JPH0119051B2 - - Google Patents

Info

Publication number
JPH0119051B2
JPH0119051B2 JP56145768A JP14576881A JPH0119051B2 JP H0119051 B2 JPH0119051 B2 JP H0119051B2 JP 56145768 A JP56145768 A JP 56145768A JP 14576881 A JP14576881 A JP 14576881A JP H0119051 B2 JPH0119051 B2 JP H0119051B2
Authority
JP
Japan
Prior art keywords
gas
temperature
generated gas
generated
heat storage
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
JP56145768A
Other languages
Japanese (ja)
Other versions
JPS5847124A (en
Inventor
Shoji Furuya
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.)
IHI Corp
Original Assignee
IHI Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by IHI Corp filed Critical IHI Corp
Priority to JP14576881A priority Critical patent/JPS5847124A/en
Publication of JPS5847124A publication Critical patent/JPS5847124A/en
Publication of JPH0119051B2 publication Critical patent/JPH0119051B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C7/00Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
    • F02C7/12Cooling of plants
    • F02C7/14Cooling of plants of fluids in the plant, e.g. lubricant or fuel
    • F02C7/141Cooling of plants of fluids in the plant, e.g. lubricant or fuel of working fluid

Description

【発明の詳細な説明】 本発明は、高炉の炉頂から排出される発生ガス
を乾式ガス清浄装置を通した後、ガスの保有する
温度/圧力エネルギーを膨張式ガスタービンで回
収する設備において、高炉はその炉況に応じて短
期間に発生ガス温度が異常に高温となるときがあ
るが、この際のガスタービンに入る前のガス温度
を制御して安定化させる方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides equipment for recovering the temperature/pressure energy possessed by the gas by an expansion gas turbine after passing generated gas discharged from the top of a blast furnace through a dry gas cleaning device. Depending on the furnace conditions, the temperature of the generated gas in a blast furnace can sometimes reach an abnormally high temperature for a short period of time, and this paper relates to a method for controlling and stabilizing the gas temperature before entering the gas turbine.

高炉の発生ガス温度は通常100〜200℃程度であ
るが、短期的に800℃を越えることがある。これ
に対し従来は、水を用いた湿式ガス清浄装置によ
り発生ガスの冷却と清浄化を行うようにしてお
り、ガス清浄化後のガス温度は常に約50℃の飽和
状態になつており、このためガス顕熱は回収の対
象とされていなかつた。
The temperature of the gas generated in a blast furnace is usually about 100 to 200°C, but it can exceed 800°C in a short period of time. In contrast, conventionally, the generated gas is cooled and purified using a wet gas purification device using water, and the gas temperature after gas purification is always in a saturated state of approximately 50°C. Therefore, gas sensible heat was not subject to recovery.

近年、従来の湿式ガス清浄装置に代つて乾式の
ものを採用してガスの温度低下を防止し、ガスの
保有する温度/圧力エネルギーを膨張ガスタービ
ンで電力として回収することが検討されている。
しかるに、発生ガスの異常な温度変動に対するし
かるべき対策を講じなければ機器の損傷などをま
ねき安定したエネルギー回収を行うことができな
い。
In recent years, consideration has been given to using a dry type gas purifier instead of the conventional wet type gas purifier to prevent the temperature of the gas from decreasing, and to recover the temperature/pressure energy possessed by the gas as electric power using an expansion gas turbine.
However, unless appropriate measures are taken against abnormal temperature fluctuations in the generated gas, equipment may be damaged and energy cannot be recovered stably.

このため、発生ガスの異常高温に対しては、エ
ネルギー回収を行う前の炉頂ガス温度を検出して
事後の対応策として炉頂部に水を噴射させ、水の
気化熱によりガス温度を下げて各機器の保護を行
うようにしている。しかしこのようにした場合、
水分を含んだガスが下流側において低温配管に接
触することにより冷却されてドレンを生じ、ダス
トが管内に固着するという問題があり、更に乾式
ガスの清浄装置の形式、種類によつては飽和に近
いガスを処理するのに適さないものがある。即
ち、ガス清浄中にガスが露点に達して集塵エレメ
ントを濡らし、捕集ダストの除去ができなくなり
その結果集塵機能を著しく低下させてしまう。
Therefore, in case of abnormally high temperature of generated gas, the temperature of the gas at the top of the furnace before energy recovery is detected and water is injected at the top of the furnace as a countermeasure after the fact, and the gas temperature is lowered by the heat of vaporization of the water. We are trying to protect each device. But if you do it like this,
When gas containing moisture comes into contact with low-temperature piping on the downstream side, it is cooled and creates drainage, which causes dust to stick inside the pipes.Furthermore, depending on the type and type of dry gas purifier, it may become saturated. There are some things that are not suitable for processing close gases. That is, during gas cleaning, the gas reaches the dew point and wets the dust collection element, making it impossible to remove the collected dust, resulting in a significant reduction in the dust collection function.

