JPH04365725A - Powder feeder - Google Patents

Powder feeder

Info

Publication number
JPH04365725A
JPH04365725A JP16743191A JP16743191A JPH04365725A JP H04365725 A JPH04365725 A JP H04365725A JP 16743191 A JP16743191 A JP 16743191A JP 16743191 A JP16743191 A JP 16743191A JP H04365725 A JPH04365725 A JP H04365725A
Authority
JP
Japan
Prior art keywords
powder
blowing
hopper
gas
pulverized coal
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
JP16743191A
Other languages
Japanese (ja)
Other versions
JPH07100545B2 (en
Inventor
Hisao Ishii
石井 久生
Tsunemi Hayashi
恒美 林
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.)
Akatake Engineering Co Ltd
Nippon Steel Corp
Original Assignee
Akatake Engineering Co Ltd
Nippon Steel Corp
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 Akatake Engineering Co Ltd, Nippon Steel Corp filed Critical Akatake Engineering Co Ltd
Priority to JP3167431A priority Critical patent/JPH07100545B2/en
Publication of JPH04365725A publication Critical patent/JPH04365725A/en
Publication of JPH07100545B2 publication Critical patent/JPH07100545B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Air Transport Of Granular Materials (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Blast Furnaces (AREA)

Abstract

PURPOSE:To suppress the compaction of powder in a hopper so as to stably supply powder to an air stream transport pipe in the case of intermittently discharging powder from a hopper and transporting the same with air stream. CONSTITUTION:Powder storing containers 5 each having a stirring blade 6 are respectively provided below plural powder blowing hoppers 4 arranged side by side below a powder tank. There are provided structures 11, 12 for always blowing gas for fluidizing powder in the storing containers 5 and structures 13, 14 for blowing gas for assisting the transport for an intermittently discharged powder in an intermittent discharge ports of the storing containers 5. Thus, the starting resistance in the lower portion of the powder blowing hopper can be decreased, the capacity of a driving motor can be reduced, and abrasion of parts can be lessened. Furthermore, the mixture of powder and air stream can be promoted so as to stably supply the power continuously.

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、高炉への微粉炭あるい
は微粉鉱石の吹き込みをはじめとして、セメント等の分
野における粉体(粉粒またはこれらの混合体を示す)搬
送に適用可能な粉体供給装置に関するものである。
[Industrial Application Field] The present invention is applicable to the transportation of powder (indicating granules or a mixture thereof) in fields such as cement, as well as the injection of pulverized coal or pulverized ore into blast furnaces. This relates to a supply device.

【0002】0002

【従来の技術】一般的に言って、粉体供給装置は粉体を
貯留するホッパーの下部に配置されており、粉体の自重
が粉体供給装置にかかっている。ホッパーに投入された
直後の粉体は空気などの気体が混在しているため、当初
流動性の良い状態であっても、投入後の貯留時間が長く
なると粉体層から気体が抜け出し、圧密化してくる。ま
た、一般にホッパーの下部は逆円錐状になっているため
、排出により粉体層が下方に移動するにしたがって圧密
化は増長され、粉体供給装置への粉体の円滑的導入が難
しくなる。
2. Description of the Related Art Generally speaking, a powder supply device is placed below a hopper for storing powder, and the weight of the powder is applied to the powder supply device. Immediately after being charged into the hopper, the powder is mixed with air and other gases, so even if it is initially fluid, the longer it is stored for a longer time after being charged, the more gas will escape from the powder layer and it will become compacted. It's coming. Furthermore, since the lower part of the hopper generally has an inverted conical shape, as the powder layer moves downward due to discharge, compaction increases, making it difficult to smoothly introduce the powder into the powder supply device.

【0003】そのため、従来は圧密化の緩和あるいは防
止を目的としてホッパー内に気体を吹き込むことで粉体
を流動化させているが、粉体供給装置の収容容器内部に
は気体で粉体の流動化を促進する機能は装備されておら
ず、攪拌翼を動かすことで強制的に流動化状態に近づけ
ている。
[0003] Conventionally, therefore, powder is fluidized by blowing gas into the hopper in order to alleviate or prevent compaction. It is not equipped with a function to promote fluidization, and is forced to approach a fluidized state by moving stirring blades.

