JP7740490B2 - METHOD FOR MEASURING MOLTEN MATERIAL LEVEL IN A BLAST FURNACE, MEASURING DEVICE FOR MOLTEN MATERIAL LEVEL IN A BLAST FURNACE, AND METHOD FOR OPERATING A BLAST FURNACE - Google Patents

METHOD FOR MEASURING MOLTEN MATERIAL LEVEL IN A BLAST FURNACE, MEASURING DEVICE FOR MOLTEN MATERIAL LEVEL IN A BLAST FURNACE, AND METHOD FOR OPERATING A BLAST FURNACE

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JP7740490B2
JP7740490B2 JP2024502016A JP2024502016A JP7740490B2 JP 7740490 B2 JP7740490 B2 JP 7740490B2 JP 2024502016 A JP2024502016 A JP 2024502016A JP 2024502016 A JP2024502016 A JP 2024502016A JP 7740490 B2 JP7740490 B2 JP 7740490B2
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blast furnace
molten material
level
vibration
vibration intensity
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大熙 岩永
亮太郎 松永
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JFE Steel Corp
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/24Test rods or other checking devices
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/006Automatically controlling the process
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B1/00Shaft or like vertical or substantially vertical furnaces
    • F27B1/10Details, accessories or equipment specially adapted for furnaces of these types
    • F27B1/28Arrangements of monitoring devices, of indicators, of alarm devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D21/00Arrangement of monitoring devices; Arrangement of safety devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D21/00Arrangement of monitoring devices; Arrangement of safety devices
    • F27D21/0028Devices for monitoring the level of the melt
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D21/00Arrangement of monitoring devices; Arrangement of safety devices
    • F27D21/02Observation or illuminating devices
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2300/00Process aspects
    • C21B2300/02Particular sequence of the process steps
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2300/00Process aspects
    • C21B2300/04Modeling of the process, e.g. for control purposes; CII
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • F27D2019/0028Regulation
    • F27D2019/0071Regulation using position sensors

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Blast Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

本発明は、高炉炉内の溶融物レベルの計測方法、高炉炉内の溶融物レベルの計測装置、及び高炉の操業方法に関する。 The present invention relates to a method for measuring the molten material level in a blast furnace, a device for measuring the molten material level in a blast furnace, and a method for operating a blast furnace.

製鉄業において、高炉は最上流工程に位置するため、その操業の安定化技術が重要視されている。高炉の安定操業には炉内の良好な通気性の確保が重要である。炉内の通気性の阻害要因の一つとして、炉下部の充填層中に滞留する溶銑及び溶融スラグ(以下、両者を合わせて溶融物と称す)の液面レベルの上昇が挙げられる。溶融物の液面レベル(以下、溶融物レベルと略記)の上昇は、炉内のガス流路の狭小化を引き起こし、送風圧の増加の直接原因となりうる。加えて、溶融物レベルが送風羽口レベルに達した場合、送風羽口の溶損、ひいては送風羽口の閉塞や滓返り(溶融物が送風羽口から逆流する現象)といった重大トラブルの原因となりうる。このため、高炉の安定操業を実現するためには、溶融物レベルが送風羽口レベルに達することを確実に回避すべきである。In the steelmaking industry, blast furnaces are the most upstream process, and technology to stabilize their operation is therefore highly valued. Ensuring good ventilation within the furnace is crucial for stable blast furnace operation. One factor impairing ventilation within the furnace is the rise in the liquid level of the molten iron and molten slag (hereinafter collectively referred to as the "molten material") remaining in the packed bed at the bottom of the furnace. A rise in the liquid level of the molten material (hereinafter abbreviated as the "molten material level") narrows the gas flow path within the furnace and can directly contribute to an increase in blast pressure. Furthermore, if the molten material level reaches the blast tuyere level, it can cause serious problems such as blast tuyere melting, blockage of the blast tuyere, and slag backflow (a phenomenon in which molten material flows back from the blast tuyere). Therefore, to ensure stable blast furnace operation, it is essential to ensure that the molten material level does not reach the blast tuyere level.

このような背景から、高炉の各種操業諸元から炉内に滞留している溶融物の量を物質収支的に評価する方法が提案されている。具体的には、特許文献1には、炉内の装入物の実績体積値と操業諸元から計算される理論体積値を用いて高炉から排出される理論溶融物量を求め、実際に排出された溶融物量と比較することにより炉内に滞留している溶融物の量を推定する方法が記載されている。また、特許文献2には、炉体に設置された複数の歪み計によって測定された変数を、連続周囲歪みに関する一般方程式に溶融物レベルを含む高炉の構成材料の性質を代表するパラメータを与えて解くことにより、炉内の溶融物レベルを推定する方法が記載されている。Against this background, methods have been proposed for evaluating the amount of molten material remaining in a blast furnace based on material balance, taking into account various operational parameters of the furnace. Specifically, Patent Document 1 describes a method for estimating the amount of molten material remaining in the furnace by calculating the theoretical amount of molten material to be discharged from the blast furnace using the actual volume of the material charged in the furnace and a theoretical volume calculated from operational parameters, and comparing this with the amount of molten material actually discharged. Furthermore, Patent Document 2 describes a method for estimating the molten material level in a furnace by solving variables measured by multiple strain gauges installed in the furnace body, applying parameters representing the properties of the blast furnace's constituent materials, including the molten material level, to a general equation for continuous ambient strain.

