JPS6219482B2 - - Google Patents
Info
- Publication number
- JPS6219482B2 JPS6219482B2 JP1251684A JP1251684A JPS6219482B2 JP S6219482 B2 JPS6219482 B2 JP S6219482B2 JP 1251684 A JP1251684 A JP 1251684A JP 1251684 A JP1251684 A JP 1251684A JP S6219482 B2 JPS6219482 B2 JP S6219482B2
- Authority
- JP
- Japan
- Prior art keywords
- steam
- blowing
- converter
- induced
- during
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/38—Removal of waste gases or dust
- C21C5/40—Offtakes or separating apparatus for converter waste gases or dust
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
【発明の詳細な説明】
本発明は、転炉排ガス処理装置の誘引送風機の
駆動方法に係り、吹錬中に発生する蒸気を精錬工
程に合わせて使用することにより、誘引送風機の
駆動エネルギーを自給自足するようにした誘引送
風機の駆動方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for driving an induced blower in a converter exhaust gas treatment equipment, and uses steam generated during blowing in conjunction with the refining process to self-sufficient drive energy for the induced blower. This invention relates to a method for driving a self-sufficient induced fan.
転炉から発生する高温のCOガスは、誘引送風
機によつて排ガス処理装置内に誘引され、冷却除
塵され、有価ガスとしてガスホルダに回収され
る。 The high-temperature CO gas generated from the converter is drawn into the exhaust gas treatment equipment by an induced fan, cooled and dust removed, and recovered as valuable gas in a gas holder.
以下転炉排ガス処理装置の概要を第1図を用い
て説明する。図において、転炉1で発生した高温
のCOガスは、誘引送風機7によつてフード3内
に誘引され、冷却器4で冷却され、除塵器5,6
で除塵され、有価ガスとしてガスホルダ10に回
収される。又、吹錬の初期と末期のCO濃度の低
いガスは、切換えダンパ9の切換えにより、煙突
8より放散される。なお2は、転炉1の炉口とフ
ード3の間を密封するスカートである。 The outline of the converter exhaust gas treatment device will be explained below with reference to FIG. In the figure, high-temperature CO gas generated in a converter 1 is drawn into a hood 3 by an induced blower 7, cooled by a cooler 4, and removed by dust removers 5, 6.
The gas is removed from the gas and collected as a valuable gas in the gas holder 10. Further, gas with low CO concentration at the beginning and end of blowing is released from the chimney 8 by switching the switching damper 9. Note that 2 is a skirt that seals between the furnace mouth of the converter 1 and the hood 3.
一方、転炉操業は次の工程で行われる。先ず高
炉で生産された溶銑は、転炉1内に投入される。
以下これを受銑工程という。この受銑工程におい
て、スカート2を上昇させ転炉1を傾動し、溶銑
を受け入れるのである。次に転炉1を直立状態に
戻してスカート2を下降してシールし、酸素吹込
みランス11より、転炉1内に純酸素を吹き込
み、転炉1内の溶銑中に含まれている炭素を反応
させ脱炭する。以下、この工程を吹錬工程とい
う。次に吹錬工程が完了した後は、スカート2を
上昇して転炉1を傾動し、脱炭した溶銑を転炉1
より取り出す。以下これを出鋼工程という。 On the other hand, converter operation is carried out in the following steps. First, hot metal produced in a blast furnace is charged into a converter 1.
Hereinafter, this will be referred to as the pig iron receiving process. In this pig iron receiving process, the skirt 2 is raised and the converter 1 is tilted to receive hot metal. Next, the converter 1 is returned to an upright position, the skirt 2 is lowered and sealed, and pure oxygen is blown into the converter 1 from the oxygen injection lance 11 to remove the carbon contained in the hot metal in the converter 1. to react and decarburize. Hereinafter, this process will be referred to as the blowing process. Next, after the blowing process is completed, the skirt 2 is raised and the converter 1 is tilted, and the decarburized hot metal is transferred to the converter 1.
Take it out. Hereinafter, this will be referred to as the steel tapping process.
このように受銑工程、吹錬工程、出鋼工程によ
り1回の精錬が完了する。次の精錬は、同じよう
に、受銑工程、吹錬工程、出鋼工程が行われ、こ
の工程のくり返しにより、3回目の精錬、4回目
の精錬という具合に転炉操業が行われるのであ
る。 In this way, one refining process is completed through the pig iron receiving process, the blowing process, and the tapping process. In the next refining process, the pig iron receiving process, blowing process, and steel tapping process are performed in the same way, and by repeating these processes, a third refining process, a fourth refining process, and so on, are carried out in the converter operation. .