【0004】この方法では攪拌翼にかかる抵抗は大きく
、攪拌翼駆動用電動機の容量が大きくなると同時に、攪
拌翼自体及び軸等の機械部品も大きなものが必要となる
。特に、粉体が圧密化された状態で停止状態から粉体供
給装置を起動するときは、多大な抵抗がかかり起動でき
ず、また機器の破損につながることがある。粉体の圧密
状態により起動時の初期切出量の変動も大きい。従って
、粉体を安定的に連続供給することは困難となる。この
ため、起動時だけのための電動機容量の増大及び攪拌翼
等の機械強度が必要となり、設備のコストアップになっ
ている(特開昭63−169315号公報)。
[0004] In this method, the resistance applied to the stirring blade is large, and the capacity of the electric motor for driving the stirring blade becomes large, and at the same time, the stirring blade itself and mechanical parts such as the shaft are also required to be large. Particularly, when starting the powder supply device from a stopped state in a state where the powder is compacted, a large amount of resistance is encountered and the device cannot be started, which may lead to damage to the device. The initial cutting amount at startup varies greatly depending on the compaction state of the powder. Therefore, it becomes difficult to stably and continuously supply powder. For this reason, an increase in the capacity of the motor and mechanical strength of the stirring blades and the like are required only for the start-up, which increases the cost of the equipment (Japanese Unexamined Patent Publication No. 169315/1983).

【0005】[0005]

【発明が解決しようとする課題】並列に複数個配列され
た粉体吹込ホッパーを交互に切り替え、粉体を連続して
排出し、これを連続搬送するには、従来の粉体供給装置
では、待機している粉体吹込ホッパーは貯留時間が長く
なることから、該吹込ホッパー内の粉体の圧密化が増長
され、排出時に攪拌翼の起動に多大の動力が必要となり
、切替時の初期切出量の変動が大きいため該吹込ホッパ
ー間のスムーズな切替えができないから安定な連続供給
もできない。
[Problems to be Solved by the Invention] In order to alternately switch between a plurality of powder blowing hoppers arranged in parallel, continuously discharge powder, and continuously transport the powder, the conventional powder supply device requires the following steps. Since the powder blowing hopper that is on standby has a long storage time, the compaction of the powder in the blowing hopper increases, and a large amount of power is required to start the stirring blades at the time of discharge. Due to large fluctuations in the output amount, smooth switching between the blow hoppers is not possible, and stable continuous supply is also not possible.

【0006】本発明は、特に粉体吹込ホッパーからの粉
体の切り出しに要する動力の低減と該吹込ホッパー間の
スムーズな切替えが可能で、粉体の安定な連続供給がで
きる粉体供給装置を提供するものである。
[0006] The present invention particularly provides a powder feeding device that is capable of reducing the power required to cut out powder from a powder blowing hopper, and smoothly switching between the blowing hoppers, and capable of stably and continuously supplying powder. This is what we provide.

【0007】[0007]

【課題を解決するための手段】本発明は、粉体貯槽の下
方に並列配置された複数の粉体吹込ホッパーの下部にそ
れぞれ攪拌翼を備えた粉体収容容器を設け、この収容容
器内に粉体を流動化させるためのガスを常時吹き込むと
ともに、該収容容器の切出口部に切出粉体の搬送を補助
するためのガスを吹き込む構造を備えたことを特徴とす
る粉体供給装置である。
[Means for Solving the Problems] The present invention provides a powder storage container each equipped with a stirring blade at the lower part of a plurality of powder blowing hoppers arranged in parallel below a powder storage tank. A powder supply device characterized by having a structure for constantly blowing gas for fluidizing the powder and for blowing gas for assisting the conveyance of the cut powder into the cutting opening of the storage container. be.

【0008】[0008]

【作用】本発明は、粉体吹込ホッパー下部の粉体収容容
器内の粉体を、ガスの吹込と攪拌翼の回転によって常に
流動状態に維持するとともに、該吹込ホッパーからの切
出しに際しては、該吹込ホッパーの切出口部へ搬送補助
ガスを吹込むことによって、該吹込ホッパーから粉体を
円滑に粉体搬送管に切出し可能とする。
[Operation] The present invention maintains the powder in the powder storage container at the bottom of the powder blowing hopper in a fluid state by blowing gas and rotating the stirring blade, and when cutting out the powder from the blowing hopper. By blowing the transport auxiliary gas into the cut-out port of the blow hopper, the powder can be smoothly cut out from the blow hopper into the powder transport pipe.

【0009】[0009]

【実施例】以下、本発明の一実施例について説明する。[Embodiment] An embodiment of the present invention will be described below.

