JP2007204179A - Powder level control method and device - Google Patents

Powder level control method and device Download PDF

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JP2007204179A
JP2007204179A JP2006022383A JP2006022383A JP2007204179A JP 2007204179 A JP2007204179 A JP 2007204179A JP 2006022383 A JP2006022383 A JP 2006022383A JP 2006022383 A JP2006022383 A JP 2006022383A JP 2007204179 A JP2007204179 A JP 2007204179A
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hopper
storage
discharge
amount
powder
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JP4992033B2 (en
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Shingo Sugioka
真吾 杉岡
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JFE Steel Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a powder level control method and a device controlling a powder level in a second hopper on a downstream side to a constant level. <P>SOLUTION: A weighing set value, i.e., a discharge target amount predetermined relative to a first discharge device is corrected based on a correction amount calculated based on a value obtained by measuring the present storage amount of the second storage hopper by a second weighing means and a discharge actual measurement value measured by a first weighing means to determine a discharge set value. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、貯蔵ホッパーから排出した粉粒体をコンベアなどの輸送手段を用いて輸送して、異なる受け側ホッパーに投入し、この受け側ホッパーに投入した後、この受け側ホッパーから下流側の設備に粉粒体を供給するための粉粒体供給設備における粉粒体のレベル制御方法および装置に関するものである。   In the present invention, the granular material discharged from the storage hopper is transported using a transportation means such as a conveyor, put into a different receiving hopper, put into the receiving hopper, and then downstream from the receiving hopper. The present invention relates to a method and an apparatus for controlling the level of powder in a powder supply facility for supplying powder to a facility.

従来の鉄鋼プロセスにおける粉粒体(石炭、コークスなど)を原料とする処理設備(高炉など)に、原料である粉粒体を投入する方法としては、第1の貯蔵ホッパー(以下、第1ホッパーと称する)から切り出した粉粒体をコンベヤを用いて輸送して、下流側の第2の貯蔵ホッパー(以下、第2ホッパーと称する)に投入し、この第2ホッパーに投入した粉粒体をさらに下流側の処理設備に供給するという方法を通常とっている。この際、第1ホッパーから定量を切り出す第1の原料排出装置(以下、第1排出装置と称する)により一定量(一定重量)の粉粒体を切り出し、コンベヤにより第2ホッパーに輸送し、さらに第2ホッパーから第2の原料排出装置(以下、第2排出装置と称する)により下流側の処理設備に粉粒体を供給するという形態をとっている。   As a method of charging the granular material, which is a raw material, into a processing facility (such as a blast furnace) using the granular material (coal, coke, etc.) as a raw material in a conventional steel process, a first storage hopper (hereinafter referred to as a first hopper) The granular material cut out from the second hopper is transported by using a conveyor, is put into a second storage hopper on the downstream side (hereinafter referred to as a second hopper), and the granular material charged into the second hopper is Furthermore, the method of supplying to the downstream processing equipment is usually taken. At this time, a fixed amount (a constant weight) of the granular material is cut out by a first raw material discharge device (hereinafter referred to as a first discharge device) that cuts a fixed amount from the first hopper, and transported to the second hopper by a conveyor. It takes the form of supplying a granular material from the 2nd hopper to the processing facility of a downstream by the 2nd raw material discharge device (henceforth a 2nd discharge device).

この第2ホッパーに投入される粉粒体のレベル制御は、第1ホッパーから第1排出装置により切り出す粉粒体量を増減したり、コンベヤの起動停止を行うことによって行われている。   The level control of the granular material thrown into this 2nd hopper is performed by increasing / decreasing the amount of the granular material cut out by the 1st discharge device from the 1st hopper, or performing starting stop of a conveyor.

