JPH0625373B2 - Gas ingress prevention method for seal device for swivel chute drive in bellless vertical furnace - Google Patents
Gas ingress prevention method for seal device for swivel chute drive in bellless vertical furnaceInfo
- Publication number
- JPH0625373B2 JPH0625373B2 JP2080929A JP8092990A JPH0625373B2 JP H0625373 B2 JPH0625373 B2 JP H0625373B2 JP 2080929 A JP2080929 A JP 2080929A JP 8092990 A JP8092990 A JP 8092990A JP H0625373 B2 JPH0625373 B2 JP H0625373B2
- Authority
- JP
- Japan
- Prior art keywords
- drainage
- furnace
- water
- gas
- pressure
- 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 - Fee Related
Links
- 238000000034 method Methods 0.000 title claims description 11
- 230000002265 prevention Effects 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 67
- 238000007789 sealing Methods 0.000 claims description 45
- 238000005192 partition Methods 0.000 claims description 8
- 239000007789 gas Substances 0.000 description 54
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 13
- 229910001873 dinitrogen Inorganic materials 0.000 description 13
- 239000000498 cooling water Substances 0.000 description 11
- 239000000428 dust Substances 0.000 description 7
- 238000001816 cooling Methods 0.000 description 4
- 238000001514 detection method Methods 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000000112 cooling gas Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
Landscapes
- Blast Furnaces (AREA)
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は、ベルレス式高炉における旋回シュート駆動装
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
ルを確保し、駆動室への炉頂ガスやダストの侵入を確実
に防止すると共に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ト駆動装置用
駆動室の炉頂ガス侵入防止方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The present invention secures a seal of a water sealing mechanism provided between a rotating part and a fixed part of a swirling chute drive device in a bellless blast furnace, and ensures a drive chamber. The present invention relates to a method for preventing the intrusion of the top gas and dust into the drive chamber and the nitrogen gas supplied to the drive chamber, and a method for preventing the top gas from entering the drive chamber for the swirling chute drive device of the bellless blast furnace. .
<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ベルレス式炉頂装
入装置が使用されている。このベルレス式炉頂装入装置
は炉内に設けた旋回シュートを連続旋回させると共に傾
動させて原料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 a blast furnace, a bellless furnace top charging device is used as a furnace top charging device used when charging raw materials such as ore and coke into the furnace. This bellless furnace top charging device is a device for continuously charging and swirling a swirling chute provided in the furnace to distribute and charge the raw material, and it is compact as a whole and the height of the device can be relatively low. Have the advantage of.
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、傾動を行う回
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(スリット)から炉内に排出することによ
って行われていた。Conventionally, in a bellless type vertical furnace, especially in a blast furnace, the gas seal and dust seal for the inside of the rotary table 21 that swivels and tilts the swirling chute 20 as shown in FIG. The rotating table 21
The exhaust gas after being blown into a drive chamber 23 formed in a casing 22 in which the rotary table 21 is cooled, and then the rotary table 21 is cooled, has an annular gap (slit) between the fixed portion 1 and the rotary portion, that is, the cover 3 of the rotary table 21. ) Was discharged into the furnace.
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
20000kcal/h程度であり、したがって冷却に必要なガ
ス量は1000Nm3/h程度で十分であるが、この供給量で
は炉内からのケーシング22内の駆動室23へのガスおよび
ダストの侵入を防ぐことができなかった。ガスおよびダ
ストの侵入を確実に回避するには6000〜10000 Nm3/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 the radiant heat from the furnace is at most
It is about 20000 kcal / h, and therefore the amount of gas required for cooling is about 1000 Nm 3 / h, but this supply amount prevents gas and dust from entering the driving chamber 23 in the casing 22 from inside the furnace. I couldn't. 6000 to 10000 Nm 3 / h to ensure that gas and dust ingress is avoided
Cost of nitrogen gas is required.
ケーシング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ット
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
を摺動面に押圧してシールする手段(特開昭61-87807号
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 casing 22, means for sealing by providing a sealing device for pressing an elastic body in the slit portion between the fixed portion and the rotating portion of the rotary table 21 (Japanese Patent Laid-Open No. 61- No. 62782, Japanese Utility Model Laid-Open No. 63-123994) or a means for accommodating carbon in the slit and pressing the carbon against the sliding surface to seal it (see Japanese Patent Laid-Open No. 61-87807). There is.
