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JPH0380834B2 - - Google Patents
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JPH0380834B2 - - Google Patents

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Publication number
JPH0380834B2
JPH0380834B2 JP59169384A JP16938484A JPH0380834B2 JP H0380834 B2 JPH0380834 B2 JP H0380834B2 JP 59169384 A JP59169384 A JP 59169384A JP 16938484 A JP16938484 A JP 16938484A JP H0380834 B2 JPH0380834 B2 JP H0380834B2
Authority
JP
Japan
Prior art keywords
cutting
weighing
coke
value
amount
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 - Lifetime
Application number
JP59169384A
Other languages
Japanese (ja)
Other versions
JPS6147535A (en
Inventor
Yoshifumi Shimizu
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)
  • Flow Control (AREA)
  • Sampling And Sample Adjustment (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Coke Industry (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、高炉コークス切出秤量設備に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to blast furnace coke cutting and weighing equipment.

[従来の技術] 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。各貯骸槽11〜14には互いに銘柄の
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によつて輸送されて、秤量ホツパ4で秤量
される。(以下、この秤量の1回分の量のコーク
スもしくはその切出秤量工程をバツチと呼ぶ) 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うある範囲
内に達した(通常は目標値の95%)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つた時点で
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. Each of the storage tanks 1 1 to 1 4 stores coke of different brands, and each of the storage tanks 1 1 to 1 4 stores coke of different brands.
Cutting devices 2 1 to 2 4 are installed in each of the cokes, and a desired brand of coke is cut out by the corresponding cutting device and transported by a belt conveyor (hereinafter referred to as BC) 3. It is weighed in the weighing hopper 4. (Hereinafter, this weighing amount of coke or its cutting and weighing process is called a batch.) Conventionally, in order to shorten the weighing time and improve the weighing accuracy, the weighed value is within a certain range of the target value. When the weighing value reaches the target value (usually 95% of the target value), stop the cutting devices 21 to 24 , switch the BC3 from high speed to low speed, and when the weighed value reaches the target value,
BC3 was stopped.

[発明が解決しようとする課題] 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、前回のバツチ
でもBC3の上にコークスが残つていたはずであ
るから、今回のバツチの秤量ホツパ4の内には、
前回のバツチでBC3の上に残されたコークス6
と今回のバツチで切出されたコークス7とが混在
することになる。従つて、今回のバツチのコーク
スの銘柄が前回のバツチのコークスの銘柄と異な
る場合には、次の2つの問題点があつた。すなわ
ち、 (1) 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Wsetにコークス
内の水分を加えた値を秤量目標値WTGTとする
と、秤量目標値WTGTは WTGT=1/1−αWset の式で決定されるが、水分含有率αが異なる異
銘柄のコークスが秤量ホツパ4内で混在すれ
ば、中性子水分計8によつて今回のバツチのコ
ークスの銘柄の水分測定を正確に行なうことが
できないので、秤量目標値WTGTまで秤量して
も必要な乾量値Wsetが得られなかつた。
[Problems to be Solved by the Invention] In this method, coke is weighed to a target value, but the remaining 5 coke remains on top of the stopped BC3.
will occur. In this way, coke should have remained on top of BC3 in the previous batch, so in weighing hopper 4 of this batch,
Coke 6 left on top of BC3 from the previous batch
and coke 7 cut out in this batch will be mixed together. Therefore, if the brand of coke in the current batch is different from the brand of coke in the previous batch, the following two problems arise. In other words, (1) The required amount of coke is first given as a dry weight (amount that does not include water), and if the value obtained by adding the water in the coke to this dry weight value W set is the weighing target value W TGT , then the weighing target The value W TGT is determined by the formula W TGT = 1/1 - αW set , but if different brands of coke with different moisture contents α are mixed in the weighing hopper 4, the neutron moisture meter 8 will determine the current value. Since it is not possible to accurately measure the moisture content of batches of coke brands, the necessary dry weight value Wset could not be obtained even if the coke was weighed to the target weighing value W TGT .

(2) 異銘柄のコークスが秤量ホツパ内に混在する
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
成績が悪くなつていた。
(2) 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 the overall furnace. As a result of the deteriorating business conditions, operational results were worsening.

