JPH03281713A - Method for preventing invasion of furnace gas into sealing device for swinging chute driving device in bellless type vertical furnace - Google Patents

Method for preventing invasion of furnace gas into sealing device for swinging chute driving device in bellless type vertical furnace

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Publication number
JPH03281713A
JPH03281713A JP8092990A JP8092990A JPH03281713A JP H03281713 A JPH03281713 A JP H03281713A JP 8092990 A JP8092990 A JP 8092990A JP 8092990 A JP8092990 A JP 8092990A JP H03281713 A JPH03281713 A JP H03281713A
Authority
JP
Japan
Prior art keywords
furnace
water
gas
tank
drainage
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.)
Granted
Application number
JP8092990A
Other languages
Japanese (ja)
Other versions
JPH0625373B2 (en
Inventor
Shuichi Taniyoshi
谷吉 修一
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP2080929A priority Critical patent/JPH0625373B2/en
Publication of JPH03281713A publication Critical patent/JPH03281713A/en
Publication of JPH0625373B2 publication Critical patent/JPH0625373B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To surely prevent the invasion of furnace gas into swinging chute driving chamber by water-sealing upper and lower parts of a rotary table fitting the swinging chute and adjusting level difference between sealed water in a water sealing trough and drainage in a drainage tank. CONSTITUTION:The rotary table 21 for working the swinging chute is set in a casing 22 at furnace top of a blase furnace and a space between the fixed part 1 and rotary part in the furnace top wall 30 is water-sealed with the water sealing troughs 2, 10 having parting plates 5, 11. The sealed water supplied into the upper water sealing trough 10 through water supplying pipe 12, is fed into the lower water sealing trough 10 through a connecting pipe 24, and further, discharged into the drainage tank 9 through a drainage pipe 6. The above drainage tank 9 is made to a sealed construction and tip part of the drainage pipe 6 is submerged into the drain 13 in the tank and air-tightly connected with the above casing 22 through a communicating pipe 14. Further, the differential pressure between gas pressure in the casing 22 and gas pressure in the furnace is detected with a differential pressure gage 26 and the above drain 13 is drawn with a pump 16 so that this differential pressure is held plus to the set value to control gas volume in the drainage tank 9. By this method, the furnace gas is prevented from invading into the driving chamber 23 in the casing 22.

Description

【発明の詳細な説明】 <j?業上の刊用分’I!i’> 本発明は、ベルレス式高炉における旋回シュド駆動装置
の回転部と固定部との間に設りられた水封機構のシール
を確保し、駆動室への炉頂ガスやダス]・の侵入を確実
に防止すると共GJ駆動室へ供給する窒素ガスを節減す
ることができるベルレス式高炉の旋回シューF駆動装置
用駆1)+室の炉頂ガス借入防止方法に関するものであ
る。
[Detailed description of the invention] <j? For professional publication 'I! i'> The present invention secures the seal of the water seal mechanism installed between the rotating part and the fixed part of the rotating sudo drive device in a bellless blast furnace, and prevents top gas and dust from flowing into the drive chamber. This invention relates to a method for preventing top gas from being borrowed from a drive chamber for a swing shoe F drive device of a bellless type blast furnace, which can reliably prevent intrusion and reduce nitrogen gas supplied to a GJ drive chamber.

〈従来の技術〉 高炉において、鉱石、コークス等の原料を炉内に装入す
る際に用いられる炉頂装入装置としてペルレス代炉頂装
人装置が使用されている。このペルレス式炉r頁装入装
置+i炉内に設りた旋回シブトを連続旋回さ−Vると共
に傾動さセて原¥1を分配装入するものであり、全体が
コンパクトでかつ装置の高さを比較的低くし得る等の利
点を有する。
<Prior Art> In blast furnaces, a pelletless top charging device is used as a top charging device used to charge raw materials such as ore and coke into the furnace. This pellet-less type furnace charging device + i is equipped with a rotating shaft installed inside the furnace that is continuously rotated and tilted to distribute and charge the raw materials. It has advantages such as being able to make the temperature relatively low.

従来、ベルレス式たて型炉なかでも高炉においては、第
3図に示すように旋回シュート20の旋回、III I
JJを行う回転テーブル21の炉内に対するガスシール
およびダストシールは、予め冷却除塵された窒素ガスを
回転テーブル21を収納したケーシング22内に形成さ
れた駆動室23に吹込み、次いで該回転テーブル21を
冷却した後の排ガスを固定部1と回転部すなわち回転テ
ーブル21のカバー3との円環状の隙間(スリン1−)
から炉内に排出することζこ、Lっで行われていた。
Conventionally, in a blast furnace among bell-less type vertical furnaces, as shown in FIG.
The gas seal and dust seal for the inside of the furnace of the rotary table 21 that performs JJ is achieved by blowing nitrogen gas, which has been cooled and dust removed in advance, into the drive chamber 23 formed in the casing 22 housing the rotary table 21, and then sealing the rotary table 21. The cooled exhaust gas is transferred to the annular gap (Srin 1-) between the fixed part 1 and the rotating part, that is, the cover 3 of the rotary table 21.
Discharging from the furnace into the furnace was carried out at ζ and L.