しかるに、これらのシール手段は弾性体やカーボンを摺
動面に押圧するため摩耗が激しく長期に渡ってシール機
能を維持することが困難であり、またシール性が不十分
なため特に高圧の大型高炉の場合には炉頂中央部の垂直
方向のガス流速が大きく、結局は炉内ガスおよびダスト
の侵入防止の目的だけに例えば2000Nm3/h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があっ
た。However, since these sealing means press the elastic body and carbon against the sliding surface, it is difficult to maintain the sealing function for a long period of time due to severe wear. Moreover, since the sealing performance is insufficient, a large blast furnace with a high pressure is required. In the case of, the gas flow rate in the vertical direction at the center of the furnace top is large, and in the end there is a problem in that a cooling gas supply of, for example, 2000 Nm 3 / h or more must be performed only for the purpose of preventing intrusion of gas and dust in the furnace. there were.
このような問題点に対処するため実開昭63−119650号公
報に水封樋と該水封樋内に配置する仕切板との組み合わ
せからなる水封機構を設けてシールする手段が開示され
ている。In order to deal with such a problem, Japanese Utility Model Laid-Open No. 63-119650 discloses means for sealing by providing a water sealing mechanism including a combination of a water sealing trough and a partition plate arranged in the water sealing trough. There is.
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21の上
部に環状の水封樋10を一体に設け、固定部1に水封樋10
内に配置する仕切板11を一体に設けてある。水封に必要
な冷却水は給水ポンプ4で昇圧され、給水流量計8によ
って冷却水量を測定しながら給水流量調節弁7の開度を
調節し、固定部1に設けた給水管12から上部水封樋10へ
供給される。That is, as shown in FIG. 2, an annular water sealing gutter 10 is integrally provided on an upper part of a rotary table 21 housed in a drive chamber 23 formed in a casing 22 at the top of a blast furnace, and a fixed portion 1 is provided with a water sealing gutter. Ten
A partition plate 11 arranged inside is integrally provided. The cooling water required for water sealing is boosted by the water supply pump 4, and while the amount of cooling water is measured by the water supply flow meter 8, the opening degree of the water supply flow rate control valve 7 is adjusted and the upper water is supplied from the water supply pipe 12 provided in the fixed part 1. Supplied to the sealing gutter 10.
また回転テーブル21の下部に対応する固定部1に環状の
水封樋2を一体に設け、回転テーブル21の上部に設けた
水封樋10から連絡間24(これは回転テーブルの冷却に利
用されている)を介して下部水封樋2に水封に必要な冷
却水を常時供給するようになっている。一方、回転テー
ブル21には水封樋2内に配置する仕切板5を一体に設
け、水封樋2と封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
部水封樋2には系外に冷却水を排出する排水管6を設け
てあり排水するようになっている。Further, an annular water-sealing gutter 2 is integrally provided on the fixed portion 1 corresponding to the lower part of the rotary table 21, and a connecting space 24 from the water-sealing gutter 10 provided on the upper part of the rotary table 21 (this is used for cooling the rotary table). The cooling water necessary for the water seal is always supplied to the lower water seal gutter 2 via the above. On the other hand, the rotary table 21 is integrally provided with a partition plate 5 arranged in the water sealing trough 2, and water is sealed by the water sealing trough 2 and the partition plate 5 submerged in the sealing water, and the fixed portion 1 and the rotating portion are separated from each other. Seal the gap. Further, a drain pipe 6 for discharging the cooling water is provided outside the system in the lower water sealing gutter 2 for draining.
ところで、高炉内は高圧であるので上部の水封樋10およ
び下部の水封樋2によりケーシング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25からN2ガス流量調節弁29を調節
しつつ窒素ガス(N2ガス)を供給して昇圧し、炉頂圧と
バランスさせると共に駆動室23内を冷却していた。By the way, since the pressure inside the blast furnace is high, in order to prevent the furnace top gas from entering the driving chamber 23 formed in the casing 22 by the upper water sealing gutter 10 and the lower water sealing gutter 2, the driving chamber
While controlling the N 2 gas flow rate control valve 29 from the nitrogen gas supply pipe 25 into the chamber 23, the nitrogen gas (N 2 gas) was supplied to increase the pressure to balance the furnace top pressure and cool the drive chamber 23. .
