Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6360801B2 - - Google Patents
[go: Go Back, main page]

JPS6360801B2 - - Google Patents

Info

Publication number
JPS6360801B2
JPS6360801B2 JP16351285A JP16351285A JPS6360801B2 JP S6360801 B2 JPS6360801 B2 JP S6360801B2 JP 16351285 A JP16351285 A JP 16351285A JP 16351285 A JP16351285 A JP 16351285A JP S6360801 B2 JPS6360801 B2 JP S6360801B2
Authority
JP
Japan
Prior art keywords
charge
ore
furnace
coke
thickness ratio
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
JP16351285A
Other languages
Japanese (ja)
Other versions
JPS6223913A (en
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 filed Critical
Priority to JP16351285A priority Critical patent/JPS6223913A/en
Publication of JPS6223913A publication Critical patent/JPS6223913A/en
Publication of JPS6360801B2 publication Critical patent/JPS6360801B2/ja
Granted legal-status Critical Current

Links

Landscapes

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

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、マイクロ波センサーを利用した装入
物分布制御を実施する高炉操業法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a blast furnace operating method that implements burden distribution control using microwave sensors.

〔従来技術〕[Prior art]

ムーバブルアーマーや旋回シユートを装備した
高炉において、装入物分布制御は、高炉の安定操
業に不可決の手段であるが、オイルレス操業下に
おいてはその重要性はさらに増大し、装入物分布
制御の精度向上のための努力がはらわれている。
従来から実施されている装入物分布制御は、高炉
シヤフト部に設置されているシヤフトゾンデのガ
ス温度、ガス組成を基に、ムーバブルアーマーや
旋回シユートを動かす方法であり、装入物分布の
結果として決まるガス流れを間接的に検出してい
るためにその制御精度はよくなかつた。
In blast furnaces equipped with movable armor and rotating chute, charge distribution control is an essential means for stable operation of the blast furnace, but its importance becomes even more important under oil-less operation. Efforts are being made to improve the accuracy of
The conventional charge distribution control is a method of moving movable armor and rotating chute based on the gas temperature and gas composition of the shaft sonde installed in the blast furnace shaft. The control accuracy was poor because the determined gas flow was detected indirectly.

これに対して、分布制御精度を向上させるため
には装入物分布例えば鉱石とコークスの層厚比等
を直接検知してフイードフオワード的にムーバブ
ルアーマーや旋回シユートを動かす必要があると
の認識から、特開昭56−142809号公報に見られる
ように磁気検出用素子を装入物内に位置させてこ
れから得られる装入物の層厚比や混在率等の情報
を利用する手段がある。
On the other hand, in order to improve distribution control accuracy, it is necessary to directly detect the charge distribution, such as the layer thickness ratio of ore and coke, and move the movable armor and rotating chute in a feed forward manner. From this recognition, as seen in Japanese Patent Application Laid-Open No. 56-142809, there is a means to place a magnetic detection element in the charge and use information such as the layer thickness ratio and mixing ratio of the charge obtained from this. be.

一方、マイクロ波を装入物情報検知手段として
用いることは、実開昭56−151958号公報などに高
炉に装入された装入物の表面形状を測定するもの
が示されているが、これはプロフイルを検出する
だけのものである。
On the other hand, the use of microwaves as a means for detecting charge information is shown in Utility Model Application Publication No. 56-151958, etc., for measuring the surface shape of charge charged into a blast furnace. is only for detecting profiles.

磁気を利用して装入物の層厚比や混在率などの
情報によつて分布制御する制御精度には一応の効
果は期待できる。しかし、ガス流れを決定する装
入物分布は、鉱石とコークスの層厚比だけではな
く、装入物の粒度が大きな構成要素となつてお
り、上述したセンサーなどでは鉱石とコークスの
層厚比が検出できるのみで装入物の粒度を検出で
きないので、制御精度向上には限界があつた。
The accuracy of control, which uses magnetism to control the distribution based on information such as the layer thickness ratio and mixture ratio of the charges, can be expected to have some effect. However, the charge distribution that determines the gas flow is not only determined by the layer thickness ratio between ore and coke, but also by the grain size of the charge. However, the particle size of the charge could not be detected, so there was a limit to the improvement of control accuracy.

