JPS6025608B2 - Reactor gas energy recovery power generation system - Google Patents

Reactor gas energy recovery power generation system

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Publication number
JPS6025608B2
JPS6025608B2 JP459678A JP459678A JPS6025608B2 JP S6025608 B2 JPS6025608 B2 JP S6025608B2 JP 459678 A JP459678 A JP 459678A JP 459678 A JP459678 A JP 459678A JP S6025608 B2 JPS6025608 B2 JP S6025608B2
Authority
JP
Japan
Prior art keywords
gas
turbine
flow rate
control device
valve
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
Application number
JP459678A
Other languages
Japanese (ja)
Other versions
JPS5498412A (en
Inventor
義重 香取
修 永田
雅昭 辻本
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP459678A priority Critical patent/JPS6025608B2/en
Publication of JPS5498412A publication Critical patent/JPS5498412A/en
Publication of JPS6025608B2 publication Critical patent/JPS6025608B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は反応炉ガスェネルギを回収して発電する反応炉
ガスェネルギ回収発電システムに関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a reactor gas energy recovery power generation system that recovers reactor gas energy to generate electricity.

従釆の斯種システムは、反応炉から出るガスをガス洗浄
装置とタービン調遠弁を介してタービン発電機に僕艶台
し、またタービン発電機と並列にセプタム弁を接続した
構造になっており、ガス洗浄装置は単に洗浄(集塵)機
能のみを持つものであった。
This type of system has a structure in which the gas coming out of the reactor is sent to the turbine generator through a gas cleaning device and a turbine control valve, and a septum valve is connected in parallel with the turbine generator. However, gas cleaning equipment only had a cleaning (dust collection) function.

そして、発電動作中においては、セプタム弁の操作によ
って反応炉の炉頂圧力を制御するようになっていた。か
)るシステム構成では、炉頂圧を安定にすることが鱗か
しく、またガス洗浄装置の前後差圧を適正に維持できな
くなり、ガス洗浄効果を充分に発揮させることができな
くなるという不都合がいまいま起った。本発明の目的は
、上述の如き問題点を解消し、安定な炉項圧および良好
なガス洗浄効果を共に確実に維持できる反応炉ガスェネ
ルギ回収発電システムを提供することにある。
During power generation operation, the top pressure of the reactor was controlled by operating a septum valve. In such a system configuration, it is difficult to stabilize the furnace top pressure, and the differential pressure across the gas cleaning device cannot be properly maintained, resulting in the inconvenience that the gas cleaning effect cannot be fully demonstrated. It just happened. SUMMARY OF THE INVENTION An object of the present invention is to provide a reactor gas energy recovery power generation system that can solve the above-mentioned problems and reliably maintain both a stable furnace pressure and a good gas cleaning effect.

しかして本発明によるシステムの主要な特徴は、ガス洗
浄装置に流量調整操作部を持たせ、発電動作中において
前記流量調整操作部を操作することにより、前記ガス洗
浄装置の前後差圧を良好な洗浄効果が得られるように制
御しつ)タービン発電機の調速弁の操作によって反応炉
の炉頂圧を制御するようにした構成にある。以下、添付
図面にしたがって本発明の一実施例を詳細に説明する。
However, the main feature of the system according to the present invention is that the gas cleaning device is provided with a flow rate adjustment operation section, and by operating the flow rate adjustment operation section during power generation operation, the pressure difference between the front and rear of the gas cleaning device can be maintained at a good level. The top pressure of the reactor is controlled by operating the regulating valve of the turbine generator while controlling the pressure so as to obtain a cleaning effect. Hereinafter, one embodiment of the present invention will be described in detail with reference to the accompanying drawings.

本実施例は高炉排ガスェネルギ回収発電システムであり
、1は高炉送風機、2は熱風炉、3は高炉、4はダスト
キャッチャ、5は流量調整操作部を内蔵するガス洗浄装
置、6はタービン入口弁、7は主塞止弁、8はタービン
調遠弁、9は発電機10を駆動するタービン、11はタ
ービン出□止弁、12,13,14はタービン9のガス
流路に並列のバイパス中に設けられたセプタム弁であり
、弁12をコントロール弁、弁13をレンジ弁、弁14
をマニュアル弁と呼ぶ。
This embodiment is a blast furnace exhaust gas energy recovery power generation system, in which 1 is a blast furnace blower, 2 is a hot blast furnace, 3 is a blast furnace, 4 is a dust catcher, 5 is a gas cleaning device with a built-in flow rate adjustment operation unit, and 6 is a turbine inlet valve. , 7 is a main blocking valve, 8 is a turbine control valve, 9 is a turbine that drives the generator 10, 11 is a turbine outlet stop valve, and 12, 13, and 14 are bypass valves parallel to the gas flow path of the turbine 9. It is a septum valve provided in the valve 12 is a control valve, valve 13 is a range valve and valve 14
is called a manual valve.