しかしながら炉頂圧の小さな変動によっても水封樋10お
よび2内の封水に息継ぎ現象がみられ、前記水封機構に
よる水封圧は 150〜200 mmAqしか取れないため急激な炉
頂圧変動が生じたときにしばしば水封が破れるという問
題点があった。However, due to the small fluctuations in the top pressure, a breathing phenomenon was observed in the sealing water in the water sealing troughs 10 and 2, and the water sealing pressure by the water sealing mechanism was only 150 to 200 mmAq. There was a problem that the water seal was often broken when it occurred.
水封が破れると水封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よるシール
ができなくなり炉内ガスやダストがケーシング内に入っ
て回転テーブルの駆動装置に悪影響を及ぼすことにな
る。If the water seal breaks, overflow from the water seal gutter will enter the furnace,
Not only will it enter the casing, but sealing by water sealing will not be possible, and gas and dust in the furnace will enter the casing and adversely affect the drive device of the rotary table.
<発明が解決しようとする課題> そこで、従来、差圧計26に接続した圧力検出配管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ΔPがプラス圧の設定
値p以上、すなわちΔP=P2−P1p0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 gauge 26 are respectively inserted into the casing 22 and the furnace top wall 30, and the pressure P 2 in the drive chamber 23 and the furnace Furnace pressure P 1 inside the top wall 30
And the differential pressure ΔP between the positive pressure and the negative pressure is detected, and the nitrogen gas is supplied from the nitrogen gas supply pipe 25 so that the differential pressure ΔP becomes equal to or higher than the set value p of the positive pressure, that is, ΔP = P 2 −P 1 p0.
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計28aに入力し、この差圧Δ
pと前記のプラスの差圧設定値pとから圧力調節計28a
で操作信号MV値を演算し、この操作信号MV値により
冷却N2パ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値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P2と炉内の圧力P1との差圧Δ
Pが差圧設定値pより大となるようにN2ガスパージ量を
コント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 gauge 26 takes out the differential pressure ΔP as a process pressure variable and inputs it to the pressure regulator 28a.
p and the above-mentioned positive differential pressure set value p from the pressure controller 28a
The operation signal MV value is calculated with the operation signal MV value, and the opening degree of the cooling N 2 purge control valve 29 is controlled by the operation signal MV value to drive the driving chamber 23.
The pressure inside the furnace top 27 was set to be higher than the positive differential pressure setting value p. However, due to the above operation, the pressure difference Δ between the pressure P 2 in the drive chamber 23 and the pressure P 1 in the furnace is always Δ.
In order to control the N 2 gas purge amount so that P becomes larger than the differential pressure set value p, it was uneconomical to follow the pressure fluctuation of the reactor internal pressure unless a large flow rate of N 2 gas was supplied.
本発明は前記従来技術の問題点を解消し、旋回シュート
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
のシールを確保し、駆動室への炉頂ガスやダストの侵入
を確実に防止すると共に、駆動室へ供給するN2ガスを節
減することができるベルレス式高炉における旋回シュー
ト駆動装置用駆動室への炉頂ガス侵入防止方法を提供す
ることを目的とするものである。The present invention solves the above-mentioned problems of the prior art, secures a seal of a water sealing mechanism provided between a rotating part and a fixed part of a swirling chute drive device, and intrudes a furnace top gas or dust into a drive chamber. It is an object of the present invention to provide a method for preventing intrusion of top gas into the drive chamber for a swirling chute drive device in a bellless blast furnace, which can reliably prevent N 2 gas supplied to the drive chamber. is there.
<課題を解決するための手段> 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である。<Means for Solving the Problems> According to the present invention for achieving the above object, a rotary table for swiveling and tilting a swirling chute is installed in a casing at the top of a furnace, and fixed at an upper part and a lower part of the rotary table. For a swirling chute drive device in a bellless vertical furnace equipped with a water-sealing mechanism formed by combining an annular water-sealing trough and an annular partition plate arranged in the water-sealing trough between a rotating part and a rotating part A method of preventing gas intrusion into the furnace of a sealing device, wherein the drain pipe taken out of the lower water sealing gutter to the outside of the furnace is immersed in the drainage stored in a drain tank having a sealed structure, and the upper part of the drain tank is used. While connecting the furnace top casing with the rotary table airtightly connected by a communication pipe, while guiding the drainage from the lower water sealing gutter into the drainage tank via the drainage pipe,
The drainage stored in the drainage tank is extracted so that the differential pressure between the gas pressure in the furnace top casing and the gas pressure in the furnace is maintained at a positive differential pressure setting value or more. A method for preventing intrusion of gas into a furnace of a seal device for a swirling chute drive device in a bellless vertical furnace, which is characterized by controlling a gas volume.