しかしながら、第1ホッパーの秤量器と第2ホッパーの秤量器の計測値は厳密には一致しておらず、両者に誤差が発生するため、第2ホッパーの貯蔵量が容量を超えてしまうオーバーフローの状態となったり、逆に予備用バックアップとして予め予定していたバッファー量よりも第2ホッパーの貯蔵量が減少してしまう場合がある。   However, the measured values of the first hopper weigher and the second hopper weigher are not exactly the same, and an error occurs between the two, so that the amount of storage in the second hopper exceeds the capacity. In some cases, the amount of storage in the second hopper may be smaller than the amount of buffer scheduled in advance as a backup for backup.

このような場合、第2ホッパーが満杯になって粉粒体が溢れ出すのを予防するためには、第2ホッパーのレベル設定値を低めにしておく方法がある。しかし、通常この第2ホッパーには、第1ホッパーの故障時に備えてのバッファー機能として、設備投入量の数チャージ分の貯蔵容量を有しているため、オーバーフローにそなえて安全をみてレベル設定値を低くし過ぎると今度は第2ホッパーの粉粒体量が少なくなりすぎて、そのバッファー機能を有効活用できないということにもなり、過不足のないレベル設定を行うのは簡単ではない。   In such a case, in order to prevent the second hopper from becoming full and overflowing the granular material, there is a method of keeping the level setting value of the second hopper low. However, this second hopper usually has a storage capacity for several charges of the amount of equipment input as a buffer function in case of failure of the first hopper. If the value is too low, the amount of powder in the second hopper becomes too small, and the buffer function cannot be used effectively, and it is not easy to set the level without excess or deficiency.

また、第2ホッパーの粉粒体量が多くなった段階でコンベヤを停止した場合は、コンベヤ上に残留する粉粒体のためにコンベヤ再起動時における駆動装置の負荷が大きくなり、これに対処するには容量の大きな電動機を要することになる。   Also, if the conveyor is stopped when the amount of powder in the second hopper has increased, the load on the drive unit when the conveyor is restarted increases because of the particles remaining on the conveyor. This requires a large capacity electric motor.

以上のような問題を解決する技術として、特許文献1には、コンベヤ上の粉粒体量と、第2ホッパー内の粉粒体量との和を、第2ホッパー内の粉粒体量とみなして、コンベヤへの切り出し量を制御することで、コンベヤと第2ホッパーとを含めた系により粉粒体の重量を一定に保つ技術が開示されている。
特開2000−118718号公報
As a technique for solving the above problems, Patent Document 1 describes the sum of the amount of powder on the conveyor and the amount of powder in the second hopper as the amount of powder in the second hopper. In view of this, a technique is disclosed in which the weight of the granular material is kept constant by a system including the conveyor and the second hopper by controlling the amount cut out to the conveyor.
JP 2000-118718 A

しかしながら、特許文献1に記載の技術でも、第1ホッパーの秤量器と第2ホッパーの秤量器の計測値が厳密には一致していないという点を解消している訳ではないために、その誤差から、算出されるコンベア上の粉粒体重量にも誤差が蓄積されてしまうこととなる。このため、従来発生していた第2ホッパーの貯蔵量が一定とならないといった問題の根本的な解決には至っていないという問題がある。   However, even the technique described in Patent Document 1 does not eliminate the point that the measured values of the weighing device of the first hopper and the weighing device of the second hopper do not exactly coincide with each other. Therefore, an error is accumulated in the calculated weight of the powder on the conveyor. For this reason, there is a problem that a fundamental solution of the problem that the storage amount of the second hopper that has conventionally occurred is not constant has been reached.

本発明は上記事情に鑑みてなされたもので、下流側の第2ホッパー内の粉粒体レベルを一定に制御する粉粒体のレベル制御方法および装置を提供することを目的とする。   This invention is made | formed in view of the said situation, and it aims at providing the level control method and apparatus of a granular material which controls the granular material level in the downstream 2nd hopper uniformly.