本発明の目的は、秤量したコークスに混在する
前回のバツチのコークスの量を減らして、コーク
スの正確な水分測定を行うことにより、コークス
の必要量の正確な秤量およびバツチごとの炉内へ
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。
The purpose of the present invention is to reduce the amount of coke from the previous batch mixed in the weighed coke and accurately measure the moisture content of the coke. An object of the present invention is to provide a blast furnace coke cutting control device that enables charging by particle size.

[課題を解決するための手段] 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−秤量ホツパで測定した
秤量値)を時々刻々求め、秤量残量値と原料搭載
量の差が負の所定量以下になつた時点で当該切出
装置を停止させるようにしたものである。
[Means for Solving the Problems] The present invention obtains 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 weighed remaining amount value and the weighed raw material value. The cutting device is stopped when the difference in loading amount becomes less than a predetermined negative amount.

すなわち、本発明の高炉コークス切出制御装置
は、前回までの複数回の各バツチについて秤量速
度から求められた切出速度の平均値と切出開始か
ら現時点までの経過時間との積と、秤量ホツパの
現時点の秤量値と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
減算結果が負の所定量以下になつたときに当該切
出装置に切出停止信号を出力する切出停止制御手
段を備えている。
That is, the blast furnace coke cutting control device of the present invention calculates the product of the average value of the cutting speed obtained from the weighing speed for each batch up to the previous batch and the elapsed time from the start of cutting to the present time, and the weighing speed. a raw material loading amount calculating means for calculating the coke loading amount on the belt conveyor from the current weighing value of the hopper; and subtracting the coke loading amount calculated by the raw material loading amount calculating means from the weighing remaining amount value with respect to the weighing target value; A cutting stop control means is provided for outputting a cutting stop signal to the cutting device when the result of this subtraction becomes less than a predetermined negative amount.

[実施例] 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] 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
のブロツク図である。
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は各バツチ終了時に、秤量
ホツパ4で測定された秤量値W(秤量ホツパ4で
の重量測定値から秤量開始時に秤量ホツパ4内に
残留していたコークス重量を差引いた値)を入力
し、その秤量値Wと秤量に要した時間から秤量速
度υWを演算し出力する。切出速度演算部12は、
各バツチごとに不図示の制御盤から切出装置指定
信号S1を入力し、各バツチ終了時には、予めわか
つている各切出装置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υWとから
切出装置指定信号S1によつて指定された切出装置
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により指定された切出装置の過去数バツチの
前記推定値の平均値(移動平均、指数平均等)を
演算して、今回のバツチの切出速度υFとして出力
する。BC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υF(初回のバ
ツチは設定値)と今回のバツチの切出開始から現
時点までの経過時間tFとの積をとり、この積と秤
量ホツパ4で測定された今回のバツチの現時点の
秤量値Wとの差をとつて、これをBC3の原料搭
載量WRとして出力する。切出停止制御部14は
前記制御盤から秤量目標値指定信号S2を入力し、
秤量目標値指定信号S2によつて指定される秤量目
標値WTGTと秤量ホツパ4で測定された秤量値W
との差をとつてこれを秤量残量値WSとし、この
秤量残量値WSとBC上原料搭載量演算部13で演
算された原料搭載量WRの差が、WS−WR≦C(C
は負の所定量)の関係を満たすようになつた時点
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、Cは切出の速度のばら
つきによつてBC3上の原料搭載量WR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。
At the end of each batch, the weighing speed calculation unit 11 calculates the weighing value W measured by the weighing hopper 4 (a value obtained by subtracting the coke weight remaining in the weighing hopper 4 from the weight measurement value at the weighing hopper 4 at the start of weighing). is input, and the weighing speed υ W is calculated and output from the weighing value W and the time required for weighing. The cutting speed calculation unit 12 is
A cutting device designation signal S 1 is input from a control panel (not shown) for each batch, and at the end of each batch, the cutting capacity ratio and weighing speed calculation unit 11 of each cutting device 2 1 to 2 4 that are known in advance are input. The estimated value of the cutting device specified by the cutting device designation signal S1 is calculated from the weighing speed υ W calculated by The average value (moving average, exponential average, etc.) of the estimated values of the past batches of the cutting device designated by the cutting device designation signal S1 is calculated and output as the cutting speed υ F of the current batch. The BC top raw material loading amount calculating section 13 calculates the cutting speed υ F (set value for the first batch) output from the cutting speed calculating section 12 and the elapsed time t F from the start of cutting of the current batch to the present time. The difference between this product and the current weight value W of the current batch measured by the weighing hopper 4 is calculated, and this is output as the raw material loading amount W R of BC3. The cutting stop control unit 14 inputs the weighing target value designation signal S2 from the control panel,
Weighing target value W specified by weighing target value designation signal S2 TGT and weighing value W measured by weighing hopper 4
This is the weighed remaining amount value W S , and the difference between this weighed remaining amount value W S and the raw material loading amount W R calculated by the raw material loading amount calculation unit 13 on the BC is W S − W R ≦C(C
is a negative predetermined amount), a cutting stop signal S3 is output to the cutting device to stop the cutting device. Note that C is a safety constant to prevent an error in the raw material loading amount W R on BC3 due to variations in the cutting speed, and to prevent the cutting amount from being insufficient.