<作 用> 下部水封樋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排水
タンク内の排水レベルつまり排水タンク内のガス容積を
制御し、これによって炉頂頂部ケーシング内のガス圧力
と炉内のガス圧力との差圧を所定のプラス圧以上に維持
する。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。<Operation> While guiding the drainage from the lower water sealing gutter into the drainage tank through the drainage pipe, the drainage stored in the drainage tank is adjusted in the drainage tank with a large volume by adjusting the amount of extraction from the drainage tank. The drainage level, that is, the volume of gas in the drainage tank is controlled, thereby maintaining the differential pressure between the gas pressure in the furnace top casing and the gas pressure in the furnace above a predetermined positive pressure. Thus, the gas in the furnace from the inside of the furnace into the drive chamber through the seal device for the swivel chute drive device is prevented.
本発明の原理は、炉頂部の炉内圧P1の変動の影響を水
封機構を介して受ける炉頂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排水タンクと接続し、排水タ
ンク内に貯留される排水のレベルを制御することによっ
てガス容積を制御し、これによって駆動室内の圧力を制
御することを骨子としている。The principle of the present invention is that the drive chamber formed in the furnace top casing, which is affected by the fluctuation of the furnace pressure P 1 at the furnace top via the water sealing mechanism, is connected to the drain tank via the communication pipe, and the drain tank is connected. The essence is to control the gas volume by controlling the level of the drainage stored inside, and thereby control the pressure in the drive chamber.
すなわち、駆動室のガス容積をVmとし排水タンクの排
水上に占めるガス容積をVTとすると全ガス容積はVm
+VTとなる。ここで炉頂圧P1の変動を補償して対抗
するにはP1×(Vm+VT)=C(一定値)になるよ
うにコントロールすればよいことになる。ここでVmと
Cは一定値であるので、炉頂圧P1が大きくなれば排水
タンクガス容積VTを小さくし、逆に炉頂圧P1が小さ
くなればVTを大きくなるように操作することになる。That is, assuming that the gas volume of the driving chamber is V m and the gas volume occupied by the drainage in the drainage tank is V T , the total gas volume is V m.
It becomes + V T. Here, in order to compensate for and counter the fluctuation of the furnace top pressure P 1 , it is sufficient to control so that P 1 × (V m + V T ) = C (constant value). Here, since V m and C is a constant value, to reduce the waste water tank gas volume V T the greater the Roitadaki圧P 1, so as to increase the V T smaller the Roitadaki圧P 1 in the opposite It will be operated.
<実施例> 以下本発明の一実施例を図面に基づいて説明する。第1
図において、給水ポンプ4で昇圧され、給水流量計8に
よって冷却水量を測定しながら給水流量調節弁7の開度
を調整し、水封に必要な冷却水(例えば工場還水)が固
定部1に設けた給水管12ら上部水封樋10へ供給される。
上部水封樋10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)を通って下部水封樋
2に水封に必要な冷却水を常時供給するようになってい
る。<Example> An example of the present invention will be described below with reference to the drawings. First
In the figure, the opening of the feed water flow rate control valve 7 is adjusted while measuring the amount of cooling water by the feed water flow meter 8 while measuring the amount of cooling water by the feed water pump 4, and the cooling water (for example, factory return water) necessary for water sealing is fixed. It is supplied to the upper water seal gutter 10 from the water supply pipe 12 provided in the.
The cooling water supplied to the upper water seal gutter 10 is always supplied to the lower water seal gutter 2 through the connecting pipe 24 (which is used for cooling the rotary table 21) to supply the cooling water necessary for the water seal. Has become.