第6図は、シヤフト上部の壁際のガス温度をセ
ンサーとした従来の制御であるが、図において、
○アは180゜側のガス温度が低下した時期、○イは180゜
側の鉱石とコークスの層厚比を低下させるアクシ
ヨンをとつた時期を示す。この図からも明らかな
ように180゜側のガス温度が低下してからでないと
旋回シユートによるこの箇所への鉱石落下量を少
なくしてやることができないので、円周方向のア
ンバランスが生じる期間が発生してしまうことが
わかる。なお同様に炉中心部における場合も第7
図に例示する。図において中心部のシヤフトゾン
デのガス温度が適正範囲をはずれる期間が発生し
ているが、この理由は、鉱石とコークスの層厚比
のみを検出する従来の方法ではこの値が低くても
装入物の粒度が小さいとガス流れが抑制される場
合があり、また逆に鉱石とコークスの層厚比が高
くても装入物粒度が大きければガス流れが抑制さ
れない場合が生じるからである。
Figure 6 shows conventional control using a sensor that measures the gas temperature near the wall at the top of the shaft.
○A indicates the period when the gas temperature on the 180° side decreased, and ○B indicates the period when an action was taken to reduce the layer thickness ratio of ore and coke on the 180° side. As is clear from this figure, it is not possible to reduce the amount of ore falling to this location by the rotating chute until the gas temperature on the 180° side has decreased, so a period of circumferential imbalance occurs. I know what you're going to do. Similarly, in the case of the center of the furnace, the seventh
An example is shown in the figure. In the figure, there is a period when the gas temperature of the shaft sonde in the center is out of the appropriate range. This is because if the particle size of the charge is small, the gas flow may be suppressed, and conversely, even if the layer thickness ratio of ore and coke is high, if the charge particle size is large, the gas flow may not be suppressed.

〔発明の目的〕[Purpose of the invention]

本発明は従来のこれらの問題に対し、制御精度
を更に高めた実用的に有用な情報を得る手段を提
案するものである。
The present invention solves these conventional problems by proposing a means for obtaining practically useful information with further improved control accuracy.

〔発明の構成〕[Structure of the invention]

本発明の要旨とするところは高炉炉口部の装入
物内における炉円周方向或いは炉半径方向の適宜
位置に挿入したマイクロ波センサーより各測定点
における鉱石とコークスの層厚比および装入物の
粒度をそれぞれ検出し、これらの検出された情報
にもとずいて装入物の分布制御を行なうことにあ
る。以下にその詳細を図示例にもとずいて述べ
る。
The gist of the present invention is to measure the layer thickness ratio of ore and coke at each measurement point and the charge amount using a microwave sensor inserted at an appropriate position in the furnace circumferential direction or furnace radial direction within the charge at the mouth of the blast furnace. The purpose is to detect the particle size of each material and control the distribution of the charging material based on the detected information. The details will be described below based on illustrated examples.

本発明においては鉱石とコークスの層厚比およ
び装入物の粒度を同時に検出するセンサーとして
マイクロ波を利用する。例えば装入物の層内に挿
入されているプローブからマイクロ波を層内へ送
信したときに鉱石層とコークス層ではその透過性
能や反射性能が異なることは原理的には知られて
いるが、本発明ではそれ自体は公知のマイクロ波
センサーを搭載したプローブを高炉炉口部に挿入
する。
In the present invention, microwaves are used as a sensor that simultaneously detects the layer thickness ratio of ore and coke and the particle size of the charge. For example, it is known in principle that when microwaves are transmitted into the layer from a probe inserted into the layer of a charge, the transmission and reflection performance of the ore layer and the coke layer are different. According to the invention, a probe equipped with a microwave sensor, which is known per se, is inserted into the blast furnace mouth.

