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JPH0613248Y2 - Pressure equalizer for blast furnace swivel chute drive - Google Patents

Pressure equalizer for blast furnace swivel chute drive

Info

Publication number
JPH0613248Y2
JPH0613248Y2 JP8316090U JP8316090U JPH0613248Y2 JP H0613248 Y2 JPH0613248 Y2 JP H0613248Y2 JP 8316090 U JP8316090 U JP 8316090U JP 8316090 U JP8316090 U JP 8316090U JP H0613248 Y2 JPH0613248 Y2 JP H0613248Y2
Authority
JP
Japan
Prior art keywords
blast furnace
swirling
pressure
cone
water
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 - Lifetime
Application number
JP8316090U
Other languages
Japanese (ja)
Other versions
JPH0440750U (en
Inventor
良親 柳橋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP8316090U priority Critical patent/JPH0613248Y2/en
Publication of JPH0440750U publication Critical patent/JPH0440750U/ja
Application granted granted Critical
Publication of JPH0613248Y2 publication Critical patent/JPH0613248Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Blast Furnaces (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、原料供給旋回シュートを有するベルレス高炉
の旋回シュート駆動部の均圧装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a pressure equalizing device for a swirling chute drive unit of a bellless blast furnace having a raw material supplying swirling chute.

〔従来の技術〕[Conventional technology]

ベルレス高炉の炉頂部には、原料装入のための旋回シュ
ートが配設されるとともに、これを回転させるための駆
動装置が設けられるが、この駆動装置は、前記旋回シュ
ートとともに回転する回転ベースとその外方に設けられ
る旋回コーンとの内空部に収納されている。
At the top of the bellless blast furnace, a swirling chute for charging the raw material is arranged and a drive device for rotating the swirling chute is provided. The driving device is a rotation base that rotates together with the swirling chute. It is housed in the inner space of the swivel cone provided on the outside.

高炉炉頂内の温度は、通常150〜300℃の間を絶えず変動
しており、吹抜時には、1000℃に達する場合もある。ま
た、炉内圧についても同様に、原料装入時に伴い、低下
と復圧を繰り返し、吹抜時には炉内圧が急激に上昇し、
1000mmH2Oに達する場合もある。
The temperature inside the furnace top of the blast furnace usually fluctuates constantly between 150 and 300 ° C, and sometimes reaches 1000 ° C during blowout. Similarly, with respect to the internal pressure of the furnace, a decrease and a return pressure are repeated as the raw material is charged, and the internal pressure of the furnace rises sharply during the blowing.
It may reach 1000 mmH 2 O.

前述のように高温・高圧とされた高炉ガスは、その圧力
差のため旋回コーン内空部に流入し、その結果、流入し
た高炉ガスの熱やダストによって駆動装置の変形、劣
化、損傷を招くという問題を引き起こしていた。
As described above, the high temperature and high pressure blast furnace gas flows into the inner space of the swirling cone due to the pressure difference, and as a result, the drive unit is deformed, deteriorated, and damaged by the heat and dust of the blast furnace gas that has flowed in. Was causing the problem.

従来、前記問題を解決するために、たとえばNガスを
旋回コーン内に供給することによって、旋回コーン内を
冷却するとともに、前記Nガスによって高炉内よりも
高圧に保持し、高炉ガスの流入を防ぐようにしていた。
Conventionally, in order to solve the above-mentioned problem, for example, by supplying N 2 gas into the swirling cone, the swirling cone is cooled, and the N 2 gas keeps the pressure higher than that in the blast furnace, so that inflow of the blast furnace gas occurs. Was trying to prevent.

しかし、通常前記回転ベースと旋回コーンとの間には、
旋回時の干渉等を防ぐため、若干の隙間が形成されてお
り、この隙間からの高炉ガスの流入を防ぐためには、炉
内圧力変動を見込んで、絶えず多量の冷却ガスを供給し
なければならず、経費が嵩み不経済であった。
However, usually between the rotary base and the swivel cone,
A small gap is formed to prevent interference during turning, and in order to prevent the blast furnace gas from flowing through this gap, it is necessary to constantly supply a large amount of cooling gas in anticipation of fluctuations in the furnace pressure. However, the cost was high and it was uneconomical.