さらに下部水封樋2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、水冷却水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の開度を調節しつつ窒素ガスを駆動室23内に
供給するN2ガス供給系を形成しているのは第2図に示す
従来例と同じである 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21を設置した炉頂頂部ケーシング22とを連通
管14で気密に接続してある。一方、排水タンク9の下端
部には排水抜取管15が接続されており、排水抜取管15に
配設された排水流量計17によって排水量を測定しつつ排
水ポンプ16によって排水タンク9内に貯留された排水13
を排出する排水系を形成してある。なお、排水タンク9
には排水レベル計18が設けてあり、排水タンク9内に貯
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。Further, a drain pipe 6 for discharging cooling water to the outside of the system is connected to the lower water sealing gutter 2 to form water cooling water, while a nitrogen gas supply pipe 25 is connected to the furnace top casing 22. It is the same as the conventional example shown in FIG. 2 that the N 2 gas supply system for supplying the nitrogen gas into the drive chamber 23 is formed while adjusting the opening degree of the N 2 gas flow valve 29. A furnace in which a drain pipe 6 taken out of the lower water gutter 2 to the outside of the furnace is immersed in the drain water 13 once stored in a drain tank 9 having a closed structure, and an upper portion of the drain tank 9 and a rotary table 21 are installed. The top casing 22 is connected to the top casing 22 by a communication pipe 14 in an airtight manner. On the other hand, a drainage sampling pipe 15 is connected to the lower end of the drainage tank 9, and the drainage pump 16 stores the drainage in the drainage tank 9 while measuring the amount of drainage with a drainage flow meter 17 arranged in the drainage sampling pipe 15. Drained 13
A drainage system that discharges is formed. In addition, drainage tank 9
A drainage level meter 18 is provided in the tank to measure the level of the drainage 13 stored in the drainage tank 9.
本発明では窒素ガス配管25からケーシング22内に供給す
る窒素ガスはN2ガス流量調節弁29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27bに接続した差圧計26
によって駆動室23内の圧力P2と炉内圧力P1との差圧
ΔPを検出し、その差圧ΔPをプロセス変量として取り
出しΔPがプラスの設定値p以上、すなわちΔP=P2
−P1p0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排水抜管15から抜き取る排水量を
調整するものである。このとき排水抜管15からの排水
は、排水流量計17で測定しつつ所定の排水量となるよう
に排水ポンプ16を回転数制御によって行われる。In the present invention, the nitrogen gas supplied from the nitrogen gas pipe 25 into the casing 22 is biased at a constant low flow rate with the N 2 gas flow rate control valve 29 set to a small opening. A differential pressure gauge 26 connected to the pressure detection pipe 27a inserted into the furnace top casing 22 and the pressure detection pipe 27b inserted into the furnace top wall 30.
The differential pressure ΔP between the pressure P 2 inside the drive chamber 23 and the furnace internal pressure P 1 is detected by and the differential pressure ΔP is taken out as a process variable and ΔP is a positive set value p or more, that is, ΔP = P 2
-Drain pipe 6 from lower water gutter 2 to become P 1 p0.
Through the drainage tank 9 through the drainage tank 9
The amount of drainage that drains the drainage stored in the drainage pipe 15 is adjusted. At this time, the drainage from the drainage pipe 15 is performed by controlling the rotation speed of the drainage pump 16 so that a predetermined amount of drainage is obtained while being measured by the drainage flow meter 17.
具体的には、差圧計26によって取り出したプロセス変量
としての差圧ΔPを圧力調節計28bに導き、予め調整計
28bに入力されているプラスの差圧設定値pと比較し、
この比較結果に基づいて操作信号(MV値)をカスケー
ド制御構成としたレベル調節計31に与え、レベル調整計
31から発する操作信号(MV値)を回転数制御器19を経
由して排水ポンプ16を回転数制御し、排水タンク9から
排出される排水量を調整する。なお、排水タンク9に設
けられた排水レベル計18によって検出された排水13のレ
ベル信号はレベル調節計31に受信されその排水タンク9
内の排水レベルを把握昭するようになっている。Specifically, the differential pressure ΔP as the process variable taken out by the differential pressure gauge 26 is guided to the pressure regulator 28b, and is adjusted in advance by the regulator.