また、特許文献3には、高炉の出銑口から排出される溶融物の排出距離、排出角度、及び排出高さから溶融物の排出速度を計算し、これを用いて炉内の溶融物レベルを推定する、いわゆるベルヌーイの定理を利用した方法が記載されている。本方法の推定精度は出銑口から排出される溶融物の排出速度の計算精度に依存し、同方法ではカメラで撮影した画像の画像解析によって排出速度の推定を行っている。また、特許文献4には、炉下部の炉壁の振動強度を測定し、予め求めた特定の周波数帯の振動強度と溶融物レベルとの対応関係から炉内の溶融物レベルを推定する方法が記載されている。 Patent Document 3 describes a method utilizing Bernoulli's theorem to calculate the discharge rate of molten material from the discharge distance, discharge angle, and discharge height of the molten material discharged from the taphole of a blast furnace, and use this to estimate the molten material level within the furnace. The accuracy of this method depends on the accuracy of the calculation of the discharge rate of molten material discharged from the taphole, and this method estimates the discharge rate through image analysis of images taken with a camera. Patent Document 4 describes a method for measuring the vibration intensity of the furnace wall at the bottom of the furnace and estimating the molten material level within the furnace from the correspondence between the vibration intensity in a specific frequency band determined in advance and the molten material level.

特開2002-302709号公報Japanese Patent Application Laid-Open No. 2002-302709 特表2015-528905号公報Special Publication No. 2015-528905 特許第7056813号公報Patent No. 7056813 国際公開第2022/201717号International Publication No. 2022/201717

しかしながら、特許文献1に記載の方法は、炉下部の充填層の空隙率や凝固層の形状を考慮していない。このため、炉内に滞留している溶融物の量を推定できたとしても、高炉の安定操業のために重要な溶融物の液面レベルの推定には課題が残る。また、各種秤量誤差の影響を受けるため、扱うマスの大きい高炉プロセスでは推定誤差が蓄積し、推定精度が経時的に低下していくという懸念も存在する。However, the method described in Patent Document 1 does not take into account the void ratio of the packed bed in the lower part of the furnace or the shape of the solidified layer. Therefore, even if it is possible to estimate the amount of molten material remaining in the furnace, there remains a problem with estimating the liquid level of the molten material, which is important for stable blast furnace operation. Furthermore, because it is affected by various weighing errors, there is a concern that estimation errors will accumulate in blast furnace processes that handle large volumes, and estimation accuracy will decrease over time.

また、特許文献2に記載の方法には以下のような課題がある。炉下部には高炉表面の鉄皮や冷却ステーブの他に耐火物レンガや炉内溶融物が冷え固まった凝固層が存在することが知られている。そして、耐火物レンガは摩耗や熱応力によって経年劣化をしていき、凝固層は炉下部の熱的状況に応じてその存在範囲が日々変化する。このため、これらの構成材料の存在状態の把握は極めて困難である。従って、特許文献2に記載の方法では、一般方程式から高炉の構成材料を代表する溶融物レベル以外の未知のパラメータを除外することは実質不可能であり、そのため一般方程式から推定される溶融物レベルの精度も満足できるものとは言い難い。 The method described in Patent Document 2 also has the following problems. It is known that in addition to the steel shell and cooling staves on the surface of the blast furnace, the lower furnace also contains refractory bricks and a solidified layer of cooled and solidified molten material inside the furnace. Refractory bricks deteriorate over time due to wear and thermal stress, and the extent of the solidified layer changes daily depending on the thermal conditions in the lower furnace. This makes it extremely difficult to grasp the state of these constituent materials. Therefore, with the method described in Patent Document 2, it is virtually impossible to exclude unknown parameters other than the molten material level, which represents the constituent materials of the blast furnace, from the general equation. Therefore, the accuracy of the molten material level estimated from the general equation cannot be said to be satisfactory.