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が切出停止制御部
14にそれぞれ入力されて、切出装置が指定され
秤量目標値WTGTが設定される。まず、切出速度
演算部12は、各バツ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ツチにわたる推定
値の平均をとり、今回のバツチの切出速度υFとし
て出力する。次に、この切出速度υFを示す信号が
BC上原料搭載量演算部13に入力されて、BC3
上の原料搭載量WRが時々刻々演算され、この原
料搭載量WRを示す信号が切出停止制御部14に
入力する。切出停止制御部14は、秤量目標値指
定信号S2によつて設定された秤量目標値WTGT
秤量ホツパ4での秤量値Wから秤量残量値WS
時々刻々演算し、そしてこの秤量残量値WSとBC
上原料搭載量演算部13から伝達された原料搭載
量WRの差WS−WRが、WS−WR≦Cとなつた時点
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、今回のバツチの秤量が終ると秤量速度演算
部11で今回のバツチの秤量速度υWが演算され、
この秤量速度υWを示す信号が切出速度演算部1
2に入力され、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、以後のバツチにおける切出速度υFの演
算に使用される。
A cutting device designation signal S1 specifying a cutting device corresponding to a desired brand of coke is input to the cutting speed calculation section 12, and a weighing target value designation signal S2 is input to the cutting stop control section 14. Then, the cutting device is designated and the weighing target value W TGT is set. First, the cutting speed calculating section 12 calculates the cutting speed specified by the cutting device designation signal S 1 , which is determined from the weighing speed υ W calculated by the weighing speed calculating section 11 at the end of each batch and is stored internally. The average of the estimated values for the past several batches of the extraction device is taken and output as the cutting speed υ F of the current batch. Next, the signal indicating this cutting speed υ F is
It is input to the BC upper raw material load calculation unit 13,
The above raw material loading amount W R is calculated every moment, and a signal indicating this raw material loading amount W R is input to the cut-out stop control section 14. The cutting-out stop control unit 14 calculates the remaining weighing amount W S from the weighing target value W TGT set by the weighing target value designation signal S 2 and the weighing value W at the weighing hopper 4, and Weighing remaining amount value W S and BC
When the difference W S − W R in the raw material loading amount W R transmitted from the upper raw material loading amount calculation unit 13 becomes W S − W R ≦C, a cutting stop signal S 3 is sent to the cutting device. Output.
This causes the cutting device to stop. In this way, when the weighing of the current batch is finished, the weighing speed υ W of the current batch is calculated in the weighing speed calculation section 11,
A signal indicating this weighing speed υ W is output from the cutting speed calculation unit 1.
2, an estimated value of the cutting speed of the cutting device designated by the cutting device designation signal S1 is obtained, and this estimated value is stored inside the cutting speed calculation unit 12 and used from now on. It is used to calculate the cutting speed υ F in batches of .

