JPS5941407A - Dry dust separator for exhaust gas from blast furnace - Google Patents

Dry dust separator for exhaust gas from blast furnace

Info

Publication number
JPS5941407A
JPS5941407A JP57149150A JP14915082A JPS5941407A JP S5941407 A JPS5941407 A JP S5941407A JP 57149150 A JP57149150 A JP 57149150A JP 14915082 A JP14915082 A JP 14915082A JP S5941407 A JPS5941407 A JP S5941407A
Authority
JP
Japan
Prior art keywords
exhaust gas
water
valve
turbine
blast furnace
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP57149150A
Other languages
Japanese (ja)
Inventor
Yoshihiro Harada
原田 佳弘
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Mitsui Zosen KK
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
Mitsui Zosen KK
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 Mitsui Engineering and Shipbuilding Co Ltd, Mitsui Zosen KK filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP57149150A priority Critical patent/JPS5941407A/en
Publication of JPS5941407A publication Critical patent/JPS5941407A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/002Evacuating and treating of exhaust gases
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2100/00Handling of exhaust gases produced during the manufacture of iron or steel
    • C21B2100/40Gas purification of exhaust gases to be recirculated or used in other metallurgical processes
    • C21B2100/44Removing particles, e.g. by scrubbing, dedusting
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2100/00Handling of exhaust gases produced during the manufacture of iron or steel
    • C21B2100/60Process control or energy utilisation in the manufacture of iron or steel
    • C21B2100/62Energy conversion other than by heat exchange, e.g. by use of exhaust gas in energy production

Abstract

PURPOSE:To protect the packings and seals of valves in by-pass and slip-stream pipe lines, by providing a water atomizer in the by-pass pipe line to enable to control the temp. of exhaust gas. CONSTITUTION:The titled apparatus arranged in the order of a blast furnace 1, a separator 3 for removing dust of coarse particle side, a dry dust separator 4 and a turbine 9 for recovering the energy of pressure at the top of the furnace. A by-pass pipe line 12 for communicating the downstream side of said dust separator 4 to the slipstream side of the turbine 9 is provided, and water atomizers 14, 15 are provided in front and in rear of a septum valve 13 to atomize water into exhaust gas. In addition, sensors 17, 18 for detecting the temp. and pressure of the exhaust gas are provided at the upper stream side of the water atomizer 14 and moved conjointly with the water atomizers 14, 15. Furthermore, a sensor 19 for detecting the opening rate of the valve 13 is attached to the valve 13. By this apparatus, the temp. of exhaust gas flowing through the pipe line 12 is controlled, so that packing and seals are protected from heat.

Description

【発明の詳細な説明】 ンにおける高炉排ガスの乾式除塵装置に関し、より詳細
には、排ガスバイパス管路及びセプタム弁等の保護を目
的とした乾式除塵装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a dry dust removing apparatus for blast furnace exhaust gas in a furnace, and more particularly to a dry dust removing apparatus for protecting exhaust gas bypass pipes, septum valves, and the like.

高炉排ガスは高温で、かなりの圧力を有し、しかもガス
量も多いので、この排ガスが有するエネルギーを回収す
べく、種々の方法が提案されている。これらの方法を、
排ガスの状態すなわち排ガスがタービンに供給される過
程における除塵方式によって区分すると、(イ)排ガス
をベンチュリスクラバーで除塵し、さらに必要に応じ排
ガス中に水を噴霧したのち、タービンに供給する湿式除
塵法、および(口)ダストキャツチャやバグフィルタ等
によって除塵する乾式除塵法に大別される。
Since blast furnace exhaust gas has a high temperature, considerable pressure, and a large amount of gas, various methods have been proposed to recover the energy contained in this exhaust gas. These methods
Classifying them according to the state of the exhaust gas, that is, the method of dust removal during the process in which the exhaust gas is supplied to the turbine, is as follows: (a) Wet dust removal method, in which the exhaust gas is removed with a Venturi scrubber, water is further sprayed into the exhaust gas as necessary, and then the exhaust gas is supplied to the turbine. It is broadly divided into dry dust removal method, which removes dust using dust catcher, bag filter, etc.