また、特許文献3に記載の方法では、出銑作業中は高温溶融物の排出に伴い多量の粉塵が発生するため、カメラを用いて明確な溶融物の排出挙動を撮影できる可能性は低い。さらに、出銑作業には横穴に代表される開口ミスの発生が避けられないため、これも溶融物の排出挙動の推定頻度の低下を助長する原因となる。また、これに付随して出銑毎の開口形状は異なるため、炉内から排出口に至る経路で溶融物が受ける摩擦力の定量は困難である。以上を総合すると、特許文献3に記載の方法では、精度の高い溶融物レベルの測定は極めて困難であると言える。 Furthermore, with the method described in Patent Document 3, a large amount of dust is generated as high-temperature molten material is discharged during the tapping operation, making it unlikely that a clear image of the molten material's discharge behavior can be captured using a camera. Furthermore, tapping operations inevitably involve opening errors, such as with horizontal holes, which also contributes to a decrease in the frequency of estimating the molten material's discharge behavior. Furthermore, because the opening shape differs for each tap, it is difficult to quantify the frictional force the molten material experiences on its path from the furnace to the discharge port. Taking all of these factors into consideration, it can be said that the method described in Patent Document 3 makes it extremely difficult to accurately measure the molten material level.

また、特許文献4に記載の方法には以下のような課題がある。実機炉体の振動強度は溶融物レベル以上に送風量の変動や炉内充填物及び炉底レンガや凝固層のような構造物の形状変化に強く影響を受ける。このため、時々刻々と操業状況が変化する高炉プロセスにおいて、炉体の振動強度と溶融物レベルの相関関係を1対1で紐づけることは不可能である。このため、特許文献4に記載の方法は、溶融物レベル以外の炉内状況が定常状態にある極めて理想的な状況でしか効力を発揮せず、長期的、且つ、安定的な溶融物レベルの計測は困難である。 The method described in Patent Document 4 also has the following issues: The vibration intensity of an actual furnace body is more strongly affected by fluctuations in the blast air volume and changes in the shape of furnace fillers and structures such as hearth bricks and the solidified layer than by the molten material level. For this reason, in a blast furnace process where operational conditions change from moment to moment, it is impossible to establish a one-to-one correlation between the vibration intensity of the furnace body and the molten material level. For this reason, the method described in Patent Document 4 is only effective in extremely ideal situations where the conditions inside the furnace other than the molten material level are steady, making it difficult to measure the molten material level stably over the long term.

本発明は、上記課題を解決すべくなされたものであり、その目的は、高炉の操業条件によらず高炉炉内の溶融物レベルを精度高く計測可能な高炉炉内の溶融物レベルの計測方法及び計測装置を提供することにある。また、本発明の他の目的は、エコフレンドリーな高炉操業を安定的に行うことが可能な高炉の操業方法を提供することにある。 The present invention was made to solve the above-mentioned problems, and its purpose is to provide a method and device for measuring the molten material level in a blast furnace that can accurately measure the molten material level in the blast furnace regardless of the blast furnace's operating conditions. Another purpose of the present invention is to provide a blast furnace operating method that enables stable, eco-friendly blast furnace operation.

本発明に係る高炉炉内の溶融物レベルの計測方法は、高炉の炉体の高さ方向に沿って所定間隔を空けて配置された複数の振動計を用いて、炉体の高さ方向の振動周波数分布を測定する測定ステップと、前記振動周波数分布をフーリエ変換することにより、各測定位置における送風由来の周波数範囲の振動強度を算出する振動強度算出ステップと、炉体の高さ方向における振動強度の変化の不連続点を算出し、該不連続点に対応する位置を高炉炉内の溶融物レベルの位置とする溶融物レベル算出ステップと、を含む。 The method for measuring the molten material level in a blast furnace according to the present invention includes a measurement step of measuring the vibration frequency distribution in the height direction of the furnace body using a plurality of vibration meters arranged at predetermined intervals along the height direction of the furnace body of the blast furnace; a vibration intensity calculation step of calculating the vibration intensity in the frequency range caused by the air blowing at each measurement position by Fourier transforming the vibration frequency distribution; and a molten material level calculation step of calculating discontinuities in the change in vibration intensity in the height direction of the furnace body and determining the positions corresponding to the discontinuities as the position of the molten material level in the blast furnace.

前記溶融物レベル算出ステップは、前記各測定位置において、該測定位置より高い測定位置における第一振動強度データと該測定位置より低い測定位置における第二振動強度データとに振動強度データを分類するステップと、前記各測定位置において、第一振動強度データ及び第二振動強度データからそれぞれ炉体の高さ方向位置と振動強度との関係を示す第一線形近似式及び第二線形近似式を構築するステップと、前記各測定位置において、前記第一線形近似式と前記第二線形近似式の測定位置における振動強度差を不連続性として算出するステップと、全測定位置の中で前記不連続性が最大になる測定位置を溶融物レベルとするステップと、を含むとよい。 The molten material level calculation step may include the steps of: classifying vibration intensity data at each measurement position into first vibration intensity data at a measurement position higher than the measurement position and second vibration intensity data at a measurement position lower than the measurement position; constructing a first linear approximation equation and a second linear approximation equation at each measurement position from the first vibration intensity data and the second vibration intensity data, respectively, which indicate the relationship between the vertical position of the furnace body and vibration intensity; calculating the difference in vibration intensity at each measurement position between the first linear approximation equation and the second linear approximation equation as a discontinuity; and determining the measurement position among all measurement positions at which the discontinuity is greatest as the molten material level.