【0010】図1及び図2は、本発明を高炉への微粉炭
吹込みのための微粉炭供給装置として適用した例を示す
図である。
FIGS. 1 and 2 are diagrams showing an example in which the present invention is applied as a pulverized coal supply device for injecting pulverized coal into a blast furnace.

【0011】予め所定の粒度範囲に調整された微粉炭C
を貯蔵する粉炭貯槽1の下部には、充填管2,2′、充
填弁3,3′を介して粉体吹込ホッパー4,4′が接続
されている。
[0011] Pulverized coal C adjusted in advance to a predetermined particle size range
Powder blowing hoppers 4, 4' are connected to the lower part of the pulverized coal storage tank 1, which stores pulverized coal, through filling pipes 2, 2' and filling valves 3, 3'.

【0012】この粉体吹込ホッパー4,4′の下部には
粉体収容容器5,5′が設けられ、粉体収容容器5,5
′内には攪拌翼6,6′が回転自在に設けられており、
攪拌翼6,6′は駆動装置M,M′により回転テーブル
7,7′を介して回転する。
Powder storage containers 5, 5' are provided at the bottom of the powder injection hoppers 4, 4'.
Stirring blades 6, 6' are rotatably provided in '.
The stirring blades 6, 6' are rotated via rotary tables 7, 7' by drive devices M, M'.

【0013】粉体吹込ホッパー4,4′内の微粉炭の重
量を測定するためのロードセル8,8′での重量測定値
は制御装置18,18′に送信され、制御装置18,1
8′により駆動装置M,M′の駆動を制御して攪拌翼6
,6′の回転を制御する。
The weight measurement values from the load cells 8, 8' for measuring the weight of the pulverized coal in the powder injection hoppers 4, 4' are transmitted to the control devices 18, 18'.
8' controls the driving of the drive devices M and M' to drive the stirring blades 6.
, 6'.

【0014】粉体吹込ホッパー4,4′には該吹込ホッ
パー内の圧力を調整するための加圧ガス吹込管9,9′
が取付けられており、圧力計P,P′による吹込ホッパ
ー4,4′の圧力値に応じて圧力調整弁10,10′を
制御して加圧ガス吹込管9,9′からの加圧ガス吹込み
流量を制御する。
The powder blowing hoppers 4, 4' are provided with pressurized gas blowing pipes 9, 9' for adjusting the pressure inside the blowing hoppers.
is installed, and the pressure regulating valves 10, 10' are controlled according to the pressure values of the blowing hoppers 4, 4' measured by the pressure gauges P, P' to control the pressurized gas from the pressurized gas blowing pipes 9, 9'. Control the blowing flow rate.

【0015】粉体収容容器5,5′内の攪拌翼6,6′
の上部には、収容容器5,5′内の微粉炭を流動化する
ための複数の吹出口110 ,1101を有する流動化
ガス吹込管11,11′が取付けられており、これから
収容容器5,5′内に加圧ガスを吹込んで収容容器5,
5′内の微粉炭を流動状態に維持する。12,12′は
吹込調整弁である。
Stirring blades 6, 6' inside the powder storage containers 5, 5'
A fluidizing gas blowing pipe 11, 11' having a plurality of outlets 110, 1101 for fluidizing the pulverized coal in the storage containers 5, 5' is attached to the upper part of the storage container 5, 5'. Pressurized gas is blown into the storage container 5,
The pulverized coal in 5' is maintained in a fluid state. Reference numerals 12 and 12' designate blow regulating valves.

【0016】粉体収容容器5,5′内の粉体切出孔50
 ,50 ′部に搬送補助ガス吹込管13,13′が取
付けられており、収容容器5,5′から微粉炭を切出す
際に加圧ガスを吹き込んで微粉炭の切出し、搬送を補助
する。14,14′は搬送補助ガス開閉弁である。
Powder cutting holes 50 in the powder storage containers 5, 5'
, 50' are equipped with transport auxiliary gas blowing pipes 13, 13', which blow pressurized gas when cutting the pulverized coal from the containers 5, 5' to assist in cutting and transporting the pulverized coal. Reference numerals 14 and 14' indicate transport auxiliary gas on-off valves.

【0017】粉体吹込ホッパー4,4′は切替えて使用
するので、一方の粉体吹込ホッパーから微粉炭を供給し
ている場合には、他方の粉炭吹込ホッパー側の搬送補助
ガス吹込管13の補助ガス開閉弁14を閉じておいても
良い。
Since the powder injection hoppers 4 and 4' are used in a switched manner, when pulverized coal is being supplied from one powder injection hopper, the conveyance auxiliary gas injection pipe 13 on the other pulverized coal injection hopper side is The auxiliary gas on-off valve 14 may be closed.

