JP2972462B2 - How to replenish powder and granular material to multiple bunker from former hopper - Google Patents

How to replenish powder and granular material to multiple bunker from former hopper

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Publication number
JP2972462B2
JP2972462B2 JP4278351A JP27835192A JP2972462B2 JP 2972462 B2 JP2972462 B2 JP 2972462B2 JP 4278351 A JP4278351 A JP 4278351A JP 27835192 A JP27835192 A JP 27835192A JP 2972462 B2 JP2972462 B2 JP 2972462B2
Authority
JP
Japan
Prior art keywords
bunker
bunkers
pulverized coal
sum
replenishing
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 - Fee Related
Application number
JP4278351A
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Japanese (ja)
Other versions
JPH06127700A (en
Inventor
好明 坪根
守 芳川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kobe Steel Ltd
Original Assignee
Kobe Steel Ltd
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Filing date
Publication date
Application filed by Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP4278351A priority Critical patent/JP2972462B2/en
Publication of JPH06127700A publication Critical patent/JPH06127700A/en
Application granted granted Critical
Publication of JP2972462B2 publication Critical patent/JP2972462B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、元ホッパから複数バン
カへの粉粒体補給方法に関し、特には、高炉への微粉炭
吹込みに際して、打込みホッパから複数のバンカへ銘柄
の異なる微粉炭を単位時間当たりのカロリー変動が一定
になるように補給する方法に関するものである。なお、
本発明は、微粉炭、セメント、砂などの粉体、粒体など
の粉粒体を対象とするものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for replenishing pulverized material from a former hopper to a plurality of bunkers, and more particularly, to pulverized coal being injected into a blast furnace, pulverized coal having different brands from a driving hopper to a plurality of bunkers. The present invention relates to a method of replenishing calorie fluctuation per unit time so as to be constant. In addition,
The present invention is directed to powders such as pulverized coal, cement, sand, and the like, and powders such as granules.

【0002】[0002]

【従来の技術】高炉への微粉炭吹込みでは、トラック等
により輸送されてくる微粉炭を、製鉄所内の複数の打込
みバンカに銘柄毎に分けて受入れ、順次切り出して使用
している。それ故、銘柄の異なる微粉炭を同時に使用す
ることがあり、この場合、高炉の安定操業のため、銘柄
の異なる微粉炭を出来るだけ均等に混合させるように
し、単位時間当たりのカロリー変動を一定にする事が大
事である。
2. Description of the Related Art When pulverized coal is injected into a blast furnace, pulverized coal transported by a truck or the like is divided into a plurality of driving bunkers in a steel mill for each brand, and cut and used sequentially. Therefore, pulverized coal of different brands may be used at the same time.In this case, in order to stably operate the blast furnace, pulverized coal of different brands should be mixed as evenly as possible to keep the calorie fluctuation per unit time constant. It is important to do.

【0003】そこで、上記単位時間当たりのカロリー変
動を一定にするために複数の銘柄の微粉炭を複数の補給
先に決められた割合で供給することが、図4乃至図5に
示す方式により行われていた。以下は理解をし易くする
ため3銘柄の微粉炭を対象に説明する。
In order to keep the calorie fluctuation per unit time constant, pulverized coal of a plurality of brands is supplied to a plurality of replenishing destinations at a predetermined ratio by the method shown in FIGS. Had been The following description focuses on three brands of pulverized coal for easy understanding.

【0004】図4においては、3銘柄の微粉炭A,B,
Cは、銘柄毎に各打込みホッパ11,12,13に受入れら
れ、4台のバンカ14〜17へは、予め定められた単位時間
当たりのカロリーになるように各打込みホッパ11,12,
13から同時に定量が切り出され、搬送コンベア群18を介
して補給される。各バンカ14〜17には、粉面レベル測定
器19が設けられ、高炉への微粉炭吹込み中は、これら粉
面レベル測定器19からの粉面レベルにより制御装置20を
介して搬送コンベア群18を制御し、消費した微粉炭の補
給が粉面レベルの低い順に行われる。
In FIG. 4, three brands of pulverized coal A, B,
C is received in each of the driving hoppers 11, 12, and 13 for each brand, and is supplied to the four bunkers 14 to 17 so that calories per unit time are predetermined.
A fixed amount is simultaneously cut out from 13 and replenished via a conveyor group 18. Each of the bunkers 14 to 17 is provided with a powder surface level measuring device 19, and during the pulverized coal injection into the blast furnace, the conveyor level is controlled via the control device 20 by the powder surface level from the powder surface level measuring device 19. 18 is controlled so that the consumed pulverized coal is replenished in ascending order of powder level.