前記振動計は、炉体の出銑口レベルから羽口レベルの間に設置されるとよい。 The vibration meter should be installed between the taphole level and the tuyere level of the furnace body.

前記送風由来の周波数範囲は700~900Hzの範囲内であるとよい。 The frequency range derived from the air blowing should preferably be within the range of 700 to 900 Hz.

本発明に係る高炉炉内の溶融物レベルの計測装置は、高炉の炉体の高さ方向に沿って所定間隔を空けて配置された、炉体の高さ方向の振動周波数分布を測定する複数の振動計と、前記振動周波数分布をフーリエ変換することにより、各測定位置における送風由来の周波数範囲の振動強度を算出し、炉体の高さ方向における振動強度の変化の不連続点を算出し、該不連続点に対応する位置を高炉炉内の溶融物レベルの位置とする情報処理装置と、を備える。 The device for measuring the molten material level in a blast furnace according to the present invention comprises a plurality of vibration meters arranged at predetermined intervals along the height direction of the blast furnace body to measure the vibration frequency distribution in the height direction of the furnace body, and an information processing device that calculates the vibration intensity in the frequency range caused by the air blowing at each measurement position by Fourier transforming the vibration frequency distribution, calculates discontinuities in the change in vibration intensity in the height direction of the furnace body, and determines the positions corresponding to the discontinuities as the position of the molten material level in the blast furnace.

本発明に係る高炉の操業方法は、本発明に係る高炉炉内の溶融物レベルの計測方法を用いて計測された溶融物レベルに従って高炉を操業するステップを含む。 The method for operating a blast furnace according to the present invention includes a step of operating the blast furnace according to the smelt level measured using the method for measuring the smelt level in a blast furnace according to the present invention.

本発明に係る高炉炉内の溶融物レベルの計測方法及び計測装置によれば、高炉の操業条件によらず高炉炉内の溶融物レベルを精度高く計測することができる。また、本発明に係る高炉の操業方法によれば、エコフレンドリーな高炉操業を安定的に行うことができる。 The method and device for measuring the molten material level inside a blast furnace according to the present invention can measure the molten material level inside a blast furnace with high accuracy regardless of the operating conditions of the blast furnace. Furthermore, the blast furnace operating method according to the present invention can ensure stable, eco-friendly blast furnace operation.

図1は、本発明の一実施形態である高炉炉内の溶融物レベルの計測装置が適用された高炉の構成を示す模式断面図である。FIG. 1 is a schematic cross-sectional view showing the configuration of a blast furnace to which a device for measuring the level of molten material inside a blast furnace according to one embodiment of the present invention is applied. 図2は、溶融物レベルを変化させたときに複数の振動計によって測定された送風由来の振動強度を、溶融物レベルに対する相対的な測定位置の高さに対してプロットした結果を示す図である。FIG. 2 shows the intensity of the air-blast-induced vibration measured by multiple vibration meters when the melt level was changed, plotted against the height of the measurement position relative to the melt level. 図3は、本発明の一実施形態である高炉炉内の溶融物レベルの計測方法の概要を示す図である。FIG. 3 is a diagram showing an outline of a method for measuring the molten material level in a blast furnace according to one embodiment of the present invention. 図4は、出銑初期から出銑末期までの溶融物レベルの計測値の時間変化を示す図である。FIG. 4 is a diagram showing the change over time in the measured value of the molten material level from the early stage to the end of tapping.

以下、図面を参照して、本発明の一実施形態である高炉炉内の溶融物レベルの計測方法、高炉炉内の溶融物レベルの計測装置、及び高炉の操業方法について説明する。 Below, with reference to the drawings, we will explain one embodiment of the present invention, which is a method for measuring the molten material level in a blast furnace, a device for measuring the molten material level in a blast furnace, and a method for operating a blast furnace.

〔構成〕
まず、図1を参照して、本発明の一実施形態である高炉炉内の溶融物レベルの計測装置の構成について説明する。
〔composition〕
First, with reference to FIG. 1, the configuration of a measuring device for measuring the level of molten material in a blast furnace according to one embodiment of the present invention will be described.