15はガスホルダ、16は高炉炉頂圧力検出器、17は
タービン入口圧力検出器、18はガス洗浄装置5の前後
差圧検出器、19はタービン回転数検出器、20は発電
機出力検出器である。
15 is a gas holder, 16 is a blast furnace furnace top pressure detector, 17 is a turbine inlet pressure detector, 18 is a differential pressure detector before and after the gas cleaning device 5, 19 is a turbine rotation speed detector, and 20 is a generator output detector. be.

21は検出器16,18の出力信号を受けてガス洗浄装
置5の流量調整操作部を操作するガス流量制御装置、2
2は検出器17の出力信号を受けてセブタム弁12,1
3,14を操作するセプタム弁制御装置、23は検出器
16,19,20の出力信号を受けてタービン調速弁を
操作するタービンガバナである。
Reference numeral 21 denotes a gas flow rate control device that receives output signals from the detectors 16 and 18 and operates the flow rate adjustment operation section of the gas cleaning device 5;
2 receives the output signal of the detector 17 and operates the septum valve 12,1.
A septum valve control device operates 3 and 14, and 23 is a turbine governor that operates a turbine speed regulating valve in response to output signals from detectors 16, 19 and 20.

24はシステムの状態および外部条件に応じて各装置2
1,22,23,24の動作を総括制御する総括制御装
置、25および26はガス流量制御装置21に炉頂圧力
設定値およびガス洗浄装置前後差圧設定値をそれぞれ与
える炉頂圧力設定器および前後差圧設定器、27はセプ
タム弁制御装置22に対してタービン入口圧力設定値を
与える夕−ビン入口圧力設定器、28,29,30はそ
れぞれタービンガバナ23に対して負荷制御値、タービ
ン回転数、発電機最大出力を設定する設定器である。
24 is for each device 2 depending on the system status and external conditions.
1, 22, 23, and 24; and 25 and 26, a furnace top pressure setting device that provides the gas flow rate control device 21 with a furnace top pressure setting value and a differential pressure setting value before and after the gas cleaning device, respectively; A front and rear differential pressure setting device, 27, a turbine inlet pressure setting device that provides a turbine inlet pressure setting value to the septum valve control device 22, and 28, 29, and 30, a load control value and a turbine rotation value to the turbine governor 23, respectively. This is a setting device for setting the number and maximum output of the generator.

前記システムにおいて、タービン9は高炉3が安定した
高圧操業状態にある時にのみ運転される。
In said system, the turbine 9 is operated only when the blast furnace 3 is in stable high pressure operating conditions.

したがって高炉操業の立上げ時および休風操作時は、セ
プタム弁12,13,14を全開して高炉発生ガスを全
てタービン9をバイパスさせる。このときの高炉炉頂圧
力は、ガス洗浄装置5の流量調整操作部をガス流量制御
装置21で操作することにより一定となるように制御さ
れる。またタービン9の運転中は、セプタム弁12,1
3,14を全閉し、高炉3の発生ガスを全て夕ービン9
に流す。この場合は、タービンガバナ23でタービン調
遠弁8を操作することにより高炉3の炉頂圧を制御し、
またガス洗浄装置5の流量調整操作部をガス流量制御装
置21で操作することにより繁塵効果を達成できるよう
なガス洗浄装置前後差圧が維持される。セプタム弁制御
装置22は、ガス流量制御装置21と協調してコントロ
ール弁12を操作することにより、高炉系へ外乱を与え
ることなくタービン9を起動させる。
Therefore, when starting up the blast furnace operation and during the wind shutdown operation, the septum valves 12, 13, and 14 are fully opened to allow all of the blast furnace generated gas to bypass the turbine 9. At this time, the blast furnace top pressure is controlled to be constant by operating the flow rate adjustment operation section of the gas cleaning device 5 with the gas flow rate control device 21. Also, while the turbine 9 is operating, the septum valves 12, 1
3 and 14 are completely closed, and all the gas generated from the blast furnace 3 is transferred to the evening bin 9.
flow to. In this case, the furnace top pressure of the blast furnace 3 is controlled by operating the turbine control valve 8 with the turbine governor 23,
Further, by operating the flow rate adjustment operation section of the gas cleaning device 5 with the gas flow rate control device 21, a pressure difference between the front and rear of the gas cleaning device is maintained such that the dust-generating effect can be achieved. The septum valve control device 22 operates the control valve 12 in cooperation with the gas flow rate control device 21 to start the turbine 9 without causing any disturbance to the blast furnace system.