【0005】また、図5においては、打込みホッパ21,
22,23の後に混合用ホッパ24が設置されており、銘柄毎
に各打込みホッパ21,22,23に受入れられている3銘柄
の微粉炭A,B,Cは、予め定められた単位時間当たり
のカロリーになるように各打込みホッパ21, 22,23から
同時に定量が切り出され、一旦混合用ホッパ24に投入さ
れ混合状態にされた後、4台のバンカ25〜28へ搬送コン
ベア群29を介して補給される。各バンカ25〜28には、上
記と同様に粉面レベル測定器30が設けられ、高炉への微
粉炭吹込み中は、これら粉面レベル測定器30からの粉面
レベルにより制御装置31を介して搬送コンベア群29を制
御し、消費した微粉炭の補給が粉面レベルの低い順に行
われる。
In FIG. 5, the driving hopper 21,
Mixing hoppers 24 are installed after 22 and 23, and the three brands of pulverized coal A, B and C that are received in each of the driving hoppers 21, 22, and 23 for each brand are separated by a predetermined unit time. The amount of calories is simultaneously cut out from each of the driving hoppers 21, 22, and 23 so as to give a calorie, and is put into the mixing hopper 24 once to be in a mixed state, and then to the four bunkers 25 to 28 via the conveyor group 29. Replenished. Each of the bunkers 25 to 28 is provided with a powder surface level measuring device 30 in the same manner as described above, and while the pulverized coal is being injected into the blast furnace, the powder surface level from these powder surface level measuring devices 30 is transmitted through the control device 31 via the control device 31. The conveyer group 29 is controlled to replenish the consumed pulverized coal in ascending order of the powder level.

【0006】[0006]

【発明が解決しようとする課題】上述した従来の技術で
は、銘柄毎に打込みホッパを必要とし、さらには必要に
応じて混合用ホッパを必要としていたため、設備が大掛
かりになると共に設備コストのアップとなり、延いては
高炉で生産される溶銑のコストアップとなる。
In the above-mentioned prior art, a driving hopper is required for each brand, and a mixing hopper is required if necessary. Therefore, the equipment becomes large and the equipment cost increases. , Which in turn increases the cost of hot metal produced in the blast furnace.

【0007】また、高炉への微粉炭吹込み中における各
バンカの微粉炭の消費量は、バンカが接続されている高
炉の吹込み位置および/または高炉の炉況等によって大
小がある。このため、消費した微粉炭の補給を、上述し
た各バンカの粉面レベルを粉面レベル測定器で測定し粉
面レベルの低いものから順に補給する方式では、上記消
費量の大小に対応させたきめ細かい補給制御ができな
い。一方、きめ細かい制御をする場合には、膨大且つ複
雑な制御ロジックになり現実的でない。
The amount of pulverized coal consumed by each bunker during the pulverized coal injection into the blast furnace varies depending on the position of the blast furnace to which the bunker is connected and / or the condition of the blast furnace. For this reason, in the method of replenishing the consumed pulverized coal, the powder surface level of each bunker is measured by the powder surface level measuring device described above, and replenishment is performed in ascending order of the powder surface level. Detailed supply control is not possible. On the other hand, when performing fine control, the control logic becomes enormous and complicated, which is not realistic.

【0008】本発明は、上記の問題点に鑑みてなされた
ものであって、その目的は、1台の打込みホッパ(元ホ
ッパ)を使用し、且つこの1台の元ホッパに順次銘柄の
異なる微粉炭を補給した場合において予め定められた単
位時間当たりのカロリーになるように各バンカへ微粉炭
を制御して補給する、元ホッパから複数バンカへの粉粒
体補給方法を提供するものである。
The present invention has been made in view of the above problems, and has as its object to use one driving hopper (original hopper), and to provide different brands to the one original hopper sequentially. It is intended to provide a method of replenishing pulverized coal to a plurality of bunkers from an original hopper by controlling and replenishing pulverized coal to each bunker so that calories per unit time are predetermined when replenishing pulverized coal. .