図1は、本発明の一実施形態である高炉炉内の溶融物レベルの計測装置が適用された高炉の構成を示す模式断面図である。図1に示すように、本発明の一実施形態である高炉1は、略円筒形状の炉体2、炉体2の下方に設けられた送風羽口(以下、羽口と略記)3、及び羽口3よりも下方の炉体2に設けられた出銑口4を備えている。また、高炉1の炉底部は炉底レンガ5及び炉壁レンガ6により構成され、炉壁レンガ6の内壁面及び外壁面はそれぞれ冷却スリーブ7及び鉄皮8により覆われている。 Figure 1 is a schematic cross-sectional view showing the configuration of a blast furnace to which a device for measuring the molten material level within a blast furnace, which is one embodiment of the present invention, is applied. As shown in Figure 1, the blast furnace 1, which is one embodiment of the present invention, comprises a substantially cylindrical furnace body 2, a blower tuyere (hereinafter abbreviated as tuyere) 3 provided below the furnace body 2, and a tap hole 4 provided in the furnace body 2 below the tuyere 3. The hearth of the blast furnace 1 is composed of hearth bricks 5 and hearth wall bricks 6, and the inner and outer wall surfaces of the hearth wall bricks 6 are covered by a cooling sleeve 7 and a steel shell 8, respectively.

また、本発明の一実施形態である高炉1は、高炉炉内の溶融物レベルの計測装置として、複数の振動計9、データロガー10、及び情報処理装置11を備えている。各振動計9は、出銑口4の高さ位置から羽口3の高さ位置にかけて、炉体2の周方向の接線に対して垂直であり、且つ、鉄皮8の表面に沿った直線に沿って等間隔で設定されている。各振動計9は、炉体2の振動値を電流値として計測し、計測された電流値を示す電気信号をデータロガー10に出力する。 Furthermore, the blast furnace 1, which is one embodiment of the present invention, is equipped with multiple vibration meters 9, data loggers 10, and information processing devices 11 as devices for measuring the molten material level within the blast furnace. Each vibration meter 9 is set at equal intervals along a straight line that is perpendicular to the circumferential tangent of the furnace body 2 and that follows the surface of the steel shell 8, from the height of the tap hole 4 to the height of the tuyere 3. Each vibration meter 9 measures the vibration value of the furnace body 2 as a current value and outputs an electrical signal indicating the measured current value to the data logger 10.

データロガー10は、各振動計9から出力された電気信号に基づいて各振動計9が計測した電流値を振動値に変換する。情報処理装置11は、データロガー10が生成した各振動計9の設置位置(測定位置)における振動値の経時データをフーリエ変換することにより各振動計9の設置位置における炉体2の振動強度を計算する。そして、情報処理装置11は、計算された振動強度を用いて以下に示す高炉炉内の溶融物レベルの計測方法を実行することにより高炉炉内の溶融物レベルを算出する。 The data logger 10 converts the current values measured by each vibration meter 9 into vibration values based on the electrical signals output from each vibration meter 9. The information processing device 11 calculates the vibration intensity of the furnace body 2 at the installation position of each vibration meter 9 by performing a Fourier transform on the time-lapse data of the vibration values at the installation position (measurement position) of each vibration meter 9 generated by the data logger 10. The information processing device 11 then calculates the molten material level in the blast furnace by using the calculated vibration intensity and executing the method for measuring the molten material level in the blast furnace shown below.

実機での測定の結果、炉体2の振動はあらゆる振動周波数帯を有し、中でも特にピーク値が高く、且つ、全測定位置でピークが確認される振動周波数帯が700~900Hzの周波数帯であることが確認された。700~900Hzの周波数帯における振動は、羽口3に近い位置で高い値を示すという大まかな傾向を有することが確認されたため、羽口3からの送風23に起因する振動(送風由来の振動)であると考えられる。そこで、本発明では、送風由来の振動に対応する700~900Hzの周波数範囲で確認される振動強度を用いて溶融物レベルを計測することとした。但し、送風由来の振動が確認される周波数帯は炉体2の形状や地盤影響等に応じて変化する可能性があり、どの高炉でも同様にこの周波数帯で評価できるという確証はない。このため、他の高炉に本発明を展開する際は、その都度、基礎的な振動周波数帯の解析をすることが望ましい。Measurements using an actual furnace revealed that vibrations of the furnace body 2 span a wide range of vibration frequencies, with the 700-900 Hz frequency band showing particularly high peak values and peaks at all measurement positions. Because it was confirmed that vibrations in the 700-900 Hz frequency band generally tend to be higher near the tuyere 3, they are thought to be vibrations caused by the air blast 23 from the tuyere 3 (air blast-derived vibrations). Therefore, in this invention, the molten material level is measured using the vibration intensity observed in the 700-900 Hz frequency range, which corresponds to air blast-derived vibrations. However, the frequency band in which air blast-derived vibrations are observed may vary depending on the shape of the furnace body 2, the influence of the ground, etc., and there is no certainty that this frequency band can be used to evaluate all blast furnaces in the same way. For this reason, when applying this invention to other blast furnaces, it is advisable to analyze the basic vibration frequency bands each time.