またタービン連続運転中でも、セプタム弁制御装置22
はガス流量制御装置21をバックアップし、高炉3の吹
抜け、発電機9の負荷遮断、タービントリツプ等の異常
事態に炉頂圧力の過度な上昇を防止し、安定した高炉作
業を確保する。次に、本実施例システムの運転について
より詳細に説明する。
Also, even during continuous turbine operation, the septum valve control device 22
backs up the gas flow rate control device 21, prevents excessive rise in furnace top pressure in abnormal situations such as blow-through of the blast furnace 3, load interruption of the generator 9, and turbine trip, and ensures stable blast furnace operation. Next, the operation of the system of this embodiment will be explained in more detail.

(1) 通常運転 01タービン駆動:セプタム弁制御装置22からのター
ビン入口圧力調節計出力およびオン・オフ信号によりそ
れぞれ操作されるコントロール弁12としンジ弁13、
さらにマニュアル弁は、タービン休止時にはすべて全開
されており、全ての高炉発ガスをタービン9からバイパ
スさせ、ガス洗浄装置5の出口圧力を可及的に下げてい
る。
(1) Normal operation 01 turbine drive: control valve 12 and hinge valve 13, each operated by the turbine inlet pressure regulator output and on/off signal from the septum valve control device 22;
Furthermore, all the manual valves are fully opened when the turbine is inactive, allowing all blast furnace gas to bypass the turbine 9 and lowering the outlet pressure of the gas cleaning device 5 as much as possible.

そしてこの時の炉頂圧力はガス流量制御装置21によっ
て制御される。つまりガス流量制御装置21は、炉頂圧
制御モードで動作している。この状態でタービン起動指
令が出ると、夕−ビン入口弁6とタービン出口弁11を
開き夕−ビン起動準備としてのタービンガス通し操作を
行ない、ついで主塞止弁7を開く。
The furnace top pressure at this time is controlled by the gas flow rate control device 21. In other words, the gas flow rate control device 21 is operating in the furnace top pressure control mode. When a turbine start command is issued in this state, the turbine inlet valve 6 and the turbine outlet valve 11 are opened to allow turbine gas to flow in preparation for starting the turbine, and then the main blocking valve 7 is opened.

次にマニュアル弁14を閉じタービン入口圧力設定器2
7を操作し、タービン入口圧力(ないしガス洗浄装置出
口圧力)をタービン9の無負荷定格回転数を維持する必
要な値(タービン起動圧力)まで上げる。ついで負荷制
限設定器28を操作してタービン9を徐々に加速し、回
転数設定器29を操作して発電機10が外電周波数と同
期した時点で同期投入操作を行ない、当該システムを外
電に並入する。総括制御装置24は、発電機10が外電
に並入した時点で、それまで抑止していたガス流量制御
装置21の差圧制御機能とタービンガバナ23の炉頂圧
制御機能に対する抑止を解く‘2} 負荷取り:タービ
ン入口圧力設定器27を圧力上昇側に操作して、そのタ
ービン入口圧力設定値を、炉項圧力設定器25で設定す
る炉頂圧設定値からガス流量制御装置21のガス洗浄装
鷹5に対する前後差圧設定器26で設定する設定値を減
じた値より若干高い値に設定する。
Next, close the manual valve 14 and close the turbine inlet pressure setting device 2.
7 to raise the turbine inlet pressure (or gas cleaning device outlet pressure) to a value (turbine starting pressure) required to maintain the no-load rated rotational speed of the turbine 9. Next, the load limit setting device 28 is operated to gradually accelerate the turbine 9, and the rotation speed setting device 29 is operated to perform a synchronization operation when the generator 10 is synchronized with the outside power frequency, thereby bringing the system into line with the outside power. Enter. When the generator 10 is connected to outside power, the general control device 24 releases the suppression of the differential pressure control function of the gas flow rate control device 21 and the furnace top pressure control function of the turbine governor 23, which had been suppressed until then. } Load removal: Operate the turbine inlet pressure setting device 27 to the pressure increasing side, and change the turbine inlet pressure setting value from the furnace top pressure setting value set by the furnace pressure setting device 25 to the gas cleaning of the gas flow rate control device 21. It is set to a value slightly higher than the value obtained by subtracting the set value set by the front and rear differential pressure setter 26 for the mounting hawk 5.