Compare with the positive differential pressure setting value p input to 28b,
Based on this comparison result, an operation signal (MV value) is given to the level controller 31 having a cascade control configuration, and the level controller 31
An operation signal (MV value) issued from 31 is controlled in rotation speed of the drainage pump 16 via the rotation speed controller 19 to adjust the amount of drainage discharged from the drainage tank 9. The level signal of the wastewater 13 detected by the drainage level meter 18 provided in the drainage tank 9 is received by the level controller 31.
It is designed to grasp the drainage level inside.
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部水封樋10や下
部水封樋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
調節計28b、レベル調節計31および回転数制御器19を経
由して排水ポンプ16の回転数を低速として排水タンク9
から抜き取る排水量を減少させる。For example, when the differential pressure ΔP <p, the gas pressure in the drive chamber 23 decreases, and the fine fluctuations in the furnace pressure cause a phenomenon in which the water seal water stored in the upper water seal gutter 10 and the lower water seal gutter 2 breathes. When the internal gas may enter the drive chamber 23, the rotation speed of the drainage pump 16 is set to a low speed via the pressure controller 28b, the level controller 31, and the rotation speed controller 19 to drain the water tank 9.
Reduce the amount of drained water.
かくして下部水封樋2から排水タンク9に導かれる排水
量が排水タンク9から抜き取る排水量より大きくして排
水タンク9内の排水レベルを上昇させ、これによって排
水タンク9内のガス容積VTを減少させ、排水タンク9
内のガスを連通管14を通してケーシング22に導入して駆
動室23の圧力を上昇させる。Thus, the amount of drainage guided from the lower water gutter 2 to the drainage tank 9 is made larger than the amount of drainage drained from the drainage tank 9 to raise the drainage level in the drainage tank 9, thereby decreasing the gas volume V T in the drainage tank 9. , Drainage tank 9
The gas inside is introduced into the casing 22 through the communication pipe 14 to increase the pressure in the drive chamber 23.
逆に駆動室23内のガス圧力が高過ぎるような異常事態が
生じるのを防止するには前記の場合と逆に排水ポンプ16
の回転数を高速として排水タンク9内からの排水量を増
加して排水タンク9内の排水レベルを下降させ、排水タ
ンク9内のガス容積を増加させケーシング22内のガスを
排水タンク9内に導き駆動室23内のガス圧力を低下させ
操作を行う。On the contrary, in order to prevent an abnormal situation in which the gas pressure in the drive chamber 23 is too high, the drain pump 16
The rotation speed of is set to a high speed to increase the amount of drainage from the drainage tank 9 to lower the drainage level in the drainage tank 9, increase the gas volume in the drainage tank 9 and guide the gas in the casing 22 into the drainage tank 9. The operation is performed by reducing the gas pressure in the drive chamber 23.
なお、前記のような制御は排水タンク9内の排水レベル
が上限レベル(Lh)と下限レベル(Ll)の範囲内に
あるときに行い、排水レベルが上限レベル(Lh)を超
えるとき、あるいは下限レベル(Ll)より低いときに
は回転数制御器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値により、N2ガス配管25配設し
たN2ガス流量調節弁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制御する。The control as described above is performed when the drainage level in the drainage tank 9 is within the range between the upper limit level (L h ) and the lower limit level (L l ) and when the drainage level exceeds the upper limit level (L h ). Alternatively, when it is lower than the lower limit level (L 1 ), the operation of controlling the gas volume V T in the exhaust gas tank 9 by the rotation speed control of the drainage pump 16 by the rotation speed controller 32 is not performed and the conventional example described in FIG. According to the signal MV value from the gas pressure adjuster 28a, the opening degree of the N 2 gas flow rate adjusting valve 29 provided in the N 2 gas pipe 25 is increased and the amount of nitrogen gas supplied into the drive chamber 23 is changed. Control gas pressure.
このような窒素ガス供給による制御を行っている間に回
転数制御器32により排水ポンプ16の回転数制御により排
水タンク9内の排水レベルを制御し、そのレベルをLh
とLlとの間に回復し、排ガスタンク9内のガス容積V
Tによる制御に備えるのは勿論である。While the control by the nitrogen gas supply is being performed, the rotation speed controller 32 controls the rotation speed of the drainage pump 16 to control the drainage level in the drainage tank 9, and the level is set to L h.
And L 1 , the gas volume V in the exhaust gas tank 9 is recovered.