回転テーブル21への炉内からの輻射熱による入熱は高
々20000にω!/)I程度であり、したがって冷却
に必要なガス量は100ONj/ h 1M度で十分で
あるが、この供給量では炉内からのケーシング22内の
駆動室23へのガスオンよびダス1の侵入を防ぐことが
できなかった。ガスおよびダストの侵入を&i実に回避
するζこは6000〜10000 Nal/ hの窒素
ガスが必要でありコスト高になる。
The heat input to the rotary table 21 by radiant heat from inside the furnace is at most 20,000ω! /)I, therefore, the amount of gas required for cooling is sufficient at 100ONj/h 1M degrees, but this supply amount prevents gas on from inside the furnace and entry of dust 1 into the drive chamber 23 in the casing 22. Couldn't prevent it. In order to effectively avoid the intrusion of gas and dust, 6000 to 10000 Nal/h of nitrogen gas is required, which increases the cost.

/、−ソング22内の駆動室23に吹込む冷却ガス量を
少なくするため回転テーブル21の固定部と回転部との
スリソt□部に弾性体を押圧するシール装置を設けてシ
ールする手段(特開昭61−62782号公報、実開昭
63−123994号公報参照)あるいはスリット部に
カーボンを収納し、カーボンを摺動面に押圧し゛ζンー
ルする手段(特開昭61−87807壮公報参照)が開
示されている。
/, - In order to reduce the amount of cooling gas blown into the drive chamber 23 in the song 22, a sealing device for pressing an elastic body is provided on the slit t section between the fixed part and the rotating part of the rotary table 21 for sealing ( (See Japanese Patent Application Laid-open No. 61-62782, Japanese Utility Model Application No. 63-123994) or a means for storing carbon in a slit and pressing the carbon against the sliding surface (see Japanese Patent Application Laid-Open No. 61-87807) ) are disclosed.

しかるに、これらのシール手段は弾性体やカボンをIN
動面に押圧するため摩耗が激しく長期に亘ってシール機
能を維持することが困難であり、またソール性が不十分
なため特に高圧の大型高炉の場合には炉Ir+中央部の
垂直方向のガス流速が大きく、結局は炉内ガスおよびダ
スi・の役人防止の1」的だけに例えば200ONJ/
 I+以上の冷却ガス供給を行わなければならないとい
う問題点かあ、っな。
However, these sealing means do not allow the elastic body or carbon to
Pressure against the moving surface causes severe wear and makes it difficult to maintain the sealing function over a long period of time, and the sole properties are insufficient, especially in the case of large high-pressure blast furnaces. The flow velocity is large, and in the end, it is necessary to prevent the gas inside the furnace and the officials from causing damage, for example, 200ONJ/
The problem is that you have to supply a cooling gas of more than I+.

このような問題点に対処するため実開昭63−1196
50壮公報に水封槽と該水封樋内に配置する仕切板との
tI;7を合わ−Uからなる水封a横を設けてシールす
る手段が開示されている。
In order to deal with these problems, Utility Model Application No. 63-1196
Japanese Patent Publication No. 50, No. 50 discloses a means for sealing a water seal tank and a partition plate disposed in the water seal gutter by connecting the tI;

すなわち第2図に示すように高炉炉頂のケーシング22
内に形成された駆動室23に収納された回転テーブル2
1の上部に環状の水封t’J10を一体に設り、固定部
1に水封JalO内に配置する仕切板11を一体に設け
である。水14に必要な冷却水は給水ポンプ4でif圧
され、給水流量耐8によって冷却水量を測定しながら給
水Kffi調節ブr7の開度を11節し2、固定部lに
設けた給水管12から十部水1.l 4a l Oへ供
給される。
That is, as shown in FIG. 2, the casing 22 at the top of the blast furnace
Rotary table 2 housed in drive chamber 23 formed inside
An annular water seal t'J10 is integrally provided on the upper part of the water seal 1, and a partition plate 11 to be disposed inside the water seal JALO is integrally provided on the fixed part 1. The cooling water necessary for the water 14 is pressurized by the water supply pump 4, and while measuring the amount of cooling water by the water supply flow rate resistance 8, the opening degree of the water supply Kffi adjustment lever r7 is adjusted to 11 points 2, and the water supply pipe 12 provided in the fixed part l is From Jubesui 1. l 4a l O.

また回転ラーブル21の下部に対応する固定部lに環状
の水封槽2を一体に設け、回転テーブル21の上部に設
りた水t、l樋10から連縮間24(これは回転テーブ
ルの冷却に利用されている)を介し″ζζ下部水封槽2
水封に必要な冷却水を常時供給するJ、うになっている
、−・方、回転チーフル21には水I44a2内に配置
する仕切板5を一体に設け、水封槽2と11水中に没す
る仕切板5とにより水封を行い固定部1と回転部との隙
間をシールする。さらに下部水11い2には系夕Iに冷
却水を排出するfJF水管らを設LJてありIJ「水す
るようになっている。
In addition, an annular water seal tank 2 is integrally installed in a fixed part l corresponding to the lower part of the rotary table 21, and a water tank 24 is connected to the water pipe 10 provided at the upper part of the rotary table 21. (Used for cooling) ``ζζ lower water seal tank 2
The rotating chiffle 21, which constantly supplies the cooling water necessary for the water seal, is integrally provided with a partition plate 5 to be placed in the water I44a2, and the water seal tanks 2 and 11 are immersed in water. A partition plate 5 is used to seal the gap between the fixed part 1 and the rotating part. Furthermore, the lower water 11 and 2 are equipped with fJF water pipes that discharge cooling water to the system I, so that the IJ water is discharged.