図1に示す高炉1では、原料である鉄鉱石21とコークス22が、炉頂から炉体2内に層状に装入され、羽口3から圧送される送風(熱風)23によって還元されて溶融物24となる。そして、溶融物24は、炉底部に貯留され、所定時間毎に出銑口4を穿孔することにより出銑口4から出銑滓25として排出される。本発明の一実施形態である高炉炉内の溶融物レベルの計測装置は、炉下部における溶融物24の液面レベルを溶融物レベルとして計測する。 In the blast furnace 1 shown in Figure 1, the raw materials, iron ore 21 and coke 22, are charged in layers into the furnace body 2 from the top of the furnace and reduced to form molten material 24 by blown air (hot air) 23 pressure-fed from the tuyere 3. The molten material 24 is then stored at the bottom of the furnace and discharged as slag 25 from the tap hole 4 by drilling the tap hole 4 at predetermined intervals. One embodiment of the present invention, a device for measuring the molten material level in a blast furnace, measures the liquid level of the molten material 24 in the lower part of the furnace as the molten material level.

〔計測方法〕
次に、図2,図3を参照して、本発明の一実施形態である高炉炉内の溶融物レベルの計測方法について説明する。
[Measurement method]
Next, a method for measuring the molten material level in a blast furnace according to one embodiment of the present invention will be described with reference to FIGS.

図2は、高炉1の炉下部を模擬した冷間模型を用いて溶融物レベルを変化させたときに複数の振動計9によって測定された送風由来の振動強度を、溶融物レベルに対する振動計9の相対的な測定位置の高さ(液面基準の振動計高さ)に対してプロットした結果である。図2に示すように、送風由来の振動強度は溶融物の表層で不連続的に変化していることがわかる。また、本実験は溶融物の物性、送風量、充填粒子径、充填粒子の粒度分布等、実機高炉で変動しうる要因を模擬して与えた複数ケースの結果を含んでいるが、いずれのケースも図2に示す傾向を覆すものではなかった。さらに、原料装入時の振動や、高炉還元材比の変動による炉内充填物の総重量変化、炉底レンガの摩耗による経年劣化に伴う構造変化、及び炉体の設置状況といった外乱的に発生すると思われる振動変動要因を模擬した実験でも、同様に図2に示す傾向が確認された。Figure 2 shows the results of plotting the blast-induced vibration intensity measured by multiple vibration meters 9 against the relative height of the measurement position of the vibration meters 9 relative to the molten material level (vibration meter height based on the liquid level) using a cold model simulating the lower furnace of a blast furnace 1 when the molten material level was changed. As shown in Figure 2, the blast-induced vibration intensity changes discontinuously at the surface of the molten material. This experiment also included results for multiple cases simulating factors that may vary in an actual blast furnace, such as the physical properties of the molten material, the blast volume, the packing particle diameter, and the packing particle size distribution. None of the cases overturned the trend shown in Figure 2. Furthermore, the trend shown in Figure 2 was also confirmed in experiments simulating factors that are thought to be caused by external disturbances, such as vibration during raw material charging, changes in the total weight of the furnace charge due to changes in the blast furnace reducing agent ratio, structural changes due to aging deterioration of the hearth bricks due to wear, and the installation conditions of the furnace body.

以上のことから、溶融物の表層での振動強度の不連続な変動はあらゆる操業条件で統一的に確認される事象であると考えられる。従って、炉体の高さ方向における振動強度の変化の不連続点を算出できれば、その不連続点付近に溶融物の液面が存在するため、高炉の操業条件によらず高炉炉内の溶融物レベルを精度高く計測できる。また、これにより、溶融物レベルの上昇を早期に検知し、溶融物レベルの上昇による通気抵抗の上昇によって引き起こされる還元材比の上昇を未然に防ぐことにより、エコフレンドリーな高炉操業を安定的に行うことができる。本発明の技術思想は以上のロジックに立脚するものである。 From the above, it is believed that discontinuous fluctuations in vibration intensity at the surface layer of the molten material are a phenomenon that is consistently observed under all operating conditions. Therefore, if the discontinuous point in the change in vibration intensity along the height of the furnace body can be calculated, the molten material level within the blast furnace can be measured with high accuracy regardless of the blast furnace's operating conditions, since the molten material surface will be located near that discontinuous point. Furthermore, this allows for early detection of a rise in the molten material level and prevents an increase in the reducing agent ratio caused by an increase in air flow resistance due to a rise in the molten material level, thereby enabling stable, eco-friendly blast furnace operation. The technical concept of this invention is based on the above logic.