第1図はそれの一態様を示したもので、高炉炉
口部の縦断面を示す概念図である。第1図aにお
いて1は炉壁、2は炉芯部、3は装入物で4は装
入物表面を示す。5はプローブ、6はマイクロ波
送受信器、7は信号処理装置である。図示例では
プローブ5の挿入位置である、装入物3の深さ方
向の高さHは、通常装入物1チヤージ分の位置で
あり、炉芯2側に向つての挿入深さL詳しくはレ
ンガ稼動面からの距離は通常300〜1000mm程度で
ある。
FIG. 1 shows one aspect of this, and is a conceptual diagram showing a vertical cross section of the mouth of the blast furnace. In FIG. 1a, 1 is the furnace wall, 2 is the furnace core, 3 is the charge, and 4 is the surface of the charge. 5 is a probe, 6 is a microwave transceiver, and 7 is a signal processing device. In the illustrated example, the height H in the depth direction of the charge 3, which is the insertion position of the probe 5, is normally the position corresponding to one charge of the charge, and the insertion depth L toward the furnace core 2 side is The distance from the brick working surface is usually about 300 to 1000 mm.

これらのプローブ5によつて炉の円周方向のバ
ランスをコントロールする場合は複数本が炉円周
方向に略々等間隔に挿入される。これを第2図の
炉平面概念図で例示する。この例では4本のプロ
ーブを円周方向に90度づつずらして配設した場合
である。このほか45度づつずらして8本挿入して
更に精度をあげるとよい。
When controlling the balance in the circumferential direction of the furnace using these probes 5, a plurality of probes are inserted at approximately equal intervals in the circumferential direction of the furnace. This is illustrated in the conceptual plan view of the furnace in FIG. In this example, four probes are arranged circumferentially offset by 90 degrees. In addition, it is a good idea to insert 8 pieces at 45 degree intervals to further improve accuracy.

次にこれらプローブ5の横断面の基本構造を第
3図の概念図で示す。第3図aは1箇所に1本の
プローブで送信口8が1個、受信口が2個組込ま
れたものである。また、第3図bは1箇所に2本
を1セツトとして設けたものでそれぞれ送信口8
が1個、受信口9が1個組込まれたものである。
Next, the basic cross-sectional structure of these probes 5 is shown in the conceptual diagram of FIG. In FIG. 3a, one transmitting port 8 and two receiving ports are incorporated in one probe in one location. In addition, Fig. 3b shows a set of two wires installed at one location, each with a transmitting port 8.
One receiving port 9 is incorporated.

マイクロ波は送受信器6により、プローブ送信
口8から炉内に送信され、装入物3を透過したも
のは受信口9を通つて、また反射されたものは送
信口8を通つて、送受信器6に達する。透過或い
は反射されたマイクロ波の強度は送受信器6によ
つて検出する。検出された信号の処理はそれ自体
は既知の手段で行ない、鉱石とコークスの層厚比
および装入物の粒度を下記の計算により述める。
Microwaves are transmitted into the furnace from the probe transmission port 8 by the transceiver 6, those that have passed through the charge 3 are transmitted through the reception port 9, and those that have been reflected are transmitted through the transmission port 8 to the transceiver. Reach 6. The intensity of the transmitted or reflected microwave is detected by the transceiver 6. The processing of the detected signals is carried out by means known per se, and the ore to coke thickness ratio and the grain size of the charge are determined by the following calculations.