本発明はこのような点に鑑みなしたもので、高
炉の炉頂から排出される発生ガスからガスタービ
ンによつてエネルギーを回収するに際して、蓄熱
装置と水噴射装置により発生ガスの温度を制御す
る方法において、前記炉頂からの発生ガスを蓄熱
装置の熱容量大なる物質に接触させた後、該蓄熱
装置の熱容量特性と接触前の発生ガス温度変化よ
り予測演算を行つた結果に基づいて水噴射装置に
より発生ガスに水を噴射せしめ前記ガスタービン
に導くガスの温度を制御することを特徴とする発
生ガス温度の制御方法、に係るものである。
The present invention has been developed in view of these points, and is a method for controlling the temperature of the generated gas using a heat storage device and a water injection device when energy is recovered by a gas turbine from the generated gas discharged from the top of a blast furnace. In the method, after the generated gas from the top of the furnace is brought into contact with a material having a large heat capacity of the heat storage device, water injection is performed based on the result of predictive calculation based on the heat capacity characteristics of the heat storage device and the temperature change of the generated gas before contact. The present invention relates to a method for controlling the temperature of generated gas, characterized in that the temperature of the gas guided to the gas turbine is controlled by injecting water into the generated gas using a device.

以下本発明の実施例を図面を参照して説明す
る。
Embodiments of the present invention will be described below with reference to the drawings.

第1図に示す如く、高炉本体1で発生したガス
を、炉頂ガス2を経由して例えばグラベル(砂状
物質)ベツド式のような乾式のガス清浄蓄熱装置
3に導き、ここで発生ガス中に含まれているダス
トを除去した後、更に清浄ガス管4によりセプタ
ム弁5と並列配置されたガスタービン6を介して
ガスホルダー7に導き、図示しない利用先に配送
して燃料ガス等として利用するようにしている。
As shown in FIG. 1, the gas generated in the blast furnace main body 1 is guided via the furnace top gas 2 to a dry type gas purifying heat storage device 3 such as a gravel bed type, where the generated gas After removing the dust contained therein, the clean gas pipe 4 guides the gas through a gas turbine 6 arranged in parallel with a septum valve 5 to a gas holder 7, and delivers it to a user (not shown) as fuel gas, etc. I'm trying to use it.

更に、前記発生ガスの短期的な異常温度上昇に
対処するために、高炉頂ガス管2に炉頂温度検出
端8を設けてガスの異常温度上昇を検出し、その
信号をコントローラ9を経由して電動弁10に送
り、ガスタービン6の上流側の清浄ガス管4に設
けた散水ノズル11より冷却水を噴射させて清浄
ガスの異常な温度上昇を防止するようにしてい
る。
Furthermore, in order to cope with the short-term abnormal temperature rise of the generated gas, a furnace top temperature detection end 8 is provided in the blast furnace top gas pipe 2 to detect the abnormal temperature rise of the gas, and the signal is sent via the controller 9. Cooling water is sent to the electric valve 10, and is injected from a water spray nozzle 11 provided in the clean gas pipe 4 on the upstream side of the gas turbine 6, thereby preventing an abnormal rise in temperature of the clean gas.

通常、高炉本体1から排出される発生ガスの温
度は、100〜200℃の間の略一定の温度に維持され
ているが、高炉内部でガスの吹付けがあつたよう
な場合は短期的に800℃を越えた高温ガスが流れ
ることがある。このような場合、ガス清浄蓄熱装
置3の内部に充填されたフイルターとしての熱容
量が大なるグラベル(砂状物質)が、前記高温ガ
スにより加熱されて一旦ガスの熱エネルギーを吸
収、蓄熱する。この過程でガスは冷却される。次
いで発生ガス温度が通常レベルに復帰すると、加
熱されたグラベルの方が温度が高いので温度がバ
ランスするまでガスを加熱することになる。
Normally, the temperature of the generated gas discharged from the blast furnace body 1 is maintained at a substantially constant temperature between 100 and 200 degrees Celsius, but if gas is blown inside the blast furnace, High-temperature gas exceeding 800℃ may flow. In such a case, gravel (sand-like substance) with a large heat capacity as a filter filled in the gas purifying heat storage device 3 is heated by the high temperature gas, and once absorbs the thermal energy of the gas and stores the heat. During this process, the gas is cooled. Then, when the generated gas temperature returns to the normal level, the heated gravel has a higher temperature, so the gas is heated until the temperatures are balanced.