そのため、特公昭63-30365号公報においては、第3図に
示されるように、旋回コーン34と回転ベース36との
隙間t部分にカーボンシール39を設け、高炉ガスの流
入を防ぐようにした乾式シール装置が開示されている。
前記装置は、回転ベース36に固着されたブラケット3
7の先端に固着された保持具38内にカーボンシール3
9が収容されて、カーボンシール39の上側に載荷され
たウエイト40により、所定の面圧となるように摺動面
42上に載置されており、回転ベース36とともに回転
するようになっている。前記保持具38とカーボン39
とは、このカーボン39が高さ方向に移動できるように
なっており、カーボンシール39が摺動面42の凹凸に
追従して上下に移動することで、封止を確実なものとし
て、高炉ガスが流入を効果的に防ぐようにしている。
Therefore, in Japanese Examined Patent Publication No. 63-30365, as shown in FIG. 3, a carbon seal 39 is provided in the gap t between the rotating cone 34 and the rotary base 36 to prevent the inflow of blast furnace gas. A sealing device is disclosed.
The device includes a bracket 3 fixed to a rotation base 36.
The carbon seal 3 is placed in the holder 38 fixed to the tip of
9 is accommodated and is placed on the sliding surface 42 by the weight 40 loaded on the upper side of the carbon seal 39 so as to have a predetermined surface pressure, and is rotated together with the rotation base 36. . The holder 38 and carbon 39
This means that the carbon 39 can move in the height direction, and the carbon seal 39 moves up and down following the irregularities of the sliding surface 42 to ensure the sealing, thereby ensuring the blast furnace gas. Try to effectively prevent the inflow.

一方、特開昭63-161107号公報においては、第2図に示
されるように、高炉内部と旋回コーン内空部とが連通す
る隙間部分A、Bの周縁に沿って水路53、54を形成
させるとともに、この水路53、54に水没する仕切り
板55、56を設けた水封構造として高炉ガスの流入を
防ぎ、さらに旋回コーン内圧力が常に高炉内圧力より高
圧となるように、圧力センサー57、58の検出値に基
づき、加圧ガスの供給量の調整を行う旋回コーン内圧調
整機構とを備えた装置が開示されている。
On the other hand, in Japanese Unexamined Patent Publication No. 63-161107, as shown in FIG. 2, water channels 53 and 54 are formed along the periphery of gaps A and B where the interior of the blast furnace communicates with the inner space of the swirling cone. In addition, a pressure sensor 57 is provided to prevent the inflow of blast furnace gas as a water-sealed structure in which partition plates 55 and 56 are submerged in the water passages 53 and 54 and to keep the swirling cone internal pressure always higher than the blast furnace internal pressure. , 58, a swirling cone internal pressure adjusting mechanism for adjusting the amount of pressurized gas supplied is disclosed.

なお、この場合の冷却システムは、旋回ベース52の背
面側に水冷パネル59を配設し、水路53に循環供給さ
れる水がこの水冷パネル59を通た後、B部の水路54
に流入する水冷構造となっている。水路54から排水さ
れる水は、排水管64を通り、一旦循環水タンク60に
貯留される。なお、この循環水タンク60と前記旋回コ
ーン51内部とは導圧管63により連通されており、常
に同圧となるようになっている。循環水タンク60に貯
留された水は、その下流側の供給管65の中間に配設さ
れるポンプ61により、熱変換器62に経て冷却された
後、再び前記水路53部に供給される。
In the cooling system in this case, a water cooling panel 59 is arranged on the back side of the swivel base 52, and the water circulated and supplied to the water channel 53 passes through the water cooling panel 59, and then the water channel 54 of the B section.
It has a water-cooled structure that flows into. The water drained from the water channel 54 passes through the drain pipe 64 and is temporarily stored in the circulating water tank 60. The circulating water tank 60 and the inside of the swirling cone 51 are communicated with each other by a pressure guiding tube 63 so that the pressure is always the same. The water stored in the circulating water tank 60 is cooled by the pump 61 arranged in the middle of the supply pipe 65 on the downstream side thereof via the heat converter 62 and then supplied to the water passage 53 again.