【0009】[0009]

【課題を解決するための手段】上記目的を達成するた
め、本発明に係わる元ホッパから複数バンカへの粉粒体
補給方法は、元ホッパに順次受ける粉粒体を複数のバン
カに各バンカ内の物理的特性等が均一になるように補給
する方法であって、バンカ毎に優先順位を定量化して重
み付けするとともに、各バンカの粉粒面レベルおよび単
位時間当たりの粉粒体消費量を測定し、その実測値の大
小に応じて各バンカの粉粒面レベルおよび単位時間当た
りの粉粒体消費量をそれぞれ重み付けし、次いでこれら
優先順位、粉粒面レベル、単位時間当たりの粉粒体消費
量の各重みのバンカ毎の和を求め、この重みの和の総和
を求めると同時にこの総和に対する各バンカの和の比率
を求めその比率に応じて粉粒体の補給量を各バンカに配
分して補給するものである。
In order to achieve the above object, a method for replenishing powdery or granular material from an original hopper to a plurality of bunker according to the present invention is a method for replenishing powdery or granular material sequentially received by an original hopper into a plurality of bunker in each bunker. Is a method of replenishing so that the physical characteristics etc. of the bunker are uniform, quantifying and weighting the priority for each bunker, and measuring the granular surface level of each bunker and the amount of granular material consumed per unit time The weight of the granular surface level of each bunker and the amount of granular material consumption per unit time are weighted according to the magnitude of the actually measured value. The sum of the weights of each bunker is calculated for each bunker, and the sum of the sums of the weights is calculated.At the same time, the ratio of the sum of each bunker to this sum is calculated and the replenishment amount of the granular material is distributed to each bunker according to the ratio. What to replenish A.

【0010】そして、上記の元ホッパから複数バンカへ
の粉粒体補給方法においては、バンカ毎の重みの大きい
ものから順に複数選択してその重みの総和を求め、選択
されたバンカのみ、その総和に対する各バンカの和の比
率を求めその比率に応じて粉粒体の補給量を各バンカに
配分して補給してもよい。
In the method of replenishing powder and granular material from the original hopper to a plurality of bunkers, a plurality of bunkers are selected in descending order of weight and the sum of the weights is determined. Only the selected bunker is summed. The ratio of the sum of each bunker to the bunker may be determined, and the replenishment amount of the granular material may be distributed and supplied to each bunker according to the ratio.

【0011】[0011]

【実施例】以下、本発明の構成並びに作用を実施例によ
り説明する。図1は、本発明方法を適用する装置の概念
図であって、この例では1台の打込みホッパと5台のバ
ンカを使用し微粉炭を補給する場合を例に説明する。図
において、1は打込みホッパ、2は搬送コンベア群、3
はバンカ群、4は制御装置を示す。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The construction and operation of the present invention will be described below with reference to embodiments. FIG. 1 is a conceptual diagram of an apparatus to which the method of the present invention is applied. In this example, a case where one driving hopper and five bunker are used to supply pulverized coal will be described as an example. In the figure, 1 is a driving hopper, 2 is a conveyor group, 3
Indicates a bunker group, and 4 indicates a control device.

【0012】打込みホッパ1には、消費量に合わせてト
ラック輸送されてくる微粉炭が順次受入れられるととも
に、搬送コンベア群2へ切り出す。
The driving hopper 1 sequentially receives pulverized coal transported by truck in accordance with the amount of consumption, and cuts the coal into a conveyor group 2.