透過波の強度は装入物が鉱石の場合の方がコー
クスの場合と較べて大きく、装入物の降下に従つ
て上、下受信口を通つてきた透過波強度の時間変
化は第8図のようになる。第8図において、Tc
は装入物がコークスである期間、T0は装入物が
鉱石である期間を示し、T0/Tcを計算すること
により、鉱石とコークスの層厚比を述める。
The intensity of the transmitted waves is greater when the charge is ore than when it is coke, and the time change in the intensity of the transmitted waves that have passed through the upper and lower receiving ports as the charge descends is shown in Figure 8. become that way. In Figure 8, Tc
indicates the period during which the charge is coke, T 0 indicates the period during which the charge is ore, and by calculating T 0 /Tc, the layer thickness ratio of ore and coke is stated.

また、反射波の強度は第9図のようになり生信
号と平滑化信号の交点を数えるクロスポイントカ
ウント法で求めた単位時間当りのピーク数nと第
8図のΔtと上下受信口間距離lから粒度l/
Δt・nの計算により求める。
In addition, the intensity of the reflected wave is as shown in Figure 9, and the number of peaks per unit time n determined by the cross-point counting method that counts the intersections of the raw signal and the smoothed signal, Δt in Figure 8, and the distance between the upper and lower receiving ports. l to particle size l/
Obtained by calculating Δt·n.

このようにして得られた炉円周方向の各測定点
における鉱石とコークスの層厚比および装入物の
粒度情報について、相対的にバランスがくずれて
いたら、バランスがとれるようにムーバブルアー
マー或いは旋回シユートなどによる装入物の装入
条件をコントロールする。すなわち、円周方向の
ある箇所において、鉱石とコークスの層厚比が高
い、または装入物粒度が小さい、あるいはこの両
方が同時に起ると、この箇所のガス流れが抑制さ
れ、還元伝熱が遅れるため、装入物が停滞した
り、付着物に成長して降下不良、通気性不良を引
き起こし安定操業が阻害されてしまう。そこで上
述したアンバランスが生じたときは、ムーバブル
アーマーの円周方向の押し出し角度を変更した
り、旋回シユートにより円周方向の落下量を変え
たりしてアンバランスを解消することにより安定
操業を継続することができる。
If the layer thickness ratio of ore and coke and particle size information of the charge obtained at each measurement point in the circumferential direction of the furnace are relatively unbalanced, moveable armor or rotating Controls charging conditions using chute, etc. In other words, if the layer thickness ratio between ore and coke is high, the grain size of the charge is small, or both occur at the same time at a certain point in the circumferential direction, the gas flow at this point is suppressed and the reductive heat transfer is inhibited. Due to the delay, the charge may stagnate or grow into deposits, causing poor descent and poor ventilation, which impede stable operation. Therefore, when the above-mentioned unbalance occurs, stable operation can be maintained by resolving the unbalance by changing the extrusion angle of the movable armor in the circumferential direction or changing the amount of fall in the circumferential direction using a rotating chute. can do.

以上に説明したようにガスの流れを敏速に、か
つ精度よくキヤツチするには鉱石とコークスの層
厚比および装入物粒度の両方の情報が必要であ
る。また円周方向に複数本設置する理由は、円周
バランスを制御するためであるが、円周バランス
がとれているときは、周辺部を制御しておけば高
炉は安定しているという事実に基く。なお、前記
円周バランスを制御する場合の外、炉半径方向の
制御にも同様に適用できる。即ち、前述のマイク
ロ波センサーを高炉に設置されているシヤフトゾ
ンデに搭載し、半径方向の鉱石とコークスの層厚
比および装入物の粒度を検出し、これらの情報が
半径方向に最適な分布となるようにムーバブルア
ーマーや旋回シユートを動かすことにより、高炉
を安定的に効率向上させる操業ができる。
As explained above, in order to catch the gas flow quickly and accurately, information on both the layer thickness ratio of ore and coke and the particle size of the charge is necessary. Also, the reason why multiple tubes are installed in the circumferential direction is to control the circumferential balance, but when the circumference is balanced, the blast furnace will be stable if the peripheral area is controlled. Based. In addition to controlling the circumferential balance, the present invention can be similarly applied to controlling the furnace radial direction. That is, the aforementioned microwave sensor is mounted on a shaft sonde installed in a blast furnace to detect the layer thickness ratio of ore and coke in the radial direction and the particle size of the charge, and this information is used to determine the optimal distribution in the radial direction. By moving the movable armor and rotating chute in such a way, it is possible to operate the blast furnace stably and improve its efficiency.