〔考案が解決しようとする課題〕[Problems to be solved by the device]

しかしながら、前記特公昭63-30365号公報においては、
カーボンシール材の摩耗、異物噛み込みによる偏摩耗等
により絶えず取り替えを必要とし、保守の面で問題が残
る。
However, in the above Japanese Patent Publication No. 63-30365,
The carbon seal material needs to be constantly replaced due to wear and uneven wear due to foreign matter being caught, and problems remain in terms of maintenance.

他方、前記特開昭63-161107号公報においては、封止構
造を水封とし、冷却構造についても前記水封部の循環水
を利用する点に関しては、構造的にも経済的にも優れて
いるが、たとえば高炉内圧力が急激に上昇した場合に
は、加圧ガス供給による圧力調整機構では追随できず、
炉内ガスが前記水封部を介して容易に旋回コーン内に入
り込み、その結果、ガスとともに侵入するダストによる
シール水の汚れ、高炉ガス中のCOが水中に溶解するこ
とによってPHが低下し配管の腐食、配管目詰まり等の
保守管理上の問題を引き起こしていた。
On the other hand, in Japanese Patent Laid-Open No. 63-161107, the sealing structure is a water seal, and the cooling structure is also excellent in terms of structure and economy in that the circulating water of the water seal part is used. However, for example, when the pressure in the blast furnace rises sharply, the pressure adjusting mechanism by the pressurized gas supply cannot follow,
The gas in the furnace easily enters the swirling cone through the water sealing part, and as a result, dirt in the sealing water due to dust that enters with the gas and CO in the blast furnace gas are dissolved in the water, resulting in a decrease in PH and piping. This caused problems in maintenance management such as corrosion of pipes and clogging of pipes.

そこで、本考案の目的は、通常の運転時においてはもち
ろんのこと、高炉ガスの急激な上昇時に際しても、水封
部から直接旋回コーン内への高炉ガス流入を防ぎ、もっ
て保守管理性の向上およびそれに伴う経費節減等を図り
得る高炉の旋回シュート駆動部の均圧装置を提供するこ
とにある。
Therefore, the object of the present invention is to prevent the blast furnace gas from directly flowing into the swirling cone from the water seal part not only during normal operation but also during a rapid rise of the blast furnace gas, thereby improving the maintainability. Another object of the present invention is to provide a pressure equalizing device for a swiveling chute drive unit of a blast furnace, which can reduce the costs associated therewith.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記課題は、高炉炉頂部に原料供給用の旋回シュート
と、この旋回シュートとともに回転する回転ベースと、
この回転ベースの外方に配されるとともに、この回転ベ
ースとの空間部に前記回転ベースの回転駆動装置を収納
する旋回コーンとから構成されるベルレス高炉の旋回シ
ュート駆動部において、 前記回転ベースと旋回コーンとの間の空間と高炉内とが
連通する隙間部分を水封構造とし、この水封構造によっ
て封鎖された前記旋回コーン内部と高炉内とに圧力を検
出するための圧力センサーをそれぞれ配設し、それらの
圧力差信号に基づいて、旋回コーン内への加圧ガス供給
量の調整を行う加圧ガス調整手段を設けるとともに、前
記旋回コーン内部に実質的に高炉内からのガスが自由に
流入する導圧管を設けたことで解決できる。
The above problem is a swirling chute for supplying raw material to the top of the blast furnace, and a rotation base that rotates together with this swirling chute,
In a swirling chute drive unit of a bellless blast furnace, which is arranged outside the rotation base and which is composed of a swirling cone for accommodating the rotation driving device of the rotation base in a space with the rotation base, The space between the swirling cone and the interior of the blast furnace communicates with a water-sealing structure, and pressure sensors for detecting pressure are provided inside the swiveling cone and inside the blast furnace, which are blocked by this water-sealing structure. Installed, and provided with a pressurized gas adjusting means for adjusting the amount of pressurized gas supplied into the swirling cone based on the pressure difference signal, and the gas from the blast furnace is substantially free inside the swirling cone. The problem can be solved by providing a pressure guiding pipe that flows into.