とこイ)で、高炉内は商用であるので1一部の水、t、
t4通10お、1−び下部の水1イ閤2に、糺りケーシ
ング22内に形成された駆動室23に炉頂ガスが侵入す
るのを防止するため、駆動室23内に窒素ガス供給管2
5からN2ガス流量:Ii、1節介29を調節しつつ窒
素ガス(Lガス)を供給して屏圧し、炉頂圧とバランス
さ・Cると旦に駆動室23内を冷却し°Cいた。
Since the inside of the blast furnace is for commercial use, some water, t,
In order to prevent top gas from entering the drive chamber 23 formed in the glue casing 22, nitrogen gas is supplied into the drive chamber 23. tube 2
5 to N2 gas flow rate: Ii, 1 While adjusting the joint 29, nitrogen gas (L gas) is supplied and pressurized, and when the pressure is balanced with the furnace top pressure, the inside of the drive chamber 23 is cooled at once. there was.

しかしながら炉頂圧の小さな変動によっても水封樋lO
才起りび2内の封水に息継ぎ現象がろられ、前記水i、
l i 4Mに3Lる水封圧は150=200 ff1
1nAql、か取れないためでご激な炉■頁圧変動が4
1゛シたときにし7ば(7ぽ水l、lが破れるという問
題点があった。
However, even small fluctuations in the furnace top pressure can cause water sealing
The breathing phenomenon is suppressed by the sealed water in the water holder 2, and the water i,
The sealing pressure of 3L of water in l i 4M is 150 = 200 ff1
1nAql cannot be removed, so the furnace is in trouble ■Page pressure fluctuation is 4
There was a problem that the 7-piece (7-po water l, l) would tear when it was 1.

水封が破れると水1,1樋からの溢水が炉内に侵入した
り、ケーシング内に侵入するばかりでなく水封に、1、
るシールができなくなり炉内ガスやダストが/、−一−
ンング内に入って回転テーブルの駆動装置に悪影響を及
ばずことになる。
If the water seal is broken, water from the water 1,1 gutter will not only enter the furnace or the casing, but also cause water to leak into the water seal.
Gas and dust inside the furnace will not be able to seal properly.
This means that the rotary table drive device will not be adversely affected by entering the rotary table drive unit.

〈発明が解決しようとする課題〉 そこで、従来、差圧5126に接続し、7た圧力検出配
管27aおよび27bをそれぞれケーシング22内と炉
頂壁30内に挿入し、駆動室23内の圧力P2と炉頂壁
30内の炉内圧力P1との差圧ΔPを検出し、その差圧
Δl)がプラス圧の設定値2以上、すなわちΔP””P
!  −P+  ≧p≧0になるように窒素ガス供給管
25から窒素ガスを供給していた。
<Problems to be Solved by the Invention> Therefore, conventionally, the pressure detection pipes 27a and 27b connected to the differential pressure 5126 and inserted into the casing 22 and the furnace top wall 30, respectively, are used to reduce the pressure P2 in the drive chamber 23. and the furnace pressure P1 in the furnace top wall 30 is detected, and the differential pressure Δl) is equal to or higher than the positive pressure set value 2, that is, ΔP""P
! Nitrogen gas was supplied from the nitrogen gas supply pipe 25 so that -P+≧p≧0.

具体的には、差圧計26にて差圧ΔPをプロセス圧力変
量として取り出して圧力調節1it28aに人力し、こ
の差圧Δpと前記のプラスの差圧設定1a pとから圧
力調節1it28aで操作信号MV値を演算し、この操
作信号MV値により冷却N、バージコントロール弁29
の開度を制御し駆動室23内が炉頂部27内の圧力より
プラスの差圧設定(i!!pより高くなるようにしてい
た。しかるに前記のような操作により常に駆動室23の
圧力P、と炉内の圧力P、との差圧ΔPが差圧設定値p
より大となるようにN2ガスバージ量をコン1〜ロール
するには大流量のN2ガスを供給しなければ炉内圧の圧
力変動に追従できず不経済であった。
Specifically, the differential pressure ΔP is taken out as a process pressure variable by the differential pressure gauge 26 and manually inputted to the pressure adjustment 1it 28a, and from this differential pressure Δp and the above-mentioned positive differential pressure setting 1a p, the pressure adjustment 1it 28a generates the operation signal MV. The cooling N and barge control valve 29 are calculated based on the operation signal MV value.
The pressure inside the drive chamber 23 was set to be higher than the pressure inside the furnace top 27 (i!!p) by controlling the opening degree of the drive chamber 23. However, due to the above operation, the pressure P in the drive chamber 23 was always maintained. , and the pressure inside the furnace P, the differential pressure ΔP is the differential pressure set value p
In order to control the amount of N2 gas barge to a larger value, a large flow rate of N2 gas must be supplied to keep up with the pressure fluctuations in the furnace, which is uneconomical.

