JPS60181211A - Method for changing over control of furnace top pressure - Google Patents
Method for changing over control of furnace top pressureInfo
- Publication number
- JPS60181211A JPS60181211A JP59034832A JP3483284A JPS60181211A JP S60181211 A JPS60181211 A JP S60181211A JP 59034832 A JP59034832 A JP 59034832A JP 3483284 A JP3483284 A JP 3483284A JP S60181211 A JPS60181211 A JP S60181211A
- Authority
- JP
- Japan
- Prior art keywords
- top pressure
- furnace top
- cleaning device
- turbine
- control
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B21—MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
- B21B—ROLLING OF METAL
- B21B38/00—Methods or devices for measuring, detecting or monitoring specially adapted for metal-rolling mills, e.g. position detection, inspection of the product
- B21B38/10—Methods or devices for measuring, detecting or monitoring specially adapted for metal-rolling mills, e.g. position detection, inspection of the product for measuring roll-gap, e.g. pass indicators
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B7/00—Blast furnaces
- C21B7/007—Controlling or regulating of the top pressure
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Blast Furnaces (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、反応炉の炉頂圧制御の切換方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for switching the top pressure control of a reactor.
化学反応炉の炉頂圧制御の切換方法に関する従来技術と
しては、同一出願人による特公昭!≦−?θ♂コ号のも
のがあるが、その内容は、炉頂圧制御機能をセプタム弁
とガスタービンとの両者に付与し、両者の炉頂圧設定値
の間に僅少の差をもたせることによつ天、一方から他方
への制御機能の切換えを自動的に行わんとするものであ
り1制御機能を付与する対象としてセプタム弁とそれと
並列に設置されたガスタービンとを選んだものである。As a prior art related to a switching method for controlling the top pressure of a chemical reactor, there is a patent application published by the same applicant. ≦−? There is a θ♂ model, and its content is that the furnace top pressure control function is provided to both the septum valve and the gas turbine, and a slight difference is created between the furnace top pressure settings of both. The purpose is to automatically switch the control function from one side to the other, and the septum valve and the gas turbine installed in parallel with it were selected as the objects to which one control function is provided.
本発明のものは、該機能を付与する対象として反応ガス
洗浄装置とその下流に設置されたガスタービンとガスタ
ービンのバイパス弁とヲ選んだものであり、上記先願の
ものと比較してその目的ならびに作用効果の点で一部類
似するところはあっても、構成の点では全く異なるもの
である。すなわち本発明は、反応ガス洗浄装置による炉
頂圧制御機能とタービンバイパス弁による炉頂圧制御機
能との間における切換操作がきわめて円滑かつ自動的に
行われ、しかも反応ガス洗浄装置の洗浄機能が安定して
維持される状態のもとに、膨張タービンを用いて反応ガ
スの保有エネルギの回収を可能とする切換方法を提供す
ることを目的とするもので、そのための手段として、反
応ガス洗浄装置の具備する制御機能とバイパス弁の具備
する制御機能とのそれぞれに対し、炉頂圧設定器によっ
て指示される炉頂圧設定値の間に僅少の差をもたせるこ
とによって、上記両制御機能を作動の状態においたま\
で炉頂圧の制御に関与する機能の所掌を一方から他方に
切シ換え、あるいは一方の反応ガス洗浄装置から他方の
バイパス弁に切り換えるとともに、反応ガス洗浄装置は
あらかじめ設定された反応ガス洗浄装置の機能を維持す
るに必要な該洗浄装置の前後差圧を超えないように作動
する定差圧制御およびまたは上限開度による制限に自動
的に切り換え、あるいはさらに−万のバイパス弁から他
方の反応ガス洗浄装置に上記機能の所掌を切り換えるこ
とによって反応ガス洗浄装置は定差圧制御およびまたは
上限開度による制限から炉頂圧制御に切り換えることを
特徴とする構成音そなえるものである。The device of the present invention has selected a reaction gas cleaning device, a gas turbine installed downstream thereof, and a bypass valve of the gas turbine as objects to be provided with this function, and is different from that of the earlier application. Although there are some similarities in purpose and effect, they are completely different in structure. That is, in the present invention, the switching operation between the furnace top pressure control function by the reaction gas cleaning device and the furnace top pressure control function by the turbine bypass valve is performed extremely smoothly and automatically, and