このため、ガス清浄蓄熱装置3の出口において
は、入口部の温度変化が第2図の実線イで示す如
くであるのに対し、破線ロで示す如く通常温度ハ
に近い温度で平準化され、しかも温度変化が少し
遅れて現われる。即ち、炉頂ガス温度の変化開始
に対し時間遅れニをおいて清浄ガス温度の変化が
現われる。清浄ガス温度の平準化の程度と変化時
間の遅れ度合は、ガス清浄蓄熱装置3内のグラベ
ルの蓄熱容量の大きさと伝熱特性によつて決まる
ので、ガス清浄蓄熱装置3の入口ガス温度の変化
状態をもとに出口ガス温度の変化を理論計算によ
り或る程度予測することができる。
Therefore, at the outlet of the gas purification heat storage device 3, the temperature change at the inlet section is as shown by the solid line A in FIG. Moreover, temperature changes appear with a slight delay. That is, a change in the clean gas temperature appears after a time delay after the start of the change in the furnace top gas temperature. The degree of equalization of the clean gas temperature and the degree of delay in the change time are determined by the heat storage capacity and heat transfer characteristics of the gravel in the gas clean heat storage device 3. Therefore, the change in the inlet gas temperature of the gas clean heat storage device 3 Based on the state, changes in the outlet gas temperature can be predicted to some extent by theoretical calculations.

従つて、炉頂温度検出端8にて炉頂ガス温度を
検出し、コントローラ9で演算、制御を行うこと
により、散水ノズル11から吹込む水量を清浄ガ
スの温度変化に応じて自動的に調節しガスタービ
ン6に入るガス温度を実質的に一定に保つことが
でき、よつてガスタービンの安全運転を確保する
ことができる。
Therefore, by detecting the furnace top gas temperature at the furnace top temperature detection end 8 and performing calculation and control using the controller 9, the amount of water blown from the water spray nozzle 11 is automatically adjusted according to the temperature change of the clean gas. Thus, the temperature of the gas entering the gas turbine 6 can be kept substantially constant, thus ensuring safe operation of the gas turbine.

尚、本発明は上記実施例にのみ限定されるもの
ではなく、ガス清浄装置と別個に蓄熱器を設ける
ようにしても同様に作用することができること、
炉頂温度検出端により炉頂部の温度を直接検出す
るようにしても良いこと、グラベルとしては種々
のものを採用し得ること、その他本発明の要旨を
逸脱しない範囲内において種々変更を加え得るこ
と、等は勿論である。
It should be noted that the present invention is not limited only to the above-mentioned embodiments, and can function in the same way even if a heat storage device is provided separately from the gas purifying device.
The temperature at the top of the furnace may be directly detected by the furnace top temperature detection end, various types of gravel may be used, and various other changes may be made without departing from the gist of the present invention. , etc., of course.

上述した本発明の発生ガス温度の制御方法によ
れば下記の如き優れた効果を奏し得る。
According to the above-described method for controlling the generated gas temperature of the present invention, the following excellent effects can be achieved.

(i) 高炉から排出される発生ガスの保有する熱エ
ネルギーを安定して回収することができる。
(i) It is possible to stably recover the thermal energy possessed by the generated gas discharged from the blast furnace.

(ii) 温度変化に時間遅れがあるので、その間の時
間を利用して対応させるので、対応遅れがな
く、冷し過ぎも防止できる。
(ii) Since there is a time lag in temperature changes, the time in between is used to respond, so there is no response delay and overcooling can be prevented.

(iii) ガス清浄蓄熱装置よりも下流側において冷却
水を噴射させるので、ガス清浄蓄熱装置の集塵
効率に影響を与える心配がなく、ドレンによる
ダストの管内固着も防止できる。
(iii) Since the cooling water is injected downstream of the gas purification heat storage device, there is no concern that it will affect the dust collection efficiency of the gas purification heat storage device, and it is possible to prevent dust from sticking inside the pipes due to drain.