(イ)は一般に除塵効率が(口)よりも高いが、水との
接触によって排ガス温度が低下するので、それだけエネ
ルギー回収効率が低下する問題点がある。
(b) generally has higher dust removal efficiency than (b), but the problem is that the exhaust gas temperature decreases due to contact with water, which reduces the energy recovery efficiency accordingly.

一方、(口)は排ガス温度の低下が少ない点では有利で
あるが、タービンが何等かの理由によって停止しだシ、
排ガス量が急激に増加したりする場合には、高炉排ガス
を高温のままで既設のバイパス管路やこれに連なる後流
の設備に流せことになり、管路の熱膨張やパツキン、シ
ールの耐熱性などの点でトラブルを生ずる欠点がある。
On the other hand, (mouth) is advantageous in that the exhaust gas temperature decreases less, but if the turbine stops for some reason,
In cases where the amount of exhaust gas increases rapidly, blast furnace exhaust gas may be allowed to flow at high temperatures through the existing bypass pipeline or downstream equipment connected to it, causing thermal expansion of the pipeline and heat resistance of packing and seals. It has the disadvantage of causing problems in terms of sexuality, etc.

そこで本発明は、かかる現状にかんがみなされたもので
あり、バイパス管路のセプタム弁の動するので、タービ
ンの停止時や、排ガス量の増加、排ガス温度や圧力変化
に速やかに対応してバイパス管路を流れる排ガスを制御
することができるなどの特長を有するものである。
Therefore, the present invention was developed in consideration of the current situation, and since the septum valve of the bypass pipe is moved, the bypass pipe can be quickly adjusted when the turbine is stopped, an increase in the amount of exhaust gas, or a change in exhaust gas temperature or pressure. It has features such as being able to control the exhaust gas flowing through the path.

すなわち本発明の乾式除塵装置は、高炉、粗粒除塵器、
乾式除塵器および炉頂圧エネルギー回収タービンの順に
管路を介して配列されており、前記乾式除塵器の下流側
と前記タービンの出向側とを連結するバイパス管路を設
け、該バイパス管路に設けたセプタム弁の前後の管路に
水噴霧器を夫々設け、更にこれら水噴霧器と連動する排
ガス温度と排ガス圧力検知センサを前およびセプタム弁
開度検出センサを前記セプタム弁に夫々取り付けたこと
を特徴とするものである。
That is, the dry dust removing device of the present invention can be used in a blast furnace, a coarse dust remover,
A dry dust remover and a furnace top pressure energy recovery turbine are arranged in this order via a pipe line, and a bypass pipe is provided that connects the downstream side of the dry dust remover and the outlet side of the turbine, and the bypass pipe is connected to the A water sprayer is provided in each of the pipes before and after the provided septum valve, and furthermore, an exhaust gas temperature and exhaust gas pressure detection sensor that is linked to these water sprayers is attached to the front, and a septum valve opening detection sensor is attached to the septum valve, respectively. That is.

以下、図面に示した実施例にもとづき本発明を訝明する
The present invention will be explained below based on the embodiments shown in the drawings.

高炉1の炉頂から排出された排ガスは、管路2を経てダ
ストキャツチャなどの粗粒除塵器乙に至り、大型のダス
トが除去されたのちに、電気集塵器、バグフィルタなど
の乾式除塵器4に送られて除塵される。
The exhaust gas discharged from the top of the blast furnace 1 passes through the pipe 2 and reaches a coarse dust remover B such as a dust catcher, where large dust particles are removed. The dust is sent to a dust remover 4 to remove dust.

次いで管路5に至り、止弁6.緊急遮断弁7゜および調
速弁8を経てタービン9に送られ、発電機10により電
機エネルギーに変換される。タービン9を出た排ガスは
管路11を経て系外に排出される。
Next, the line 5 is reached and the stop valve 6. It is sent to the turbine 9 via the emergency shutoff valve 7° and the speed control valve 8, and is converted into electrical energy by the generator 10. Exhaust gas exiting the turbine 9 is discharged to the outside of the system via a pipe 11.