moreover, the cleaning function of the reaction gas cleaning device is The purpose is to provide a switching method that enables recovery of the energy possessed by a reaction gas using an expansion turbine under a stable condition, and as a means for that purpose, a reaction gas cleaning device is used. By creating a slight difference between the furnace top pressure setting values instructed by the furnace top pressure setting device for the control function provided by the bypass valve and the control function provided by the bypass valve, both of the above control functions are activated. I was in a state of
At the same time, the responsibility for the function related to the control of the furnace top pressure is switched from one side to the other, or from one reaction gas cleaning device to the other bypass valve. Automatically switch to constant differential pressure control that operates so as not to exceed the differential pressure across the cleaning device that is necessary to maintain the function of the cleaning device, or limit the opening by the upper limit, or furthermore, the other reaction from the 10,000 bypass valve. By switching responsibility for the above-mentioned functions to the gas scrubbing device, the reaction gas scrubbing device is equipped with a configuration sound characterized by switching from constant differential pressure control and/or restriction by upper limit opening to furnace top pressure control.
図は本発明の一実施例を示し、/は送風機、λは熱風炉
、3は高炉、グはダストキャツチャ、夕はガス洗浄装置
、乙はタービン人口弁、7は主塞止弁、?は調速弁、り
はガスタービン、/θはガスタービンタに直結された発
電機、//はタービン出目弁である。/2はバイパス弁
で、ノ(イパス弁炉頂圧制御装置Bによって開閉を制御
される。/3は炉頂圧検出器、/りはガス洗浄装置の差
圧制御装置Fに検出差圧を入力する差圧検出器、/!は
タービンガバナJに検出回転数を入力するタービン回転
数検出装置である。Aは炉頂圧設定器で、バイパス弁炉
頂圧制御装置B。The figure shows an embodiment of the present invention, where / is a blower, λ is a hot blast furnace, 3 is a blast furnace, G is a dust catcher, Y is a gas cleaning device, O is a turbine population valve, 7 is a main blocking valve, ? is a speed governor valve, ri is a gas turbine, /θ is a generator directly connected to the gas turbine, and // is a turbine exit valve. /2 is a bypass valve, the opening and closing of which is controlled by the furnace top pressure control device B. A differential pressure detector for input, /! is a turbine rotation speed detection device that inputs the detected rotation speed to the turbine governor J. A is a furnace top pressure setting device, and a bypass valve furnace top pressure control device B.
ガス洗浄装置炉頂圧制御装置C1およびタービンガバナ
Jのそれぞれに対し炉頂圧設定値を指示するためのもの
である。炉頂圧検出器/3によって検出された炉頂圧は
、バイパス弁炉頂圧制御装置B1ガス洗浄装置炉頂圧制
御装置C1ならびにタービンガバナJのそれぞれに送信
され、設定値と比較のうえ所掌の制御機能対象に向って
指令を発する。Eは炉頂圧制御切換スイツチで、制御機
能を付与する対象をバイパス弁/2とガス洗浄装置夕と
の間で切換を行ない、圧偏差設定器りの設定値を非選択
側の対象に向って送信するだめのものである。This is for instructing the furnace top pressure set value to each of the gas cleaning device furnace top pressure control device C1 and the turbine governor J. The furnace top pressure detected by the furnace top pressure detector/3 is transmitted to each of the bypass valve furnace top pressure control device B1, the gas cleaning device furnace top pressure control device C1, and the turbine governor J, and is compared with the set value before being determined. issues commands to the control function target. E is the furnace top pressure control changeover switch, which switches the target to which the control function is applied between the bypass valve/2 and the gas cleaning device, and changes the set value of the pressure deviation setting device toward the target on the non-selected side. It should not be sent.
