JPS6147535A - Apparatus for controlling feeding of shaft furnace coke - Google Patents

Apparatus for controlling feeding of shaft furnace coke

Info

Publication number
JPS6147535A
JPS6147535A JP16938484A JP16938484A JPS6147535A JP S6147535 A JPS6147535 A JP S6147535A JP 16938484 A JP16938484 A JP 16938484A JP 16938484 A JP16938484 A JP 16938484A JP S6147535 A JPS6147535 A JP S6147535A
Authority
JP
Japan
Prior art keywords
weighing
coke
cutting
value
material loading
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
JP16938484A
Other languages
Japanese (ja)
Other versions
JPH0380834B2 (en
Inventor
Yoshifumi Shimizu
清水 喜文
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.)
Yaskawa Electric Corp
Original Assignee
Yaskawa Electric Manufacturing Co 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 Yaskawa Electric Manufacturing Co Ltd filed Critical Yaskawa Electric Manufacturing Co Ltd
Priority to JP16938484A priority Critical patent/JPS6147535A/en
Publication of JPS6147535A publication Critical patent/JPS6147535A/en
Publication of JPH0380834B2 publication Critical patent/JPH0380834B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B31/00Charging devices

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Sampling And Sample Adjustment (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Coke Industry (AREA)
  • Blast Furnaces (AREA)
  • Flow Control (AREA)

Abstract

PURPOSE:To enable the accurate measurement of the moisture of coke, the accurate weighing of necessary quantity and the batchwise charging classified by particle size of coke into a furnace, by hourly calculating the stock coke loading quantity and weighed residual quantity value on a belt conveyor and stopping a feeding apparatus at the point of time when the difference between both of them reached predetermined quantity or less. CONSTITUTION:Estimated values over several past batches of the feeding apparatus indicated by a feeding apparatus indication signal S1 are averaged to be outputted as the feeding speed VF of a lately batch. Next, the signal showing this feeding speed VF is inputted to the stock material loading quantity operation part 13 on BC3 to hourly operate the stock material loading quantity WR on BC3 and the operated value is inputted to a feeding stop timing control part 14. This feeding stop timing control part 14 operates a weighed residual quantity value WS from the weighing objective quantity WTGT set by a weighing objective value indication signal S2 and the weighed value W in a weighing hopper 4 and outputs a feeding stop signal S3 at the point of time when the difference WS-WR of the weighed residual quantity value WS and the stock material loading quantity WR transmitted from the stock material loading quantity operation part 13 on BC3 came to WS-WR<=C. By this method, the feeding apparatus is stopped.

Description

【発明の詳細な説明】 [技術分!!7] 本発明は、高炉コークス切出秤量設備に関する。[Detailed description of the invention] [Technology! ! 7] The present invention relates to blast furnace coke cutting and weighing equipment.

[従来技術] 第2図は公知の高炉コークス切出秤量設備の概略図であ
る。各貯肢槽11〜14には互1zlこ銘柄の異なるコ
ークスが貯蔵され、また貯骸槽11〜14のそれぞれに
切出装置21〜24が設置されており、所望の銘柄のコ
ークスが対応する切出装置により切出され、ベルトコン
ベア(以下、BCとする)3によって輸送されて、秤量
ホッパ4で秤量される。(以下、この秤量の工程をパッ
チと呼ぶ) 従来、秤量の時間を短縮しかつ秤量の精度を向上させる
ため、秤量した値が目標値からある範囲内に達した(通
常は目標値の85%)時点で、切出装置21〜24を停
止し、BC3を高速から低速に切替え、さらに秤量値が
目標値になった時点でBC3を停止していた。
[Prior Art] FIG. 2 is a schematic diagram of a known blast furnace coke cutting and weighing equipment. Different brands of coke are stored in each of the storage tanks 11 to 14, and cutting devices 21 to 24 are installed in each of the storage tanks 11 to 14, so that a desired brand of coke can be stored. It is cut out by a cutting device, transported by a belt conveyor (hereinafter referred to as BC) 3, and weighed by a weighing hopper 4. (Hereinafter, this weighing process will be referred to as patching.) Conventionally, in order to shorten the weighing time and improve the accuracy of weighing, the weighed value has reached within a certain range from the target value (usually 85% of the target value). ), the cutting devices 21 to 24 were stopped, the BC3 was switched from high speed to low speed, and when the weighed value reached the target value, the BC3 was stopped.