図3は、本発明の一実施形態である高炉炉内の溶融物レベルの計測方法の概要を示す図である。本発明の一実施形態である高炉炉内の溶融物レベルの計測方法では、まず、出銑口4から羽口3の高さ位置にかけて炉体2の周方向の接線に対して垂直な線上の複数個所に等間隔で設置した振動計9を用いて送風由来の周波数帯の振動強度を測定する。本実施形態では、振動計9をn(≧2)個設置したとする。次に、情報処理装置11が、各測定位置(振動測定点)i(=1~n)において、その測定位置より高い測定位置の第一振動強度データとその測定位置より低い測定位置の第二振動強度データに振動強度データを分類する。次に、情報処理装置11は、各測定位置iにおいて、第一振動強度データ及び第二振動強度データからそれぞれ炉体2の高さ方向位置と振動強度との関係を示す第一線形近似式及び第二線形近似式を構築する。次に、情報処理装置11が、図3に示すように、各測定位置iにおいて、2つの線形近似式の測定位置iにおける振動強度差を不連続性Δe(i)として算出する。そして最後に、情報処理装置11は、n箇所の不連続性Δe(i)の内、最大値max[Δe(i)]i=1,nを示す測定位置iを溶融物レベルとする。 FIG. 3 is a diagram illustrating an overview of a method for measuring the molten material level in a blast furnace according to one embodiment of the present invention. In this method for measuring the molten material level in a blast furnace according to one embodiment of the present invention, first, vibration intensity in the frequency band caused by the air blowing is measured using vibration meters 9 installed at equal intervals at multiple locations on a line perpendicular to a tangent line in the circumferential direction of the furnace body 2 from the tap hole 4 to the height of the tuyere 3. In this embodiment, n (≧2) vibration meters 9 are installed. Next, the information processing device 11 classifies the vibration intensity data at each measurement position (vibration measurement point) i (=1 to n) into first vibration intensity data at a measurement position higher than the measurement position and second vibration intensity data at a measurement position lower than the measurement position. Next, the information processing device 11 constructs, at each measurement position i, a first linear approximation equation and a second linear approximation equation, respectively, from the first vibration intensity data and the second vibration intensity data, which respectively indicate the relationship between the vertical position of the furnace body 2 and the vibration intensity. Next, as shown in FIG. 3, the information processing device 11 calculates, at each measurement position i, the vibration intensity difference between the two linear approximations as the discontinuity Δe(i). Finally, the information processing device 11 determines the measurement position i showing the maximum value max[Δe(i)] i=1,n among the n discontinuities Δe(i) as the melt level.

本実施例では、容量約5000mの大型高炉において、通常の装入原料を用いて羽口より微粉炭の吹込みを行い、出銑口レベル(高さ位置2m)から羽口レベルにかけて炉体の周方向の接線に対して垂直な線上に等間隔に設置した振動計を用いて炉体の振動を測定し、高炉炉内の溶融物レベルを計測した。表1に実施例1と実施例2の操業条件を示す。図4に出銑初期から出銑末期までの溶融物レベルの計測値の時間変化を示す。図4に示すように、実施例1,2共に溶融物レベルが最終的に出銑口レベルと同程度になっている。このことから、本発明によれば、溶融物レベルを精度高く計測できることが確認された。 In this example, a large blast furnace with a capacity of approximately 5,000 m3 was used, and pulverized coal was injected through the tuyere using normal charging materials. The vibration of the furnace body was measured using vibration meters installed at equal intervals on a line perpendicular to the tangent line of the circumferential direction of the furnace body from the tap hole level (height 2 m) to the tuyere level, and the molten material level in the blast furnace was measured. Table 1 shows the operating conditions for Examples 1 and 2. Figure 4 shows the time change in the measured molten material level from the beginning to the end of tapping. As shown in Figure 4, in both Examples 1 and 2, the molten material level ultimately reached the same level as the tap hole level. This confirmed that the present invention allows for highly accurate measurement of the molten material level.

以上、本発明者らによってなされた発明を適用した実施の形態について説明したが、本実施形態による本発明の開示の一部をなす記述及び図面により本発明が限定されることはない。すなわち、本実施形態に基づいて当業者等によりなされる他の実施の形態、実施例、及び運用技術等は全て本発明の範疇に含まれる。 The above describes an embodiment of the invention developed by the inventors, but the present invention is not limited to the descriptions and drawings that form part of the disclosure of the present invention according to this embodiment. In other words, all other embodiments, examples, and operational techniques, etc., developed by those skilled in the art based on this embodiment are included in the scope of the present invention.

本発明によれば、高炉の操業条件によらず高炉炉内の溶融物レベルを精度高く計測可能な高炉炉内の溶融物レベルの計測方法及び計測装置を提供することができる。また、本発明によれば、エコフレンドリーな高炉操業を安定的に行うことが可能な高炉の操業方法を提供することができる。 The present invention provides a method and device for measuring the molten material level in a blast furnace, which can accurately measure the molten material level in the blast furnace regardless of the operating conditions of the blast furnace. Furthermore, the present invention provides a method for operating a blast furnace, which enables stable, eco-friendly blast furnace operation.