Gは低位選択器で、ガス洗浄装置の炉頂圧制御装置Cお
よび差圧制御装置Fのそれぞれの制御値のうち低位選択
を行なったうえでガス洗浄装置オのガス#、量を制御す
る。Hは差圧制御装置Fに対する差圧設定器、Kはター
ビンガバナJに対する弁開度制限器であシ、Lはタービ
ンガバナJに対する負荷設定器である。G is a low selector which selects a low value among the respective control values of the furnace top pressure control device C and the differential pressure control device F of the gas scrubbing device, and then controls the gas # and amount of the gas scrubbing device O. H is a differential pressure setting device for the differential pressure control device F, K is a valve opening limiter for the turbine governor J, and L is a load setting device for the turbine governor J.
つぎに、以上の構成よシなる本発明方法の作用について
説明する。最初、ガス洗浄装置夕によって炉頂圧制御が
行われているものとする。Next, the operation of the method of the present invention having the above configuration will be explained. Initially, it is assumed that the furnace top pressure is controlled by the gas scrubber.
このときは、差圧検出器/グの検出値が差圧設定器Hの
設定値よシも大であるため、低位選択器Gによシ、ガス
洗浄装置の炉頂圧制御装置Cの出力が選択されてガス洗
浄装置夕を開閉し、炉頂圧を制御する。At this time, the detected value of the differential pressure detector/G is larger than the set value of the differential pressure setting device H, so the low selector G is used to control the output of the furnace top pressure control device C of the gas cleaning device. is selected to open and close the gas scrubber and control the furnace top pressure.
一方、バイパス弁炉頂圧制御装置Bの設定値は、炉頂圧
設定器Aの設定値より圧偏差設定器りの値を減じたもの
であるので、炉頂圧よりも小となり、バイパス弁/2は
全開の状態となっている。また、ガスタービン9は1亭
止しており、タービン人口弁乙およびタービン出目弁/
/は全開、主塞止弁7および調速弁どは全閉となつ、て
いる。On the other hand, the setting value of the bypass valve furnace top pressure control device B is the value obtained by subtracting the value of the pressure deviation setting device from the setting value of the furnace top pressure setting device A, so it is smaller than the furnace top pressure, and the bypass valve /2 is in a fully open state. In addition, the gas turbine 9 is stopped, and the turbine population valve O and the turbine outlet valve
/ is fully open, and the main blocking valve 7 and speed regulating valve are fully closed.
この状態で炉頂圧をバイパス弁/2側に切り換えるため
に炉頂圧制御切換スイッチEをガス洗浄装置炉頂圧制御
装置CnIに切り換えると、その設定値は炉頂圧設定器
Aの設定値より圧偏差設定器りの設定値を減じたものと
なり、炉頂圧よりも低くなるので、ガス洗浄装置の開閉
弁14は開いてゆき、その差圧が減少し、炉頂圧もガス
洗浄装置炉頂圧制御装置Cの設定値まで下ろうとする。In this state, when the furnace top pressure control switch E is switched to the gas cleaning device furnace top pressure control device CnI in order to switch the furnace top pressure to the bypass valve/2 side, the set value is changed to the setting value of the furnace top pressure setting device A. The setting value of the pressure deviation setting device is reduced, and it becomes lower than the furnace top pressure, so the on-off valve 14 of the gas cleaning device opens, the differential pressure decreases, and the furnace top pressure also decreases. The furnace top pressure will try to drop to the set value of the control device C.