本発明の請求項1に係る発明は、粉粒体を一時貯蔵する第1の貯蔵ホッパーから排出し、前記粉粒体を輸送して一時貯蔵する第2の貯蔵ホッパーに投入するに際し、前記第1の貯蔵ホッパーから排出する排出設定値を、前記第1の貯蔵ホッパーの排出実測値および前記第2の貯蔵ホッパーの貯蔵量を計測した値に基づいて決定することにより前記第2の貯蔵ホッパーの粉粒体レベルを制御することを特徴とする粉粒体のレベル制御方法である。   In the invention according to claim 1 of the present invention, when the powder is discharged from the first storage hopper that temporarily stores the granular material, and is transported to the second storage hopper that temporarily stores the granular material, the first By determining a discharge set value to be discharged from one storage hopper based on a discharge actual measurement value of the first storage hopper and a value obtained by measuring a storage amount of the second storage hopper, the second storage hopper It is a level control method of a granular material characterized by controlling a granular material level.

また本発明の請求項2に係る発明は、粉粒体を一時貯蔵する第1の貯蔵ホッパーと、この第1の貯蔵ホッパーから粉粒体を排出する、第1の秤量手段を有する第1の排出装置と、排出された粉粒体を輸送する輸送手段と、その下流でさらに一時貯蔵する、第2の秤量手段を有する第2の貯蔵ホッパーとを備えた粉粒体供給設備における第2の貯蔵ホッパーの粉粒体レベルを制御する粉粒体のレベル制御装置であって、該レベル制御装置は、前記排出装置に対する排出設定値を、予め決められた排出目標量である秤量設定値と、第2の秤量手段で第2の貯蔵ホッパーの現在の貯蔵量を計測した値に基づいて算出した補正量と、第1の秤量手段で計測した排出実測値とに基づいて求めることを特徴とする粉粒体のレベル制御装置である。   The invention according to claim 2 of the present invention includes a first storage hopper for temporarily storing powder particles, and a first weighing means for discharging the powder particles from the first storage hopper. 2nd in the granular material supply equipment provided with the discharge | emission apparatus, the transport means which conveys the discharged | emitted granular material, and the 2nd storage hopper which has a 2nd weighing | measuring means further temporarily stored in the downstream. A granular level control device for controlling a granular level of a storage hopper, wherein the level control device sets a discharge set value for the discharge device, a weighing set value that is a predetermined discharge target amount, and It is calculated | required based on the correction amount computed based on the value which measured the present storage amount of the 2nd storage hopper with the 2nd weighing means, and the discharge actual value measured by the 1st weighing means. It is a level control apparatus of a granular material.

なお、本発明は、2つのホッパーの組合せのみに限らず、2個より多い数のホッパーからの粉粒体の搬送装置であっても、前後2個のセット(「i+1番目(下流側ホッパー)」の情報を、「i番目(上流側ホッパー)」にフィードバックする)を複数のセット、組合せていくことで、適用可能であることはいうまでもない。   Note that the present invention is not limited to the combination of two hoppers, and even if it is a conveying device for powder particles from more than two hoppers, a set of two front and rear ("i + 1th (downstream side) Needless to say, it is possible to apply the information by feeding back the information of “hopper” to the “i-th (upstream hopper)” in a plurality of sets.

本発明は、第1排出装置の排出目標設定値に、第2ホッパーにおける現在の貯蔵量を計測した値に基づいて算出した補正量と、第1ホッパーの秤量器で計測した実測値の値をフィードバックするようにしたので、第2ホッパーレベルを一定に制御することが出来るようになり、第2ホッパーからのオーバーフローや予定していたバッファー量よりも少なくなるといったトラブルがなくなった。   In the present invention, the discharge target set value of the first discharge device is set to a correction amount calculated based on a value obtained by measuring a current storage amount in the second hopper, and an actual measurement value measured by the weighing device of the first hopper. Since the feedback is provided, the second hopper level can be controlled to be constant, and there is no trouble such as overflow from the second hopper or less than the planned buffer amount.