本発明は前記従来技術の問題点を解消し、旋回シュー1
駆動装置の回転部と固定部との間に設けられた水封機構
のシールを6i保し、駆動室への炉ffIガスやダス1
−の侵入を硲実に防止すると共に、駆動室へ供給JるN
2ガスを節減することができるベルレス式高炉におりる
旋回シュート駆動装置用駆動室−1の炉頂ガス侵入防止
方法を従供することを目的とするものである。
The present invention solves the problems of the prior art and provides a rotating shoe 1.
The seal of the water seal mechanism provided between the rotating part and the fixed part of the drive device is maintained at 6i, and the furnace ffI gas and dust 1 are kept in the drive chamber.
- In addition to thoroughly preventing the intrusion of
The object of the present invention is to provide a method for preventing the intrusion of top gas into a drive chamber-1 for a rotating chute drive device in a bell-less type blast furnace, which can save gas.

〈課題を解決するだめの手段〉 前記目的を達成するための本発明は、炉頂頂部のケーシ
ング内に旋回シj−1・の旋回および傾動を行う回転テ
ーブルを設置し、該回転テーブルの上部および下部にお
ける固定部と回転部との間に環状の水144Mと該水1
,1樋的に配置−イる環状のイ1、切板とを組合わ・I
゛ζなる水封機構を設けたベルレス式たて型炉に才昌J
る旋回ンユート駆動装置用ノール装:6の炉内ガス侵入
防止方法であって、前記下部水J、I!から炉外に取り
出した排水管を密閉JMi貴の排水タンク内に貯留され
た排水中に浸漬すると共に、前記排水タンクの土部と前
記回転テーブルを設置した炉1f1頂部ゲーンングとを
連通管で気密に接続し、前記下部水封槽からの排水をI
JF水管を介して排水タンク内に導きつつ、前記炉頂頂
部ケーシング内のガス圧力と炉内のガス圧力との差圧が
プラスの差圧設定値以上に維持されるように前記排水タ
ンク内に貯留された排水を抜き取って該排水タンク内の
ガス容積を制御することを特徴とするペルレス人たて型
炉における旋回シュート駆動装置用ソール装置の炉内ガ
ス侵入防止方法である。
<Means for Solving the Problems> The present invention for achieving the above object includes installing a rotary table for rotating and tilting the rotary shear j-1 in a casing at the top of the furnace; And an annular water 144M between the fixed part and the rotating part at the lower part and the water 1
, 1 Arranged in a gutter-like annular shape 1, combined with a cutting board ・I
Saisho J is a bellless type vertical furnace equipped with a water seal mechanism called ゛ζ.
Knoll installation for a rotating unit drive device: 6. A method for preventing gas intrusion into a furnace, comprising the lower water J, I! The drain pipe taken out of the furnace is immersed in the waste water stored in the sealed JMi's waste water tank, and the soil part of the waste water tank and the top section of the furnace 1f1 where the rotary table is installed are airtight with a communicating pipe. is connected to I, and the drainage from the lower water seal tank is connected to I.
While guiding the gas into the drainage tank through the JF water pipe, the gas pressure inside the furnace top casing and the gas pressure inside the furnace are maintained at a positive differential pressure setting value or higher. This is a method for preventing gas intrusion into a furnace of a sole device for a swing chute drive device in a perless vertical furnace, which is characterized by extracting stored waste water and controlling the gas volume in the waste water tank.

〈作 川〉 下部水封槽から排水管を介して排水タンク内に排水を導
きつつ、排水タンク内に貯留される排水を該排水タンク
からの抜取量を調整することによって容積の大きいfJ
i水タンク内の1)[水レヘルつまりtJj水タンク内
のガス容積を制j1シ、これによって炉頂頂部ケーシン
グ内のガス圧力と炉内のガス圧ツノとの差圧を所定のプ
ラス圧以上に維持する。
<Saku Kawa> While guiding wastewater from the lower water seal tank into the wastewater tank via the drain pipe, the wastewater stored in the wastewater tank is made into a large-volume fJ by adjusting the amount of wastewater extracted from the wastewater tank.
1) [Water level in the water tank, that is, tJj The gas volume in the water tank is controlled, thereby increasing the differential pressure between the gas pressure in the furnace top casing and the gas pressure horn in the furnace to a predetermined positive pressure or higher. maintain it.

かくして炉内から駆動室への旋回シュート駆動装置用シ
ール装置を介する炉内ガス侵入を防止する。
In this way, gas in the furnace is prevented from entering the drive chamber through the sealing device for the rotating chute drive device.

