JP2000309810A - Method for controlling temperature of blast furnace top gas - Google Patents

Method for controlling temperature of blast furnace top gas

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Publication number
JP2000309810A
JP2000309810A JP11113929A JP11392999A JP2000309810A JP 2000309810 A JP2000309810 A JP 2000309810A JP 11113929 A JP11113929 A JP 11113929A JP 11392999 A JP11392999 A JP 11392999A JP 2000309810 A JP2000309810 A JP 2000309810A
Authority
JP
Japan
Prior art keywords
flow rate
water
blast furnace
riser
temperature
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
Application number
JP11113929A
Other languages
Japanese (ja)
Other versions
JP4045047B2 (en
Inventor
Genichi Terada
元一 寺田
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP11392999A priority Critical patent/JP4045047B2/en
Publication of JP2000309810A publication Critical patent/JP2000309810A/en
Application granted granted Critical
Publication of JP4045047B2 publication Critical patent/JP4045047B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacture Of Iron (AREA)
  • Blast Furnaces (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for controlling the temp. of blast furnace top gas to that moisture in the blast furnace top gas at the furnace top part does not become the saturating state or higher. SOLUTION: The moisture content in the blast furnace top gas in an uptake tube is measured with a moisture meter 11 and this measured value and the moisture content in the saturating state at the upper part of the uptake tube, are compared and a spraying water flow rate till becoming the saturating state is obtd. On the other hand, the blast furnace top gas temp. in the uptake tube is measured with a thermometer 4, and this measured value and a regulating temp. at the upper part of the uptake tube are compared, and a spraying water flow rate for cooling till regulating temp. is obtd. These two spraying water flow rates are compared and the smaller side in these flow rates is set as the spraying water flow rate to an adjusting value 6 for adjusting the spraying water flow rate. Further, the spraying water flow rate is measured with a flow meter 13 arranged at the front of the adjusting valve 6, and while adjusting the opening degree of the adjusting valve 6 based on this difference between the measured value and the spraying water flow rate setting value, the cooling water is sprayed from a spraying water nozzle 3 to indirectly cool the blast furnace top gas.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、高炉炉頂ガス温度
の制御技術分野に属し、さらに詳しくは、炉頂ガス中の
水分量と炉頂ガスの温度とから散水ノズルの散水流量を
調節して炉頂ガスを冷却する高炉炉頂ガス温度の制御技
術分野に属するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention belongs to the technical field of controlling the temperature of a blast furnace top gas, and more particularly, to controlling the water spray flow rate of a water spray nozzle based on the amount of water in the furnace gas and the temperature of the furnace gas. It belongs to the technical field of controlling the temperature of the blast furnace top gas for cooling the top gas.

【0002】[0002]

【従来の技術】高炉炉頂ガスは、高炉排ガス上昇管で集
められ、下降管を経由してダストキャッチャに導入さ
れ、ここで粗粒ダストが除かれ、その後、湿式集塵機ま
たは乾式集塵機で微細ダストが除かれる。除塵された炉
頂ガスは、炉頂発電タービンに導入され発電した後、熱
風炉や、ガスホルダーに導入される。炉頂発電タービン
に導入される炉頂ガス温度は、発電量を増すために高い
方が好ましい。
2. Description of the Related Art Blast furnace top gas is collected by a blast furnace exhaust gas riser and introduced into a dust catcher via a downcomer, where coarse dust is removed, and then fine dust is collected by a wet dust collector or a dry dust collector. Is excluded. The dust-removed furnace top gas is introduced into a furnace top power generation turbine to generate power, and then introduced into a hot blast stove or a gas holder. The temperature of the top gas introduced into the top power generation turbine is preferably higher in order to increase the amount of power generation.

【0003】炉頂ガスの温度が上昇すると、炉頂に設置
してあるベルやクロスゾンデなどの機器の寿命を短くす
るとともに、乾式集塵機(バッグフィルター)を採用し
ている場合は、バッグフィルターの濾布の熱損傷をひき
起こすことになる。したがって、炉頂ガス温度を適切に
制御することは重要である。特に、微粉炭吹き込み量が
増加すると、炉頂ガス温度は上昇する傾向がある。
[0003] When the temperature of the furnace top gas rises, the life of equipment such as a bell and a cross sonde installed on the furnace top is shortened, and when a dry dust collector (bag filter) is employed, the bag filter is not used. This will cause thermal damage to the filter cloth. Therefore, it is important to properly control the furnace gas temperature. In particular, as the pulverized coal injection amount increases, the furnace top gas temperature tends to increase.