上記工程の中で、吹錬工程時は、純酸素と溶銑
中の炭素とが反応して大量のCOガスが発生する
が、受銑及び出鋼工程中は、このようなガスは発
生しない。以下受銑、出鋼及び準備工程を非吹錬
時という。 Among the above processes, during the blowing process, pure oxygen and carbon in the hot metal react and a large amount of CO gas is generated, but during the pig iron receiving and tapping processes, such gas is not generated. Hereinafter, the pig iron receiving, tapping and preparation processes are referred to as non-blowing time.
さて、従来の誘引送風機は、電動機によつて駆
動され、吹錬工程中は勿論のこと非吹錬中も駆動
されていた。 Now, the conventional induced blower is driven by an electric motor, and is driven not only during the blowing process but also during the non-blowing process.
転炉操業において、非吹錬中は、COガスが発
生しないので、誘引送風機の駆動は、必要ではな
く、この分無駄な電力を消費するという欠点があ
つた。 During converter operation, CO gas is not generated during non-blowing periods, so driving the induced blower is not necessary, which has the disadvantage of wasting power.
又、特開昭54−1206号には、誘引送風機の消費
電力を補うという目的から、誘引送風機の駆動方
式として、電動機と蒸気タービンを併用する技術
が示されているが、この場合も誘引送風機は、連
続的に運転され、非吹錬中に電力乃至は蒸気を無
駄に消費するという欠点があつた。 In addition, Japanese Patent Application Laid-open No. 1206/1986 discloses a technology that uses both an electric motor and a steam turbine as the drive method for an induced fan, with the aim of supplementing the power consumption of the induced fan, but in this case as well, the induced fan had the disadvantage that it was operated continuously, and electricity or steam was wasted during non-blowing.
本発明は、転炉操業の工程に合わせて、誘引送
風機駆動用蒸気タービンに蒸気を供給するように
し、無駄な蒸気の消費をなくして、誘引送風機の
駆動エネルギーを自給自足するようにした誘引送
風機の駆動方法を提供せんとするものである。 The present invention provides an induced fan that supplies steam to a steam turbine for driving an induced fan in accordance with the process of converter operation, eliminates wasteful steam consumption, and makes the induced fan self-sufficient in drive energy. The present invention aims to provide a driving method for the following.
即ち本発明は、吹錬工程中に発生する蒸気を一
坦蒸気溜めに貯え、この貯えた蒸気を吹錬工程中
にのみ誘引送風機駆動用蒸気タービンに導いて、
誘引送風機を駆動しながら吹錬中に蒸気を発生し
て次の吹錬工程における誘引送風機駆動用蒸気を
貯え、非吹錬中は誘引送風機駆動用蒸気タービン
への蒸気供給を停止して、常時蒸気溜めに蒸気を
貯えるようにしたことを特徴とする。 That is, the present invention stores steam generated during the blowing process in a steam reservoir, and guides the stored steam to a steam turbine for driving an induced blower only during the blowing process.
While driving the induced blower, steam is generated during blowing to store the steam for driving the induced blower in the next blowing process, and during non-blowing, the steam supply to the steam turbine for driving the induced blower is stopped and the steam is constantly It is characterized by storing steam in a steam reservoir.
以下本発明の一実施例について、詳細に説明す
る。第2図において、装置の概要を説明する。図
において、吹錬工程中に転炉1から発生するCO
ガスは、誘引送風機7により誘引され、冷却器4
にて冷却され、除塵器5′にて除塵された後、有
価ガスとして回収される。なお、図中9は切換ダ
ンパ、8は煙突である。 An embodiment of the present invention will be described in detail below. Referring to FIG. 2, the outline of the apparatus will be explained. In the figure, CO generated from converter 1 during the blowing process
The gas is induced by an induced blower 7 and is passed through the cooler 4.
After being cooled in a dust collector 5' and dust removed in a dust remover 5', the gas is recovered as a valuable gas. In addition, in the figure, 9 is a switching damper, and 8 is a chimney.
冷却器4内には、多数の伝熱管から成るふく射
伝熱部と接触伝熱部19が設けられており、循環
ポンプ15にて冷却水が循環している。 Inside the cooler 4, a radiant heat transfer section and a contact heat transfer section 19 each consisting of a large number of heat transfer tubes are provided, and cooling water is circulated by a circulation pump 15.
この冷却水は、転炉1から発生する高温のCO
ガス(約1200℃)によつて加熱され、蒸発してボ
イラドラム21に導かれる。このボイラドラム2
1内の蒸気は、配管16にて蒸気溜め12に貯え
られる。この蒸気溜め12に貯えられた蒸気は、
配管17、電動弁18を通つて、蒸気タービン1
3に導かれ、誘引送風機7を駆動する。 This cooling water is the high temperature CO generated from converter 1.
It is heated by gas (approximately 1200° C.), evaporates, and is led to the boiler drum 21. This boiler drum 2
Steam in the steam tank 1 is stored in a steam reservoir 12 via a pipe 16. The steam stored in this steam reservoir 12 is
Steam turbine 1 passes through piping 17 and electric valve 18
3 to drive the induced blower 7.