〔作用〕[Action]

本考案においては、先ず旋回シュート駆動装置を収納す
る旋回コーン内空部に直接高炉ガスが流入しないよう
に、回転ベースと旋回コーンとの隙間部分を水封構造と
している。高炉内のガス圧の変動が小さければ通常はこ
の水封構造のみでガスの流入を完全に封止できるが、高
炉においては、時に急激に高炉内圧が上昇・下降する場
合があり、その場合には、容易に前記水封部より炉内ガ
スが流入してしまい、前述のように種々の障害を引き起
こしていた。また、特開昭63-161107号公報のように旋
回シュート内に加圧ガスを供給を行っていても、急激な
高炉内圧の上昇に追随できず、容易に水封部より炉内ガ
スが流入していた。
In the present invention, first, the gap between the rotating base and the rotating cone has a water-sealing structure so that the blast furnace gas does not directly flow into the inner space of the rotating cone that houses the rotating chute drive device. If the fluctuation of gas pressure in the blast furnace is small, the inflow of gas can be completely sealed with only this water sealing structure, but in the blast furnace, the blast furnace pressure sometimes rises and falls rapidly. In the furnace, the gas in the furnace easily flowed in from the water sealing portion, causing various obstacles as described above. Further, even if the pressurized gas is supplied into the swirling chute as in Japanese Patent Laid-Open No. 63-161107, it is not possible to follow the rapid rise in the internal pressure of the blast furnace, and the in-furnace gas easily flows in from the water seal part. Was.

そこで、本考案においては、水封構造によって封鎖され
た前記旋回コーン内部と高炉内とに圧力を検出するため
の圧力センサーをそれぞれ配設し、それらの圧力差信号
に基づいて、旋回コーン内への加圧ガス供給量の調整を
行う加圧ガス調整手段を設けるとともに、前記旋回コー
ン内部に実質的に高炉内からのガスが自由に流入する導
圧管を設けている。
Therefore, in the present invention, pressure sensors for detecting pressure are respectively provided inside the swirling cone and the inside of the blast furnace, which are sealed by a water sealing structure, and based on the pressure difference signals between them, the swirling cone is moved into the swirling cone. In addition to providing a pressurized gas adjusting means for adjusting the amount of pressurized gas supplied, a pressure guiding pipe into which the gas from the blast furnace substantially flows is provided inside the swirling cone.

したがって、導圧管によって、旋回コーン内部には高炉
炉内圧力の急激上昇時に高炉ガスが自由に流入するため
に、瞬時に旋回コーン内圧も追随して上昇することがで
き、前記高炉内圧の急激な上昇に際しても、水封部から
のガス流入を防ぐことができる。旋回コーン内部へ供給
される加圧ガス量は、前述のように、導圧管によってほ
ぼ均等に保たれるため、従来に比して大幅に節減するこ
とができ、旋回コーン内圧が高炉内圧と同圧、もしくは
高炉内圧より若干高めになる程度に加圧ガスの供給を制
御することで、前記水封部からの炉内ガス流入を完全に
防ぐことができる。
Therefore, since the blast furnace gas freely flows into the swirling cone inside the swirling cone when the pressure inside the swirling cone rapidly rises, the swirling cone internal pressure can also be instantaneously increased to follow the rapid increase in the blast furnace pressure. Even when rising, it is possible to prevent gas from flowing in from the water seal portion. As described above, the amount of pressurized gas supplied to the inside of the swirling cone is kept almost equal by the pressure guiding tube, so it is possible to significantly reduce the swirling cone internal pressure to the same level as the blast furnace internal pressure. By controlling the supply of the pressurized gas to such an extent that the pressure is slightly higher than the internal pressure of the blast furnace, it is possible to completely prevent the inflow of the internal gas from the water sealing portion.