この方法では、コークスは目標値まで秤量されるが、停
止したBC3の上にはコークスの残り5が生じてしまう
、このようにして、前回のバッチでもBO2の上にコー
クスが残っていたはずであるから、今回のバッチの秤量
ホッパ4の内には、前回の/へンチでBO3の上に残さ
れたコークス6と今回のバンチで切出されたコークス7
とが混在することになる。従って、今回のバッチのコー
クスの銘柄が前回のバッチのコークスの銘柄と異なる場
合には1次の3つの問題点があった。すなわち。
In this method, the coke is weighed to the target value, but there is still 5 coke left on top of the stopped BC3.In this way, there should have been some coke left on top of BO2 in the previous batch as well. Therefore, in the weighing hopper 4 of this batch, there are coke 6 left on top of BO3 in the previous batch and coke 7 cut out in this batch.
There will be a mixture of Therefore, if the brand of coke in the current batch is different from the brand of coke in the previous batch, there are the following three problems. Namely.

■コークスはその銘柄ごとに異なる水分含有率αを有し
ているので、中性子水分計8によって今回のバッチのコ
ークスの銘柄の水分′測定を正確に行なうことができな
かった。
-Since each brand of coke has a different moisture content α, it was not possible to accurately measure the moisture content of the brands of coke in this batch using the neutron moisture meter 8.

■コークスの必要量はまず乾量(水分を含まない量)で
与えられ、この乾量値W2にコークス内の水分を加えた
値を秤量目標値WTGrとするので、秤量目標値WTg
Tは の式で決定され、水分含有率αが異なる異銘柄のコーク
スが秤量ホッパ4内で混在すれば、秤量目標値W1まで
秤量しても必要な乾量値WsRtが得られなかった1 、′■異銘柄のコークスが秤量ホッパ内に混在するため
、粒度の異なるコークスが同時に炉内に装入されて、炉
内のガス流分布が乱れ、炉の局所的な異常や全体的な炉
況悪化に結びついて操業成績が悪くなっていた。
■The required amount of coke is first given as a dry amount (amount that does not include moisture), and the value obtained by adding the moisture in the coke to this dry amount value W2 is set as the weighing target value WTGr, so the weighing target value WTg
T is determined by the formula, and if different brands of coke with different moisture contents α are mixed in the weighing hopper 4, the required dry weight value WsRt cannot be obtained even if the coke is weighed up to the target weighing value W1. ′■ Because different brands of coke are mixed in the weighing hopper, coke with different particle sizes are charged into the furnace at the same time, which disrupts the gas flow distribution in the furnace, causing local abnormalities in the furnace and overall furnace condition. This led to deterioration in operational performance.

[発明の目的] 本発明の目的は、秤量したコークスに混在する前回のバ
ッチのコークスの量を削減して、コークスの正確な水分
測定、コークスの必要量の正確な秤量およびバッチごと
の炉内への粒度別装入を可能とする高炉コークス切出制
御装置を提供することにある。
[Object of the Invention] The object of the present invention is to reduce the amount of coke from the previous batch mixed in weighed coke, to accurately measure the moisture content of coke, accurately weigh the required amount of coke, and to reduce the amount of coke in the furnace for each batch. An object of the present invention is to provide a blast furnace coke cutting control device that enables charging of coke according to particle size.

[発明の構成1 本発明は、ベルトコンベア上の原料搭載量と秤量残量値
(=秤量目標値−秤量ホッパで測定した秤量値)を時々
刻々求め、秤量残量値と原料搭載量の差が所定量以下に
なった時点で当該切出装置を停止させるようにしたもの
である。
[Configuration 1 of the Invention] The present invention calculates the amount of raw material loaded on the belt conveyor and the weighed remaining amount value (= target weighing value - the weighed value measured by the weighing hopper) from time to time, and calculates the difference between the weighed remaining amount value and the loaded material amount. The cutting device is stopped when the amount becomes less than a predetermined amount.