なお、16′及び17′は、別の排ガス処理装置
との関連を示し、通常製鉄所には、複数の転炉が
設けられ、16′は他の排ガス処理装置のボイラ
ドラムからの蒸気系を示し、又17′は、他の排
ガス処理装置の蒸気タービン13に蒸気を導く配
管を示す。 Note that 16' and 17' indicate the relationship with another exhaust gas treatment equipment, and usually a steelworks is equipped with a plurality of converters, and 16' indicates the connection with the steam system from the boiler drum of another exhaust gas treatment equipment. and 17' indicates piping that guides steam to the steam turbine 13 of another exhaust gas treatment device.
さて、最初の段階、例えば未だ蒸気溜に蒸気が
ない状態では、別に設けた蒸気源より蒸気を得て
タービン13を駆動する必要がある。このように
して、一坦起動された後においては順次吹錬工程
中に蒸気溜め12に蒸気を貯えておき、次の吹錬
工程において、この貯えた蒸気を使用し、誘引送
風機を駆動する。 Now, in the first stage, for example, when there is no steam in the steam reservoir yet, it is necessary to obtain steam from a separately provided steam source to drive the turbine 13. In this manner, after the blowing process is started, steam is stored in the steam reservoir 12 during the blowing process, and in the next blowing process, the stored steam is used to drive the induced blower.
今吹錬工程中の図示の状態において、蒸気溜め
12に予じめ貯えられている蒸気を使用して、蒸
気タービン13を駆動し、誘引送風機7を駆動し
て吹錬工程が行われる。一方、吹錬によつてふく
射伝熱部及び接触伝熱部19の中を循環している
冷却水は加熱昇温して、蒸発し、蒸気溜め12に
貯えられる。このようにして、吹錬工程中は、蒸
気溜め12内の蒸気が消費されると同時に、一方
において補われ、蒸気溜め12内には常に一定量
の蒸気が存することになる。 In the illustrated state during the blowing process, steam previously stored in the steam reservoir 12 is used to drive the steam turbine 13 and the induced blower 7 to perform the blowing process. On the other hand, the cooling water circulating through the radiation heat transfer section and the contact heat transfer section 19 by blowing is heated to an elevated temperature, evaporated, and stored in the steam reservoir 12. In this way, during the blowing process, the steam in the steam reservoir 12 is consumed and at the same time replenished, so that a constant amount of steam is always present in the steam reservoir 12.
非吹錬時においては、酸素吹込みランス11か
らの信号20により、電動弁18は閉められ、蒸
気溜め12内の蒸気量は、一定量に保持される。 During non-blowing, the electric valve 18 is closed by the signal 20 from the oxygen blowing lance 11, and the amount of steam in the steam reservoir 12 is maintained at a constant amount.
受銑工程が完了し、次の精錬を行う時は、酸素
吹込みランス11からの信号20により、電動弁
18が開き、蒸気溜め12内の蒸気が流通して蒸
気タービン13に供給され、誘引送風機7が駆動
し、酸素吹込みランス11より純酸素が吹き込ま
れ、吹錬工程が開始される。これと同時に蒸気が
発生し、蒸気溜め12に貯えられる。 When the pig iron receiving process is completed and the next refining is to be performed, the electric valve 18 is opened in response to the signal 20 from the oxygen injection lance 11, and the steam in the steam reservoir 12 is circulated and supplied to the steam turbine 13, and the induction The blower 7 is driven, pure oxygen is blown from the oxygen blowing lance 11, and the blowing process is started. At the same time, steam is generated and stored in the steam reservoir 12.
以上詳述した通り、本発明による誘引送風機の
駆動方法によれば、誘引送風機の駆動方式として
蒸気タービンを採用し、吹錬工程中のみ蒸気ター
ビンに蒸気を供給し、非吹錬中は、蒸気の供給を
停止し、吹錬中に蒸気を使いながら補うようにし
たので、蒸気溜めには常時一定量の蒸気が貯えら
れ、誘引送風機の駆動エネルギーを自給自足する
ことができ、無駄なエネルギー消費をなくすとと
もに、消費力を大巾に消滅することができ、省エ
ネルギーの点で多大な効果がある。 As detailed above, according to the method for driving an induced fan according to the present invention, a steam turbine is adopted as the driving method for the induced fan, and steam is supplied to the steam turbine only during the blowing process, and steam is supplied to the steam turbine during the non-blowing process. By stopping the supply of steam and supplementing it with steam during blowing, a certain amount of steam is always stored in the steam reservoir, making it self-sufficient in driving energy for the induced blower, and eliminating unnecessary energy consumption. In addition to eliminating energy consumption, consumption power can also be largely eliminated, which has a significant effect in terms of energy conservation.