なお、前記導圧管が接続される「高炉内」とは、高炉炉
内に限定されず、実質的に高炉炉内とほぼ同圧の部分、
たとえば排気ダクト内(上昇管)とすることができる。
この場合に生じる若干の圧力差は、前記加圧ガス調整手
段によって調整すればよい。
Incidentally, the "inside the blast furnace" to which the pressure guiding pipe is connected is not limited to the inside of the blast furnace, and a portion having substantially the same pressure as the inside of the blast furnace,
For example, it can be in the exhaust duct (upflow pipe).
The slight pressure difference generated in this case may be adjusted by the pressurized gas adjusting means.

また、導圧管により導入される炉内ガスは、粉塵等を含
むため、除塵装置を介して導くのが望ましい。また、定
常的には旋回コーン内圧を炉内より高めるために、該導
圧管を閉塞する逆止弁を設けるのが望ましい。これによ
り通常は、均圧用の外部加圧ガスで内圧調整を行い、急
激な炉内圧力変動時のみ、外部加圧ガス管に比べて太径
の導圧管により、差圧分を一時的に炉内ガスで補充する
ことができる。
Further, since the in-furnace gas introduced by the pressure guiding tube contains dust and the like, it is desirable to introduce it through the dust removing device. Further, it is desirable to provide a check valve for closing the pressure guiding pipe in order to constantly increase the internal pressure of the swirling cone higher than that in the furnace. As a result, normally, the internal pressure is adjusted by the external pressurized gas for pressure equalization, and only when the pressure inside the furnace changes suddenly, the pressure differential pipe with a diameter larger than that of the external pressurized gas pipe temporarily holds the differential pressure. Can be replenished with internal gas.

〔考案の具体的な構成〕[Specific configuration of device]

以下、本考案を第1図に示す実施例に基づき詳説する。 Hereinafter, the present invention will be described in detail with reference to the embodiment shown in FIG.

ベルレス高炉1の炉頂部においては、旋回コーン2の内
方に、旋回シュート6およびこの旋回シュート6ととと
もに回転する回転ベース3が配設されている。前記旋回
コーン2と回転ベース3との間の空間Pには、前記回転
ベース3および旋回シュート6を回転させるために図示
されない駆動装置が収納されている。
At the top of the bellless blast furnace 1, a swirl chute 6 and a rotary base 3 that rotates together with the swirl chute 6 are disposed inside the swirl cone 2. A drive device (not shown) for rotating the rotation base 3 and the rotation chute 6 is housed in a space P between the rotation cone 2 and the rotation base 3.

前記旋回コーン2の内方には、前述のように回転ベース
3が配設されているが、回転ベース3の上端縁および下
端縁部においては、旋回コーン2との隙間A、B部分を
高炉ガス流入を封止するための水封構造としている。
The rotary base 3 is disposed inside the swivel cone 2 as described above. At the upper end edge and the lower end edge of the rotary base 3, the gaps A and B with the swivel cone 2 are provided in the blast furnace. It has a water-sealing structure for sealing the gas inflow.

前記水封構造は、回転ベース3の上端縁部Aにおいて
は、回転ベース3より延在して凹状溝3aを形成し、こ
の凹状溝3aに水を供給して水路5を形成させ、この水
路5に水没する仕切り板4を旋回コーン2より延在して
設けた構造となっている。一方、回転ベース3の下端縁
においても、同様に、旋回コーン2から延在して形成さ
れる凹状溝2aによって形成される水路7に旋回コーン
3の縁端部3aが水没した水封構造となっている。
In the water sealing structure, at the upper edge A of the rotary base 3, a concave groove 3a is formed extending from the rotary base 3, and water is supplied to the concave groove 3a to form a water channel 5. A partition plate 4 submerged in water 5 is provided so as to extend from the swivel cone 2. On the other hand, also at the lower end edge of the rotating base 3, similarly, a water sealing structure in which the edge portion 3a of the swiveling cone 3 is submerged in the water channel 7 formed by the concave groove 2a extending from the swiveling cone 2. Has become.