本発明を実施するための最良の形態について、以下に図および式を参照して説明を行う。図1は、本発明が係る粉粒体供給装置の概要を示す図である。図中、1は第1ホッパー、2は第2ホッパー、3は第1排出装置、4は秤量器、5は第2排出装置、6はレベル計、7はコンベア、および8はレベル制御装置をそれぞれ表す。   The best mode for carrying out the present invention will be described below with reference to the drawings and equations. FIG. 1 is a diagram showing an outline of a granular material supply apparatus according to the present invention. In the figure, 1 is a first hopper, 2 is a second hopper, 3 is a first discharge device, 4 is a weighing device, 5 is a second discharge device, 6 is a level meter, 7 is a conveyor, and 8 is a level control device. Represent each.

粉粒体(石炭やコークスなどの原料)は、粉粒体を収容した第1ホッパー1から、所定の重量を切り出し可能な、秤量器4を備えた第1排出装置3によって、コンベア7の上に排出される。そして、コンベア7によって第2ホッパー2まで搬送されて、第2ホッパー2に投入される。さらに、第2ホッパー2から粉粒体を所定量を切り出して、処理設備((図示せず、例えば、高炉など)に供給される。   The powder (raw material such as coal and coke) is transferred onto the conveyor 7 by the first discharge device 3 equipped with a weighing device 4 capable of cutting out a predetermined weight from the first hopper 1 containing the powder. To be discharged. Then, it is conveyed to the second hopper 2 by the conveyor 7 and is put into the second hopper 2. Further, a predetermined amount of the granular material is cut out from the second hopper 2 and supplied to a processing facility (not shown, for example, a blast furnace).

本発明では、第2ホッパー2に貯蔵されている粉粒体レベルを一定に保つように制御するものであり、粉粒体を一時貯蔵する第1ホッパー1における第1排出装置3で切り出す粉粒体の量を調整するためのものである。   In this invention, it controls so that the granular material level stored in the 2nd hopper 2 may be kept constant, and the granular material cut out with the 1st discharge device 3 in the 1st hopper 1 which temporarily stores a granular material. It is for adjusting the amount of the body.

なお、第2ホッパー2は、処理設備への一度に供給する量の数倍(例えば、3倍から5倍程度)の容量を有している。また、第1ホッパー1から切り出される粉粒体の量は、第2ホッパー2の数分の1程度の量である。よって、第1ホッパー1からの排出やコンベア7の運転トラブル等の故障が発生した場合においても、少なくとも数回分程度の供給量を第2ホッパーに貯蔵可能であり、それを処理設備に供給することによって、全体の設備を停止することなく、操業可能としている。   In addition, the 2nd hopper 2 has a capacity | capacitance several times (for example, about 3 to 5 times) the quantity supplied to the processing equipment at once. Further, the amount of the granular material cut out from the first hopper 1 is about one-fifth the amount of the second hopper 2. Therefore, even when a failure such as discharge from the first hopper 1 or operation trouble of the conveyor 7 occurs, the supply amount of at least several times can be stored in the second hopper and supplied to the processing equipment. Therefore, it is possible to operate without stopping the entire equipment.

なお、この2つの貯蔵ホッパーにおける、粉粒体の切り出し量(排出量)や切り出し(排出)タイミング等は、ホッパー制御装置8によって制御、調整されている。   Note that the cutout amount (discharge amount), cutout (discharge) timing, and the like of the powder particles in these two storage hoppers are controlled and adjusted by the hopper control device 8.

図2は、本発明に係るレベル制御装置における信号処理フローを示すブロック図である。さらに図3は、本発明に係るレベル制御装置における信号処理フローを示すフローチャートである。   FIG. 2 is a block diagram showing a signal processing flow in the level control apparatus according to the present invention. FIG. 3 is a flowchart showing a signal processing flow in the level control apparatus according to the present invention.