【0004】炉頂ガス温度を制御する方法として、一般
的に炉頂の各部に散水する方法が取られているが、散水
が炉頂ガスの冷却に効果的に働いていることを確認する
ことが重要である。従来の炉頂ガス温度制御方法の一例
を図3に示す。図3に示すように、高炉炉頂部に設けた
散水ノズル9から高炉内を上昇してきた炉頂ガスに直接
散水して炉頂ガスを冷却し、さらに高炉排ガス上昇管下
部外周に設けた散水ノズル3から高炉排ガス上昇管2の
外周に散水して上昇管内を上昇する炉頂ガスを間接冷却
する炉頂ガス温度の制御方法がある。
[0004] As a method of controlling the temperature of the top gas, a method of spraying water on each part of the furnace top is generally adopted. However, it is necessary to confirm that the water spray is effectively working for cooling the top gas. is important. FIG. 3 shows an example of a conventional furnace top gas temperature control method. As shown in FIG. 3, water is directly sprayed from a water spray nozzle 9 provided at the top of the blast furnace to the furnace gas rising in the blast furnace to cool the furnace gas, and further, a water spray nozzle provided at the lower periphery of the lower part of the blast furnace exhaust gas riser 3 there is a method of controlling the temperature of the top gas, which indirectly cools the top gas rising in the riser by spraying water on the outer circumference of the blast furnace exhaust gas riser 2.

【0005】すなわち、高炉内を上昇してきた炉頂ガス
温度は 650℃程度あり、これを下げるために、散水ノズ
ル9の上方に設置した温度計7で上昇してきた炉頂ガス
温度を測定し、この測定値に基づいて温度調節計8で規
定温度、例えば、上昇管下部で 350℃になるようにPI
D演算して散水流量を求め、この散水流量に基づいて調
節弁10の開閉を調節して散水ノズル9から冷却水を散水
して炉頂ガスを直接冷却している。さらに炉頂ガス温度
を下げるために、上昇管上部に設置した温度計4で上昇
してきた炉頂ガス温度を測定し、この測定値に基づいて
温度調節計5で規定温度、例えば、上昇管上部で 180℃
になるようにPID演算して散水流量を求め、この散水
流量に基づいて調節弁6の開閉を調節して散水ノズル3
から高炉排ガス上昇管2の外周に散水して炉頂ガスを間
接冷却している。
That is, the temperature of the top gas that has risen in the blast furnace is about 650 ° C. In order to lower this temperature, the temperature of the top gas that has risen is measured by a thermometer 7 installed above the watering nozzle 9. Based on this measured value, the temperature controller 8 sets the PI to a specified temperature, for example, 350 ° C at the lower part of the riser.
D calculation is performed to determine a watering flow rate, and the opening and closing of the control valve 10 is adjusted based on the watering flow rate to spray cooling water from the watering nozzle 9 to directly cool the furnace top gas. In order to further lower the furnace top gas temperature, the temperature of the furnace top gas that has risen is measured by a thermometer 4 installed above the riser pipe, and based on the measured value, a temperature controller 5 determines a specified temperature, for example, the upper part of the riser pipe. At 180 ℃
PID calculation is performed to obtain the watering flow rate, and the opening and closing of the control valve 6 is adjusted based on the watering flow rate to obtain the watering nozzle 3
From the blast furnace exhaust gas riser 2 to indirectly cool the furnace top gas.

【0006】[0006]

【発明が解決しようとする課題】しかし、上記のように
炉頂ガスを冷却することに重点をおき、散水ノズルから
の散水流量を調節した場合は、散水量が多過ぎると、す
なわち、炉頂ガス中の水分が飽和状態以上になると、散
水した水分は蒸発しきれず水の状態で残存する。残存し
た水分は、炉内で発生する亜硫酸ガスや塩素ガスなどを
溶かし込み、高炉炉頂部や上昇管の内張耐火物を濡ら
し、あるいは染み込んで耐火物と反応して耐火物の劣化
を促進する。さらに耐火物の亀裂から浸入した亜硫酸ガ
スや塩素ガスなどを溶かし込んだ水分が鉄皮を腐食させ
ることにもなる。高炉炉頂部や上昇管の内張耐火物の補
修は高炉巻きかえ時まで行うことができず、内張耐火物
の損傷を防止することは高炉操業上、重要なことであ
る。
However, in the case where the emphasis is placed on cooling the furnace top gas and the flow rate of water sprayed from the water spray nozzle is adjusted as described above, if the amount of water sprayed is too large, When the water content in the gas becomes more than the saturated state, the water sprinkled does not evaporate and remains in the water state. The remaining moisture dissolves sulfurous acid gas and chlorine gas generated in the furnace, wets the refractory lining of the blast furnace top and riser, or soaks and reacts with the refractory to promote deterioration of the refractory. . In addition, the moisture dissolved in sulfurous acid gas, chlorine gas, or the like that has invaded through cracks in the refractory also corrodes the steel skin. Repair of the refractory lining at the top of the blast furnace or the riser cannot be performed until the blast furnace is rolled over, and preventing damage to the refractory lining is important for blast furnace operation.