例えば半径方向の中心部において、鉱石とコー
クスの層厚比が高い、または装入物粒度が小さ
い。あるいはこの両方が同時に起ると、中心部の
ガス流れが抑制され、還元伝熱が遅れるため、融
着帯低下による装入物降下不良、通気不良を引き
起し、安定操業が阻害されてしまう。よつて、中
心部のガス流れを促進するために、ムーバブルア
ーマーあるいは旋回シユートにより、中心部への
鉱石装入量を少なくしたり、細粒の装入量を減少
することにより安定操業を継続することができ
る。
For example, in the radial center the ore to coke thickness ratio is high or the charge particle size is small. Or, if both of these occur simultaneously, the gas flow in the center is suppressed and reduction heat transfer is delayed, resulting in poor lowering of the charge due to the lowering of the cohesive zone and poor ventilation, which impedes stable operation. . Therefore, in order to promote gas flow in the center, stable operation can be maintained by reducing the amount of ore charged into the center by using a movable armor or rotating chute, and by reducing the amount of fine particles charged. be able to.

〔実施例〕〔Example〕

第4図は本発明による炉円周バランス制御の場
合の実施例を示す。図において○アは90゜側の鉱石
粒度低下時期、○イ90゜側の鉱石とコークスの層厚
比を低下させるアクシヨンをとつた時期、であ
る。プローブ5の挿入は第1図aおよび第2図に
もとずき高さHは装入物表面から高さ方向に350
mm装入物内に入つた位置、挿入深さLはレンガ稼
動面から350mmである。4本のプローブに搭載し
たセンサー情報のうち、鉱石とコークスの層厚比
は管理範囲に入つているが、90゜側の装入物粒度
が小さくなつたため、旋回シユートによりこの箇
所への鉱石落下量を少なくし円周バランスを解消
した。円周バランスの結果は、シヤフト上部の壁
際のガス温度でみているが、管理範囲におさまつ
ていることがわかる。本実施例では、装入物の粒
度が小さくなつた箇所の鉱石とコークスの層厚比
を小さくしたが、鉱石の粒度別装入を実施してい
る高炉であれば、この箇所への細粒の量を減らし
てやることもできる。また第5図は本発明の他の
側で炉半径方向の制御をした場合を示す。図にお
いて○アは中心部の鉱石粒度が低下した時期、○イは
中心部の鉱石とコークスの層厚比を低下させるア
クシヨンをとつた時期である。シヤフトゾンデ
5′の挿入は第1図bにもとずき高さHは周辺部
において、装入物表面から高さ方向に400mm装入
物に入つた位置、挿入深さL′は炉芯部まで5500mm
である。中心部におけるセンサー情報のうち、鉱
石とコークスの層厚比は管理範囲に入つている
が、装入物粒度が小さくなつたため、ムーバブル
アーマーより、中心部への鉱石装入量を少なくし
て中心流を確保した。結果はシヤフトゾンデの中
心部のガス温度でみているが、管理範囲におさま
つている。
FIG. 4 shows an embodiment of furnace circumferential balance control according to the present invention. In the figure, ○A is the time when the ore particle size decreases on the 90° side, and ○B is the time when an action is taken to reduce the layer thickness ratio of ore and coke on the 90° side. The insertion of the probe 5 is based on Figures 1a and 2, and the height H is 350 mm in the height direction from the surface of the charge.
The insertion depth L, which is the position inserted into the mm charge, is 350 mm from the brick operating surface. Among the sensor information mounted on the four probes, the layer thickness ratio of ore and coke is within the control range, but since the grain size of the charge on the 90° side has become smaller, the ore is not allowed to fall to this location by the rotating chute. The amount was reduced and the circumferential balance was resolved. The circumferential balance results are measured by the gas temperature near the wall at the top of the shaft, and it can be seen that the temperature is within the control range. In this example, the layer thickness ratio between the ore and coke was reduced at the location where the grain size of the charge became small, but if the blast furnace is charging ore by grain size, fine grains would be added to this location. You can also reduce the amount. FIG. 5 shows another aspect of the present invention in which the furnace is controlled in the radial direction. In the figure, ○A is the period when the grain size of the ore in the center decreased, and ○B is the period when an action was taken to reduce the layer thickness ratio between the ore and coke in the center. The insertion of the shaft sonde 5' is based on Figure 1b, the height H is at the periphery, 400 mm from the charge surface in the height direction into the charge, and the insertion depth L' is at the furnace core. up to 5500mm
It is. Among the sensor information in the center, the layer thickness ratio of ore and coke is within the control range, but because the particle size of the charge has become smaller, the amount of ore charged to the center has been reduced compared to movable armor. The flow was secured. The results are measured by the gas temperature at the center of the shaft sonde, which is within the control range.