まず第1ホッパーに対して、第1排出装置で切り出す量の目標設定値である、秤量設定値SV0が与えられる。この値は、コンベアの搬送能力や第2ホッパーから処理設備に供給する1回分の量などから予め決定された量である。   First, a weighing set value SV0, which is a target set value of the amount to be cut out by the first discharging device, is given to the first hopper. This value is a predetermined amount based on the conveying capacity of the conveyor and the amount of one time supplied from the second hopper to the processing facility.

本発明では、この秤量設定値に対して、第2ホッパーにおける現在の貯蔵量を計測した値に基づいて算出した補正量と、第1ホッパーの秤量器で計測した実測値の値をフィードバックすることによって、第1ホッパーへの切り出し量を決定し、その値を切り出し装置に設定する。   In the present invention, the correction amount calculated based on the value obtained by measuring the current storage amount in the second hopper and the value of the actual measurement value measured by the first hopper weighing device are fed back to the weighing setting value. To determine the cutout amount to the first hopper and set the value in the cutout device.

以下に、第2ホッパーにおける現在の貯蔵量に基づいて行う、補正の方法を説明する。
まず、第2ホッパーの貯蔵量(貯蔵重量)を計測するには、第2ホッパー上部に設定されたレベル計6を用いる。このレベル計6は、一般的には貯留された粉粒体の表面位置を計測できる距離センサで十分であり、例えばレーザ距離計などで十分である。このレベル計によって、貯蔵されている粉粒体(原料)の高さを算出し、この高さレベルにもとづいて、予め設定されているレベルを重量に換算するための検量データを用いて、第2ホッパー内の重量に換算して、求める。
Hereinafter, a correction method performed based on the current storage amount in the second hopper will be described.
First, in order to measure the storage amount (storage weight) of the second hopper, a level meter 6 set at the upper part of the second hopper is used. The level meter 6 is generally a distance sensor that can measure the surface position of the stored granular material, and a laser distance meter, for example, is sufficient. With this level meter, the height of the stored granular material (raw material) is calculated, and based on this height level, calibration data for converting a preset level into weight is used. 2 Calculated by converting to the weight in the hopper.

この貯蔵量Wが、予め設定されている所定の貯蔵目標重量Wと比較して、その偏差ΔWによって、第1ホッパーの切り出し量の補正量δを決定する。 The storage amount W is compared with a predetermined storage target weight W 0 set in advance, and the correction amount δ of the cut-out amount of the first hopper is determined by the deviation ΔW.

ΔW=W―W・・・・(1)
なお、第2ホッパーの貯蔵量は、第2ホッパーに直接計測可能な秤量器を有していれば、それによって計測してもよい。
ΔW = W−W 0 (1)
In addition, if the 2nd hopper has the measuring instrument which can be measured directly, you may measure the storage amount of a 2nd hopper.

補正量算出処理の手順は、以下の通りである。
Wmax:補正判断重量上限値、Wmin:補正判断重量下限値とすると、以下に示す(2)式を満足する場合には、第2ホッパーの貯蔵量が多すぎる。
The procedure of the correction amount calculation process is as follows.
Assuming that Wmax is the correction judgment weight upper limit value and Wmin is the correction judgment weight lower limit value, the storage amount of the second hopper is too large when the following expression (2) is satisfied.

ΔW>Wmax・・・(2)
あるいは、以下に示す(3)式を満足する場合には、第2ホッパーの貯蔵量が少なすぎる状態となっていると判断する。
ΔW> Wmax (2)
Alternatively, when the following expression (3) is satisfied, it is determined that the storage amount of the second hopper is too small.

ΔW<Wmin ・・・(3)
このように、(2)式または(3)式の条件を満足する場合には、第1ホッパーでの切り出し量を補正する必要がある、と判断し、偏差ΔWを、補正量δとして加える。
また、以下に示す(4)式を満足する場合は、正常な操業であると判断し、補正量δ=0を出力する(すなわち補正しない)。
ΔW <Wmin (3)
As described above, when the condition of the expression (2) or (3) is satisfied, it is determined that it is necessary to correct the cutout amount in the first hopper, and the deviation ΔW is added as the correction amount δ.
If the following expression (4) is satisfied, it is determined that the operation is normal, and the correction amount δ = 0 is output (that is, not corrected).