すなわち、本発明の高炉コークス切出制御装置は、Lf
ffi速度から求められた切出速度と切出開始から現時
点までの経過時間の積と秤量ホッパの現時点の秤量値か
らベルトコンベア上のコークス搭載量を演算する原料搭
載量演算手段と、秤量目標値に対する秤量残量値からこ
の原料搭載量演算手段で演算したコークス搭載量を減算
し、この減算結果が所定量以下になったときに当該切出
装置に切出停旧信号を出力する切出伴出タイミング制御
手段を備えたことを特徴とする。
That is, the blast furnace coke cutting control device of the present invention has Lf
A raw material loading amount calculation means for calculating the amount of coke loaded on the belt conveyor from the product of the cutting speed obtained from the ffi speed and the elapsed time from the start of cutting to the current time and the current weighing value of the weighing hopper, and a weighing target value. A cut-off mechanism that subtracts the loaded coke amount calculated by the raw material loaded amount calculation means from the weighed remaining amount value for the weight, and outputs a cut-off stop old signal to the cut-out device when the subtraction result becomes less than a predetermined amount. It is characterized by being equipped with output timing control means.

本発明の実施態様は、特許請求の範囲に記載の装置にお
いて、秤量ホッパがコークスを秤量した秤量速度を演算
する秤量速度演算手段と、前記秤量速度演算手段で演算
された秤量速度から当該切出装置の切出速度の推定値を
求めて内部に記憶するとともに、内部に記憶されている
当該切出装置の過去数バッチの前記推定値の平均値を演
算して今回の1<ツチの切出速度として出力する切出速
度演算手段とを、さらに備えてなる装置である。
An embodiment of the present invention is an apparatus according to the claims, which includes a weighing speed calculation means for calculating a weighing speed at which the weighing hopper weighs coke, and a weighing speed calculation means for calculating the weighing speed at which the coke is weighed by the weighing hopper, and a weighing speed calculated by the weighing speed calculation means. The estimated value of the cutting speed of the device is calculated and stored internally, and the average value of the estimated values of the past several batches of the cutting device is calculated to determine the current cutting speed of 1<T. The apparatus further includes a cutting speed calculating means for outputting the cutting speed as a speed.

[実施例1 次に、本発明の実施例について図面を参照、しながら説
明する。
[Example 1] Next, an example of the present invention will be described with reference to the drawings.

第1図は本発明の一実施例に係る高炉コークス切出〃制
御装置を備えた高炉コークス切出秤量設備のブロック図
である。
FIG. 1 is a block diagram of a blast furnace coke cutting and weighing equipment equipped with a blast furnace coke cutting control device according to an embodiment of the present invention.