前記旋回コーン2部における冷却構造は、回転ベース3
の背面側に水冷パネル8を配設し、上縁側水路5に供給
される循環水を利用した水冷構造としている。すなわ
ち、前記水路5に供給される冷却水がこの水冷パネル8
を通過した後、下縁側水封部の水路7で受け取るように
なっており、この下縁側水封部より排水される冷却水
は、冷却水排水管9を通り、一旦循環水タンク10に貯
留される。なお、この循環水タンク10と前記旋回コー
ン2内部とは第1導圧管11により連通されており、同
圧となるようになっている。前記循環水タンク10に貯
留された冷却水は、その下流側の冷却水供給管14の中
間に配設されるポンプ12により、熱変換器13を経て
冷却された後、再び前記水路5に供給される。
The cooling structure in the swivel cone 2 part includes a rotating base 3
A water cooling panel 8 is provided on the back side of the above, and has a water cooling structure using the circulating water supplied to the upper edge side water passage 5. That is, the cooling water supplied to the water channel 5 is the water cooling panel 8
After passing through, the cooling water discharged from the lower edge side water sealing portion passes through the cooling water drain pipe 9 and is temporarily stored in the circulating water tank 10. To be done. The circulating water tank 10 and the inside of the swirl cone 2 are communicated with each other by a first pressure guiding pipe 11 so that they have the same pressure. The cooling water stored in the circulating water tank 10 is cooled through a heat converter 13 by a pump 12 arranged in the middle of a cooling water supply pipe 14 on the downstream side, and then supplied to the water channel 5 again. To be done.

一方、本考案においては、高炉1の上昇管1aと前記旋
回コーン2内部とは、第2導圧管20により連通されて
いる。したがって、急激な高炉内圧の上昇に際しても、
旋回コーン2内部の圧力を前記高炉圧力の上昇に伴い急
上昇させることができるため、水封部からの高炉ガスの
侵入を防ぐことができる。前述のように、導圧管によっ
て高炉内と旋回コーン内との差圧を瞬時にほぼ無くすこ
とができるため、前記旋回コーン2内への加圧ガスの供
給量を大幅に減らすことができ、前記加圧ガスの供給量
としては、高炉内圧よりわずか5〜10mmH2O高めにな
る程度の供給量としている。
On the other hand, in the present invention, the rising pipe 1a of the blast furnace 1 and the inside of the swirling cone 2 are connected by the second pressure guiding pipe 20. Therefore, even when the blast furnace pressure rises rapidly,
Since the pressure inside the swirling cone 2 can be rapidly increased along with the increase in the blast furnace pressure, it is possible to prevent the blast furnace gas from entering from the water sealing portion. As described above, since the pressure difference between the blast furnace and the swirling cone can be almost instantaneously eliminated by the pressure guiding tube, the amount of pressurized gas supplied to the swirling cone 2 can be significantly reduced. The amount of pressurized gas supplied is such that it is only 5 to 10 mmH 2 O higher than the internal pressure of the blast furnace.

前記加圧ガスの供給量の制御を行うために、先ず旋回コ
ーン2内と上昇管1a内とにそれぞれ圧力センサー1
6、17を設けている。この圧力センサー16、17に
よる検出値は、指示器21、22を経て、制御器23に
送られる。制御器23では、圧力センサー16、17の
差圧に基づき、加圧ガス供給管24の中間に配されてい
る調整弁25の制御により、加圧ガスの供給量の調整が
行われる。
In order to control the supply amount of the pressurized gas, first, the pressure sensor 1 is provided in each of the swirling cone 2 and the rising pipe 1a.
6 and 17 are provided. The values detected by the pressure sensors 16 and 17 are sent to the controller 23 via the indicators 21 and 22. In the controller 23, the supply amount of the pressurized gas is adjusted by controlling the adjusting valve 25 arranged in the middle of the pressurized gas supply pipe 24 based on the pressure difference between the pressure sensors 16 and 17.