本発明の原理は、炉頂部の炉内圧P1の変動の影7Pを
水封機構を介L7て受ける炉頂■部ケーシング内に形成
される駆動室を連通管を介して11[水タンクと接続し
、tJr水タンク内に貯留されるtJt水のレヘルを制
t111することによっ”Cガス容積を制御し、ごれに
、j、って駆動室内の圧力を制御することを壮丁と17
”ζいる。
The principle of the present invention is that the drive chamber formed in the furnace top casing, which receives the influence 7P of fluctuations in the furnace internal pressure P1 at the furnace top through the water seal mechanism L7, is connected to the water tank 11 through a communication pipe. By controlling the level of tJt water stored in the tJr water tank t111, the "C gas volume is controlled, and the pressure in the drive chamber is controlled by t111.
“ζ is there.

づなわら、駆動室のガス容積をV、としfJr水タンク
のttt水上ζこ占めるガス容積を■。とすると全ガス
容積は■、F■、となる。ごこで炉頂圧P。
Suppose that the gas volume of the drive chamber is V, and the gas volume occupied by ttt water ζ of the fJr water tank is ■. Then, the total gas volume becomes ■, F■. Furnace top pressure P.

の変動を補償して対抗するにはP 、 X (V、I−
VT)−C(一定植)になるように:】ントロールすれ
ばよいごとになる。ごこでV、とCは一定(直であるの
で、炉Tn圧1)lが大きくなれば排水タンクガス容積
■、を小さくし、逆に炉「(圧p1が小さくなれば■□
を太き(なるように操作することになる。
To compensate and counter the fluctuation of P, X (V, I-
VT) - C (constant planting):] If you control it, it will be a good thing. Here, V and C are constant (direct, so the furnace Tn pressure 1) increases, the drain tank gas volume ■, becomes smaller, and conversely, if the furnace pressure p1 decreases, the furnace Tn pressure 1 decreases.
It will be operated so that it becomes thick.

〈実施例〉 以下本発明の−・実施例を図面に2λついて説明する。<Example> Embodiments of the present invention will be described below with reference to the drawings.

第1図において、給水ポンプ4で昇圧され、給水流量旧
8によって冷却水量を測定しながら給水′/r、■調節
弁7の開度を調整し、水封に必要な冷加水(例えば工場
還水)が固定部1に設けた給水管12から上部水封樋1
0へ供給される。上部水11樋lOへ供給された冷却水
は連絡管24(これは回転テーブル21の冷却に使用さ
れる)を通って下部水封槽2に水封ζこ必要な冷却水を
常時1)+給するようになっ°ζいる。
In Fig. 1, the pressure is increased by the water supply pump 4, and while measuring the amount of cooling water using the water supply flow rate 8, the water supply '/r, and the opening degree of the control valve 7 are adjusted. water) from the water supply pipe 12 provided in the fixed part 1 to the upper water seal gutter 1
0. The cooling water supplied to the upper water 11 gutter 10 passes through the connecting pipe 24 (this is used for cooling the rotary table 21) and is sent to the lower water seal tank 2 through a water seal. It is now possible to supply.

さらに下部水封φ2には系外に冷却水を排出する排水管
6が接続されていて、水冷却系を形成している一方、炉
頂頂部ケーシング22に窒素ガス供給管25を接続し、
N2ガス流量弁29の開度を調節し1つ窒素ガスを駆動
室23内に供給するN、ガス供給系を形成しているのは
第2図に示す従来例と同しである。
Further, a drain pipe 6 for discharging cooling water outside the system is connected to the lower water seal φ2, forming a water cooling system, while a nitrogen gas supply pipe 25 is connected to the furnace top casing 22.
The N2 gas supply system for supplying nitrogen gas into the drive chamber 23 by adjusting the opening degree of the N2 gas flow valve 29 is the same as the conventional example shown in FIG.

本発明においては、下部水封樋2から炉外に取り出され
た排水管6を密閉構造の排水タンク9内に一旦貯留され
た排水13中に浸漬すると共に、排水タンク9の上部と
回転テーブル2!を設置した炉TFi頂部ケーシング2
2とを連通管+4で気密に接続しである。一方、排水タ
ンク9の下端部にはtJ1水抜取管15が接続されてお
り、排水抜取管15に配設された排水流醪31■7によ
って排水量を測定しつつJJt水ポンプ16によって排
水タンク9内に貯留されたIJF水1水含3JF出する
排水系を形成しである。なお、排水ク水タンク90ト水
レベル汎tlBが設けてあり、iJF水ク水タンク9内
留されている排水13のレベルを測定するようになって
いる。
In the present invention, the drain pipe 6 taken out of the furnace from the lower water seal trough 2 is immersed in the waste water 13 temporarily stored in the drain tank 9 having a sealed structure, and the upper part of the drain tank 9 and the rotary table 2 ! Furnace TFi top casing 2 with installed
2 and 2 are airtightly connected through a communication pipe +4. On the other hand, a tJ1 water extraction pipe 15 is connected to the lower end of the drainage tank 9, and while the amount of drainage is measured by the drainage flow mash 317 installed in the drainage extraction pipe 15, the JJt water pump 16 is operated by the drainage tank 9. A drainage system is formed to discharge 1 water containing 3JF of IJF water stored in the tank. In addition, a water level control tlB is provided in the waste water tank 90 to measure the level of the waste water 13 stored in the iJF water tank 9.