バイパス弁炉頂圧制御装置Bは、その設定値が炉頂圧設
定器Aの設定値と等しくなって、炉頂圧が設定値よフも
低くなると、バイパス弁を閉動作させヤガス洗浄装置出
口圧(以後タービン入口圧と称する)を上昇させて炉頂
圧を維持する。バイパス弁/2が炉頂圧を制御するので
、ガス洗浄装置炉頂圧制御装置Cは圧偏差設定器りの設
定値を減じた値に炉頂圧を下降させようとして開いてゆ
き、その差圧をますます下げ、バイパス弁はこれを補正
しようとして閉じてゆき、タービン入口圧を上昇させる
。遂には差圧設定器Hの設定値よりもガス洗浄装置の差
圧が小さくなると、低位選択器Gはガス洗浄装置の差圧
制御装置Fの出力を選択してその差圧を維持するようガ
ス洗浄装置の開閉弁/≦を制御し、ガス洗浄装置!は定
差圧制御に切り換わる。このようにしてガス洗浄装置夕
は定差圧制御、バイパス弁/2は炉頂圧制御に切9換わ
る。Bypass valve furnace top pressure control device B closes the bypass valve when its set value becomes equal to the set value of furnace top pressure setting device A, and the furnace top pressure becomes lower than the set value. The pressure (hereinafter referred to as turbine inlet pressure) is increased to maintain the furnace top pressure. Since the bypass valve/2 controls the furnace top pressure, the gas scrubber furnace top pressure control device C opens in an attempt to lower the furnace top pressure to a value that is less than the set value of the pressure deviation setting device, and the difference between the furnace top pressure and The pressure drops further and further, and the bypass valve closes in an attempt to compensate, causing the turbine inlet pressure to rise. When the differential pressure of the gas cleaning device finally becomes smaller than the set value of the differential pressure setting device H, the low selector G selects the output of the differential pressure control device F of the gas cleaning device to adjust the gas pressure to maintain the differential pressure. Gas cleaning equipment that controls the opening/closing valve/≦ of the cleaning equipment! switches to constant differential pressure control. In this way, the gas cleaning device is switched to constant differential pressure control, and the bypass valve/2 is switched to furnace top pressure control.
つぎに、前記先願(特公昭j乙−♂θざコ号)の方法V
Cより、タービンを起動しタービンの炉頂圧制御に切p
換える。Next, method V of the earlier application (Tokuko Shoj Otsu-♂θzako No.)
From C, start the turbine and switch to turbine top pressure control.
exchange.
主塞止弁7を全開にし、弁開度制限器Kを増操作シて、
タービンガバナJによシ調速弁♂を開けてゆくと、ガス
タービンタは回転し始める。タービン回転数検出装置/
!の出力をタービンガバナJに与えて調速弁rによp回
転数制御を行い、発電機/θの周波数が系統の周波数と
一致したとき、発電機遮断器を閉にし、以後は負荷設定
器りによシ発電機出力を増加させてゆく。Fully open the main stop valve 7, increase the valve opening limiter K,
When the speed regulating valve ♂ of the turbine governor J is opened, the gas turbine motor begins to rotate. Turbine rotation speed detection device/
! The output of θ is given to the turbine governor J to control the rotation speed of p using the regulating valve r, and when the frequency of the generator/θ matches the frequency of the grid, the generator circuit breaker is closed, and from then on, the load setter As a result, the generator output is increased.