一方、本発明においては、乾式除塵器4の後流側と、タ
ービン9の後流側とを連結するバイパス管路12が設け
られており、このバイパス管路12にはセプタム弁16
をはさんで、その上流側と下流側に夫々、水噴霧器14
および15が設けられている。
On the other hand, in the present invention, a bypass line 12 is provided that connects the downstream side of the dry dust remover 4 and the downstream side of the turbine 9, and this bypass line 12 is provided with a septum valve 16.
Water sprayers 14 are installed on the upstream and downstream sides of the
and 15 are provided.

なお、好ましくは、後流側の水噴霧器15の後流に消音
器16を設けることもできる。この消音器16は、セプ
タム弁が生ずる大きな騒音を低減するための役目をする
Preferably, a muffler 16 can also be provided downstream of the water sprayer 15 on the downstream side. This muffler 16 serves to reduce the loud noises produced by the septum valve.

更に本発明においては、セプタム弁16の上流側の水噴
霧器14の前のバイパス管路上に排ガス温度検知センサ
17および排ガス圧力検知センサ18が設けられ、また
セプタム弁16にはセプタム弁開度感知センサ19が取
付けられており、これらのセンサは、噴射水量調整弁2
0および21と夫々、連動するようになっている。通常
ではセプタム弁13は閉止され、排ガスはすべてタービ
ン9に供給されるが、タービ/9が何等かの理由で停止
した場合、あるいは高炉1で発生する排ガス量が異状に
増加したり、ガス圧が異状に上昇したりした場合は、セ
プタム弁13が緊急に開かれ、同時に止め弁6および緊
急遮断弁7が閉じられて発電機10の負荷が遮断される
。セプタム弁16を開くことによって、直ちにセプタム
弁開度検知センサ19が作動し、同時に噴射水量調整弁
20 、21が開いて、水噴霧装置14 、15で排ガ
ス中に水が噴霧され、排ガス中の夕゛ストがセプタム弁
や消音器内部に付着するのを防止するとともにこれらダ
ストの除去も期待できる。
Furthermore, in the present invention, an exhaust gas temperature detection sensor 17 and an exhaust gas pressure detection sensor 18 are provided on the bypass line in front of the water sprayer 14 on the upstream side of the septum valve 16, and the septum valve 16 is provided with a septum valve opening detection sensor. 19 is installed, and these sensors are connected to the injection water amount adjustment valve 2.
0 and 21, respectively. Normally, the septum valve 13 is closed and all exhaust gas is supplied to the turbine 9, but if the turbine 9 stops for some reason, or the amount of exhaust gas generated in the blast furnace 1 increases abnormally, or the gas pressure If there is an abnormal rise in the septum valve 13, the stop valve 6 and the emergency shutoff valve 7 are closed at the same time, and the load on the generator 10 is cut off. By opening the septum valve 16, the septum valve opening detection sensor 19 is activated immediately, and at the same time, the injection water amount adjustment valves 20 and 21 are opened, and water is sprayed into the exhaust gas by the water spray devices 14 and 15. It can be expected to prevent dust from adhering to the septum valve and the inside of the muffler, and also to remove such dust.

同時に、排ガス温度が低下される。At the same time, the exhaust gas temperature is reduced.

更にこの噴霧氷量は排ガス温度検知センサ17および圧
力検知センサ18によっても制御され、排ガス温度や圧
力が異状に上昇した場合には、センサ17 、18によ
って、より多くの水が噴霧されるようになる。
Furthermore, the amount of sprayed ice is also controlled by an exhaust gas temperature detection sensor 17 and a pressure detection sensor 18, and when the exhaust gas temperature or pressure rises abnormally, the sensors 17 and 18 control the amount of water to be sprayed. Become.

このように本発明においては、セプタム弁13を開くこ
とによって、一定量の水噴霧が直ちに行なわれるばかり
でなく、排ガスの温度および圧力に対応して噴霧水の増
減がはかられる。
As described above, in the present invention, by opening the septum valve 13, not only is a fixed amount of water sprayed immediately, but also the amount of water sprayed is increased or decreased in accordance with the temperature and pressure of the exhaust gas.

このように水噴霧によって冷却された排ガスは管路22
から系外に排出され、高温の排ガスのままでの排出が防
止される。
The exhaust gas cooled by the water spray is transferred to the pipe 22.
This prevents the exhaust gas from being discharged as a high-temperature exhaust gas.

