JPS5913005A - Pressure equalizing and releasing method of top charger for blast furnace - Google Patents
Pressure equalizing and releasing method of top charger for blast furnaceInfo
- Publication number
- JPS5913005A JPS5913005A JP11948482A JP11948482A JPS5913005A JP S5913005 A JPS5913005 A JP S5913005A JP 11948482 A JP11948482 A JP 11948482A JP 11948482 A JP11948482 A JP 11948482A JP S5913005 A JPS5913005 A JP S5913005A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- hoppers
- hopper
- valve
- equalizing
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B7/00—Blast furnaces
- C21B7/007—Controlling or regulating of the top pressure
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Blast Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は複数個の均圧ホッパーを有する溶鉱炉の炉頂装
入装置における省エネルギーを目的とした均排圧方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a pressure equalization method for the purpose of energy saving in a top charging device of a blast furnace having a plurality of pressure equalization hoppers.
先ず従来の均排圧方法を第1図に基いて説明する。First, a conventional pressure equalization method will be explained with reference to FIG.
原料は大気圧状態の上部ホッパー/、2に交互に投入さ
れる。溶鉱炉炉内3は普通7〜3 kg/crl −G
の高圧であるた−め上部ホッパー1.2内の原料を集合
シュートクを介して炉内3までスムーズに装入するため
、これらの中間に均圧ホッパー3.t(ホッパー2ケの
場合)が設けられる。又この均圧ホッパーj、tの均排
圧をするため、均圧管7゜9、均圧弁1./θ及び排圧
管//、/グ、排圧弁/2./Sが設けられ、更にホッ
パーの均圧圧力の高い場合に対しては排圧時の騒音を軽
減するため、消音器/3 、 /4が設置されることも
ある。Raw materials are alternately introduced into the upper hopper 2 under atmospheric pressure. Blast furnace furnace 3 is normally 7 to 3 kg/crl -G
Because of the high pressure in the upper hopper 1.2, a pressure equalizing hopper 3.2 is installed between these to smoothly charge the raw materials in the upper hopper 1.2 to the furnace 3 via the collecting chute. t (in the case of two hoppers) is provided. In addition, in order to equalize the pressure in the pressure equalizing hoppers j and t, a pressure equalizing pipe 7°9 and a pressure equalizing valve 1. /θ and exhaust pressure pipe//, /g, exhaust pressure valve/2. A /S is installed, and if the equalization pressure of the hopper is high, mufflers /3 and /4 may be installed to reduce noise during exhaust pressure.
次に上部ホッパー/、2より炉内3までの原料の流れに
ついて詳述する。Next, the flow of the raw material from the upper hopper 2 to the furnace interior 3 will be described in detail.
例えば上部ホッパー/より均圧ホッパー3に原料を移す
だめには、均圧ホッパー5を大気圧まで排圧する必要が
あり、このために排圧弁12を開”にした後、排圧が完
了した時点で上部シール弁19及び上部ゲート弁17を
順次”開”となし、原料を均圧ホッパーjへ装入する。For example, in order to transfer raw materials from the upper hopper/to the pressure equalization hopper 3, it is necessary to evacuate the pressure equalization hopper 5 to atmospheric pressure. Then, the upper seal valve 19 and the upper gate valve 17 are sequentially opened, and the raw material is charged into the pressure equalizing hopper j.
原料の均圧ホッパーjへの装入が完了すると、上部ゲー
ト弁/7 、上部シール弁/9 、排圧弁12を順次閉
”となし、次に均圧ホッパーjの均圧を開始する。即ち
均圧弁gを”開”と6し、均圧気体を供給することで均
圧ホッパー5を炉内圧まで充圧する。均圧ホッパー5が
均圧されて後、下部シール弁n及び下部ゲート弁2/を
順次“開”−とな′シ、原料を炉内3に装入する。原料
−゛。When the charging of the raw materials to the pressure equalizing hopper j is completed, the upper gate valve /7, the upper seal valve /9, and the exhaust pressure valve 12 are closed in sequence, and then pressure equalization of the pressure equalizing hopper j is started. The pressure equalization valve g is set to "open" 6, and pressure equalization gas is supplied to fill the pressure equalization hopper 5 to the furnace internal pressure.After the pressure equalization hopper 5 is equalized, the lower seal valve n and the lower gate valve 2 are opened. / are sequentially opened and the raw material is charged into the furnace 3. Raw material -゛.