この間、調速弁?は開いてゆき、バイパス弁/2は炉頂
圧を制御しながら閉じてゆく。さらに負荷設定器りによ
シ発電機出力を増加させてゆくと、遂にはバイパス弁/
2は全閉となり、炉頂圧制御の機能を失う、タービンガ
バナJは、炉頂圧設定値人の設定値よシも僅かに低い値
をタービン用の炉頂圧設定値(以後前圧設定値と称す)
として有しておシ、前圧設定値よりも炉頂圧が下ろうと
すると調速弁?が閉じ、炉頂圧を維持する。タービン連
続運転は、ガス洗浄装置夕は定差圧制御、バイパス弁は
全閉、調速弁は炉頂圧制御で行われる。The other day, the regulating valve? is gradually opened, and bypass valve/2 is closed while controlling the furnace top pressure. When the generator output is further increased using the load setting device, the bypass valve/
2 is fully closed and the furnace top pressure control function is lost.The turbine governor J sets the furnace top pressure set value for the turbine to a value that is slightly lower than the human set value (hereinafter referred to as the front pressure setting). (referred to as value)
If the top pressure of the furnace is about to drop below the pre-pressure setting value, the regulating valve will be activated. is closed to maintain furnace top pressure. Continuous operation of the turbine is performed using constant differential pressure control for the gas scrubber, fully closed bypass valve, and furnace top pressure control for the governor valve.
なお、この場合、ガス洗浄装置に与えられる定差圧の代
シに、該装置の内蔵する開閉弁の上限開度によって該装
置の作動を制限するやシ方が行われることがある0図に
おいて、Mは、ガス洗浄装置!の内蔵する開閉弁/乙に
対して開度の上限値を指示するための上限開度設定器で
ある。上限開度設定器による開度制限は、上記定差比に
よる制限に代えて使用してもよく、また両制限を同時に
並用してもよい。図は両制限を並用した場合の例を示す
。In this case, in place of the constant pressure differential applied to the gas cleaning device, the operation of the device may be limited by the upper limit opening of the on-off valve built into the device. , M is for gas cleaning equipment! This is an upper limit opening setting device for instructing the upper limit value of the opening for the built-in on-off valve/B. The opening limit by the upper limit opening setting device may be used in place of the limit by the constant difference ratio, or both limits may be used at the same time. The figure shows an example where both restrictions are used together.
タービン停止時には、まず負荷設定器りを減少させて調
速弁?を閉動作させる。タービン入口圧が上昇し、ガス
洗浄装置!は定差圧制御を行っているので炉頂圧が上昇
し、炉頂圧設定器Aの設定値に達すると、バイパス弁/
2が全閉位置から開き始めて炉頂圧を制御する。負荷設
定器りを減少させて下限に到達すると、発電Jt!A1
0の遮断器を開にし、ついで弁開度制限器Kを減少させ
て−って調速弁♂を閉めていく。調速弁tが全閉となる
と、トリップ信号を発して主塞止弁2ち全開にする。こ
の間バイパス弁12は炉頂圧を制御しながら開いてゆく
。When the turbine is stopped, the load setting value is first reduced and the regulating valve is activated. operate to close. The turbine inlet pressure increases and the gas cleaning device! Since the furnace performs constant differential pressure control, when the furnace top pressure rises and reaches the set value of the furnace top pressure setting device A, the bypass valve /
2 begins to open from the fully closed position to control the furnace top pressure. When the load setting value is decreased and the lower limit is reached, power generation Jt! A1
0 is opened, then the valve opening degree limiter K is decreased to close the speed regulating valve ♂. When the regulating valve t is fully closed, a trip signal is issued to fully open the main blocking valve 2. During this time, the bypass valve 12 opens while controlling the furnace top pressure.