【0007】こうした状態は散水ノズルの性能、炉頂ガ
スの流れに対する散水ノズルの設置位置、炉頂ガス流量
に対する散水流量などの不適合があったときに発生す
る。これらの不適合を防止するためには、多くのセンサ
を設置することで可能かも知れないが、多くのセンサか
らの情報を正確に把握することは困難である。したがっ
て、数少ないセンサで散水ノズルからの散水流量を調節
し、散水した水分が全て蒸発し水の状態で残存しない炉
頂ガス温度の制御方法が望まれている。
Such a state occurs when there is an incompatibility in the performance of the water spray nozzle, the installation position of the water spray nozzle with respect to the flow of the furnace top gas, the flow rate of the water spray with respect to the flow rate of the furnace top gas, and the like. To prevent these inconsistencies, it may be possible to install many sensors, but it is difficult to accurately grasp information from many sensors. Therefore, there is a demand for a method of controlling the temperature of the furnace top gas by adjusting the flow rate of water sprayed from the water spray nozzle with a small number of sensors and evaporating all of the water sprayed so that the water remains in the water state.

【0008】本発明は、上記の問題点を解決するために
なされたもので、散水ノズルから散水して炉頂ガス温度
を制御する方法において、炉頂ガス温度と炉頂ガス中の
水分量を測定することによって、散水ノズルからの散水
流量を精度よく調節し、かつ散水した水分が全て蒸発し
水の状態で残存せず、炉頂部で炉頂ガスの水分が飽和状
態以上にならないように、高炉炉頂ガス温度を制御する
方法を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems. In a method for controlling the temperature of the top gas by spraying water from a water spray nozzle, the temperature of the top gas and the amount of water in the top gas are controlled. By measuring, the sprinkling flow rate from the sprinkling nozzle is adjusted accurately, and all the sprinkled water does not evaporate and remain in the water state, so that the water in the furnace top gas does not become saturated at the furnace top or more. It is an object of the present invention to provide a method for controlling a blast furnace top gas temperature.

【0009】[0009]

【課題を解決するための手段】その要旨は、散水ノズル
から散水して炉頂ガス温度を制御する方法において、高
炉排ガス上昇管上部に設置した水分計で上昇管内の炉頂
ガス中の水分量を測定し、この測定値と上昇管上部の飽
和状態における水分量とを比較し飽和状態になるまでの
散水流量を求め、一方、上昇管上部に設置してある温度
計で上昇管内の炉頂ガス温度を測定し、この測定値と上
昇管上部の規定温度とを比較し規定温度まで冷却する散
水流量を求め、これら二つの散水流量を比較し小さい方
の散水流量を、散水流量を調節する調節弁に散水流量と
して設定し、さらに前記調節弁の前方に設けた流量計で
散水流量を測定し、この測定値と散水流量設定値との差
に基づいて調節弁の開閉を調節しながら高炉排ガス上昇
管下部外周に設けた散水ノズルから冷却水を散水して上
昇管外周部を冷却し炉頂ガスを間接冷却する高炉炉頂ガ
ス温度の制御方法である。
The gist of the present invention is to control the furnace gas temperature by spraying water from a water spray nozzle, and to measure the amount of water in the furnace gas in the furnace blast furnace exhaust gas using a moisture meter installed above the furnace gas riser. Is measured and the measured value is compared with the water content in the saturated state at the upper part of the riser to determine the watering flow rate until the state becomes saturated. Measure the gas temperature, compare this measured value with the specified temperature at the upper part of the riser pipe, find the water flow rate to cool down to the specified temperature, compare these two water flow rates, and adjust the smaller water flow rate, and adjust the water flow rate The control valve is set as the watering flow rate, and the watering flow rate is measured by a flow meter provided in front of the control valve.The blast furnace is adjusted while opening and closing the control valve based on the difference between the measured value and the watering flow setting value. Provided on the lower periphery of the exhaust gas riser The riser outer periphery by sprinkling cooling water from the water spray nozzle is a control method of blast furnace top gas temperature indirectly cool the cooled top gas.