この操作によって、コントロール弁12を閉じてゆくと
、(レンジ弁13は閉じている)、それにつれてタービ
ン入口圧力が上昇し、ガス洗浄装置5の前後差圧が減少
するので、ガス流量制御装置21は自動的に炉頂圧力制
御モードから葦圧制御モードに移行する。かくしてガス
流量制御装置21によってガス洗浄装置5の流量調整操
作部が操作され、良好な除塵効果を得るために必要とさ
れるガス洗浄装置5の最小前後差圧が確保される。これ
と同時にタービンガバナ23の炉頂圧力制御機能が自動
的に作動してタービン調遠弁8を操作し、炉頂圧が一定
値に制御される。この状態では、ガスはその全量がター
ビン9に流れる。‘3’タービン停止:タービン停止指
令とともに、タービン入口圧力設定器Gを圧力下降側に
操作していくと、コントロール弁12が徐々に開かれ、
それにつれてタービン入口圧力が低下する。
As the control valve 12 is closed by this operation (the range valve 13 is closed), the turbine inlet pressure increases accordingly, and the differential pressure across the gas cleaning device 5 decreases. automatically shifts from furnace top pressure control mode to reed pressure control mode. In this way, the gas flow rate control device 21 operates the flow rate adjusting operation section of the gas cleaning device 5, and the minimum differential pressure across the gas cleaning device 5 required to obtain a good dust removal effect is ensured. At the same time, the furnace top pressure control function of the turbine governor 23 is automatically activated to operate the turbine control valve 8, and the furnace top pressure is controlled to a constant value. In this state, the entire amount of gas flows to the turbine 9. '3' Turbine stop: When the turbine inlet pressure setting device G is operated to the pressure lowering side along with the turbine stop command, the control valve 12 is gradually opened.
The turbine inlet pressure decreases accordingly.

この圧力低下によって、ガス流量制御装置21が自動的
に炉頂圧力制御モードへ移行し、ガス洗浄装置5に炉頂
圧制御を行なわせる。同様にタービンガバナ23のモー
ドが炉項圧制徴から回転数制御へ移行し、発電機10が
外電から解列される。コントロール弁12がさらに開き
全開した後、主塞止弁7を閉じてタービン9を停止させ
る。総括制御装置24は、発電機10の鱗列と同時にガ
ス流量制御装置21の差圧制御機能とタービンガバナ2
3の炉頂圧力制御機能を抑止する。(0) 非常運転 ‘1)タービントリツプおよび負荷遮断:この場合は、
発電機10を外電から解列しタービン調途弁8を直ちに
閉じる。
Due to this pressure drop, the gas flow rate control device 21 automatically shifts to the furnace top pressure control mode, and causes the gas cleaning device 5 to perform furnace top pressure control. Similarly, the mode of the turbine governor 23 shifts from furnace pressure control to rotation speed control, and the generator 10 is disconnected from the external power. After the control valve 12 is further opened and fully opened, the main blocking valve 7 is closed to stop the turbine 9. The general control device 24 controls the differential pressure control function of the gas flow rate control device 21 and the turbine governor 2 at the same time as the scale row of the generator 10.
3. Suppresses the furnace top pressure control function. (0) Emergency operation'1) Turbine trip and load shedding: In this case,
The generator 10 is disconnected from the external power and the turbine adjustment valve 8 is immediately closed.