ついで、再び炉頂圧制御切換スイッチEをバイパス弁炉
頂圧制御装置B側に切り換えると、その設定値は炉頂圧
設定器Aの設定値より圧偏差設定器Bの設定値を減じた
ものとなり、炉頂圧よりも低いので、バイパス弁/2は
開いてゆき、タービン入口圧は下降してゆく。このとき
には、ガス洗浄装置!は定差圧制御を行っているが、タ
ービン入口圧の下降に伴って炉頂圧が下ると、ガス洗浄
装置の炉頂圧−御装置Cは炉頂圧設定器Aを設定値とし
ているので、ただちに低位選択器Gで炉頂圧−伸側を選
択してガス洗浄装置!の開閉弁/乙を閉動作させて炉頂
圧を維持する。バイパス弁/2は炉頂圧を圧偏差設定器
Bの設定値分子げようとしてさらに開いてゆくが、ガス
洗浄装置jが炉頂圧を制御しているので、遂には全開に
至る。Then, when the furnace top pressure control changeover switch E is switched again to the bypass valve furnace top pressure control device B side, the set value is the set value of the furnace top pressure setting device A minus the setting value of the pressure deviation setting device B. Since this is lower than the furnace top pressure, the bypass valve/2 opens and the turbine inlet pressure decreases. At this time, gas cleaning equipment! is performing constant differential pressure control, but when the furnace top pressure decreases due to a decrease in the turbine inlet pressure, the furnace top pressure control device C of the gas cleaning device uses the furnace top pressure setting device A as the set value. , Immediately select the furnace top pressure-expansion side with the low selector G and turn on the gas cleaning device! The on-off valve/B is closed to maintain the furnace top pressure. The bypass valve /2 opens further in an attempt to lower the furnace top pressure to the set value of the pressure deviation setting device B, but since the gas cleaning device j controls the furnace top pressure, it finally opens fully.
このようにして、ガス洗浄装置!が炉頂圧制御、バイパ
ス弁が全開、タービンが停止の初期状態に戻る。In this way, gas cleaning equipment! controls the furnace top pressure, the bypass valve is fully open, and the turbine returns to its initial state of being stopped.
本発明の炉頂圧制御の切換方法と前記先願(特公昭!乙
−♂θ?2号)の方法とによp1ガス洗浄装置とタービ
ンとの炉頂圧制御機能の間における切換操作が、バイパ
ス弁の炉頂圧制御機能を介在させることによってきわめ
て円滑かつ自動的に行われ、しかもガス洗浄装置の洗浄
機能が安定して維持される状態のもとに、膨張タービン
を用いて反応ガスの保有エネルギーの回収を図ることが
できるというすぐれた効果がある。The switching method of the furnace top pressure control of the present invention and the method of the prior application (Special Publication Show! Otsu-♂θ? No. 2) enable the switching operation between the furnace top pressure control function of the p1 gas cleaning device and the turbine. This is done very smoothly and automatically by intervening the furnace top pressure control function of the bypass valve, and the reaction gas is removed using an expansion turbine under conditions where the cleaning function of the gas cleaning device is stably maintained. This has the excellent effect of being able to recover the energy retained in the system.
なお、同一システムの制御例として特公昭−t3−32
θぶ6号があるが、ガス洗浄装置は常時炉頂圧制御を行
い、タービンはタービン入口圧を制御して連続運転全行
う場合に比較して、本発明はガス洗浄装置の差圧が減少
することによってガス流量ゲインが低下しても、炉頂圧
制御の制御性の悪化をもたらさずにタービンの運転が可
能といった長所を有している。In addition, as a control example of the same system, Tokuko Sho-t3-32
There is θbu No. 6, but compared to the case where the gas cleaning device constantly controls the furnace top pressure and the turbine is operated continuously by controlling the turbine inlet pressure, the present invention reduces the differential pressure of the gas cleaning device. This has the advantage that even if the gas flow rate gain decreases, the turbine can be operated without deteriorating the controllability of the furnace top pressure control.