なお、前記第2導圧管20の中間部には、高炉ガスに混
在するダストの除去のために、たとえばサイクロン等の
除塵器18を設けるとともに、旋回コーン内圧の洩れ防
止のために逆止弁19を設けている。前記除塵器として
は、通常のフィルター等を用いることができるが、この
場合には目詰まり防止のための点検・保守を必要とする
ため、好ましくはフリーメンテナンスのものを採用する
ことが望ましい。
A dust remover 18 such as a cyclone is provided in the middle of the second pressure guiding pipe 20 to remove dust mixed in the blast furnace gas, and a check valve 19 is provided to prevent leakage of the swirling cone pressure. Is provided. As the dust remover, an ordinary filter or the like can be used. In this case, however, inspection and maintenance for preventing clogging are required. Therefore, it is preferable to use a free maintenance.

また、前記加圧ガスとしては、従来冷却ガスとして使用
されているNガスを使用することはもちろんのこと、
たとえば清浄高炉ガス等、高炉炉内に浸入(漏洩)して
も問題のないガスであれば使用することができる。
In addition, as the pressurized gas, it is needless to say that N 2 gas which is conventionally used as a cooling gas is used.
For example, a clean blast furnace gas or any other gas that does not cause a problem even if it enters (leaks) into the blast furnace can be used.

以上に示されるような、旋回シュート駆動部均圧装置を
有するベルレス高炉により操業を行った結果、水封部を
介して高炉ガスの流入が無くなったため、冷却水の汚れ
が少なくなり、従来2ケ月に1回の頻度で行っていた水
路および配管等の清掃を年1回の頻度で行えばよくなっ
た。また、同時に冷却水のPH調整についても、中性化
のためのNaOHの投入量が1/3に減少した。
As a result of operating the bellless blast furnace having a swirling chute drive pressure equalizing device as described above, the inflow of blast furnace gas through the water sealing part was eliminated, and the contamination of the cooling water was reduced. It was only necessary to clean the waterways and pipes once a year, once a year. At the same time, when adjusting the pH of the cooling water, the amount of NaOH added for neutralization was reduced to 1/3.

さらに、従来、第2導圧管を備えない炉頂構造において
はNガス供給量が1500Nm3/hrであったのに対し、本実
施例の場合には500Nm3/hrとなり、大幅に供給ガス量を
減少させることができ、経費節減を図ることができた。
Further, conventionally, while N 2 gas supply quantity in the furnace top structure without the second connecting pipe was 1500 Nm 3 / hr, in the case of the embodiment 500 Nm 3 / hr, and the significantly supplying gas We were able to reduce the amount and save costs.

〔考案の効果〕[Effect of device]

以上詳説した通り、本考案によれば、高炉ガスの急激な
上昇に際しても、水封部からの炉内ガス流入を防ぎ、も
って保守管理性の向上並びに供給ガス量の削減により大
幅に経費節減を図ることができる。
As described in detail above, according to the present invention, even when the blast furnace gas rises sharply, the inflow of gas from the water sealing part into the furnace is prevented, and maintenance cost is improved and the amount of supplied gas is greatly reduced. Can be planned.

【図面の簡単な説明】[Brief description of drawings]