また逆にタービン9の始動時には、止弁6および緊急遮
断弁7を開き、セプタム弁13をしぼりながら、調速弁
8を開くことによりタービン9を始動させ、タービン9
の回転が定常に達し。
Conversely, when starting the turbine 9, the stop valve 6 and the emergency shutoff valve 7 are opened, the septum valve 13 is squeezed, and the regulating valve 8 is opened to start the turbine 9.
The rotation of reaches steady state.

たところで発電機10を回転させる。At this point, the generator 10 is rotated.

この操作中には、タービン9を通過したガスと、バイパ
ス管路12を通過したガスが混合状態で管路22から系
外に排出されるが、セプタム弁16が閉じられた時点で
すべての排ガスがタービン9を通過するようになる。こ
の間、排ガス温度検知センサ17、圧力検知センサ18
およびセプタム弁開度センサ19からの信号によって噴
射水量調整弁20 、21が制御され、最終的には水噴
霧器14および15における水噴霧が中止される。
During this operation, the gas that has passed through the turbine 9 and the gas that has passed through the bypass line 12 are discharged from the system through the line 22 in a mixed state. However, when the septum valve 16 is closed, all the exhaust gas is comes to pass through the turbine 9. During this time, the exhaust gas temperature detection sensor 17 and the pressure detection sensor 18
The injection water amount adjusting valves 20 and 21 are controlled by the signal from the septum valve opening sensor 19, and finally the water spraying in the water sprayers 14 and 15 is stopped.

更に本発明においては、セプタム弁16の下流側の水噴
霧器15と消音器16との間に噴射水量調整弁20 、
21と連動する排ガス温度検知センサ17Aを設けるこ
ともできる。このセンサ17Aにより、水噴霧後の排ガ
ス温度が、なお上昇している場合には、更に水噴霧量が
追加される。
Furthermore, in the present invention, an injection water amount adjustment valve 20 is provided between the water sprayer 15 and the muffler 16 on the downstream side of the septum valve 16.
It is also possible to provide an exhaust gas temperature detection sensor 17A that works in conjunction with 21. This sensor 17A detects that if the exhaust gas temperature after water spraying is still rising, the amount of water sprayed is further added.

以上述べたように、本発明によれば、バイパス管12に
設けたセプタム弁16にセプタム弁開度検知センサが設
けであるので、セプタム弁16の開閉に対応しておくれ
なく、直ちに水噴霧器14 、15における水噴霧を開
始したり、中止することができる。
As described above, according to the present invention, since the septum valve 16 provided in the bypass pipe 12 is provided with a septum valve opening detection sensor, the water sprayer 14 is immediately activated without having to respond to the opening and closing of the septum valve 16. , 15 can be started or stopped.

しかも本発明においては、セプタム弁13の開閉によっ
て単に機械的に水噴霧を開始したり、中止したりするば
かりでなく、上流側の水噴霧器14の前の排ガス温度検
知センサ17および圧力検知センサ18によって、排ガ
スの温度や圧力に対応して自動的に噴霧水量を変化させ
ることができ、排ガス温度や圧力が高い場合には、より
多くの水が、低い場合にはより少量の水が噴霧され、こ
の結果、排ガスのより効率的な冷却が達成される。
Moreover, in the present invention, water spraying is not only started or stopped mechanically by opening and closing the septum valve 13, but also the exhaust gas temperature detection sensor 17 and the pressure detection sensor 18 in front of the water sprayer 14 on the upstream side. The amount of water sprayed can be automatically changed according to the temperature and pressure of the exhaust gas, so when the exhaust gas temperature and pressure are high, more water is sprayed, and when the exhaust gas temperature and pressure are low, less water is sprayed. , As a result, more efficient cooling of the exhaust gas is achieved.

従って本発明によれば、排ガスのバイパス管路に流れる
状態に応じて直ちに水噴射が行なわれるので、水噴射の
おくれが全くなくなり、排ガス温度をバイパス管路や、
このバイパス管路の先に連なる排ガス管路の設計温度以
下に保持することができ、これら管路を異状熱膨張ある
いは熱応力さらに各管路や弁のパツキンやシールを熱に
よる破損から完全に防止することができる。
Therefore, according to the present invention, since water is injected immediately according to the state of the exhaust gas flowing into the bypass pipe, there is no delay in water injection, and the temperature of the exhaust gas can be controlled by the bypass pipe or
It is possible to maintain the temperature of the exhaust gas pipes connected to the end of this bypass pipe below the design temperature, completely preventing these pipes from abnormal thermal expansion or thermal stress, and the gaskets and seals of each pipe and valve from being damaged by heat. can do.