【0010】上記の高炉炉頂ガス温度の制御方法に加え
て、さらに前記上昇管下部に設置した水分計で上昇管内
の炉頂ガス中の水分量を測定し、この測定値と上昇管下
部の飽和状態における水分量とを比較し飽和状態になる
までの散水流量を求め、一方、高炉内を上昇してきた炉
頂ガスに直接散水して炉頂ガスを冷却する散水ノズルの
上方に設置してある温度計で炉頂ガス温度を測定し、こ
の測定値と高炉排ガス上昇管下部の規定温度とを比較し
規定温度まで冷却する散水流量を求め、これら二つの散
水流量を比較し小さい方の散水流量を、散水流量を調節
する調節弁に散水流量として設定し、さらに前記調節弁
の前方に設けた流量計で散水流量を測定し、この測定値
と散水流量設定値との差に基づいて調節弁の開閉を調節
しながら高炉炉頂部に設けた散水ノズルから冷却水を散
水して高炉内を上昇してきた炉頂ガスを直接冷却する高
炉炉頂ガス温度の制御方法である。
In addition to the above-described method of controlling the temperature of the furnace top gas, the amount of moisture in the furnace top gas in the riser is measured by a moisture meter installed in the lower part of the riser. Compare the amount of water in the saturated state and determine the water flow rate until the saturated state is reached.On the other hand, install directly above the spray nozzle that cools the top gas by spraying water directly on the top gas that has risen in the blast furnace. Measure the gas temperature at the furnace top with a thermometer, compare the measured value with the specified temperature at the bottom of the blast furnace exhaust gas riser, determine the water flow rate for cooling to the specified temperature, compare these two water flow rates, and compare the smaller water flow rate The flow rate is set as a sprinkling flow rate in a control valve for adjusting the sprinkling flow rate, and the sprinkling flow rate is measured with a flow meter provided in front of the control valve, and the flow rate is adjusted based on a difference between the measured value and the sprinkling flow rate set value. Blast furnace top while adjusting valve opening and closing In a blast furnace top gas temperature controlling method of the water spray nozzles and sprinkling cooling water to cool directly the top gas which has been raised a blast furnace provided.

【0011】[0011]

【発明の実施の形態】本発明では、測温部位での炉頂ガ
ス中の水分が飽和状態になるまでの散水流量と同じ測温
部位での温度が規定温度に冷却するまでの散水流量とを
比較して、小さい方の散水流量をもとにして散水ノズル
から散水して炉頂ガス温度を制御する。すなわち、測温
部位での炉頂ガス中の水分が飽和状態になるまでの散水
流量の方が小さいときは、飽和状態になるまでの散水流
量の余裕が少ないことであり、この時、散水流量の大き
い同じ測温部位での温度が規定温度に冷却するまでの散
水流量で炉頂ガス温度を制御すれば、過剰の散水となり
蒸発しきれない水分は水の状態で残存することになる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the present invention, the water flow rate until the moisture in the furnace top gas at the temperature measurement site becomes saturated is the same as the water flow rate until the temperature at the temperature measurement site is cooled to a specified temperature. And spraying water from the watering nozzle based on the smaller watering flow rate to control the furnace top gas temperature. In other words, when the water flow in the furnace top gas at the temperature measuring part is smaller than the water flow rate until the water is saturated, the water flow rate before the water is saturated is less. If the furnace top gas temperature is controlled by the water spray flow rate until the temperature at the same temperature measurement site where the temperature is large is cooled to the specified temperature, the water that is excessively sprayed and cannot be evaporated remains in the water state.

【0012】また、測温部位での温度が規定温度に冷却
するまでの散水流量の方が小さいときは、規定温度に冷
却するまでの散水流量の余裕が少ないことであり、この
時、散水流量の大きい同じ測温部位での炉頂ガス中の水
分が飽和状態になるまでの散水流量で炉頂ガス温度を制
御すれば、過剰の散水となり炉頂ガス温度が下がり過ぎ
ることになる。したがって、炉頂ガス温度の制御は、測
温部位での飽和状態になるまでの散水流量と同じ測温部
位での規定温度に冷却するまでの散水流量とを比較し
て、小さい方の散水流量で行う。ただし、炉頂ガス中の
水分が飽和状態以上、あるいは炉頂ガス温度が規定温度
未満であれば、これ以上散水して炉頂ガスを冷却するこ
とはできない。
When the water flow rate at which the temperature at the temperature measuring part is cooled to the specified temperature is smaller, there is less room for the water flow rate at which the temperature is cooled to the specified temperature. If the temperature of the top gas is controlled by the water flow rate until the moisture in the top gas at the same temperature measurement site is saturated, the water is excessively sprayed and the temperature of the top gas becomes too low. Therefore, control of the furnace top gas temperature is performed by comparing the sprinkling flow rate until the temperature at the temperature measurement site reaches the saturation state and the sprinkling flow rate until cooling to the specified temperature at the same temperature measurement site. Do with. However, if the moisture in the furnace top gas is above the saturation state or the furnace top gas temperature is lower than the specified temperature, it is not possible to spray more water to cool the furnace top gas.