秤量速度演算部11は各バッチ終了時に、秤量ホッパ4
で測定した秤量値Wを出力し、その秤量値Wと秤量に要
した時間から各バッチの秤量速度υWを演算し出力する
。切出速度演算部12は、各バッチごとに不図示の制御
盤から切出装置指定信号S五を入力し、各バッチ終了時
には、予めわかっている各切出装置21〜24の切出能
力比と秤量速度演算部11で演算された秤量速度Vwか
ら切出装置指定信号Siによって指定された切出装置の
切出速度の推定値を求めて、この推定値を内部に記憶す
るとともに、内部に記憶されている、切出装置指定信号
S1により指定される切出装置の過去数パッチの前記推
定値の平均値(移動平均、指数平均部)を演算して今回
のバッチの切出速度υFとして出力する。 Be上原料
搭載量演算部13は、切出速度演算部12から出力され
た切出速度’l/F(初回のバッチは設定値)と今回の
バッチの切出開始から現時点までの経過時間1F との
積をとり、この積と秤量ホッパ4で測定された今回のバ
ッチの現時点の秤量値Wとの差をとって、これをEC3
の原料搭載量WRとし出力する。切出停止タイミング制
御部14は前記の不図示の制御盤からトf叶目標値指定
信号S2を入力し、秤量目標値指定信号S2によって指
定される秤量目標値WTcrと秤量ホッパ4で測定され
た秤量値Wとの差をとってこれを秤量残量値Wsとし、
この秤量残量値WsとBe上原料搭載量演算部13で演
算された原料搭I&、量WRの差が、Ws−WR≦Cの
関係を満たすようになった時点で、当該切出装置へ切出
停止信号S3を出力して切出装置を停止する。なお。
At the end of each batch, the weighing speed calculation unit 11
The weighing value W measured in is output, and the weighing speed υW of each batch is calculated and output from the weighing value W and the time required for weighing. The cutting speed calculation unit 12 inputs a cutting device designation signal S5 from a control panel (not shown) for each batch, and calculates the cutting capacity ratio of each cutting device 21 to 24, which is known in advance, at the end of each batch. An estimated value of the cutting speed of the cutting device designated by the cutting device designation signal Si is obtained from the weighing speed Vw calculated by the weighing speed calculating section 11, and this estimated value is stored internally. The average value (moving average, exponential average part) of the estimated values of the past few patches of the cutting device designated by the cutting device designation signal S1 that is stored is calculated and set as the cutting speed υF of the current batch. Output. The Be fine raw material loading amount calculation section 13 calculates the cutting speed 'l/F (set value for the first batch) output from the cutting speed calculation section 12 and the elapsed time 1F from the start of cutting of the current batch to the present time. EC3
The loaded raw material amount WR is output. The cutout stop timing control unit 14 inputs the weight target value designation signal S2 from the control panel (not shown), and calculates the weight target value WTcr specified by the weighing target value designation signal S2 and the weight value measured by the weighing hopper 4. Take the difference from the weighed value W and set this as the weighed remaining amount Ws,
When the difference between this weighed residual amount value Ws and the raw material tower I & amount WR calculated by the Be top raw material loading amount calculating section 13 satisfies the relationship Ws-WR≦C, the cut-out device is The cutting device is stopped by outputting a cutting stop signal S3. In addition.

Cは切出の速度のばらつきによってEC3上の原料F5
 載量W Rに誤差を生じ、切出量が不足することを防
ぐための安全定数である。
C is the raw material F5 on EC3 due to variations in cutting speed.
This is a safety constant to prevent an error in the loading amount WR and an insufficient cutting amount.

次に、本実施例の動作を説明する。Next, the operation of this embodiment will be explained.

所望の銘柄のコークスに対応している切出装置、を指定
する切出装置指定信号S1が切出速度演算部12に、秤
量目標値指定信号S2が切出停止タイミング制御部14
にそれぞれ入力して、切出装置が指定され秤量目標値W
wが設定される。まず、切出速度演算部12は、バッチ
終了時に秤量速度演算部11で演算された秤量速度υW
から求められて、内部に記憶されている。切出装置指定
信号S1により指定された切出装置の過去数バッチにわ
たる推定値の平均をとり、今回のバッチの切出速度υF
として出力する0次に、この切出速度υFを示す信号が
Be上原料搭載量演算部13に入力して、EC3上の原
料搭載量WRが時々刻々@算され、この原料搭載量WR
を示す信号が切出停止タイミング制御部14に入力する
。切出停止タイミング制御部14は、秤量目標値指定信
号S2によって設定された秤量目標値Wwと秤量ホッパ
4での秤量値Wから秤量残量値Wsを演算し、そしてこ
の秤量残量値WsとBC上原料塔a量演算部13から伝
達された原料搭載量WFIの差Ws−WRが、Ws−W
R≦Cとなった時点で、切出停止信号S3を当該切出装
置に出力する。これにより当該切出装置は停止する。こ
のようにして、今回のバッチの秤量が終ると秤量速度演
算部11で今回のパンチの秤量速度υWが演算され、こ
の秤量速度υ1を示す信号が切出速度演算部12に入力
し、ここで切出装置指定信号S1により指定された切出
装置の切出速度の推定値が求められ、この推定値が切出
速度演算部12の内部に記憶されて、以後のパンチにお
ける切出速度υ、の演算に使用される。
A cutting device designation signal S1 that specifies a cutting device corresponding to a desired brand of coke is sent to the cutting speed calculation unit 12, and a weighing target value designation signal S2 is sent to the cutting stop timing control unit 14.
, the cutting device is specified and the target weight value W is input.
w is set. First, the cutting speed calculation section 12 calculates the weighing speed υW calculated by the weighing speed calculation section 11 at the end of the batch.
It is requested from and stored internally. The cutting speed υF of the current batch is calculated by averaging the estimated values of the cutting device specified by the cutting device designation signal S1 over the past several batches.
Next, a signal indicating this cutting speed υF is input to the Be raw material loading amount calculating section 13, and the raw material loading amount WR on the EC3 is calculated every moment.
A signal indicating this is input to the cutting stop timing control section 14. The cutout stop timing control unit 14 calculates a weighing remaining amount value Ws from the weighing target value Ww set by the weighing target value designation signal S2 and the weighing value W in the weighing hopper 4, and calculates the weighing remaining amount value Ws and the weighing remaining amount value Ws. The difference Ws-WR in the raw material loading amount WFI transmitted from the BC upper raw material tower a amount calculation unit 13 is Ws-W
When R≦C, a cutting stop signal S3 is output to the cutting device. This causes the cutting device to stop. In this way, when the weighing of the current batch is finished, the weighing speed υW of the current punch is calculated in the weighing speed calculating section 11, and a signal indicating this weighing speed υ1 is input to the cutting speed calculating section 12, where the weighing speed υW of the current punch is calculated. An estimated value of the cutting speed of the cutting device specified by the cutting device designation signal S1 is obtained, and this estimated value is stored inside the cutting speed calculating section 12, and the cutting speed υ, used for calculations.