本発明では窒素ガス配管25からケージング22内に供
給する窒素ガスはN8ガス流ft1iJ節介2つを小開
度として一定の低流量でバイアス的に供給するにとどめ
る。そして炉頂ケーシング22内に挿入した圧力検出配
管27aおよび炉頂壁30内に挿入した圧力検出配管2
7bに接続した差圧8126によって駆動室23内の圧
力P、と炉内圧力P1との差圧ΔF)を検出し、その差
圧ΔPをプロセス変量として取り出しΔ1)がプラスの
設定(11!p以上、すなわち八P””Pg  P+ 
≧ρ〉0になるように下部水封樋2から排水管6を通し
て排水タンク9に排水を導きつつ、排水タンク9内に貯
留された排水をuト水抜?T]5から抜き取る排水量を
調整するものである。
In the present invention, the nitrogen gas supplied from the nitrogen gas pipe 25 into the casing 22 is limited to being supplied in a biased manner at a constant low flow rate with two N8 gas flow ft1iJ joints set at a small opening. The pressure detection pipe 27a inserted into the furnace top casing 22 and the pressure detection pipe 2 inserted into the furnace top wall 30
The differential pressure ΔF) between the pressure P in the drive chamber 23 and the pressure P1 in the furnace is detected by the differential pressure 8126 connected to 7b, and the differential pressure ΔP is taken out as a process variable, and Δ1) is set to be positive (11!p). Above, that is, eight P””Pg P+
While guiding the wastewater from the lower water seal gutter 2 to the drain tank 9 through the drain pipe 6 so that ≧ρ>0, the wastewater stored in the drain tank 9 is drained. T] This is to adjust the amount of water discharged from 5.

このときuU水抜管15からのnt水は、排水流量計1
7でΔII+定しつつ所定の排水量となるようにt7F
水ポンプ16を回転数制御によって行われる。
At this time, the nt water from the uU water drain pipe 15 is
At t7F, set ΔII+ constant at 7 to reach the specified displacement amount.
This is done by controlling the rotation speed of the water pump 16.

具体的には、差圧812GによっC取り出したプロセス
変量としての差圧ΔPを圧力調!![t28bに導き、
予め調fl[L28bに入力され°Cいるプラスの差圧
設定値PL!:比較し、この比較結果に基づいて操作1
8号(MV値)をカスリ゛−1′制御構成としたレベル
調節8131に与え、レベルllf!fI+’t131
から発する操作信号(MV(a)を回転数詞?IHH1
9を経由して排水ポンプ16を回転数制御し、iJF水
ク水タンク9排出される排水量を調整する。なお、排水
タンク9に設けられたV[水レベル計18によって検出
された排水I3のレベル信号はレベル調節計31に受信
され子のl[水タンク9内のiJF水レベルを把握する
ようになっている。
Specifically, the pressure difference ΔP as a process variable extracted by the pressure difference 812G is adjusted! ! [Lead to t28b,
The positive differential pressure setting value PL input in advance to adjustment fl[L28b in °C! : Compare and perform operation 1 based on this comparison result.
No. 8 (MV value) is applied to the level adjustment 8131 having a Kasuri-1' control configuration, and the level llf! fI+'t131
The operation signal (MV(a) issued from
The rotation speed of the drainage pump 16 is controlled via the iJF water tank 9 to adjust the amount of drainage discharged from the iJF water tank 9. Note that the level signal of the waste water I3 detected by the water level meter 18 provided in the water tank 9 is received by the level controller 31, and the water level in the water tank 9 is grasped. ing.

例えば、差圧ΔP〈Pとなって駆動室23内のガス圧力
が低下し炉内圧力の細かい変動によって上011水封榊
]0や下部水封梼2に収容された水封水の息継ぎ現象に
よって炉内ガスが駆動室23内に侵入する恐れがあると
きには圧力調flff!t28b、レベル1PイI!1
Li1お、Lび回転数11i制御2;19を経由して1
ノ1水ポンプ16の回転数を低速としてU[水タンク9
から抜き取る排水■を減少さ一ロる。
For example, the gas pressure in the drive chamber 23 decreases due to the differential pressure ΔP<P, and due to small fluctuations in the pressure in the furnace, the upper 011 water seal] 0 and the breathing phenomenon of the water seal contained in the lower water seal 2 When there is a risk that furnace gas may enter the drive chamber 23 due to the pressure adjustment flff! t28b, level 1P I! 1
Li1, L and rotation speed 11i control 2; 1 via 19
No. 1 The rotation speed of the water pump 16 is set to low and U [water tank 9
Reduces the amount of wastewater extracted from the tank.

かくして下部水I、I梼2から排水タンク9に導かれる
111水〒がjlF水タンク9から抜き取るFIL水間
より人きくしてiJt水ク水タンク9内水レベルを−L
昇さυ、ごれに、LっでINF水ク水タンク9内ス容積
■□を減少させ、ti[水タンク9内のガスをJ!l!
通管14を通して/7−−タンク22に導入し−(駆動
室23の圧力を1−胃さ・lる。
In this way, the 111 water led from the lower water I and I tower 2 to the drainage tank 9 is more concentrated than the FIL water extracted from the JIF water tank 9, and the water level in the iJt water tank 9 is -L.
As the temperature rises, the volume of the INF water tank 9 is reduced with L, and the gas in the water tank 9 is reduced with ti [J! l!
It is introduced into the tank 22 through the passage pipe 14 (the pressure in the drive chamber 23 is reduced by 1).