【0013】搬送コンベア群2は、5台の正逆回転可能
な搬送コンベア2a〜2dで構成され、上記打込みホッパ1
から切り出されてくる微粉炭を次の如くしてバンカ群3
へ補給する。すなわち、搬送コンベア2aでは、コンベア
2aが逆回転するとバンカ3aに微粉炭が補給され、正回転
すると搬送コンベア2b上へ微粉炭が移送される。以下同
様に、搬送コンベア2bでは、コンベア2bが逆回転すると
バンカ3bに微粉炭が補給され、正回転すると搬送コンベ
ア2c上へ微粉炭が移送される。搬送コンベア2cでは、コ
ンベア2cが逆回転するとバンカ3cに微粉炭が補給され、
正回転すると搬送コンベア2d上へ微粉炭が移送される。
そして、搬送コンベア2dでは、コンベア2dが逆回転する
とバンカ3dに微粉炭が補給され、正回転するとバンカ3e
に微粉炭が補給される。なお、この搬送コンベア2a〜2d
の正または逆回転は制御装置4により制御され、正回転
は微粉炭が図1の右方向に移送される場合、逆回転は微
粉炭が図1の左方向に移送される場合である。
The transport conveyor group 2 is composed of five forward and reverse rotatable transport conveyors 2a to 2d.
Pulverized coal cut out from bunka group 3 as follows
Replenish. That is, in the conveyor 2a, the conveyor
When the 2a rotates in the reverse direction, pulverized coal is supplied to the bunker 3a, and when rotated in the forward direction, the pulverized coal is transferred onto the conveyor 2b. Similarly, in the conveyor 2b, pulverized coal is supplied to the bunker 3b when the conveyor 2b rotates in the reverse direction, and pulverized coal is transferred onto the conveyor 2c when the conveyor 2b rotates in the forward direction. In the conveyor 2c, when the conveyor 2c rotates in the reverse direction, pulverized coal is supplied to the bunker 3c,
When it rotates forward, the pulverized coal is transferred onto the conveyor 2d.
In the conveyor 2d, pulverized coal is supplied to the bunker 3d when the conveyor 2d rotates in the reverse direction, and the bunker 3e is rotated when the conveyor 2d rotates in the forward direction.
Is supplied with pulverized coal. In addition, this conveyor 2a ~ 2d
The forward or reverse rotation is controlled by the controller 4. The forward rotation is when the pulverized coal is transported rightward in FIG. 1, and the reverse rotation is when the pulverized coal is transported leftward in FIG.

【0014】バンカ群3は、5台のバンカ3a〜3eからな
り、各バンカ3a〜3eには、バンカ内の微粉炭の粉面レベ
ルを測定する粉面レベル測定器5a〜5eと、微粉炭の単位
時間当たりの消費量を求める計測手段(本例ではロート
セル)6a〜6eが装備されている。また、各測定器5a〜5e
と各計測手段6a〜6eによる測定信号は制御装置4に入力
され、各バンカ3a〜3eの粉面レベルおよび単位時間当た
りの微粉炭消費量がそれぞれ演算されて重み付けされ
る。そして、高炉への微粉炭吹込み中は、別に入力され
る各バンカ3a〜3eの優先順位の重み付けと合わせ、総合
重み付けの大きいバンカ3a〜3eから順に微粉炭の補給が
行われる。
The bunker group 3 includes five bunkers 3a to 3e. Each of the bunkers 3a to 3e has a powder level measuring device 5a to 5e for measuring the powder level of the pulverized coal in the bunker, and a pulverized coal. Measuring means (rotor cells in this example) 6a to 6e for calculating the consumption amount per unit time of the above are provided. In addition, each measuring instrument 5a-5e
The measurement signals from the measuring means 6a to 6e are input to the control device 4, and the powder level of each of the bunkers 3a to 3e and the pulverized coal consumption per unit time are calculated and weighted. During the pulverized coal injection into the blast furnace, pulverized coal is supplied in order from the bunker 3a to 3e having the larger total weight, together with the weighting of the priorities of the respective bunkers 3a to 3e which are input separately.

【0015】次に上記装置による、打込みホッパ1から
各バンカ3a〜3eへの微粉炭補給例を説明する。図2は、
粉面レベルと重み付けのポイントとの関係を示す関数グ
ラフ図、図3は、単位時間当たりの粉体消費量と重み付
けのポイントとの関係を示す関数グラフ図をそれぞれ示
す。
Next, an example of replenishing pulverized coal from the driving hopper 1 to each of the bunkers 3a to 3e by the above apparatus will be described. FIG.
FIG. 3 is a function graph showing the relationship between the powder surface level and the weighting points, and FIG. 3 is a function graph showing the relationship between the powder consumption per unit time and the weighting points.

