furnace discharge control method of the present invention is a blast furnace discharge control method for discharging the molten iron in the blast furnace together with the molten iron from the discharge hole. The pulverized fuel introduced from the tuyere above the tap hole is less than the pulverized fuel introduced from the other tuyere or zero.
而して、本発明の高炉の出銑滓制御方法によれば、出銑孔の上方の羽口から投入する微粉状燃料を、他の羽口から投入する微粉状燃料より少なくするか、又は零とすることにより、出銑孔前のコークスの消費が大きくなり、その結果、出銑孔前の空間が大きくなって出銑滓量が増大する。 Thus, according to the blast furnace tapping control method of the present invention, the pulverized fuel introduced from the tuyere above the tapping hole is less than the pulverized fuel fed from the other tuyere, or By setting it to zero, the consumption of coke before the tap hole is increased, and as a result, the space before the tap hole is increased and the amount of the tap is increased.
次に本発明に係る高炉の出銑滓制御方法の一実施形態を図面に基づいて詳細に説明する。
まず、図1には、本実施形態の高炉の羽口から炉床部までの縦断面図を示す。高炉の炉壁1の下部には、その全周に渡って、熱風送風口としての羽口2が多数設けられている。この羽口2には、図示されない熱風炉で1000℃程度まで加熱されたガスが供給され、当該羽口2から高炉内に吹出された熱風は、後述するコークス充填層4にレースウエイ3と呼ばれる高熱空間部を形成する。なお、羽口2には、微粉状の燃料、具体的には微粉炭を噴出するノズル10が設けられており、通常は、全ての羽口2のノズル10から微粉炭を噴出しながら操業を行う。
Next, an embodiment of a method for controlling the output of a blast furnace according to the present invention will be described in detail with reference to the drawings.
First, in FIG. 1, the longitudinal cross-sectional view from the tuyere of the blast furnace of this embodiment to a hearth part is shown. A large number of tuyere 2 as hot air blowing ports are provided in the lower part of the furnace wall 1 of the blast furnace over the entire circumference. The tuyere 2 is supplied with gas heated to about 1000 ° C. in a hot air furnace (not shown), and the hot air blown out from the tuyere 2 into the blast furnace is called a raceway 3 in a coke packed bed 4 to be described later. A high heat space is formed. The tuyere 2 is provided with a
一方、高炉の上方から投入されたコークスや鉱石等は、前記羽口2より下方では、ほぼコークスだけからなるコークス充填層4を形成する。これは、前記レースウエイ3での高温加熱によって鉱石が溶融し、それが溶銑及び溶滓,つまり溶銑滓9として炉床部に流下するためである。
また、炉床部は、耐火材からなるマッドで覆われて、マッド堆積層5を構成している。このマッドは、炉壁からマッド堆積層5まで穿設された出銑孔7を閉塞するために用いられるものであり、このマッド堆積層5が、本来の炉床を保護している。
On the other hand, coke, ore, and the like charged from above the blast furnace form a coke packed bed 4 made of only coke below the tuyere 2. This is because the ore is melted by high-temperature heating in the raceway 3 and flows down to the hearth as hot metal and hot metal, that is,
Further, the hearth part is covered with a mud made of a refractory material to constitute a mud deposition layer 5. This mud is used to close the tap hole 7 drilled from the furnace wall to the mud deposition layer 5, and this mud deposition layer 5 protects the original hearth.
そして、高炉の炉床部,つまり前記マッド堆積層5上に溶銑滓9が或る程度溜まったら、前記炉壁1からマッド堆積層5まで出銑孔7を貫通し、この出銑孔7から溶銑滓9を出銑滓として排出する。
そして、本実施形態では、前記出銑滓の排出に先立ち或いはそれと同時に、出銑孔7の上方の羽口2から噴出する微粉炭の量を、他の羽口2から噴出する微粉炭の量より少なくする、或いは当該出銑孔7の上方の羽口2から噴出する微粉炭の量を零にする。その理由を以下に説明する。
When a certain amount of
In the present embodiment, the amount of pulverized coal ejected from the tuyere 2 above the spout hole 7 prior to or simultaneously with the discharge of the slag is changed to the amount of pulverized coal ejected from the other tuyere 2. The amount of pulverized coal discharged from the tuyere 2 above the tap hole 7 is reduced to zero. The reason will be described below.
図2は、図1の高炉内を簡潔に表したものであり、高炉の内部にはコークス及び鉱石が充満しているものとする。前述のように、羽口2は、高炉1の炉壁全周にわたって設けられているので、炉内のコークス充填層4を炉の外周部、即ち図に破線で分断した領域Aと、炉の中央部、即ち図に破線で分断した領域Bとに分けて考える。このうち、炉の外周部(領域A)に存在するコークス充填層4内のコークスは、レースウエイ3に向けて上方から直接接近する(レースウエイ3に入る)。一方、炉の中央部(領域B)に存在するコークス充填層4内のコークスは、出銑滓に伴って、一旦、羽口レベルより降下し、溶銑滓レベルの上下に伴って浮沈し、レースウエイ3には下方から接近する(レースウエイ3に入る)。この領域Bでのコークス浮上量が大きいほど、出銑滓時の出銑孔前の空間6が大きくなり、出銑滓量が増大する。そのためには、出銑孔上方のレースウエイ3でのコークス消費が大きいことが望まれる。 FIG. 2 is a simplified representation of the inside of the blast furnace of FIG. 1, and it is assumed that the inside of the blast furnace is filled with coke and ore. As described above, the tuyere 2 is provided over the entire circumference of the furnace wall of the blast furnace 1, so that the coke packed bed 4 in the furnace is surrounded by the outer periphery of the furnace, that is, the region A divided by a broken line in the drawing, Consider the central portion, that is, the region B divided by a broken line in the figure. Among these, the coke in the coke packed bed 4 existing in the outer peripheral portion (region A) of the furnace approaches directly from above toward the raceway 3 (enters the raceway 3). On the other hand, the coke in the coke packed bed 4 existing in the center of the furnace (region B) once falls from the tuyere level as it comes out, and floats and sinks as the hot metal level rises and falls. Approaching Way 3 from below (entering Race Way 3). The larger the coke flying height in this region B, the larger the space 6 before the tapping hole at the time of tapping, and the amount of tapping increases. For this purpose, it is desired that the coke consumption in the raceway 3 above the tap hole is large.