逆に駆動室23内のガス圧力が高iMぎるような巽常事
態が生しるのを防止するには前記の場合と逆にIJr水
ポンプ1Gの回転数を高速として排水タンク9内からの
tJr水量を増加して排水タンク9内の?JIl水レヘ
ルしベ降さ一1!、OF水タンク9内のガス容Inを増
加さ−lツノ゛−シタン22内のガスを11ト水タンク
9内に導き駆動室23内のガス圧力を低下さ−Uる斤作
を行う。
On the contrary, in order to prevent a situation in which the gas pressure in the drive chamber 23 is too high, conversely to the above case, the rotation speed of the IJr water pump 1G is set to a high speed, and the rotation speed from the inside of the drainage tank 9 is increased. tJr Increase the amount of water in the drainage tank 9? JIl water level and be down 11! , the gas volume In in the OF water tank 9 is increased, the gas in the cylinder 22 is introduced into the water tank 9, and the gas pressure in the drive chamber 23 is reduced.

なお、0;l記のような制御はtJ)水タンク9内の排
水レベルが上限レベル(1、わ)と下限レー・ル(L、
 J )の範囲内にあるときに行い、排水レベルが上限
レベル(L、)を超えるとき、あるいは下限レベル(L
l)より低いときには回転数詞jn器32による排水ポ
ンプ16の回転数制御による排ガスタンク9内のガス容
積vTを制御する操作を行わないで第2図で説明した従
来例に準じて、ガス圧力調節器28aからの信号MV埴
により、N!ガス配管25に配設したNtガス流ffi
調節#29の開度を大きくして駆動室23内に供給され
る窒素ガス量によりガス圧をItIII御する。
In addition, the control as described in 0;l is performed when the drainage level in the water tank 9 is set to the upper limit level (1, wa) and the lower limit level (L,
J), and when the drainage level exceeds the upper limit level (L,) or the lower limit level (L,).
l) When the rotation speed is lower than that, the gas pressure is adjusted according to the conventional example explained in FIG. Due to the signal MV Hani from the device 28a, N! Nt gas flow ffi arranged in the gas pipe 25
The gas pressure is controlled by the amount of nitrogen gas supplied into the drive chamber 23 by increasing the opening degree of the adjustment #29.

このような窒素ガス供給による制ンnを行っている間に
回転数制御器32により排水ポンプ1Gの回転数制御に
より1ノ[水タンク9内の排水レベルを制御し、そのレ
ベルを146とり、 tとの間に回復し、IJFガスタ
ンク9内のガス容積■、による制御に備えるのは勿論で
ある。
While this control is being performed by supplying nitrogen gas, the rotation speed controller 32 controls the rotation speed of the drainage pump 1G to control the drainage level in the water tank 9 and set the level to 146. It goes without saying that the IJF gas tank 9 recovers during the period t and prepares for control based on the gas volume 1 in the IJF gas tank 9.

前述の実施例では排水タンクから排出される排水mを排
水抜取管に配設した回転数制御される排水ポンプによっ
て調整する場合について説明したが、排水タンクからの
UF水水制制御排水抜取管に配設した’tHJ調節ブr
等の他のtJII水抜取水抜取上段て同様に行うことが
可能である。
In the above-mentioned embodiment, the case where the drainage m discharged from the drainage tank is adjusted by the rotation speed-controlled drainage pump installed in the drainage extraction pipe was explained. 'tHJ adjustment brake installed
It is possible to perform the same procedure for other tJII water extractions such as the upper stage of water extraction.