It goes without saying that the control by T is prepared.
前述の実施例では排水タンクから排出される排水量を排
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
排水量制御は排水抜取管に配設した流量調節弁等の他の
排水抜取手段によって同様に行うことが可能である。In the above-mentioned embodiment, the case where the amount of drainage discharged from the drainage tank is adjusted by the rotation speed controlled drainage pump arranged in the drainage extraction pipe has been described, but the drainage amount control from the drainage tank is arranged in the drainage extraction pipe. It can be similarly performed by other drainage means such as a flow rate control valve.
<発明の効果> 以上説明したよ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、その得られる効果は多大なものがある。<Effects of the Invention> As described above, according to the present invention, not only the intrusion of the gas in the furnace from the seal device for the swivel chute drive device into the drive chamber can be reliably prevented, but also the amount of nitrogen gas used is significantly reduced. However, the effect obtained is enormous.
第1図は本発明の実施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
ュート駆動装置の概略断面図である。 1……固定部、2……下部水封樋、 3……カバー、4……給水ポンプ、 5……仕切板、6……排水管、 7……給水量調節弁、8……給水流量計、 9……排水タンク、10……上部水封樋、 11……仕切板、12……給水管、 13……排水、14……連通管、 15……排水抜取管、16……排水ポンプ、 17……排水流量計、18……排水レベル計、 19……回転数制御器、20……旋回シュート、 21……回転テーブル、22……ケーシング、 23……駆動室、24……連絡管、 25……N2ガス供給管、26……差圧計、 27……圧力検出配管、28……圧力調節計、 29……N2ガス流量調節弁、30……炉頂壁、 31……レベル調節計。FIG. 1 is a sectional view showing a sealing device for a swiveling chute driving device according to an embodiment of the present invention, FIG. 2 is a sectional view showing a sealing device for a swiveling chute driving device according to a conventional example, and FIG. 3 is a chute driving device. FIG. 1 ... Fixed part, 2 ... Lower water gutter, 3 ... Cover, 4 ... Water supply pump, 5 ... Partition plate, 6 ... Drain pipe, 7 ... Water supply control valve, 8 ... Water supply flow rate Total, 9 ... Drainage tank, 10 ... Upper water gutter, 11 ... Partition plate, 12 ... Water supply pipe, 13 ... Drainage, 14 ... Communication pipe, 15 ... Drainage extraction pipe, 16 ... Drainage Pump, 17 ... Drainage flow meter, 18 ... Drainage level meter, 19 ... Rotation speed controller, 20 ... Rotating chute, 21 ... Rotary table, 22 ... Casing, 23 ... Drive room, 24 ... Connection pipe, 25 …… N 2 gas supply pipe, 26 …… Differential pressure gauge, 27 …… Pressure detection pipe, 28 …… Pressure regulator, 29 …… N 2 gas flow control valve, 30 …… Top wall of furnace, 31 ...... Level controller.
Claims (1)
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。1. A rotary table for swiveling and tilting a swirling chute is installed in a casing at the top of a furnace, and an annular water-sealing gutter and an annular water trough are provided between a fixed part and a rotary part at the upper and lower parts of the rotary table. A method for preventing gas intrusion in a furnace of a seal device for a swirling chute drive device in a bellless type vertical furnace equipped with a water sealing mechanism that is combined with an annular partition plate arranged in a water sealing trough, wherein While immersing the drain pipe taken out of the reactor from the water sealing gutter into the drainage stored in the drainage tank of the closed structure, the upper part of the drainage tank and the furnace top casing in which the rotary table is installed are connected by a communication pipe. Airtightly connected, while guiding the drainage from the lower water gutter into the drainage tank through the drainage pipe, the differential pressure between the gas pressure in the furnace top casing and the gas pressure in the furnace is a positive differential pressure. Maintain above the set value The drainage stored in the drainage tank is controlled so as to control the gas volume in the drainage tank. Method.
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 JPH03281713A (en) | 1991-12-12 |
| JPH0625373B2 true 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) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104004871B (en) * | 2014-05-30 | 2015-12-02 | 中冶南方工程技术有限公司 | Enclosed distributor water-cooled and nitrogen seal device |
-
1990
- 1990-03-30 JP JP2080929A patent/JPH0625373B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03281713A (en) | 1991-12-12 |
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