このようにして、BC3上の原料搭載量WR
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BC3上のコークスの残りは
わずかなものとなる。しかも、安全定数Cによつ
て、切出量が秤量目標値WTGTに至らずに不足す
ることを防止している。従つて、切出量が秤量目
標値より不足することはなく、また秤量ホツパ4
の内に混在する前回のバツチのコークスの量はわ
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 W R on BC3 from time to time, only a small amount of coke remains on BC3 when weighing is completed. Moreover, the safety constant C prevents the cutting amount from becoming insufficient and not reaching the weighing target value W TGT . Therefore, the cutting amount will not be insufficient than the weighing target value, and the weighing hopper 4
The amount of coke from the previous batch mixed in is small.

[発明の効果] 以上説明したように本発明によれば、バツチ終
了時にBC3上に残るコークスの量が少なく、前
回のバツチのコークスの銘柄と今回のバツチのコ
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
のとなり、したがつて、中性子水分計8を用いて
今回のバツチのコークスの銘柄の正確な水分測定
を行うことができ、また、必要な乾量値を正確に
含む秤量が可能となり、さらに、バツチごとに粒
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できる効果がある。
[Effects of the Invention] As explained above, according to the present invention, even if the amount of coke remaining on the BC3 at the end of a batch is small and the coke brand of the previous batch and the coke brand of the current batch are different, The amount of different brands of coke mixed in the weighed coke is small, so the neutron moisture meter 8 can be used to accurately measure the moisture content of this batch of coke brands, and the necessary It is possible to weigh accurately including the dry weight value, and furthermore, it is possible to charge coke with the same particle size in each batch into the furnace, which maintains a good gas flow distribution in the furnace and improves operational performance. It has the effect of

【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
切出制御装置のブロツク図、第2図は高炉コーク
ス切出秤量設備の概略図である。 11〜14……貯骸槽、21〜24……切出装置、
3……ベルトコンベア、4……秤量ホツパ、5,
6,7……コークス、8……中性子水分計、11
……秤量速度演算部、12……切出速度演算部、
13……BC上原料搭載量演算部、14……切出
停止制御部、W……秤量値、WR……原料搭載量、
WTGT……秤量目標値、υW……秤量速度、υF……
切出速度、S1……切出装置指定信号、S2……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 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. 1 1 to 1 4 ... carcass storage tank, 2 1 to 2 4 ... cutting device,
3...Belt conveyor, 4...Weighing hopper, 5,
6,7...Coke, 8...Neutron moisture meter, 11
... Weighing speed calculation section, 12 ... Cutting speed calculation section,
13... BC raw material loading amount calculation unit, 14... Cutting stop control unit, W... weighing value, W R ... raw material loading amount,
W TGT ...Weighing target value, υ W ...Weighing speed, υ F ...
Cutting speed, S 1 ... Cutting device designation signal, S 2 ... Weighing target value designation signal, S 3 ... Cutting stop signal.

Claims (1)

【特許請求の範囲】 1 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
ホツパとを有する高炉コークス切出秤量設備にお
いて、 前回までの複数回の各バツチについて秤量速度
から求められた切出速度の平均値と切出開始から
現時点までの経過時間との積と、秤量ホツパの現
時点の秤量値と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、この減算結果が負の所定量以下になつたとき
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。
[Claims] 1. In 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, Coke loading on the belt conveyor is determined based on the product of the average value of the cutting speed calculated from the weighing speed for each batch of multiple times up to and the elapsed time from the start of cutting to the present time, and the current weighing value of the weighing hopper. a raw material loading amount calculating means for calculating the amount, and a coke loading amount calculated by this raw material loading amount calculating means from the weighed remaining amount value with respect to the weighing target value, and when the result of this subtraction becomes a negative predetermined amount or less. A blast furnace coke cutting control device comprising a cutting stop control means for outputting a cutting stop signal to the cutting device.
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 JPS6147535A (en) 1986-03-08
JPH0380834B2 true 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)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2608968B2 (en) * 1989-12-19 1997-05-14 富士電機株式会社 Control method of cut-out amount of auxiliary raw material
JP6683082B2 (en) * 2016-09-14 2020-04-15 日本製鉄株式会社 Control device for raw material cutting equipment, control method for raw material cutting equipment, and program

Family Cites Families (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

Also Published As

Publication number Publication date
JPS6147535A (en) 1986-03-08

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