総括制御装置24は、タービントリップまたは負荷遮断
信号を受けると、ガス流量制御装置21のモードを炉頂
圧力制御モード‘こ切換え、かつセプタム弁制御装置2
2に対するタービン入口圧力設定値をタービン起動圧力
まで下げるとともにレンジ弁13を開きフィードフオワ
ード補償回路を動作させるようにセプタム弁制御装置に
指令する。なお、セプタム弁制御装置22によってター
ビン入口圧力をタービン起動圧力に維持させるのは、異
常時態発生と同時にコントロール弁12としンジ弁13
を共に全開するとガス洗浄装置5の出口圧力が急激に低
下し、ガス流量制御装置21が炉頂圧力制御機能を過渡
的に失うばかりか、ガス洗浄装置5の出側とタービン9
との間のガス流路に蓄積しているガスが瞬間的にガスホ
ルダ15へ向って放出し、ガスホルダ15の入口側に至
るガス流路の圧力が過度に上昇する危険があるためであ
る。■ 高炉吹抜け:タービン運転中に高炉3が吹抜け
を起しその結果大量の高炉ガスが瞬時にタービン9側に
流れ込む場合には、セプタム弁制御装置22がタービン
入口圧力の急上昇を検出して、セプタム弁12,13を
内部安全弁として操作し、高炉3に装備されたブリータ
の吹く回数を減らす。
When the general control device 24 receives a turbine trip or load cutoff signal, it switches the mode of the gas flow rate control device 21 to the furnace top pressure control mode, and also switches the mode of the gas flow rate control device 21 to the furnace top pressure control mode.
The septum valve control device is commanded to lower the turbine inlet pressure set value for No. 2 to the turbine starting pressure, open the range valve 13, and operate the feed forward compensation circuit. Note that the septum valve control device 22 maintains the turbine inlet pressure at the turbine starting pressure by controlling the control valve 12 and the engine valve 13 at the same time as an abnormal condition occurs.
When both are fully opened, the outlet pressure of the gas scrubbing device 5 drops rapidly, and the gas flow rate control device 21 not only temporarily loses its top pressure control function, but also the outlet side of the gas scrubbing device 5 and the turbine 9
This is because there is a danger that the gas accumulated in the gas flow path between the gas flow path and the gas flow path will be instantaneously released toward the gas holder 15, and the pressure in the gas flow path leading to the inlet side of the gas holder 15 will rise excessively. ■ Blast furnace blow-through: When the blast furnace 3 causes blow-through during turbine operation and as a result, a large amount of blast furnace gas instantly flows into the turbine 9 side, the septum valve control device 22 detects a sudden rise in the turbine inlet pressure and The valves 12 and 13 are operated as internal safety valves to reduce the number of times the bleater installed in the blast furnace 3 blows.

以上に述べたことから明らかなように、本発明によれば
、ガス洗浄装置の前後差圧が適正に制御され良好な洗浄
効果を確保できるため、従来付設されていた電気集塵機
等が不要になり、またガス洗浄装置から排出される反応
ガスをセプタム弁でバイパスすることなくその全量でタ
ービン発電機を駆動し反応ガスの保有するェネルギを有
効に利用しながら、タービン調速弁にて炉頂圧力を制御
するので安定した炉頂圧力の制御を行なうことができ、
またヱネルギの回収効率も改善される等の多大の効果を
奏することができる。
As is clear from the above, according to the present invention, the differential pressure between the front and rear of the gas cleaning device can be appropriately controlled and a good cleaning effect can be ensured, making it possible to eliminate the need for an electric precipitator, etc., which was conventionally attached. In addition, the reactant gas discharged from the gas cleaning device is not bypassed by the septum valve and the entire amount drives the turbine generator, effectively utilizing the energy possessed by the reactant gas while controlling the furnace top pressure with the turbine governor valve. The furnace top pressure can be controlled stably.
Furthermore, it is possible to achieve great effects such as improved energy recovery efficiency.

前述したように、本発明は製鉄プラントの高炉システム
に適用して著しい効果を挙げることができるが、さらに
一般のダストを多量に含有する高圧ガスを排出する化学
反応槽等を含む各種システムに汎く適用して効果を発揮
できることは言うまでもない。
As mentioned above, the present invention can be applied to the blast furnace system of a steelmaking plant and achieve remarkable effects, but it can also be applied to various systems including chemical reaction tanks that discharge high-pressure gas containing a large amount of general dust. Needless to say, it can be applied effectively and effectively.

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

図は本発明による反応炉ガスェネルギ回収発電システム
の一実施例である。 3・・・・・・高炉、5・・・・・・流量調整操作部を
持つガス洗浄装置、8・・・・・・タービン調遠弁、9
・・・・・・タービン、10…・・・発電機、12,1
3,14・・・・・・セプタム弁、16・・・・・・炉
頂圧力検出器、17・・・・・・タービン入口圧力検出
器、18・・・・・・ガス洗浄装置前後差圧検出器、2
1…・・・ガス流量制御装置、22・・・…セプタム弁
制御装置、23……夕−ビンガバナ、24・・・・・・
総括制御装置。
The figure shows an embodiment of the reactor gas energy recovery power generation system according to the present invention. 3... Blast furnace, 5... Gas cleaning device with flow rate adjustment operation section, 8... Turbine tuning valve, 9
... Turbine, 10... Generator, 12,1
3, 14... Septum valve, 16... Furnace top pressure detector, 17... Turbine inlet pressure detector, 18... Gas cleaning device front and back difference Pressure detector, 2
1...Gas flow control device, 22...Septum valve control device, 23...Evening bin governor, 24...
General control device.