【0013】以上のように、二つの散水流量を比較し
て、小さい方の散水流量をもとに炉頂ガス温度を制御す
ることによって、水の状態で残存する水分がなくなり、
高炉炉頂部や上昇管の内張耐火物を劣化させることがな
くなり、さらに耐火物の亀裂から浸入した亜硫酸ガスや
塩素ガスなどを溶かし込んだ水分が鉄皮を腐食すること
もなくなる。また、炉頂ガス温度を規定温度に維持でき
るため、炉頂発電量も安定し、乾式集塵機の濾布の熱損
傷を回避することができる。
As described above, by comparing the two watering flow rates and controlling the furnace top gas temperature based on the smaller watering flow rate, there is no water remaining in the water state,
The refractory lining at the top of the blast furnace and the riser does not deteriorate, and the moisture dissolved in sulfurous acid gas, chlorine gas, or the like that has penetrated from cracks in the refractory does not corrode the steel shell. Further, since the furnace top gas temperature can be maintained at the specified temperature, the furnace top power generation amount is also stabilized, and the thermal damage to the filter cloth of the dry dust collector can be avoided.

【0014】[0014]

【実施例1】以下に、本発明の実施例を図に基づいて説
明する。図1は高炉排ガス上昇管2の外周に散水して上
昇管内を上昇する炉頂ガス温度を制御する例で、高炉頂
部から上方に伸びる2本の高炉排ガス上昇管2が1本の
上昇管となる結合点Aに水分計11を設置している。その
理由は、炉況が不安定となり炉頂ガス温度が急激に上昇
した時など、急激に炉頂ガスに散水することになり、こ
うしたとき、一時的に過剰散水が発生する。過剰水分を
含んだ炉頂ガスは、流れが曲げられる部分などで側壁に
衝突し、その部分を濡らすことになるからである。した
がって、炉頂ガスの流れが曲げられる結合点Aに水分計
11を設置している。水分計11には中性子水分計を用いる
ことができる。
Embodiment 1 An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows an example in which the temperature of the furnace top gas rising from the blast furnace exhaust gas riser by spraying water on the outer periphery of the blast furnace exhaust gas riser 2 is two blast furnace exhaust gas risers 2 extending upward from the top of the blast furnace exhaust gas. The moisture meter 11 is installed at the connection point A. The reason is that when the furnace condition becomes unstable and the top gas temperature rises sharply, water is rapidly sprayed on the top gas, and in such a case, excessive water is temporarily generated. This is because the furnace top gas containing excess moisture collides with the side wall at a portion where the flow is bent and wets the portion. Therefore, the moisture meter is located at the junction A where the flow of the furnace top gas is bent.
11 are installed. As the moisture meter 11, a neutron moisture meter can be used.

【0015】水分計11で上昇管内の炉頂ガス中の水分量
を測定し、この測定値に基づき水分調節計12でPID演
算して飽和状態になるまでの散水流量を求める。一方、
上昇管上部に設置してある温度計4で上昇管内の炉頂ガ
ス温度を測定し、この測定値に基づき温度調節計5でP
ID演算して規定温度に冷却するまでの散水流量を求め
る。そして上記、二つの散水流量の信号が演算器15に送
られる。
The moisture content in the furnace top gas in the riser is measured by the moisture meter 11, and based on the measured value, PID calculation is performed by the moisture controller 12 to determine the watering flow rate until saturation. on the other hand,
The temperature of the furnace top gas in the riser is measured by a thermometer 4 installed at the upper part of the riser.
An ID calculation is performed to determine a watering flow rate until cooling to a specified temperature. Then, the signals of the two sprinkling flow rates are sent to the calculator 15.

【0016】水分調節計12からと温度調節計5から送ら
れてきた二つの散水流量信号を演算器15で比較し、小さ
い方の散水流量信号についてPID演算して求めた散水
流量を流量調節計14に設定散水流量として設定する。流
量調節計14は前記設定散水流量に基づき調節弁6の開閉
を調節する。さらに前記調節弁6の前方に設けた流量計
13で散水流量を測定し、この測定値と散水流量設定値と
の差に基づいて、流量調節計14は調節弁6の開閉を調節
することによって、散水ノズル3からの散水流量の精度
を高めることができる。このように調節弁6の開閉を調
節しながら高炉排ガス上昇管下部に設けた散水ノズル3
から冷却水を散水して上昇管外周部を冷却して炉頂ガス
を間接冷却することによって、炉頂ガス温度を制御す
る。
An arithmetic unit 15 compares two sprinkling flow rate signals sent from the moisture controller 12 and the temperature controller 5 and calculates a sprinkling flow rate obtained by performing PID calculation on the smaller sprinkling flow rate signal. Set the watering flow rate to 14 The flow controller 14 controls opening and closing of the control valve 6 based on the set watering flow rate. A flow meter provided in front of the control valve 6
The water flow rate is measured at 13, and based on the difference between the measured value and the water flow rate set value, the flow controller 14 adjusts the opening and closing of the control valve 6 to increase the accuracy of the water flow rate from the watering nozzle 3. be able to. The watering nozzle 3 provided below the blast furnace exhaust gas riser while adjusting the opening and closing of the control valve 6 in this manner.
The temperature of the furnace top gas is controlled by indirectly cooling the furnace top gas by spraying cooling water from above to cool the outer periphery of the riser pipe.