【0018】粉体収容容器5,5′からの切出管15,
15′は切出弁16,16′を介して高炉への粉体搬送
管17に接続されている。粉体搬送管17に切出された
粉炭は、搬送ガスによって高炉へ吹込まれる。
Cutting tube 15 from powder storage container 5, 5',
15' is connected to a powder conveying pipe 17 to the blast furnace via cut-off valves 16, 16'. The powdered coal cut into the powder transport pipe 17 is blown into the blast furnace by the transport gas.

【0019】便宜的に、例えば粉体吹込ホッパー4側か
らの微粉炭吹込みについて説明する。粉体収容容器5お
よび粉体吹込ホッパー4内に粉体貯槽1から充填管2、
充填弁3を介して微粉炭Cが供給充填されており、流動
化ガス吹込管11のガス吹出口110 から流動化ガス
の吹込調節弁12により空塔速度が一定になるように加
圧ガスが吹込まれ、粉体収容容器5および粉体吹込ホッ
パー4内の微粉炭は流動化している。この状態で攪拌翼
駆動モータMを駆動して回転テーブル7を回転し、攪拌
翼6を回転する。この状態では、粉体収容容器5内の微
粉炭は加圧ガスによって流動しているため、攪拌翼駆動
モータMに対する起動抵抗は非常に小さい。従って、攪
拌翼駆動モータMの容量は小さくてよく、例えば前記従
来例の場合に比し50%程度の容量のもので十分である
For convenience, the injection of pulverized coal from, for example, the powder injection hopper 4 side will be explained. Filling pipe 2 from powder storage tank 1 into powder storage container 5 and powder blowing hopper 4;
Pulverized coal C is supplied and filled through the filling valve 3, and pressurized gas is supplied from the gas outlet 110 of the fluidizing gas blowing pipe 11 by the fluidizing gas blowing control valve 12 so that the superficial velocity is constant. The pulverized coal in the powder storage container 5 and the powder blowing hopper 4 is fluidized. In this state, the stirring blade drive motor M is driven to rotate the rotary table 7 and the stirring blade 6 to rotate. In this state, the pulverized coal in the powder storage container 5 is fluidized by the pressurized gas, so the starting resistance to the stirring blade drive motor M is very small. Therefore, the capacity of the agitating blade drive motor M may be small; for example, a capacity of about 50% of that of the conventional example is sufficient.

【0020】攪拌翼駆動モータMの起動と同時に搬送補
助ガス開閉弁14を操作して、搬送補助ガスを空塔速度
が一定になるように粉体排出口部50 に吹出す。粉体
切出弁16を開くと流動化用加圧ガスの作用との相乗効
果により、微粉炭は気流と良好な混合状態を維持しなが
ら粉体搬送管17に切出しされ、搬送ガスによって粉体
搬送管17を経て羽口から高炉炉内に吹込まれる。
At the same time as the stirring blade drive motor M is started, the auxiliary transport gas on-off valve 14 is operated to blow out the auxiliary transport gas to the powder discharge port 50 so that the superficial velocity is constant. When the powder cutting valve 16 is opened, the pulverized coal is cut into the powder conveying pipe 17 while maintaining a good mixing state with the air flow due to the synergistic effect with the action of the fluidizing pressurized gas, and the powder is pulverized by the conveying gas. It is blown into the blast furnace from the tuyere through the conveying pipe 17.

【0021】通常の場合、一方の粉体吹込ホッパー4か
ら粉体搬送管17に微粉炭を供給している間は他方の粉
体吹込ホッパー4′からの微粉炭の供給は行わないが、
粉体吹込ホッパー4′内には微粉炭が充填され、常に流
動化のため流動化ガス吹込管11′から加圧ガスを吹込
んで流動化状態を維持する。そして、粉体吹込ホッパー
4からの微粉炭吹込みの終了に合わせて攪拌翼6′を回
転して微粉炭と気流を攪拌し、均一混合すると共に、粉
体吹込ホッパー4′の排出口部に搬送補助ガスを吹き込
んで更に流動化し、粉体吹込ホッパー4からの粉炭切出
しの終了と同時に粉体切出弁16′を開いて粉体吹込ホ
ッパー4′から微粉炭を粉体搬送管17に切出し、高炉
へ連続的に吹込むことができる。
Normally, while pulverized coal is being supplied from one powder injection hopper 4 to the powder transport pipe 17, pulverized coal is not supplied from the other powder injection hopper 4'.
The inside of the powder blowing hopper 4' is filled with pulverized coal, and pressurized gas is constantly blown into the coal from the fluidizing gas blowing pipe 11' to maintain the fluidized state. Then, at the end of the injection of pulverized coal from the powder injection hopper 4, the stirring blades 6' are rotated to stir the pulverized coal and the air flow, uniformly mixing them, and the air flow is delivered to the discharge port of the powder injection hopper 4'. A conveyance auxiliary gas is blown in to further fluidize the coal, and at the same time as the powder coal cutting from the powder blowing hopper 4 is finished, the powder cutting valve 16' is opened to cut the pulverized coal from the powder blowing hopper 4' into the powder conveying pipe 17. , can be continuously blown into the blast furnace.