図面は本発明にか\る炉頂圧制御の切換方法の一実施例
を適用した高炉システムの要部の配置系統図である。
/06.送風m、λ10.熱風炉、300.高炉、り0
0.ダストキャツチャ、j−、、、ガス洗浄装置、乙0
0.タービン人口弁、? 、、、主塞止弁、?68.調
速弁、ワ00.ガスタービン、/θ000発電機、//
、、、タービン出目弁、 /2.、、バイパス弁、 /
3.0.炉頂圧検出器、/グ00.差圧検出器、/タ0
0.タービン回転数検出装置、 /4.、、開閉弁、A
16.炉頂圧設定器、 B 、、、バ・fパス弁炉頂圧
制御装置、 C、、、ガス洗浄装置炉頂圧制御装置、D
、、、圧偏差設定器、g 、、、炉頂圧制御切換スイ
ッチ、? 、、、ガス洗浄装置の差圧制御装置、 G
、、、低位選択器、H,、、差圧設定器、J。
91.タービンガバナ、K 、、、弁開度制限器、L1
9.負荷設定器、 M 、、、上限1度設定器。The drawing is a layout diagram of the main parts of a blast furnace system to which an embodiment of the switching method of furnace top pressure control according to the present invention is applied. /06. Air blow m, λ10. Hot stove, 300. Blast furnace, Ri0
0. Dust catcher, j-,, gas cleaning equipment, Otsu 0
0. Turbine valve,? ,,,main blocking valve,? 68. Speed regulating valve, Wa00. Gas turbine, /θ000 generator, //
,,,turbine outlet valve, /2. ,, bypass valve, /
3.0. Furnace top pressure detector, /g00. Differential pressure detector, /ta 0
0. Turbine rotation speed detection device, /4. ,,on-off valve,A
16. Furnace top pressure setting device, B, B/F pass valve furnace top pressure control device, C, gas cleaning device furnace top pressure control device, D
,,,Pressure deviation setting device, g ,,,Furnace top pressure control changeover switch, ? ,,, differential pressure control device for gas cleaning equipment, G
, ,Low selector, H, ,Differential pressure setter, J. 91. Turbine governor, K, , valve opening limiter, L1
9. Load setting device, M,, Upper limit 1 degree setting device.
Claims (1)
けられた反応ガス洗浄装置と、その下流のガス流路に設
けられた膨張タービンと、該タービンをバイパスするガ
ス流路に設けられたバイパス弁とをそなえてそのいずれ
もが反応炉の炉頂圧を制御する機能を具備する化学反応
炉システムにおいて、反応ガス洗浄装置の上記制御機能
とバイパス弁の制御機能とのそれぞれに対し、炉頂圧設
定器によって指示される炉頂圧設定値の間に僅少の差を
もたせることによって、上記両制御機能を作動の状態に
おいたま\で炉頂圧の制御に関与する機能の所掌を自動
的に一方から他方に切9換えることを特徴とする炉頂圧
制御の切換方法。 伐)反応炉から取9出された反応ガスのガス流路に設け
られた反応ガス洗浄装置と、その下流のガス流路に設け
られた膨張タービンと、該タービンをバイパスするガス
流路に設けられたバイパス弁とをそなえてそのいずれも
が反応炉の炉頂圧を制御する機能を具備する化学反応炉
システムにおいて、反応ガス洗浄装置の上記制御機能と
バイパス弁の制御機能とのそれぞれに対し、炉頂圧設定
器によって指示される炉頂圧設定値の間に僅少の差をも
たせることによって、上記両制御機能を作動の状態にお
いたま\で炉頂圧の制御に関する機能の所掌を反応ガス
洗浄装置からバイパス弁に切り換えるとともに、反応ガ
ス洗浄装置はあらかじめ設定されん反応ガス洗浄装置の
機能を維持するに必要な該洗浄装置の前後差圧を超えな
いように作動する定差圧制御およびまたは上限開度によ
る制限に自動的に切り換えるtとを特徴をする炉頂圧制
御の切換方法。 (3) 反応炉から取シ出された反応ガスのガス流路に
設けられた反応ガス洗浄装置と、その下流のガス流路に
設けられた膨張タービンと、該タービンをバイパスする
ガス流路に設けられたバイパス弁とをそなえてそのいず
れもが反応炉の炉頂圧を制御する機能を具備する化学反
応炉システムにおいて、反応ガス洗浄装置の上記制御機
能とバイパス弁の制御機能とのそれぞれに対し、炉頂圧
設定器によって指示される炉頂圧設定値の間に僅少の差
をもたせることによって、上記両制御機能を作動の状態
においたま\で炉頂圧の制御に関する機能の所掌をバイ
パス弁から反応ガス洗浄装置に切り換えることによって
反応ガス洗浄装置は定差圧制御およびまたは上限開度に
よる制限から炉頂圧制御に自動的に切り換えることを特
徴とする炉頂圧制御の切換方法。[Scope of Claims] (1) A reaction gas cleaning device provided in the gas flow path for the reaction gas taken out from the reactor, an expansion turbine provided in the downstream gas flow path, and a device that bypasses the turbine. In a chemical reactor system equipped with a bypass valve provided in a gas flow path, each of which has a function of controlling the furnace top pressure of the reactor, the above control function of the reaction gas cleaning device and the control function of the bypass valve By creating a slight difference between the furnace top pressure setting values indicated by the furnace top pressure setting device for each, the furnace top pressure can be controlled while both of the above control functions are in operation. 9. A switching method for furnace top pressure control, characterized in that the responsibility for the function to be controlled is automatically switched from one to the other. 