【0017】[0017]

【実施例2】図2は、図1に示す炉頂ガス温度の制御方
法に、さらに、高炉排ガス上昇管2の下部B点に水分計
16を設置し散水ノズル9からの散水流量の精度を高めた
ものである。すなわち、炉況が不安定となり炉頂ガス温
度が急激に上昇した時など、急激に炉頂ガスに散水する
ことになり、こうしたとき、一時的に過剰散水(水分が
飽和状態以上)となることがあるため、ここに水分計16
を設置して炉頂ガス中の水分量を測定することは高炉炉
頂部や上昇管の内張耐火物の損傷を回避する上から重要
なことである。水分計11には中性子水分計を用いること
ができる。
Embodiment 2 FIG. 2 shows a method of controlling the furnace top gas temperature shown in FIG.
16 is installed to improve the accuracy of the water flow rate from the watering nozzle 9. In other words, when the furnace condition becomes unstable and the temperature of the top gas rises sharply, water is rapidly sprayed on the top gas, and in such a case, the water temporarily becomes excessively water (moisture is more than saturated). There is a moisture analyzer here 16
It is important to measure the amount of water in the furnace top gas by installing a blast furnace in order to avoid damage to the refractory lining of the blast furnace top and the riser pipe. As the moisture meter 11, a neutron moisture meter can be used.

【0018】水分計16で上昇管内の炉頂ガス中の水分量
を測定し、この測定値に基づき水分水分調節計17でPI
D演算して飽和状態になるまでの散水流量を求める。一
方、散水ノズル9の上方に設置してある温度計7で高炉
炉頂部の炉頂ガス温度を測定し、この測定値に基づき温
度調節計8でPID演算して規定温度に冷却するまでの
散水流量を求める。そして上記、二つの散水流量の信号
が演算器20に送られる。
The moisture content in the furnace top gas in the riser is measured by a moisture meter 16, and based on the measured value,
D is calculated to determine the watering flow rate until the water is saturated. On the other hand, the temperature of the top gas at the top of the blast furnace is measured by the thermometer 7 installed above the watering nozzle 9, PID calculation is performed by the temperature controller 8 based on the measured value, and watering is performed until the temperature reaches the specified temperature. Find the flow rate. Then, the two sprinkling flow rate signals are sent to the computing unit 20.

【0019】水分調節計16からと温度調節計9から送ら
れてきた二つの散水流量信号を演算器20で比較し、小さ
い方の散水流量信号についてPID演算して求めた散水
流量を流量調節計19に設定散水流量として設定する。流
量調節計19は前記設定散水流量に基づき調節弁10の開閉
を調節する。さらに前記調節弁10の前方に設けた流量計
18で散水流量を測定し、この測定値と散水流量設定値と
の差に基づいて、流量調節計19は調節弁10の開閉を調節
することによって、散水ノズル9からの散水流量の精度
を高めることができる。このように調節弁10の開閉を調
節しながら高炉炉頂部に設けてある散水ノズル9から冷
却水を散水して炉頂ガスを直接冷却することによって炉
頂ガス温度を制御する。
The arithmetic unit 20 compares the two sprinkling flow rate signals sent from the moisture controller 16 and the temperature controller 9 and calculates the sprinkling flow rate obtained by performing PID calculation on the smaller sprinkling flow rate signal. Set to 19 as the set watering flow rate. The flow controller 19 adjusts the opening and closing of the control valve 10 based on the set watering flow rate. Further, a flow meter provided in front of the control valve 10
The sprinkling flow rate is measured at 18, and based on the difference between the measured value and the sprinkling flow rate set value, the flow controller 19 adjusts the opening and closing of the control valve 10 to increase the accuracy of the sprinkling flow rate from the sprinkling nozzle 9. be able to. While controlling the opening and closing of the control valve 10, the cooling water is sprayed from the water spray nozzle 9 provided at the top of the blast furnace to directly cool the furnace gas, thereby controlling the furnace gas temperature.