第1図は、転炉排ガス処理装置の全体を示す説
明図である。第2図は、本発明の方法を実施する
ための一実施例を示す系統図である。
1…転炉、4…冷却器、5,6…冷却器、7…
誘引送風機、11…酸素吹込ランス、12…蒸気
溜め、13…蒸気タービン。
FIG. 1 is an explanatory diagram showing the entire converter exhaust gas treatment apparatus. FIG. 2 is a system diagram showing one embodiment for carrying out the method of the present invention. 1...Converter, 4...Cooler, 5, 6...Cooler, 7...
Induced blower, 11...oxygen blowing lance, 12...steam reservoir, 13...steam turbine.
Claims (1)
し、除塵して回収する転炉排ガス処理装置におい
て、転炉から発生するガスを排ガス処理装置内に
誘引するための送風機を蒸気タービン駆動とし、
吹錬工程中に、蒸気を発生させて蒸気溜めにその
蒸気を一坦貯え、その貯えた蒸気を吹錬工程中の
み誘引送風機駆動用蒸気タービンに導いて誘引送
風機を駆動しながら吹錬中に蒸気を発生して次の
吹錬工程における誘引送風機駆動用蒸気を貯え、
非吹錬中は、誘引送風機駆動用蒸気タービンへの
蒸気供給はタービンの保温用途に限定して供給量
を減少させ、常時蒸気溜めに蒸気を貯えるように
したことを特徴とする転炉排ガス処理装置の誘引
送風機駆動方法。1. In a converter exhaust gas treatment device that cools the exhaust gas generated from the converter using a cooler, removes dust, and recovers the exhaust gas, the blower for drawing the gas generated from the converter into the exhaust gas treatment device is driven by a steam turbine,
During the blowing process, steam is generated and stored in a steam reservoir, and the stored steam is guided to a steam turbine for driving an induced fan only during the blowing process. Generates steam and stores the steam for driving the induced blower in the next blowing process,
During non-blowing, the steam supply to the steam turbine for driving the induced draft fan is limited to the purpose of keeping the turbine warm, and the supply amount is reduced, so that the steam is constantly stored in the steam reservoir. How to drive the induced blower of the device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1251684A JPS60155613A (en) | 1984-01-25 | 1984-01-25 | Method for driving induced draft fan of device for treating converter waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1251684A JPS60155613A (en) | 1984-01-25 | 1984-01-25 | Method for driving induced draft fan of device for treating converter waste gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60155613A JPS60155613A (en) | 1985-08-15 |
| JPS6219482B2 true JPS6219482B2 (en) | 1987-04-28 |
Family
ID=11807509
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1251684A Granted JPS60155613A (en) | 1984-01-25 | 1984-01-25 | Method for driving induced draft fan of device for treating converter waste gas |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60155613A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01148073U (en) * | 1988-03-31 | 1989-10-13 |
-
1984
- 1984-01-25 JP JP1251684A patent/JPS60155613A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01148073U (en) * | 1988-03-31 | 1989-10-13 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60155613A (en) | 1985-08-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102859008B (en) | Waste heat recovery facility for electric arc furnace for steelmaking, electric arc furnace facility for steelmaking, and waste heat recovery method for electric arc furnace for steelmaking | |
| JPH0547601B2 (en) | ||
| JP4179496B2 (en) | Atmospheric pressure combustion turbine system | |
| JPS61178505A (en) | Method and device for operating power plant | |
| JPS6219482B2 (en) | ||
| JPS5920954B2 (en) | Waste heat recovery method | |
| TWI227730B (en) | Circularly blowing method of CDQ and system of the same | |
| JPS6274009A (en) | Method for generating electric power by recovery of pressure from top of blast furnace | |
| JPH0322525B2 (en) | ||
| JP2972050B2 (en) | heating furnace | |
| JPS6118165Y2 (en) | ||
| CA2302267A1 (en) | Method and device for the extraction of iron by direct reduction | |
| JPH10265825A (en) | Smelting reduction equipment | |
| JPS6347310A (en) | Smelting, reducing and refining equipment | |
| JPH0694378A (en) | Cupola waste heat recovery method | |
| JPH06228623A (en) | Energy-saving steelmaking method | |
| JPS6213537A (en) | coil annealing furnace | |
| JPS61104011A (en) | Melt reduction method of iron ore | |
| JPS62156213A (en) | Construction of spout for preliminary refining of molten iron | |
| JPH06147777A (en) | Exhaust gas cooling equipment for ladle refining | |
| JPS5616618A (en) | Continuous annealing furnace | |
| JPS6360218A (en) | Melting reduction smelting method | |
| JPS60142192A (en) | Molten pig iron pretreatment waste heat recovery facility | |
| JPS5932782A (en) | How to operate hot air cupola | |
| JPS61235681A (en) | Method of preheating scrap |