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

第1図は本発明の方法を実施する装置の一例を
示す説明図、第2図は発生ガスの温度変化を示す
線図である。 1は高炉本体、2は炉頂ガス管、3はガス清浄
蓄熱装置、4は清浄ガス管、6はガスタービン、
8は炉頂温度検出端、9はコントローラ、11は
散水ノズルを示す。
FIG. 1 is an explanatory diagram showing an example of an apparatus for implementing the method of the present invention, and FIG. 2 is a diagram showing temperature changes of generated gas. 1 is a blast furnace main body, 2 is a furnace top gas pipe, 3 is a gas clean heat storage device, 4 is a clean gas pipe, 6 is a gas turbine,
8 is a furnace top temperature detection end, 9 is a controller, and 11 is a water nozzle.

Claims (1)

【特許請求の範囲】[Claims] 1 高炉の炉頂から排出される発生ガスからガス
タービンによつてエネルギーを回収するに際し
て、蓄熱装置と水噴射装置により発生ガスの温度
を制御する方法において、前記炉頂からの発生ガ
スを蓄熱装置の熱容量大なる物質に接触させた
後、該蓄熱装置の熱容量特性と接触前の発生ガス
温度変化より予測演算を行つた結果に基づいて水
噴射装置により発生ガスに水を噴射せしめ前記ガ
スタービンに導くガスの温度を制御することを特
徴とする発生ガス温度の制御方法。
1 In a method of controlling the temperature of the generated gas using a heat storage device and a water injection device when energy is recovered from the generated gas discharged from the top of a blast furnace using a gas turbine, the generated gas from the top of the blast furnace is After contacting with a substance with a large heat capacity, a water injection device injects water into the generated gas based on the result of predictive calculation based on the heat capacity characteristics of the heat storage device and the temperature change of the generated gas before contact, and the gas turbine is injected with water. A method for controlling the temperature of generated gas, characterized by controlling the temperature of the gas being introduced.
JP14576881A 1981-09-16 1981-09-16 Control method for temperature of gas generated at the furnace top Granted JPS5847124A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14576881A JPS5847124A (en) 1981-09-16 1981-09-16 Control method for temperature of gas generated at the furnace top

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14576881A JPS5847124A (en) 1981-09-16 1981-09-16 Control method for temperature of gas generated at the furnace top

Publications (2)

Publication Number Publication Date
JPS5847124A JPS5847124A (en) 1983-03-18
JPH0119051B2 true JPH0119051B2 (en) 1989-04-10

Family

ID=15392707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14576881A Granted JPS5847124A (en) 1981-09-16 1981-09-16 Control method for temperature of gas generated at the furnace top

Country Status (1)

Country Link
JP (1) JPS5847124A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61202606A (en) * 1985-03-04 1986-09-08 株式会社クボタ Agricultural tractor
JPH0767325B2 (en) * 1985-10-03 1995-07-26 セイレイ工業株式会社 Automatic plowing control device
JPH0773446B2 (en) * 1987-05-18 1995-08-09 本田技研工業株式会社 Lifting position control device for work machine in traveling work machine
JPS63296602A (en) * 1987-05-28 1988-12-02 Kubota Ltd Tilling depth display device for rotary tiller
JPH0614802B2 (en) * 1987-05-29 1994-03-02 株式会社クボタ Control device for rotary tiller

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52131904A (en) * 1976-04-01 1977-11-05 Mitsui Eng & Shipbuild Co Ltd Protector for blast furnace top gas turbine against channeling of blast furnace
JPS53113706A (en) * 1977-03-16 1978-10-04 Ishikawajima Harima Heavy Ind Co Ltd Recovering device for energy of blast furnace gas
JPS5440207A (en) * 1977-09-07 1979-03-29 Nippon Kokan Kk <Nkk> Recovering apparatus for energy of furnace top gas of blast furnace
JPS56138422A (en) * 1980-03-28 1981-10-29 Sumitomo Metal Ind Ltd Recovery of energy from blast furnace gas

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52131904A (en) * 1976-04-01 1977-11-05 Mitsui Eng & Shipbuild Co Ltd Protector for blast furnace top gas turbine against channeling of blast furnace
JPS53113706A (en) * 1977-03-16 1978-10-04 Ishikawajima Harima Heavy Ind Co Ltd Recovering device for energy of blast furnace gas
JPS5440207A (en) * 1977-09-07 1979-03-29 Nippon Kokan Kk <Nkk> Recovering apparatus for energy of furnace top gas of blast furnace
JPS56138422A (en) * 1980-03-28 1981-10-29 Sumitomo Metal Ind Ltd Recovery of energy from blast furnace gas

Also Published As

Publication number Publication date
JPS5847124A (en) 1983-03-18

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