一方、前述した羽口2から噴出される微粉炭は、レースウエイ3を高温に保持するために用いられるが、微粉炭の噴出量が大きくなりすぎると、未燃チャー(石炭の中の不燃物)や灰化物によって、レースウエイ3の外側に形成される、シェルと呼ばれる硬化層が肥大化する。このシェルは、通気性も通液性もよくないので、コークスの消費を阻害し、コークス充填層4の浮上も阻害する。更に、出銑孔7の上方に噴出された微粉炭自身の燃焼に酸素が消費されてしまうために、その下方のコークスの消費が阻害され、これによってもコークス重縁層4の浮上が阻害される。 On the other hand, the pulverized coal ejected from the tuyere 2 described above is used to keep the raceway 3 at a high temperature, but if the amount of pulverized coal ejected becomes too large, unburned char (incombustible material in the coal). ) And ashed product, a hardened layer called a shell formed outside the raceway 3 is enlarged. Since this shell has neither good air permeability nor liquid permeability, it inhibits the consumption of coke and also inhibits the floating of the coke packed layer 4. Further, since oxygen is consumed in the combustion of the pulverized coal itself ejected above the tap hole 7, the consumption of coke below it is inhibited, and this also inhibits the floating of the coke multi-layer 4. The
そのため、本実施形態では、出銑孔7の上方の羽口2から噴出する微粉炭の量を、他の羽口2から噴出する微粉炭の量より少なくする、或いは当該出銑孔7の上方の羽口2から噴出する微粉炭の量を零にすることで、出銑孔7の上方のコークス充填層4内のコークスの消費を促進し、もって出銑孔7近傍のコークス充填層4を浮上させ、出銑孔7前の空間6を大きくして、出銑滓量を増大する。
このように、本実施形態の高炉の出銑滓制御方法によれば、出銑孔7の上方の羽口2から噴出する微粉炭の量を、他の羽口2から噴出する微粉炭の量より少なくする、或いは当該出銑孔7の上方の羽口2から噴出する微粉炭の量を零にすることで、出銑孔7前の空間6を大きくして出銑滓量を増大することができるので、手間や時間をかけずに、容易に出銑滓量を確保することができる。
Therefore, in this embodiment, the amount of pulverized coal ejected from the tuyere 2 above the tap hole 7 is made smaller than the amount of pulverized coal ejected from the other tuyere 2 or above the tap hole 7. The consumption of coke in the coke packed bed 4 above the tap hole 7 is promoted by making the amount of pulverized coal ejected from the tuyere 2 zero, so that the coke packed bed 4 near the tap hole 7 is It floats up, the space 6 before the tap hole 7 is enlarged, and the amount of tapping increases.
Thus, according to the blast furnace tapping control method of the present embodiment, the amount of pulverized coal ejected from the tuyere 2 above the tapping hole 7 is changed to the amount of pulverized coal ejected from the other tuyere 2. By reducing the amount of pulverized coal ejected from the tuyere 2 above the tap hole 7 to be smaller, the space 6 in front of the tap hole 7 is enlarged and the amount of tapping is increased. Therefore, it is possible to easily secure the amount of output without taking time and effort.
1は炉壁
2は羽口
3はレースウエイ
4はコークス充填層
5はマッド堆積層
6は空間
7は出銑孔
8は流量制御弁
9は溶銑滓
10はノズル
1 is a furnace wall 2 is a tuyere 3 is a raceway 4 is a coke packed bed 5 is a mud deposit layer 6 is a space 7 is a spout hole 8 is a
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6436711A (en) * | 1987-07-31 | 1989-02-07 | Nippon Steel Corp | Blast furnace operating method |
JPH05156329A (en) * | 1991-12-02 | 1993-06-22 | Sumitomo Metal Ind Ltd | Method for operating powder injection from tuyere in blast furnace |
JP2002146415A (en) * | 2000-11-08 | 2002-05-22 | Kawasaki Steel Corp | Method for operating blast furnace |
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2004
- 2004-03-29 JP JP2004096415A patent/JP4808931B2/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6436711A (en) * | 1987-07-31 | 1989-02-07 | Nippon Steel Corp | Blast furnace operating method |
JPH05156329A (en) * | 1991-12-02 | 1993-06-22 | Sumitomo Metal Ind Ltd | Method for operating powder injection from tuyere in blast furnace |
JP2002146415A (en) * | 2000-11-08 | 2002-05-22 | Kawasaki Steel Corp | Method for operating blast furnace |
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