1 高炉
2 炉体
3 送風羽口、羽口
4 出銑口
5 炉底レンガ
6 炉壁レンガ
7 冷却スリーブ
8 鉄皮
9 振動計
10 データロガー
11 情報処理装置
21 鉄鉱石
22 コークス
23 送風
24 溶融物
25 出銑滓
REFERENCE SIGNS LIST 1 blast furnace 2 furnace body 3 blast tuyere, tuyere 4 tap hole 5 hearth brick 6 furnace wall brick 7 cooling sleeve 8 iron shell 9 vibration meter 10 data logger 11 information processing device 21 iron ore 22 coke 23 blast 24 molten material 25 tapping slag

Claims (4)

高炉の炉体の高さ方向に沿って所定間隔を空けて配置された複数の振動計を用いて、炉体の高さ方向の振動周波数分布を測定する測定ステップと、
前記振動周波数分布をフーリエ変換することにより、各測定位置における送風由来の周波数範囲の振動強度を算出する振動強度算出ステップと、
炉体の高さ方向における振動強度の変化の不連続点を算出し、該不連続点に対応する位置を高炉炉内の溶融物レベルの位置とする溶融物レベル算出ステップと、
を含
前記振動計は、炉体の出銑口レベルから羽口レベルの間に設置され、
前記送風由来の周波数範囲は700~900Hzの範囲内である、
高炉炉内の溶融物レベルの計測方法。
a measuring step of measuring a vibration frequency distribution in the height direction of the furnace body using a plurality of vibrometers arranged at predetermined intervals along the height direction of the furnace body of the blast furnace;
a vibration intensity calculation step of calculating the vibration intensity in a frequency range caused by air blowing at each measurement position by performing a Fourier transform on the vibration frequency distribution;
A molten material level calculation step of calculating a discontinuous point in the change in vibration intensity in the height direction of the furnace body and determining the position corresponding to the discontinuous point as the position of the molten material level in the blast furnace;
Including ,
The vibration meter is installed between the tap hole level and the tuyere level of the furnace body,
The frequency range from the air blowing is within the range of 700 to 900 Hz.
A method for measuring the molten material level inside a blast furnace.
前記溶融物レベル算出ステップは、
前記各測定位置において、該測定位置より高い測定位置における第一振動強度データと該測定位置より低い測定位置における第二振動強度データとに振動強度データを分類するステップと、
前記各測定位置において、第一振動強度データ及び第二振動強度データからそれぞれ炉体の高さ方向位置と振動強度との関係を示す第一線形近似式及び第二線形近似式を構築するステップと、
前記各測定位置において、前記第一線形近似式と前記第二線形近似式の測定位置における振動強度差を不連続性として算出するステップと、
全測定位置の中で前記不連続性が最大になる測定位置を溶融物レベルとするステップと、
を含む、請求項1に記載の高炉炉内の溶融物レベルの計測方法。
The melt level calculation step includes:
classifying vibration intensity data at each measurement position into first vibration intensity data at a measurement position higher than the measurement position and second vibration intensity data at a measurement position lower than the measurement position;
At each of the measurement positions, a first linear approximation formula and a second linear approximation formula are constructed from the first vibration intensity data and the second vibration intensity data, respectively, which represent the relationship between the height direction position of the furnace body and the vibration intensity;
calculating a vibration intensity difference between the first linear approximation formula and the second linear approximation formula at each measurement position as a discontinuity;
determining the measurement position at which the discontinuity is greatest among all measurement positions as the melt level;
2. The method for measuring the melt level in a blast furnace according to claim 1, comprising:
高炉の炉体の高さ方向に沿って所定間隔を空けて配置された、炉体の高さ方向の振動周波数分布を測定する複数の振動計と、
前記振動周波数分布をフーリエ変換することにより、各測定位置における送風由来の周波数範囲の振動強度を算出し、炉体の高さ方向における振動強度の変化の不連続点を算出し、該不連続点に対応する位置を高炉炉内の溶融物レベルの位置とする情報処理装置と、
を備え
前記振動計は、炉体の出銑口レベルから羽口レベルの間に設置され、
前記送風由来の周波数範囲は700~900Hzの範囲内である、
高炉炉内の溶融物レベルの計測装置。
a plurality of vibrometers arranged at predetermined intervals along the height direction of the furnace body of the blast furnace, for measuring the vibration frequency distribution in the height direction of the furnace body;
An information processing device that calculates the vibration intensity in the frequency range caused by the air blowing at each measurement position by Fourier transforming the vibration frequency distribution, calculates discontinuities in the change in vibration intensity in the height direction of the furnace body, and determines the position corresponding to the discontinuity as the position of the molten material level in the blast furnace;
Equipped with
The vibration meter is installed between the tap hole level and the tuyere level of the furnace body,
The frequency range from the air blowing is within the range of 700 to 900 Hz.
A device for measuring the molten material level inside a blast furnace.
請求項1又は2に記載の高炉炉内の溶融物レベルの計測方法を用いて計測された溶融物レベルに従って高炉を操業するステップを含む、高炉の操業方法。 A method for operating a blast furnace, comprising the step of operating the blast furnace according to the smelt level measured using the method for measuring the smelt level within the blast furnace according to claim 1 or 2.
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