第1図は本考案に係る高炉の旋回シュート駆動部均圧装
置を示す図、第2図は従来の高炉の旋回シュート駆動部
均圧装置を示す図、第3図は公知例における旋回コーン
部の隙間封止構造を示す図である。 1…高炉、2…旋回コーン、3…回転ベース、5…上縁
側水路、7…下縁側水路、8…冷却パネル、9…冷却水
排水管、10…循環水タンク、11…第1導圧管、12
…ポンプ、13…熱変換器、14…冷却水供給管、1
6,17…圧力センサー、18…除塵器、19…逆止
弁、20…第2導圧管、21,22…指示器、23…制
御器、24…加圧ガス供給管、25…調整弁
FIG. 1 is a diagram showing a pressure equalizing device for a swirling chute drive unit of a blast furnace according to the present invention, FIG. 2 is a diagram showing a pressure equalizing device for a swirling chute drive unit of a conventional blast furnace, and FIG. 3 is a swirling cone unit in a known example. It is a figure which shows the gap sealing structure of. DESCRIPTION OF SYMBOLS 1 ... Blast furnace, 2 ... Swivel cone, 3 ... Rotation base, 5 ... Upper edge side water channel, 7 ... Lower edge side water channel, 8 ... Cooling panel, 9 ... Cooling water drainage pipe, 10 ... Circulating water tank, 11 ... First pressure pipe , 12
… Pump, 13… Heat converter, 14… Cooling water supply pipe, 1
6, 17 ... Pressure sensor, 18 ... Dust remover, 19 ... Check valve, 20 ... Second pressure guiding tube 21, 22 ... Indicator, 23 ... Controller, 24 ... Pressurized gas supply tube, 25 ... Regulator valve

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】高炉炉頂部に原料供給用の旋回シュート
と、この旋回シュートとともに回転する回転ベースと、
この回転ベースの外方に配されるとともに、この回転ベ
ースとの空間部に前記回転ベースの回転駆動装置を収納
する旋回コーンとから構成されるベルレス高炉の旋回シ
ュート駆動部において、 前記回転ベースと旋回コーンとの間の空間と高炉内とが
連通する隙間部分を水封構造とし、この水封構造によっ
て封鎖された前記旋回コーン内部と高炉内とに圧力を検
出するための圧力センサーをそれぞれ配設し、それらの
圧力差信号に基づいて、旋回コーン内への加圧ガス供給
量の調整を行う加圧ガス調整手段を設けるとともに、前
記旋回コーン内部に実質的に高炉内からのガスが自由に
流入する導圧管を設けたことを特徴とする高炉旋回シュ
ート駆動部の均圧装置。
1. A swirling chute for supplying a raw material to the top of a blast furnace, and a rotating base which rotates together with the swirling chute.
In a swirling chute drive unit of a bellless blast furnace, which is arranged outside the rotation base and which is composed of a swirling cone for accommodating the rotation driving device of the rotation base in a space with the rotation base, The space between the swirling cone and the interior of the blast furnace communicates with a water-sealing structure, and pressure sensors for detecting pressure are provided inside the swiveling cone and inside the blast furnace, which are blocked by this water-sealing structure. Installed, and provided with a pressurized gas adjusting means for adjusting the amount of pressurized gas supplied into the swirling cone based on the pressure difference signal, and the gas from the blast furnace is substantially free inside the swirling cone. A pressure equalizing device for a blast furnace swirling chute drive unit, characterized in that a pressure guiding pipe is introduced into the blast furnace.
JP8316090U 1990-08-06 1990-08-06 Pressure equalizer for blast furnace swivel chute drive Expired - Lifetime JPH0613248Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8316090U JPH0613248Y2 (en) 1990-08-06 1990-08-06 Pressure equalizer for blast furnace swivel chute drive

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8316090U JPH0613248Y2 (en) 1990-08-06 1990-08-06 Pressure equalizer for blast furnace swivel chute drive

Publications (2)

Publication Number Publication Date
JPH0440750U JPH0440750U (en) 1992-04-07
JPH0613248Y2 true JPH0613248Y2 (en) 1994-04-06

Family

ID=31630591

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8316090U Expired - Lifetime JPH0613248Y2 (en) 1990-08-06 1990-08-06 Pressure equalizer for blast furnace swivel chute drive

Country Status (1)

Country Link
JP (1) JPH0613248Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20140048288A (en) * 2011-07-22 2014-04-23 풀 부르스 에스.에이. Charging device for shaft furnace with controller for clean gas fed to its main casing

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20140048288A (en) * 2011-07-22 2014-04-23 풀 부르스 에스.에이. Charging device for shaft furnace with controller for clean gas fed to its main casing

Also Published As

Publication number Publication date
JPH0440750U (en) 1992-04-07

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