【0016】図2および図3から明らかなように、粉面
レベルについては、レベルが高いバンカはポイントが小
さく、微粉炭が消費されレベルが低くなったバンカはポ
イントが大きくなるように関数を定める。一方、単位時
間当たりの微粉炭消費量については、消費量が小さいバ
ンカはポイントが小さく、消費量が大きいバンカはポイ
ントが大きくなるように関数を定める。なお、前記関数
は、例えば粉面レベルの場合、レベルLが0〜 100%の
間全てを図2に実線で示すような式(ポイントP=−a
L+b)、あるいは、例えば、0≦L≦20:P=一定,
20<L≦70:P=−a'L+b'20,70<L≦ 100:P=一
定(図2に破線参照)のように適宜微粉炭の消費の状況
に応じて定めることができる。また、単位時間当たりの
微粉炭消費量の場合の関数も同様にして定める。
As is clear from FIGS. 2 and 3, the function is determined such that the bunker with a high level has a small point, and the bunker with a low level of pulverized coal has a large point with respect to the powder level. . On the other hand, regarding the pulverized coal consumption per unit time, the function is determined such that a bunker with a small consumption has a small point and a bunker with a large consumption has a large point. Note that, for example, in the case of the powder surface level, the above function is expressed by an equation (point P = −a
L + b) or, for example, 0 ≦ L ≦ 20: P = constant,
20 <L ≦ 70: P = −a′L + b′20, 70 <L ≦ 100: P = constant (see the broken line in FIG. 2), which can be appropriately determined according to the situation of pulverized coal consumption. In addition, the function for pulverized coal consumption per unit time is determined in the same manner.

【0017】上記関数は予め制御装置4に入力され、各
バンカ3a〜3eの粉面レベルおよび単位時間当たりの微粉
炭消費量の測定値を元に、各バンカ3a〜3e毎にそれらの
重み付け(ポイント)を演算する。次いで、制御装置4
では、別に入力される各バンカ3a〜3eの優先順位の重み
付け(ポイント)と合わせ、バンカ3a〜3e毎の合計ポイ
ントPa〜Peを求めるとともに、それらの合計ポイントPa
〜Peの総和ポイントPtを求め、さらにこの総和ポイント
Ptに対する各合計ポイントPa〜Peとの比率(例えばバン
カ3aの比率Pa/Pt)を求める。
The above functions are input to the controller 4 in advance, and based on the powder surface level of each of the bunkers 3a to 3e and the measured value of the pulverized coal consumption per unit time, their weights are assigned to each of the bunkers 3a to 3e ( Point). Next, the control device 4
Then, the total points Pa to Pe for each of the bunker 3a to 3e are obtained by combining the weights (points) of the priorities of the respective bunkers 3a to 3e, and the total points Pa
Calculate the total point Pt of ~ Pe, and further calculate this total point
The ratio of each of the total points Pa to Pe to Pt (for example, the ratio Pa / Pt of the bunker 3a) is determined.

【0018】次に、上記で求めた各バンカ3a〜3eの比率
Pa/Pt〜Pb/Ptを元に打込みホッパ1からの総補給量を
按分し、その按分した補給量を合計ポイントPa〜Peの大
きいバンカ3a〜3eから順に補給する。このような補給を
輸送トラック毎あるいは一定時間毎に計算して行うこと
により、消費量の大きいバンカには常に多量の補給が行
われるため、各バンカ3a〜3eの粉面レベルLは、高炉へ
の吹込み開始時にバラツキがあっても吹込み中にほぼ平
準化され、また同時に、各バンカ3a〜3eにおける銘柄の
異なる微粉炭の補給比率は、ほぼ一定に制御されること
になり、1台の打込みホッパ1より、予め定められた単
位時間当たりのカロリーになるように各バンカ3a〜3eへ
微粉炭を制御して補給することができる。
Next, the ratio of each bunker 3a to 3e obtained above
Based on Pa / Pt to Pb / Pt, the total replenishment amount from the driving hopper 1 is apportioned, and the apportioned replenishment quantity is replenished in order from the bunker 3a-3e having the larger total point Pa-Pe. By performing such replenishment for each transport truck or for each fixed time, a large amount of replenishment is always performed for the bunker with large consumption, so that the powder level L of each of the bunkers 3a to 3e is transferred to the blast furnace. Even if there is variation at the start of the injection, the leveling is substantially leveled during the injection, and at the same time, the supply ratio of pulverized coal of different brands in each of the bunker 3a to 3e is controlled to be substantially constant, From the driving hopper 1, pulverized coal can be controlled and supplied to each of the bunkers 3a to 3e such that calories per unit time are predetermined.