このようにして、BO3上の原料搭載量W8を時々刻々
演算しながらコークスの切出を制御するので、秤量完了
時のEC3上のコークスの残りはわずかなものとなる。
In this way, since the cutting of coke is controlled while calculating the raw material loading amount W8 on the BO3 every moment, only a small amount of coke remains on the EC3 when weighing is completed.

しかも、安全定数Cによって、切出量が秤量目標値WW
に至らずに不足することを防止している。従って、切出
量が秤量目標値より不足することはなく、また秤量ホッ
パ4の内に混在する前回のバッチのコークスの紙はわず
かなものとなる。
Furthermore, due to the safety constant C, the cutting amount is reduced to the weighing target value WW.
This prevents shortages without reaching . Therefore, the cutout amount will not fall short of the target weighing value, and only a small amount of coke paper from the previous batch will be mixed in the weighing hopper 4.

〔発明の効果J 以上説明したように本発明によれば、バッチ終了時にE
C3状に残るコークスの量が少なく、前回のバッチのコ
ークスの銘柄と今回のバッチのコークスの銘柄とが異な
る場合でも、秤量したコークスに混在する異銘柄のコー
クス量はわずかなものとなる。したがって、中性子水分
計8を用いて今回のバッチのコークスの銘柄の正確な水
分測定を行なうことができ、また、必要な乾量値を正確
に含むL’f量が可能となる。さらに、パンチごとに粒
度が等しいコークスを炉内に装入することができるので
、炉内の良好なガス流分布を保持して操業成績を上げる
ことが可能である。
[Effect of the invention J As explained above, according to the present invention, E
Even if the amount of coke remaining in the C3 form is small and the brand of coke in the previous batch is different from the brand of coke in the current batch, the amount of different brands of coke mixed in the weighed coke will be small. Therefore, it is possible to accurately measure the moisture content of the coke brand of the current batch using the neutron moisture meter 8, and it is also possible to determine the L'f amount that accurately includes the required dry weight value. Furthermore, since coke having the same particle size can be charged into the furnace for each punch, it is possible to maintain a good gas flow distribution in the furnace and improve operational performance.