【0020】以上述べたように、水分計11および16を設
けることによって、炉頂ガス中の水分量が測定でき、こ
れに基づいて炉頂ガス中の水分が飽和状態になるまでの
散水流量を求めることができる。一方、温度計4および
7で測定した温度に基づいて測温部位の温度を規定温度
まで冷却するまでの散水流量を求めることができる。上
記、二つの散水流量を比較して小さい方の散水流量で炉
頂ガス温度を制御すれば、炉頂ガス温度は規定温度を超
えることなく、かつ炉頂ガス中の水分は飽和状態以上に
なることもない。したがって、高炉炉頂部や上昇管の内
張耐火物の損傷を防止することができる。
As described above, by providing the moisture meters 11 and 16, the amount of water in the top gas can be measured, and based on this, the water flow rate until the water in the top gas becomes saturated can be measured. You can ask. On the other hand, based on the temperatures measured by the thermometers 4 and 7, it is possible to determine the watering flow rate until the temperature of the temperature measuring part is cooled to the specified temperature. If the top gas temperature is controlled at the smaller flow rate by comparing the two flow rates, the top gas temperature does not exceed the specified temperature, and the water content in the top gas becomes more than the saturated state. Not even. Therefore, it is possible to prevent damage to the refractory lining of the blast furnace top and the riser pipe.

【0021】[0021]

【発明の効果】以上述べたところから明らかなように、
本発明によれば、炉頂ガス中の水分が飽和状態以上にな
らないように炉頂ガス温度を制御することができるた
め、高炉炉頂部で炉頂ガスに直接散水した水分が蒸発し
きれずに水の状態で残存することはない。したがって、
亜硫酸ガスや塩素ガスなどを溶かし込んだ水分が高炉炉
頂部や上昇管の内張耐火物を濡らし、あるいは染み込む
こともなくなり、その結果、耐火物の損傷や鉄皮の腐食
を防止することができる。
As is apparent from the above description,
According to the present invention, since the temperature of the top gas can be controlled so that the water in the top gas does not become saturated or higher, the water directly sprayed on the top gas at the top of the blast furnace does not completely evaporate. Will not remain in the state. Therefore,
Water dissolved in sulfurous acid gas, chlorine gas, etc. does not wet or infiltrate the refractory lining of the blast furnace top and riser, and as a result, damage to the refractory and corrosion of the steel shell can be prevented .

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

【図1】請求項1の高炉炉頂ガス温度の制御方法を説明
する図である。
FIG. 1 is a diagram illustrating a method for controlling a blast furnace top gas temperature according to claim 1;

【図2】請求項2の高炉炉頂ガス温度の制御方法を説明
する図である。
FIG. 2 is a diagram illustrating a method for controlling a blast furnace top gas temperature according to claim 2;

【図3】従来の高炉炉頂ガス温度の制御方法を説明する
図である。
FIG. 3 is a diagram illustrating a conventional method for controlling a blast furnace top gas temperature.

【符号の説明】[Explanation of symbols]