【0019】また、各バンカ3a〜3eの優先順位のポイン
トは、別に設定して制御装置4に入力するので、高炉の
微粉炭吹込み前に吹込み状況を勘案して設定することが
でき、きめ細かい且つ精度の高い制御が簡単なロジック
で行うことができる。
Further, since the priority points of the respective bunkers 3a to 3e are separately set and input to the control device 4, they can be set in consideration of the state of injection before pulverized coal is injected into the blast furnace. Fine and accurate control can be performed with simple logic.

【0020】なお、上記実施例では、全バンカ3a〜3eへ
の補給を例に説明したが、本発明はこの実施例に限定さ
れるものではなく、上記合計ポイントPa〜Peの内より大
きいポイントを有する3バンカ、例えば3a, 3c, 3dを対
象として、上記と同様に、この3バンカの合計ポイント
Pa, Pc, Pdの総和さらにこの総和に対する比率を求め、
その比率で総補給量を按分し、その按分した補給量を合
計ポイントPa, Pc, Pdの大きいバンカ3a, 3c, 3dから順
に補給するようにしてもよい。
In the above embodiment, the replenishment to all the bunkers 3a to 3e has been described as an example. However, the present invention is not limited to this embodiment, and points larger than the total points Pa to Pe are described. As above, the total points of the three bunker with the three bunker having, for example, 3a, 3c, 3d
The sum of Pa, Pc, and Pd, and the ratio to this sum,
The total supply amount may be apportioned at that ratio, and the apportioned supply amount may be supplied in order from the bunker 3a, 3c, 3d with the larger total point Pa, Pc, Pd.

【0021】[0021]

【発明の効果】以上説明したように、本発明に係わる元
ホッパから複数バンカへの粉粒体補給方法によれば、1
台の元ホッパを使用し、且つこの1台の元ホッパに順次
銘柄の異なる粉粒体を補給した場合において、予め定め
られた粉粒体の物理的特性等が均一になるように各バン
カへ粉粒体を制御して補給することができる。
As described above, according to the method for replenishing powder and granular materials from a source hopper to a plurality of bunker according to the present invention, the
When using one original hopper and replenishing powder particles of different brands sequentially into this one original hopper, the bunker is transferred to each bunker so that the physical characteristics of the predetermined powder particles become uniform. The powder can be controlled and replenished.

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

【図1】本発明方法を適用する装置の概念図である。FIG. 1 is a conceptual diagram of an apparatus to which the method of the present invention is applied.

【図2】本発明に係わる粉面レベルと重み付けのポイン
トとの関係を示す関数グラフ図である。
FIG. 2 is a function graph showing a relationship between a powder surface level and weighting points according to the present invention.

【図3】本発明に係わる単位時間当たりの粉体消費量と
重み付けのポイントとの関係を示す関数グラフ図であ
る。
FIG. 3 is a function graph showing a relationship between a powder consumption amount per unit time and a weighting point according to the present invention.

【図4】従来の微粉炭補給装置の概念図である。FIG. 4 is a conceptual diagram of a conventional pulverized coal supply device.

【図5】従来の微粉炭補給装置の概念図である。FIG. 5 is a conceptual diagram of a conventional pulverized coal supply device.