の炉内装、人が完了し冬時点で、下部ゲート、・1升、
2乙及53..7、び下部シール弁B、均圧弁lを閉”
となし、次に排圧弁/2を”開”□として均崖ホッパー
jの排圧を完了する。以上が上部ホッパーlより炉内3
まで原料を装入する場合の各機器の作動手順であるが、
この手順は1稠ホッパー−の経路についても同様である
9゜
炉頂装入装置に於て、例えば上部ホッパー/、2の如く
複数個の装入経路を設けるのは上述装入サイクルの所要
時間の制約のため、必要な装入原料量の確保が困難にな
るのを避けるためである。Inside the furnace, by winter, the lower gate, 1 sho,
2 and 53. .. 7. Close lower seal valve B and pressure equalization valve L.
Then, the exhaust pressure valve /2 is set to "open" □ to complete exhaustion of the pressure in the level hopper j. Above is the inside of the furnace 3 from the upper hopper l.
The operating procedure for each device when charging raw materials up to
This procedure is the same for the 1-consistency hopper route.In the 9° furnace top charging device, providing multiple charging routes, such as upper hopper/2, reduces the time required for the above-mentioned charging cycle. This is to avoid difficulty in securing the necessary amount of raw material to be charged due to constraints.
以上説明した従来に洲□ける装入手順では、その排圧工
程に於キ均圧ホッパー3.≦内の気体は全量大気中に放
出される。。従って均′圧用気体として利用される窒素
ガスあるいは高炉発生ガスが各ホッパーの装入サイクル
毎に消費され省エネルギーの見地より好ましくなかった
。In the conventional charging procedure described above, the pressure equalization hopper 3. All gases within ≦ are released into the atmosphere. . Therefore, nitrogen gas or blast furnace gas used as a pressure equalization gas is consumed in each charging cycle of each hopper, which is not desirable from the viewpoint of energy saving.
本発明は斯る従来の欠点を解消するためになされだもの
で、その要旨は各均圧ホッパー間にバイ′にス管゛及び
バイパス弁を設け、排圧すべきホッパ4−内の気体を均
圧すべきホッパーの充圧用気体として利用するところに
ある。The present invention has been made in order to eliminate such conventional drawbacks, and its gist is to provide a bypass pipe and a bypass valve in the bypass between each pressure equalizing hopper, and to equalize the gas in the hopper 4 to be evacuated. It is used as a gas for filling the hopper that is to be pressurized.
以下本発明を第2図によシ説明する。The present invention will be explained below with reference to FIG.
本発明方法と従来法の差異は、バイパス管B及びバイパ
ス弁にを各均圧ホッパー3,4の間に設けた点にある。The difference between the method of the present invention and the conventional method is that a bypass pipe B and a bypass valve are provided between the pressure equalizing hoppers 3 and 4.
例えば前記従来の装入手順の中で均圧ホッパーSの排圧
弁12及び均圧ホッパー6の均圧弁lθを夫々”開”に
する直前にバイパス弁ぶを”開”にすれば両ホッパー内
の圧力差により均圧ホッパー5内の気体が均圧ホッパー
6側に流れ、両ホッパーの内圧は平均化される。For example, in the conventional charging procedure, if the bypass valve is opened immediately before opening the exhaust valve 12 of the pressure equalizing hopper S and the pressure equalizing valve lθ of the pressure equalizing hopper 6, the Due to the pressure difference, the gas in the pressure equalization hopper 5 flows to the pressure equalization hopper 6 side, and the internal pressures of both hoppers are averaged.