1…高炉、2…高炉排ガス上昇管、3…散水ノズル、4
…温度計、5…温度調節計、6…調節弁、7…温度計、
8…温度調節計、9…散水ノズル、10…調節弁、11…水
分計、12…水分調節計、13…流量計、14…流量調節計、
15…演算器、16…水分計、17…水分調節計、18…流量
計、19…流量調節計、20…演算器。
1: Blast furnace, 2: Blast furnace exhaust gas riser, 3: Sprinkler nozzle, 4
... thermometer, 5 ... temperature controller, 6 ... control valve, 7 ... thermometer,
8 ... temperature controller, 9 ... watering nozzle, 10 ... control valve, 11 ... moisture meter, 12 ... moisture controller, 13 ... flow meter, 14 ... flow controller,
15… Calculator, 16… Moisture meter, 17… Moisture controller, 18… Flow meter, 19… Flow controller, 20… Calculator.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 散水ノズルから散水して炉頂ガス温度を
制御する方法において、高炉排ガス上昇管上部に設置し
た水分計で上昇管内の炉頂ガス中の水分量を測定し、こ
の測定値と上昇管上部の飽和状態における水分量とを比
較し飽和状態になるまでの散水流量を求め、一方、上昇
管上部に設置してある温度計で上昇管内の炉頂ガス温度
を測定し、この測定値と上昇管上部の規定温度とを比較
し規定温度まで冷却する散水流量を求め、これら二つの
散水流量を比較し小さい方の散水流量を、散水流量を調
節する調節弁に散水流量として設定し、さらに前記調節
弁の前方に設けた流量計で散水流量を測定し、この測定
値と散水流量設定値との差に基づいて調節弁の開閉を調
節しながら高炉排ガス上昇管下部外周に設けた散水ノズ
ルから冷却水を散水して上昇管外周部を冷却し炉頂ガス
を間接冷却することを特徴とする高炉炉頂ガス温度の制
御方法。
In a method for controlling a furnace gas temperature by spraying water from a water spray nozzle, a moisture meter installed above a blast furnace exhaust gas riser is used to measure the amount of moisture in the furnace top gas in the riser, and this measured value is compared with the measured value. Compare the water content in the upper part of the riser with the saturated water content to determine the water flow until saturation, and measure the furnace top gas temperature in the riser with a thermometer installed on the upper part of the riser. Compare the value with the specified temperature at the top of the riser pipe to determine the watering flow rate for cooling to the specified temperature, compare these two watering flow rates, and set the smaller watering flow rate as the watering flow rate at the control valve that controls the watering flow rate. Further, the sprinkling flow rate was measured with a flow meter provided in front of the control valve, and provided on the outer periphery of the lower part of the blast furnace exhaust gas riser pipe while adjusting the opening and closing of the control valve based on the difference between the measured value and the sprinkling flow rate set value. Watering the cooling water from the watering nozzle A method for controlling the temperature of the blast furnace top gas, comprising cooling the outer periphery of the riser pipe and indirectly cooling the top gas.
【請求項2】 請求項1記載の高炉炉頂ガス温度の制御
方法に加えて、さらに前記上昇管下部に設置した水分計
で上昇管内の炉頂ガス中の水分量を測定し、この測定値
と上昇管下部の飽和状態における水分量とを比較し飽和
状態になるまでの散水流量を求め、一方、高炉内を上昇
してきた炉頂ガスに直接散水して炉頂ガスを冷却する散
水ノズルの上方に設置してある温度計で炉頂ガス温度を
測定し、この測定値と高炉排ガス上昇管下部の規定温度
とを比較し規定温度まで冷却する散水流量を求め、これ
ら二つの散水流量を比較し小さい方の散水流量を、散水
流量を調節する調節弁に散水流量として設定し、さらに
前記調節弁の前方に設けた流量計で散水流量を測定し、
この測定値と散水流量設定値との差に基づいて調節弁の
開閉を調節しながら高炉炉頂部に設けた散水ノズルから
冷却水を散水して高炉内を上昇してきた炉頂ガスを直接
冷却することを特徴とする高炉炉頂ガス温度の制御方
法。
2. In addition to the method for controlling a blast furnace furnace gas temperature according to claim 1, the amount of water in the furnace gas in the riser is further measured by a moisture meter installed below the riser. And the amount of water in the lower part of the riser in the saturated state to determine the water flow rate until the saturated state is reached.On the other hand, the water spray nozzle directly cools the furnace gas by spraying water directly on the furnace gas rising in the blast furnace. Measure the gas temperature at the top of the furnace with a thermometer installed above, compare this measured value with the specified temperature at the bottom of the blast furnace exhaust gas riser, find the water flow rate for cooling to the specified temperature, and compare these two water flow rates. The smaller sprinkling flow rate is set as a sprinkling flow rate in a control valve for adjusting the sprinkling flow rate, and the sprinkling flow rate is measured with a flow meter provided in front of the control valve,
While controlling the opening and closing of the control valve based on the difference between the measured value and the water flow setting value, cooling water is sprayed from a water spray nozzle provided at the top of the blast furnace to directly cool the furnace gas rising in the blast furnace. A method for controlling a blast furnace top gas temperature, characterized in that:
JP11392999A 1999-04-21 1999-04-21 Blast furnace top gas temperature control method Expired - Fee Related JP4045047B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11392999A JP4045047B2 (en) 1999-04-21 1999-04-21 Blast furnace top gas temperature control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11392999A JP4045047B2 (en) 1999-04-21 1999-04-21 Blast furnace top gas temperature control method

Publications (2)

Publication Number Publication Date
JP2000309810A true JP2000309810A (en) 2000-11-07
JP4045047B2 JP4045047B2 (en) 2008-02-13

Family

ID=14624742

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11392999A Expired - Fee Related JP4045047B2 (en) 1999-04-21 1999-04-21 Blast furnace top gas temperature control method

Country Status (1)

Country Link
JP (1) JP4045047B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101220585B1 (en) 2010-12-27 2013-01-10 주식회사 포스코 Apparatus for controlling temperature of furnace and method using the same
JP2021091948A (en) * 2019-12-12 2021-06-17 日本製鉄株式会社 Operation method of blast furnace
CN115537486A (en) * 2022-09-15 2022-12-30 首钢集团有限公司 Combustion control method of hot blast stove

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101220585B1 (en) 2010-12-27 2013-01-10 주식회사 포스코 Apparatus for controlling temperature of furnace and method using the same
JP2021091948A (en) * 2019-12-12 2021-06-17 日本製鉄株式会社 Operation method of blast furnace
JP7348518B2 (en) 2019-12-12 2023-09-21 日本製鉄株式会社 How to operate a blast furnace
CN115537486A (en) * 2022-09-15 2022-12-30 首钢集团有限公司 Combustion control method of hot blast stove
CN115537486B (en) * 2022-09-15 2023-09-15 首钢集团有限公司 Combustion control method of hot blast stove

Also Published As

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