Claims (1)

【特許請求の範囲】[Claims] 1 反応炉から排出されるガスを洗浄する洗浄部とその
ガス流量を調節する流量調整操作部とを有するガス洗浄
装置を具備し、該ガス洗浄装置からのガスを、一方はセ
プタム弁を介し、他方は入力にタービン調速弁を設置し
たタービン発電機を介して排出させる反応炉ガスエネル
ギ回収発電プラントにおいて、前記ガス洗浄装置のガス
流量を制御するガス流量制御装置と、前記セプタム弁を
制御するセプタム弁制御装置と、前記タービン調速弁を
操作するタービンガバナと、前記ガス流量制御装置、セ
プタム弁制御装置、タービンガバナに対し運転状態の変
更や異常信号による制御モードの切換を総括して指令す
る総括制御装置とを設け、通常の発電動作中には、前記
ガス流量制御装置によりガス洗浄装置の流量調整操作部
を操作して、ガス洗浄装置の前後差圧を制御し、かつ、
前記タービンガバナによりタービン調速弁を操作して、
反応炉の炉頂圧を制御して運転すると共に、前記セプタ
ム制御装置は、反応炉やタービン発電機の異常に対して
セプタム弁を操作すべく待期状態とし、タービン発電機
が発電動作中でない場合には、前記ガス流量制御装置は
、ガス洗浄装置の流量調整操作部を操作して反応炉の炉
頂圧を制御して運転することを特徴とする反応炉ガスエ
ネルギ回収発電システム。
1 Equipped with a gas cleaning device having a cleaning section that cleans gas discharged from the reactor and a flow rate adjustment operation section that adjusts the gas flow rate, one side of which passes the gas from the gas cleaning device through a septum valve, The other is a gas flow rate control device that controls the gas flow rate of the gas cleaning device and a gas flow rate control device that controls the septum valve in a reactor gas energy recovery power generation plant in which the gas is discharged through a turbine generator equipped with a turbine regulating valve at its input. Collectively commands the septum valve control device, the turbine governor that operates the turbine regulating valve, the gas flow rate control device, the septum valve control device, and the turbine governor to change the operating state or switch the control mode based on an abnormal signal. A general control device is provided, and during normal power generation operation, the gas flow rate control device operates the flow rate adjustment operation section of the gas cleaning device to control the differential pressure across the gas cleaning device, and
operating a turbine regulating valve by the turbine governor;
In addition to operating the reactor by controlling the top pressure of the reactor, the septum control device is placed in a standby state in order to operate the septum valve in response to an abnormality in the reactor or turbine generator, and when the turbine generator is not in power generation operation. In this case, the reactor gas energy recovery power generation system is characterized in that the gas flow rate control device is operated by controlling the top pressure of the reactor by operating a flow rate adjustment operation section of the gas cleaning device.
JP459678A 1978-01-19 1978-01-19 Reactor gas energy recovery power generation system Expired JPS6025608B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP459678A JPS6025608B2 (en) 1978-01-19 1978-01-19 Reactor gas energy recovery power generation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP459678A JPS6025608B2 (en) 1978-01-19 1978-01-19 Reactor gas energy recovery power generation system

Publications (2)

Publication Number Publication Date
JPS5498412A JPS5498412A (en) 1979-08-03
JPS6025608B2 true JPS6025608B2 (en) 1985-06-19

Family

ID=11588413

Family Applications (1)

Application Number Title Priority Date Filing Date
JP459678A Expired JPS6025608B2 (en) 1978-01-19 1978-01-19 Reactor gas energy recovery power generation system

Country Status (1)

Country Link
JP (1) JPS6025608B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6025609B2 (en) * 1978-02-03 1985-06-19 三井造船株式会社 Control method for blast furnace exhaust gas energy recovery plant
JPS5632078A (en) * 1979-08-22 1981-04-01 Mitsubishi Petrochem Co Ltd Energy recovering method
JP4710336B2 (en) * 2005-02-02 2011-06-29 Jfeスチール株式会社 Blast furnace top pressure control method

Also Published As

Publication number Publication date
JPS5498412A (en) 1979-08-03

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