Wmin ≦ ΔW ≦ Wmax ・・・(4)
なお、本発明は、2つのホッパーの組合せのみに限らず、2個より多い数のホッパーから粉粒体の搬送装置であっても、前後2個を、前述の説明において、上流ホッパーを第1ホッパー、下流ホッパーを第2ホッパーと考えることによって、N個のホッパーを備えた設備において、i+1番目ホッパー(上流から1番、2番と数えるものとする)を下流側ホッパーで第2ホッパーとし、その情報をi番目(上流側ホッパー)の第1ホッパーにフィードバックすると考えれば、2個より多い数のホッパーを備えて設備においても、順次に組合せていくことで、適用可能であることはいうまでもない。また、全てのホッパーに適用しても良いし、任意のホッパーに限定して適用してもよい。
Wmin ≦ ΔW ≦ Wmax (4)
Note that the present invention is not limited to the combination of two hoppers, and even if it is a conveying device for a granular material from more than two hoppers, the upstream hopper is the first in the above description. By considering the hopper and the downstream hopper as the second hopper, in the facility equipped with N hoppers, the i + 1 hopper (which is counted as No. 1 and No. 2 from the upstream) is the second hopper at the downstream hopper. If the information is considered to be fed back to the first hopper of the i-th (upstream hopper), it can be applied by combining more than two hoppers in order and combining them sequentially. Needless to say. Moreover, you may apply to all the hoppers, and you may apply limiting to arbitrary hoppers.

以上のように補正値δを求めたら、秤量設定値SV0から(5)式のように設定値SV1を求める。
設定値SV1=秤量設定値SV0−補正量δ ・・・(5)
さらに、第1排出装置の計量器から秤量実績PVを得て、秤量補正値ΔVを(6)式のように求める。
秤量補正値ΔV=設定値SV1−秤量実績PV ・・・(6)
そして、最終的に第1ホッパーの第1排出装置に与える設定値SV2は、(7)式のように求める。
設定値SV2=設定値SV1−秤量補正値ΔV ・・・(7)
When the correction value δ is obtained as described above, the set value SV1 is obtained from the weighing set value SV0 as shown in equation (5).
Set value SV1 = Weighing set value SV0-Correction amount δ (5)
Further, a weighing result PV is obtained from the weighing device of the first discharging device, and a weighing correction value ΔV is obtained as in equation (6).
Weighing correction value ΔV = Setting value SV1 – Actual weighing PV (6)
Then, the set value SV2 finally given to the first discharging device of the first hopper is obtained as in equation (7).
Set value SV2 = Set value SV1 – Weighing correction value ΔV (7)

本発明が係る粉粒体供給装置の概要を示す図である。It is a figure which shows the outline | summary of the granular material supply apparatus which this invention concerns. 本発明に係るレベル制御装置における信号処理フローを示すブロック図である。It is a block diagram which shows the signal processing flow in the level control apparatus which concerns on this invention. 本発明に係るレベル制御装置における信号処理フローを示すフローチャートである。It is a flowchart which shows the signal processing flow in the level control apparatus which concerns on this invention.

符号の説明Explanation of symbols

1 第1ホッパー
2 第2ホッパー
3 第1排出装置
4 秤量器
5 第2排出装置
6 レベル計
7 コンベア
8 レベル制御装置
DESCRIPTION OF SYMBOLS 1 1st hopper 2 2nd hopper 3 1st discharge device 4 Weighing device 5 2nd discharge device 6 Level meter 7 Conveyor 8 Level control device

Claims (2)