9) A reaction gas cleaning device installed in the gas flow path for the reaction gas taken out from the reactor, an expansion turbine installed in the downstream gas flow path, and a gas flow path that bypasses the turbine. In a chemical reactor system equipped with a bypass valve, each of which has a function of controlling the top pressure of the reactor, the above-mentioned control function of the reaction gas cleaning device and the control function of the bypass valve are respectively controlled. By creating a slight difference between the furnace top pressure set values indicated by the furnace top pressure setting device, the functions related to controlling the furnace top pressure can be controlled by the reactant gas while both of the above control functions are in operation. At the same time as switching from the cleaning device to a bypass valve, the reactive gas cleaning device is set in advance. A switching method for furnace top pressure control characterized by automatically switching to restriction based on an upper limit opening degree. (3) A reaction gas cleaning device installed in the gas flow path for the reaction gas taken out from the reactor, an expansion turbine installed in the downstream gas flow path, and a gas flow path that bypasses the turbine. In a chemical reactor system equipped with a bypass valve, each of which has a function of controlling the top pressure of the reactor, the control function of the reaction gas cleaning device and the control function of the bypass valve are respectively controlled. On the other hand, by creating a slight difference between the furnace top pressure set values indicated by the furnace top pressure setting device, the responsibility of the function related to the furnace top pressure control can be bypassed while leaving both of the above control functions in the operating state. A method for switching furnace top pressure control, characterized in that by switching from a valve to a reaction gas cleaning device, the reaction gas cleaning device automatically switches from constant differential pressure control and/or restriction by upper limit opening to furnace top pressure control.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59034832A JPS60181211A (en) | 1984-02-25 | 1984-02-25 | Method for changing over control of furnace top pressure |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59034832A JPS60181211A (en) | 1984-02-25 | 1984-02-25 | Method for changing over control of furnace top pressure |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60181211A true JPS60181211A (en) | 1985-09-14 |
JPH0314884B2 JPH0314884B2 (en) | 1991-02-27 |
Family
ID=12425169
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59034832A Granted JPS60181211A (en) | 1984-02-25 | 1984-02-25 | Method for changing over control of furnace top pressure |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60181211A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63186903A (en) * | 1987-01-28 | 1988-08-02 | Kawasaki Heavy Ind Ltd | Control device of furnace top pressure turbine |
JPH0529783U (en) * | 1991-09-30 | 1993-04-20 | 金三郎 松田 | Flattoile |
-
1984
- 1984-02-25 JP JP59034832A patent/JPS60181211A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63186903A (en) * | 1987-01-28 | 1988-08-02 | Kawasaki Heavy Ind Ltd | Control device of furnace top pressure turbine |
JPH0529783U (en) * | 1991-09-30 | 1993-04-20 | 金三郎 松田 | Flattoile |
Also Published As
Publication number | Publication date |
---|---|
JPH0314884B2 (en) | 1991-02-27 |
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