〔発明の効果〕〔Effect of the invention〕

以上の如く、円周方向の鉱石とコークスの層厚
比および装入物の粒度のバランスを検出し、バラ
ンスがとれるようにムーバブルアーマーや旋回シ
ユートを動かすことにより高炉を安定的に効率向
上させる操業が可能となつた。
As described above, operations that stably improve blast furnace efficiency by detecting the thickness ratio of ore and coke in the circumferential direction and the balance of particle size of the charge, and moving the movable armor and rotating chute to achieve the balance. became possible.

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

第1図aは本発明によるプローブ挿入状態を示
す縦断面概念図、第1図bは本発明によるシヤフ
トゾンデ挿入状態を示す縦断面概念図、第2図は
本発明による円周バランス制御用のプローブ挿入
状態を示す平面概念図、第3図aは本発明に用い
たプローブの断面説明図で1本構成の例、第3図
bは他の例で2本1組構成した場合、第4図は本
発明による炉円周バランス制御の実施例説明図、
第5図は本発明による炉半径方向制御の実施例説
明図、第6図および第7図は従来法による比較例
の説明図、第8図及び第9図は透過波および反射
波の時間変化を示す図である。 1…炉壁、2…炉芯、3…装入物、5…プロー
ブ、6…マイクロ波送受信器、7…信号処理装
置、8…送信口、9…受信口。
FIG. 1a is a conceptual longitudinal cross-sectional view showing a probe inserted state according to the present invention, FIG. 1b is a vertical cross-sectional conceptual diagram showing a shaft sonde inserted state according to the present invention, and FIG. 2 is a conceptual longitudinal cross-sectional view showing a probe insertion state according to the present invention. FIG. 3a is a cross-sectional explanatory diagram of the probe used in the present invention, showing an example in which one probe is configured, FIG. 3b is another example in which two probes are configured in a set, and FIG. is an explanatory diagram of an embodiment of furnace circumferential balance control according to the present invention,
Fig. 5 is an explanatory diagram of an embodiment of furnace radial direction control according to the present invention, Figs. 6 and 7 are explanatory diagrams of a comparative example using the conventional method, and Figs. 8 and 9 are temporal changes in transmitted waves and reflected waves. FIG. DESCRIPTION OF SYMBOLS 1... Furnace wall, 2... Furnace core, 3... Charge, 5... Probe, 6... Microwave transceiver, 7... Signal processing device, 8... Transmission port, 9... Receiving port.