このことは均圧ホッパー3が炉内圧より上記平均Wまで
減圧されること及び均圧ホッパー6が大気圧状態より上
記平均圧まで充圧されることを意味する。この様な現象
は両ホッパーが上記と全く逆の均圧及び排圧工程にある
場合にも成立する。This means that the pressure in the pressure equalization hopper 3 is reduced from the furnace internal pressure to the above average W, and that the pressure equalization hopper 6 is filled from the atmospheric pressure state to the above average pressure. Such a phenomenon also occurs when both hoppers are in the pressure equalization and depressurization process, which is completely opposite to the above.
両ホッパーが平均圧力に達した時点でバイパス弁にを“
閉”とし、同時に排圧弁12及び均圧弁/θを共に“開
”にすれば抑圧ホッパー51.t1夫々の排圧、云び均
圧工程に移行する。そし、て本発明の場合も上記バイパ
ス弁ス、均圧弁t 、10及び排圧弁/2.。When both hoppers reach average pressure, the bypass valve is turned on.
If both the exhaust pressure valve 12 and the pressure equalization valve /θ are opened at the same time, the pressure of each suppression hopper 51.t1 will be exhausted and the pressure will be equalized.In the case of the present invention, the above-mentioned bypass Valve, pressure equalization valve t, 10 and exhaust pressure valve/2.
/S各々の作業手順の差異を除き上部ホッパ、−よシ炉
内に至る原料の流れは従来と同一である。/S Except for the differences in each work procedure, the flow of raw materials from the upper hopper to the bottom furnace is the same as in the conventional method.
、バイパス弁26を設、けた場合について各機器の作動
手順をシーケンスで図示したも、のが第53図である。FIG. 53 shows a sequence of operating procedures for each device when the bypass valve 26 is provided.
以上の通り、本発明になる検圧ホッパー間のノくイパス
管及びバイパス弁を利用すれば、均圧ガスの大気中への
放出量の低減蒸び供給すべき均圧ガス量の低減が可能と
なるため省エネルギー−とって極めて好条件を付与する
ことになる。As described above, by using the bypass pipe and bypass valve between the pressure detection hoppers of the present invention, it is possible to reduce the amount of pressure equalization gas released into the atmosphere, and to reduce the amount of pressure equalization gas that must be supplied. This provides extremely favorable conditions for energy conservation.
更に上記バイパス弁”開”吟に於てエゼク、ターあるい
はインゼクターの効果勲付加すればバイパス均圧の時間
短縮あるいは排圧すべきホッパー5から均圧すべきホラ
、パーへの強制的なガそ流れの促進によるガスリ収の大
幅な増大が可能になる。 。Furthermore, if the effect of the ejector, tar or injector is added when the bypass valve is "opened", the bypass pressure equalization time can be shortened or gas can be forced to flow from the hopper 5 to be evacuated to the hole and par to be equalized. By promoting this, it becomes possible to significantly increase the gas removal yield. .
又本発明によれば上述のガス回収による省エネ効果の他
に排圧初期圧力が下がることにより排圧時の騒音レベル
も下がるので高価な消音器を設置する。必要がないこと
の副次的設備費低減の効果も期待できる。Furthermore, according to the present invention, in addition to the energy-saving effect due to the above-mentioned gas recovery, the initial pressure of exhaust pressure is lowered, so that the noise level during exhaust pressure is also lowered, so an expensive muffler is installed. It can also be expected to have the effect of reducing secondary equipment costs since it is not necessary.