【符号の説明】[Explanation of symbols]

1:打込みホッパ 2:搬送コンベア群 2a
〜2d:搬送コンベア 3:バンカ群 3a〜3e:バンカ
4:制御装置 5a〜5e:粉面レベル測定器 6a〜6e:微粉炭の単位時間当たりの消費量を求める計測
手段
1: Driving hopper 2: Transport conveyor group 2a
~ 2d: Conveyor conveyor 3: Bunker group 3a ~ 3e: Bunker
4: Control device 5a to 5e: Powder surface level measuring instrument 6a to 6e: Measuring means for calculating the consumption of pulverized coal per unit time

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭56−56434(JP,A) 特開 昭58−216837(JP,A) 特開 昭61−124434(JP,A) 実公 昭52−11335(JP,Y1) (58)調査した分野(Int.Cl.6,DB名) B65G 65/30 - 65/48 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-56-56434 (JP, A) JP-A-58-216837 (JP, A) JP-A-61-124434 (JP, A) 11335 (JP, Y1) (58) Field surveyed (Int. Cl. 6 , DB name) B65G 65/30-65/48

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 元ホッパに順次受ける粉粒体を複数のバ
ンカに各バンカ内の物理的特性等が均一になるように補
給する方法であって、バンカ毎に優先順位を定量化して
重み付けするとともに、各バンカの粉粒面レベルおよび
単位時間当たりの粉粒体消費量を測定し、その実測値の
大小に応じて各バンカの粉粒面レベルおよび単位時間当
たりの粉粒体消費量をそれぞれ重み付けし、次いでこれ
ら優先順位、粉粒面レベル、単位時間当たりの粉粒体消
費量の各重みのバンカ毎の和を求め、この重みの和の総
和を求めると同時にこの総和に対する各バンカの和の比
率を求めその比率に応じて粉粒体の補給量を各バンカに
配分して補給することを特徴とする元ホッパから複数バ
ンカへの粉粒体補給方法。
1. A method of replenishing granular materials sequentially received by an original hopper to a plurality of bunkers so that physical characteristics and the like in each bunker become uniform, and quantifies and weights priorities for each bunker. At the same time, the granular surface level of each bunker and the granular material consumption per unit time are measured, and the granular surface level of each bunker and the granular material consumption per unit time are respectively determined according to the magnitude of the measured value. The weights are then obtained, and the sum of the weights of the priority, the grain surface level, and the amount of the granules consumed per unit time is obtained for each bunker, and the sum of the sums of the weights is obtained, and at the same time, the sum of each bunker for this sum is obtained. A method of replenishing powder and granules from an original hopper to a plurality of bunkers, wherein the replenishment amount of powder and granules is distributed to each bunker according to the ratio.
【請求項2】 上記請求項1記載の元ホッパから複数バ
ンカへの粉粒体補給方法において、バンカ毎の重みの大
きいものから順に複数選択してその重みの総和を求め、
選択されたバンカのみ、その総和に対する各バンカの和
の比率を求めその比率に応じて粉粒体の補給量を各バン
カに配分して補給する元ホッパから複数バンカへの粉粒
体補給方法。
2. A method for replenishing powdery and granular materials from an original hopper to a plurality of bunkers according to claim 1, wherein a plurality of bunkers are selected in descending order of weight, and the sum of the weights is obtained.
A method for replenishing a plurality of bunkers from an original hopper, in which a ratio of a sum of each bunker to a total sum of only selected bunkers is determined and a replenishment amount of the granules is distributed to each bunker according to the ratio and replenished.
JP4278351A 1992-10-16 1992-10-16 How to replenish powder and granular material to multiple bunker from former hopper Expired - Fee Related JP2972462B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4278351A JP2972462B2 (en) 1992-10-16 1992-10-16 How to replenish powder and granular material to multiple bunker from former hopper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4278351A JP2972462B2 (en) 1992-10-16 1992-10-16 How to replenish powder and granular material to multiple bunker from former hopper

Publications (2)

Publication Number Publication Date
JPH06127700A JPH06127700A (en) 1994-05-10
JP2972462B2 true JP2972462B2 (en) 1999-11-08

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Country Link
JP (1) JP2972462B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6245197B2 (en) * 2015-03-06 2017-12-13 Jfeスチール株式会社 Raw material level control method, raw material blending method, raw material level control device and raw material blending device

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