Claims (1)

【特許請求の範囲】[Claims] 1 高炉炉口部の装入物内における炉円周方向或
いは炉半径方向の適宜位置に挿入したマイクロ波
センサーより各測定点における鉱石とコークスの
層厚比および装入物の粒度をそれぞれ検出し、こ
れらの検出された情報にもとずいて装入物の分布
制御を行なうことを特徴とする高炉操業法。
1 The layer thickness ratio of ore and coke and the particle size of the charge at each measurement point are detected by a microwave sensor inserted at an appropriate position in the furnace circumferential direction or furnace radial direction within the charge at the mouth of the blast furnace. , a blast furnace operating method characterized by controlling the distribution of the charge based on the detected information.
JP16351285A 1985-07-24 1985-07-24 Operating method for blast furnace Granted JPS6223913A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16351285A JPS6223913A (en) 1985-07-24 1985-07-24 Operating method for blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16351285A JPS6223913A (en) 1985-07-24 1985-07-24 Operating method for blast furnace

Publications (2)

Publication Number Publication Date
JPS6223913A JPS6223913A (en) 1987-01-31
JPS6360801B2 true JPS6360801B2 (en) 1988-11-25

Family

ID=15775271

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16351285A Granted JPS6223913A (en) 1985-07-24 1985-07-24 Operating method for blast furnace

Country Status (1)

Country Link
JP (1) JPS6223913A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0569501U (en) * 1992-02-21 1993-09-21 株式会社ホクシン Charcoal stove for leisure

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5155259B2 (en) * 2009-07-13 2013-03-06 新日鐵住金株式会社 Coal particle size measurement system, method and program
LU92351B1 (en) * 2014-01-09 2015-07-10 Tmt Tapping Measuring Technology Sarl Method and probe for determining the material distribution in a blast furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0569501U (en) * 1992-02-21 1993-09-21 株式会社ホクシン Charcoal stove for leisure

Also Published As

Publication number Publication date
JPS6223913A (en) 1987-01-31

Similar Documents

Publication Publication Date Title
US5961214A (en) Determining protective layer thickness of blast furnaces
JP7176561B2 (en) Blast furnace operation method
EP3092321B1 (en) Method and probe for determining the material distribution in a blast furnace
JP5387066B2 (en) Blast furnace gas flow distribution estimation method, blast furnace gas flow distribution estimation device, and blast furnace gas flow distribution estimation program
JPS6360801B2 (en)
JP3855639B2 (en) Profile measurement method of blast furnace interior entrance surface
JP6547474B2 (en) Blast furnace and measurement method for measuring the level of blast furnace charge
JPS5850290B2 (en) Sonde for measuring electrical resistance of contents in reduction melting furnace
JP3514120B2 (en) Distribution control method of blast furnace top charge
JPH0598324A (en) Method for counting charging time of raw material in bell-less blast furnace charging device
JP2017150035A (en) Display method for blast furnace profile meter, and method for charging material to be charged in blast furnace
JPH05186811A (en) Method for operating blast furnace
JPS63243215A (en) Method for operating blast furnace
JPS62235404A (en) Detection of behavior of charge in vertical type furnace
JP7594490B2 (en) Device for measuring pile shape of blast furnace charge and blast furnace
JPH0525518A (en) Method of detecting flow mode of blast furnace interior contents using microwave
JPS6191307A (en) Detection of descending of charge in blast furnace
JPS5862570A (en) Detection of falling speed distribution for charge in blast furnace
JPS599116A (en) Method for measuring inside of blast furnace
JPH06271916A (en) Measuring method of slag level in blast furnace
CA2383538A1 (en) Method for determining the trajectory of materials when charging a shaft kiln
JPS58197207A (en) Detection of channeling of charge in vertical chute part of charger for blast furnace
JPS6129674A (en) Method of detecting extraneous matter on inner wall of vertical type furnace
JPS6116405B2 (en)
JPS55134115A (en) Furnace center position estimating method of blast furnace