、第7図は従来の炉頂装入装置における均排方法を示す
図・、第2図は本発明のバイパス管を有する炉頂装入装
置における均排方法を示す図、第3図、は本発明を使用
した装入タイムスケジュールを示す、図である。
/、2・・・上部ホッパー、3・・・炉内、j、4・・
・均・圧ホッパー、7,9・・・均圧管、r、10・・
・均圧弁、l/、14I・・=婢圧管、/2 、 /3
・・・排圧、弁1. /J 、 /6・・・消音器、1
7・、/I・・・上部ゲート弁、/9 、 ff・・・
上部シール弁、2/ 、 22・・・下部ゲート弁、2
? 、 24I・・・下部シール弁、n、−・・バイパ
ス管、ぶ・・・バイパス弁。, FIG. 7 is a diagram showing a leveling method in a conventional furnace top charging device, FIG. 2 is a diagram showing a leveling method in a furnace top charging device having a bypass pipe of the present invention, and FIG. FIG. 2 is a diagram showing a charging time schedule using the present invention. /, 2... Upper hopper, 3... Inside the furnace, j, 4...
・Equalization/pressure hopper, 7, 9...Pressure equalization pipe, r, 10...
・Pressure equalization valve, l/, 14I...=pressure pipe, /2, /3
...exhaust pressure, valve 1. /J, /6...silencer, 1
7., /I... Upper gate valve, /9, ff...
Upper seal valve, 2/, 22...lower gate valve, 2
? , 24I...Lower seal valve, n, -...Bypass pipe, B...Bypass valve.
Claims (1)
おいて、各均圧ホッパー間に均圧用バイパス管及びバイ
パス弁を設け、排圧すべき均圧ホッパー内の気体を均圧
すべきホッパーの充圧用気体として利用することを特徴
とする溶鉱炉炉頂装入装置の均排圧方法。In the top charging device of a blast furnace having multiple pressure equalizing hoppers, a pressure equalizing bypass pipe and a bypass valve are provided between each pressure equalizing hopper, and the gas in the pressure equalizing hopper to be evacuated is used for filling the hopper to equalize the pressure. A method for equalizing and exhausting pressure in a blast furnace top charging device characterized in that it is used as a gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11948482A JPS5913005A (en) | 1982-07-09 | 1982-07-09 | Pressure equalizing and releasing method of top charger for blast furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11948482A JPS5913005A (en) | 1982-07-09 | 1982-07-09 | Pressure equalizing and releasing method of top charger for blast furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5913005A true JPS5913005A (en) | 1984-01-23 |
Family
ID=14762416
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11948482A Pending JPS5913005A (en) | 1982-07-09 | 1982-07-09 | Pressure equalizing and releasing method of top charger for blast furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5913005A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100398406B1 (en) * | 1999-12-27 | 2003-09-19 | 주식회사 포스코 | Pression apparatus for charing hopper of blast furnace |
| KR100792741B1 (en) * | 2001-07-06 | 2008-01-08 | 주식회사 포스코 | Top bunker in furnace with multi-stage charging |
| KR100851222B1 (en) * | 2002-06-24 | 2008-08-07 | 주식회사 포스코 | Static pressure control device in blast furnace |
| LU92316B1 (en) * | 2013-11-27 | 2015-05-28 | Wurth Paul Sa | Method and device for equalizing the pressure in a charging system of a blast furnace |
-
1982
- 1982-07-09 JP JP11948482A patent/JPS5913005A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100398406B1 (en) * | 1999-12-27 | 2003-09-19 | 주식회사 포스코 | Pression apparatus for charing hopper of blast furnace |
| KR100792741B1 (en) * | 2001-07-06 | 2008-01-08 | 주식회사 포스코 | Top bunker in furnace with multi-stage charging |
| KR100851222B1 (en) * | 2002-06-24 | 2008-08-07 | 주식회사 포스코 | Static pressure control device in blast furnace |
| LU92316B1 (en) * | 2013-11-27 | 2015-05-28 | Wurth Paul Sa | Method and device for equalizing the pressure in a charging system of a blast furnace |
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