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

第1図は本発明の一実施例に係る高炉コークス切出訪御
装置のブロック図、第2図は高炉コークス切出秤量設備
の概略図である。 I I”’ l 4・−・貯fyi槽 2、〜24・・・切出量jδ 3・・・ベルトコンベア 4・・・秤量ホッパ 5,6.7・・・コークス 8・・・中性子水分計 11・・・秤騎速度演算部 12・・・切出速度演算部 13・・・BC上原料搭載量@算部 14・・・切出停止タイミング制御部 W・・・秤量値 WR・・・原料搭載量 WTGr・・・秤量目標値 υW・・・秤量速度 υF・・・切出速度 Sl・・・切出装置指定信号 Sl・・・秤量目標値指定信号 S3・・・切出停止信号
FIG. 1 is a block diagram of a blast furnace coke cutting and visiting control device according to an embodiment of the present invention, and FIG. 2 is a schematic diagram of a blast furnace coke cutting and weighing equipment. I I"' l 4...Storage fyi tank 2,~24...Cutting amount jδ 3...Belt conveyor 4...Weighing hopper 5,6.7...Coke 8...Neutron moisture Total 11... Scale speed calculation section 12... Cutting speed calculation section 13... Raw material loading amount on BC @ calculation section 14... Cutting stop timing control section W... Weighing value WR... - Raw material loading amount WTGr... Weighing target value υW... Weighing speed υF... Cutting speed Sl... Cutting device designation signal Sl... Weighing target value designation signal S3... Cutting stop signal

Claims (1)

【特許請求の範囲】 複数の貯骸槽と、各貯骸槽に対応して設けられた複数の
切出装置と、ベルトコンベアと、秤量ホッパとを有する
高炉コークス切出秤量設備において、 秤量速度から求められた切出速度と切出開始から現時点
までの経過時間の積と秤量ホッパの現時点の秤量値から
ベルトコンベア上のコークス搭載量を演算する原料搭載
量演算手段と、 秤量目標値に対する秤量残量値からこの原料搭載量演算
手段で演算したコークス搭載量を減算し、この減算結果
が所定量以下になったときに当該切出装置に切出停止信
号を出力する切出停止タイミング制御手段を備えたこと
を特徴とする高炉コークス切出制御装置。
[Scope of Claim] A blast furnace coke cutting and weighing equipment having a plurality of storage tanks, a plurality of cutting devices provided corresponding to each storage tank, a belt conveyor, and a weighing hopper, comprising: a weighing speed; a raw material loading amount calculating means for calculating the coke loading amount on the belt conveyor from the product of the cutting speed obtained from the calculation and the elapsed time from the start of cutting to the present time and the current weighing value of the weighing hopper; Cutting stop timing control means for subtracting the coke loading amount calculated by the raw material loading amount calculation means from the residual amount value and outputting a cutting stop signal to the cutting device when the subtraction result becomes a predetermined amount or less. A blast furnace coke cutting control device characterized by comprising:
JP16938484A 1984-08-15 1984-08-15 Apparatus for controlling feeding of shaft furnace coke Granted JPS6147535A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16938484A JPS6147535A (en) 1984-08-15 1984-08-15 Apparatus for controlling feeding of shaft furnace coke

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16938484A JPS6147535A (en) 1984-08-15 1984-08-15 Apparatus for controlling feeding of shaft furnace coke

Publications (2)

Publication Number Publication Date
JPS6147535A true JPS6147535A (en) 1986-03-08
JPH0380834B2 JPH0380834B2 (en) 1991-12-26

Family

ID=15885594

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16938484A Granted JPS6147535A (en) 1984-08-15 1984-08-15 Apparatus for controlling feeding of shaft furnace coke

Country Status (1)

Country Link
JP (1) JPS6147535A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03240911A (en) * 1989-12-19 1991-10-28 Fuji Electric Co Ltd Method for controlling cutting out quantity of auxiliary raw material

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57117422A (en) * 1981-01-14 1982-07-21 Nippon Steel Corp Method of controlling delivery of powdery material

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57117422A (en) * 1981-01-14 1982-07-21 Nippon Steel Corp Method of controlling delivery of powdery material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03240911A (en) * 1989-12-19 1991-10-28 Fuji Electric Co Ltd Method for controlling cutting out quantity of auxiliary raw material

Also Published As

Publication number Publication date
JPH0380834B2 (en) 1991-12-26

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