〈発明の効果〉 以−L説明1.たまうに本発明によれば、旋回シュート
駆動装置用シール装置から駆動室内への炉内ガス侵入が
確実に防止できるばかりでなく窒素ガスの使用量が大幅
に低減され、その()られる効果は多大なものがある。
<Effects of the invention> Below-L explanation 1. According to the present invention, not only can gas intrusion into the drive chamber from the sealing device for the rotating chute drive device be reliably prevented, but also the amount of nitrogen gas used can be significantly reduced, and the effects thereof are significant. There is something.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の実施例に係る旋回シュー1−駆動装置
用シール装置を示す断面図、第2図は従来例に係る旋回
シュート駆動装置用シール装置を示す断面図、第3図は
シュー]・駆動装置の概略断面図である。 1・・・固定部、 3・・・カバー 5・・・仕切板、 7・・・給水計調箭弁、 9・・・tJ[水タンク、 2・・・下部水封樋、 4・・・給水ポンプ、 6・・・排水管、 8・・・給水流ffHf、 IO・・・上部水封部、 11・・・仕切板、 13・・・排 水、 15・・・0[水抜散性、 17・・・排水流量針、 19・・・回転数制御器、 21・・・回転テーブル、 23・・・駆動室、 25・・・N2ガス供給管、 27・・・圧力検出配管、 29・・・N、ガス流量調節ブr、 31・・・レベル1llllfT!L。 12・・・給水管、 14・・・連通管、 16・・・排水ポンプ、 18・・・排水レベル針、 20・・・旋回シ、1. 22・・・ケーシング、 2イ・・・連絡管、 26・・・差圧旧、 28・・・圧力調ハ■1. 30・・・炉頂壁、 特約出願人 川崎製鉄株式会社 第 図
FIG. 1 is a sectional view showing a seal device for a swing chute 1-drive device according to an embodiment of the present invention, FIG. 2 is a sectional view showing a seal device for a swing chute drive device according to a conventional example, and FIG. ] - It is a schematic sectional view of a drive device. 1... Fixed part, 3... Cover 5... Partition plate, 7... Water meter control valve, 9... tJ [water tank, 2... Lower water seal gutter, 4...・Water supply pump, 6...Drain pipe, 8...Water flow ffHf, IO...Upper water seal section, 11...Partition plate, 13...Drainage, 15...0 [Water drainage] 17...Drain flow rate needle, 19...Rotation speed controller, 21...Rotary table, 23...Drive chamber, 25...N2 gas supply pipe, 27...Pressure detection pipe, 29...N, gas flow rate adjustment b, 31...Level 1llllfT! L. 12...Water supply pipe, 14...Communication pipe, 16...Drainage pump, 18...Drainage level needle, 20...Swivel switch, 1. 22...Casing, 2i...Connecting pipe, 26...Differential pressure old, 28...Pressure adjustment ■1. 30...Furnace top wall, special applicant Kawasaki Steel Co., Ltd. Figure

Claims (1)

【特許請求の範囲】[Claims]  炉頂頂部のケーシング内に旋回シュートの旋回および
傾動を行う回転テーブルを設置し、該回転テーブルの上
部および下部における固定部と回転部との間に環状の水
封樋と該水封樋内に配置する環状の仕切板とを組合わせ
てなる水封機構を設けたベルレス式たて型炉における旋
回シュート駆動装置用シール装置の炉内ガス侵入防止方
法であって、前記下部水封樋から炉外に取り出した排水
管を密閉構造の排水タンク内に貯留された排水中に浸漬
すると共に、前記排水タンクの上部と前記回転テーブル
を設置した炉頂頂部ケーシングとを連通管で気密に接続
し、前記下部水封樋からの排水を排水管を介して排水タ
ンク内に導きつつ、前記炉頂頂部ケーシング内のガス圧
力と炉内のガス圧力との差圧がプラスの差圧設定値以上
に維持されるように前記排水タンク内に貯留された排水
を抜き取って該排水タンク内のガス容積を制御すること
を特徴とするベルレス式たて型炉における旋回シュート
駆動装置用シール装置の炉内ガス侵入防止方法。
A rotary table for rotating and tilting the rotating chute is installed in the casing at the top of the furnace, and an annular water seal is installed between the fixed part and the rotating part at the upper and lower parts of the rotary table, and an annular water seal is installed inside the water seal. A method for preventing gas intrusion into the furnace of a sealing device for a swing chute drive device in a bellless type vertical furnace equipped with a water sealing mechanism in combination with an annular partition plate arranged in the furnace, the method comprising: The drain pipe taken outside is immersed in the waste water stored in a drain tank with a closed structure, and the upper part of the drain tank and the furnace top casing in which the rotary table is installed are airtightly connected by a communicating pipe, While guiding the waste water from the lower water seal gutter into the drain tank through the drain pipe, the differential pressure between the gas pressure in the furnace top casing and the gas pressure inside the furnace is maintained at a positive differential pressure set value or higher. Gas intrusion into the furnace of a sealing device for a rotating chute drive device in a bell-less type vertical furnace, characterized in that the gas volume in the drainage tank is controlled by extracting the wastewater stored in the drainage tank so as to How to prevent it.
JP2080929A 1990-03-30 1990-03-30 Gas ingress prevention method for seal device for swivel chute drive in bellless vertical furnace Expired - Fee Related JPH0625373B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2080929A JPH0625373B2 (en) 1990-03-30 1990-03-30 Gas ingress prevention method for seal device for swivel chute drive in bellless vertical furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2080929A JPH0625373B2 (en) 1990-03-30 1990-03-30 Gas ingress prevention method for seal device for swivel chute drive in bellless vertical furnace

Publications (2)

Publication Number Publication Date
JPH03281713A true JPH03281713A (en) 1991-12-12
JPH0625373B2 JPH0625373B2 (en) 1994-04-06

Family

ID=13732131

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2080929A Expired - Fee Related JPH0625373B2 (en) 1990-03-30 1990-03-30 Gas ingress prevention method for seal device for swivel chute drive in bellless vertical furnace

Country Status (1)

Country Link
JP (1) JPH0625373B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104004871A (en) * 2014-05-30 2014-08-27 中冶南方工程技术有限公司 Closed water-cooling and nitrogen-sealing device for distributors

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104004871A (en) * 2014-05-30 2014-08-27 中冶南方工程技术有限公司 Closed water-cooling and nitrogen-sealing device for distributors

Also Published As

Publication number Publication date
JPH0625373B2 (en) 1994-04-06

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