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

図は本発明の実施例を示す概要図である。 1・・・高炉、6・・・粗粒除塵器、4・・・乾式除塵
器、9・・・タービン、12・・・バイパス管路、16
・・・セプタム弁、14 、15・・・水噴霧器、17
・・・排ガス温度検知センサ、18・・・排ガス圧力検
知センサ、19・・・セプタム弁開度検知センサ。 代理人 弁理士 小 川 信 − 弁理士 野 口 賢 照 弁理士斎下和彦
The figure is a schematic diagram showing an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1...Blast furnace, 6...Coarse dust remover, 4...Dry dust remover, 9...Turbine, 12...Bypass pipe line, 16
...Septum valve, 14, 15...Water sprayer, 17
...Exhaust gas temperature detection sensor, 18...Exhaust gas pressure detection sensor, 19...Septum valve opening detection sensor. Agent: Patent Attorney Shin Ogawa − Patent Attorney Ken Noguchi Teru Patent Attorney Kazuhiko Saishita

Claims (1)

【特許請求の範囲】[Claims] 高炉、粗粒除塵器、乾式除塵器および炉頂圧エネルギー
回収タービンの順に管路を介して配列されておシ、前記
乾式除塵器の下流側と前記タービンの後流側とを連結す
るバイパス管路を設け、該バイパス管路に設けたセプタ
ム弁の前後の該バイパス管路に水噴霧器を夫々設け、更
にこれら水噴霧器と連動する排ガス温度と排ガス圧力検
知センサを前記セプタム弁の上流側の前記水噴霧器の前
に、およびセグタム弁開度検知センサを前記セプタム弁
に夫々取り付けたことを特徴とする高炉排ガスの乾式除
塵装置。
A blast furnace, a coarse dust remover, a dry dust remover, and a furnace top pressure energy recovery turbine are arranged in this order via a pipe line, and a bypass pipe connects the downstream side of the dry dust remover and the downstream side of the turbine. A water sprayer is provided in each of the bypass pipes before and after the septum valve provided in the bypass pipe, and exhaust gas temperature and exhaust gas pressure detection sensors linked to these water sprayers are installed in the bypass pipe on the upstream side of the septum valve. 1. A dry dust removal device for blast furnace exhaust gas, characterized in that a segment valve opening detection sensor is installed in front of the water sprayer and on the septum valve.
JP57149150A 1982-08-30 1982-08-30 Dry dust separator for exhaust gas from blast furnace Pending JPS5941407A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57149150A JPS5941407A (en) 1982-08-30 1982-08-30 Dry dust separator for exhaust gas from blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57149150A JPS5941407A (en) 1982-08-30 1982-08-30 Dry dust separator for exhaust gas from blast furnace

Publications (1)

Publication Number Publication Date
JPS5941407A true JPS5941407A (en) 1984-03-07

Family

ID=15468868

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57149150A Pending JPS5941407A (en) 1982-08-30 1982-08-30 Dry dust separator for exhaust gas from blast furnace

Country Status (1)

Country Link
JP (1) JPS5941407A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0611590A1 (en) * 1993-02-18 1994-08-24 Asahi Glass Company Ltd. Method for operating a filtration apparatus for flue gas
EP2574873A1 (en) * 2011-09-28 2013-04-03 Siemens VAI Metals Technologies GmbH Method and device for decreasing the temperature of blast furnace gas temperature peaks

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0611590A1 (en) * 1993-02-18 1994-08-24 Asahi Glass Company Ltd. Method for operating a filtration apparatus for flue gas
EP2574873A1 (en) * 2011-09-28 2013-04-03 Siemens VAI Metals Technologies GmbH Method and device for decreasing the temperature of blast furnace gas temperature peaks
WO2013045534A1 (en) * 2011-09-28 2013-04-04 Siemens Vai Metals Technologies Gmbh Method and devices-system for decreasing the temperature of blast furnace gas temperature peaks

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