粉粒体を一時貯蔵する第1の貯蔵ホッパーから排出し、前記粉粒体を輸送して一時貯蔵する第2の貯蔵ホッパーに投入するに際し、
前記第1の貯蔵ホッパーから排出する排出設定値を、前記第1の貯蔵ホッパーの排出実測値および前記第2の貯蔵ホッパーの貯蔵量を計測した値に基づいて決定することにより前記第2の貯蔵ホッパーの粉粒体レベルを制御することを特徴とする粉粒体のレベル制御方法。
When discharging from the first storage hopper for temporarily storing the powder, and transporting the powder to the second storage hopper for temporary storage,
The second storage is determined by determining a discharge set value to be discharged from the first storage hopper based on a measured discharge value of the first storage hopper and a value obtained by measuring a storage amount of the second storage hopper. A method for controlling the level of powder particles, comprising controlling the level of powder particles in a hopper.
粉粒体を一時貯蔵する第1の貯蔵ホッパーと、この第1の貯蔵ホッパーから粉粒体を排出する、第1の秤量手段を有する第1の排出装置と、排出された粉粒体を輸送する輸送手段と、その下流でさらに一時貯蔵する、第2の秤量手段を有する第2の貯蔵ホッパーとを備えた粉粒体供給設備における第2の貯蔵ホッパーの粉粒体レベルを制御する粉粒体のレベル制御装置であって、
該レベル制御装置は、
前記排出装置に対する排出設定値を、
予め決められた排出目標量である秤量設定値と、
第2の秤量手段で第2の貯蔵ホッパーの現在の貯蔵量を計測した値に基づいて算出した補正量と、
第1の秤量手段で計測した排出実測値とに基づいて求めることを特徴とする粉粒体のレベル制御装置。
A first storage hopper for temporarily storing powder, a first discharge device having a first weighing means for discharging the powder from the first storage hopper, and transporting the discharged powder For controlling the granular material level of the second storage hopper in the granular material supply facility comprising a transporting means for transporting and a second storage hopper having a second weighing means for further temporary storage downstream thereof A body level control device,
The level controller is
The discharge setting value for the discharge device is
A weighing set value which is a predetermined discharge target amount;
A correction amount calculated based on a value obtained by measuring the current storage amount of the second storage hopper by the second weighing means;
A level control apparatus for a granular material, which is obtained based on an actual discharge value measured by a first weighing means.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013195400A (en) * 2012-03-22 2013-09-30 Chugoku Electric Power Co Inc:The Weight measurement apparatus and weight measurement method
CN104097876A (en) * 2014-07-07 2014-10-15 三一汽车制造有限公司 Powder tank material level real-time detecting system and method and mixing station

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JPS57117422A (en) * 1981-01-14 1982-07-21 Nippon Steel Corp Method of controlling delivery of powdery material
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JPH05332804A (en) * 1991-02-14 1993-12-17 Teiriyou Sangyo Kk Powder particle constant supplier
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JPS4914845Y1 (en) * 1970-09-17 1974-04-12
JPS5325071U (en) * 1976-08-10 1978-03-03
JPS5464356A (en) * 1977-10-29 1979-05-24 Ebara Corp Method of controlling powder feeding
JPS57117422A (en) * 1981-01-14 1982-07-21 Nippon Steel Corp Method of controlling delivery of powdery material
JPS6179120A (en) * 1984-09-26 1986-04-22 Yamato Scale Co Ltd Device for supplying fixed quantity
JPH05332804A (en) * 1991-02-14 1993-12-17 Teiriyou Sangyo Kk Powder particle constant supplier
JP2000118718A (en) * 1998-10-15 2000-04-25 Kawasaki Steel Corp Granular material level control method for receiving hopper
JP2005327118A (en) * 2004-05-14 2005-11-24 Kyowa:Kk Multivariable control optimization program and volumetric feeder

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013195400A (en) * 2012-03-22 2013-09-30 Chugoku Electric Power Co Inc:The Weight measurement apparatus and weight measurement method
CN104097876A (en) * 2014-07-07 2014-10-15 三一汽车制造有限公司 Powder tank material level real-time detecting system and method and mixing station

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