【0022】なお、本実施例は高炉への微粉炭吹込みに
適用し、1個の粉体貯槽の下方に2個の粉体吹込ホッパ
ーを交互に切替え可能に設けているが、本発明はこの実
施例に限定されるものではなく、その適用対象も微粉炭
の他、鉱石粉、セメント、あるいはセメント原料等の搬
送、吹込み等の粉体の供給にも適用でき、その構造もそ
の適用対象によって適宜変更されることがある。
Note that this embodiment is applied to the injection of pulverized coal into a blast furnace, and two powder injection hoppers are provided below one powder storage tank so that they can be switched alternately. It is not limited to this example, and its application can also be applied to powder supply such as conveying and blowing of ore powder, cement, or cement raw materials in addition to pulverized coal, and its structure is also applicable. It may be changed as appropriate depending on the subject.

【0023】[0023]

【発明の効果】本発明においては、粉体吹込ホッパーに
加圧ガスを吹込んで粉体を流動化して、該ホッパーの下
部における粉体攪拌翼に対する起動抵抗を小さくでき、
攪拌翼駆動モータを小容量化でき、また攪拌翼各種機械
部品等の損傷を軽減することができる。更に、排出口部
に搬送補助ガスを吹込んで粉体の攪拌と共に粉体と気流
との均一混合が十分に行われ、複数の粉体吹込ホッパー
を切替え使用する場合においても、切替え移行が極めて
スムーズにでき、粉体の安定的連続供給が可能である。
Effects of the Invention In the present invention, pressurized gas is blown into the powder blowing hopper to fluidize the powder, and the starting resistance to the powder stirring blades in the lower part of the hopper can be reduced.
The capacity of the stirring blade drive motor can be reduced, and damage to various mechanical parts of the stirring blade can be reduced. Furthermore, by blowing a conveyance auxiliary gas into the discharge port, the powder is stirred and the airflow is sufficiently mixed with the powder, making the switching transition extremely smooth even when switching between multiple powder blowing hoppers. This enables stable and continuous supply of powder.

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

【図1】本発明の粉体供給装置の一実施例の下部構造を
示す図である。
FIG. 1 is a diagram showing a lower structure of an embodiment of a powder supply device of the present invention.

【図2】本発明の粉体供給装置の一実施例を示す図であ
る。
FIG. 2 is a diagram showing an embodiment of the powder supply device of the present invention.

【符号の説明】[Explanation of symbols]

1    粉体貯槽 2    充填管 3    充填弁 4    粉体吹込ホッパー 5    粉体収容容器 6    攪拌翼 7    回転テーブル 8    ロードセル 9    加圧ガス吹込管 10  圧力調整弁 11  流動化ガス吹込管 12  吹込調整弁 13  搬送補助ガス吹込管 14  搬送補助ガス開閉弁 15  切出管 16  切出弁 17  粉体搬送管 18  制御装置 1 Powder storage tank 2 Filling tube 3 Filling valve 4 Powder injection hopper 5 Powder storage container 6 Stirring blade 7 Rotary table 8 Load cell 9 Pressurized gas blowing pipe 10 Pressure regulating valve 11 Fluidization gas blowing pipe 12 Blow regulating valve 13 Transport auxiliary gas blowing pipe 14 Transport auxiliary gas on-off valve 15 Cutting tube 16 Cutoff valve 17 Powder conveyance pipe 18 Control device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  粉体貯槽の下方に並列配置された複数
の粉体吹込ホッパーの下部にそれぞれ攪拌翼を備えた粉
体収容容器を設け、この収容容器内に粉体を流動化させ
るためのガスを常時吹き込むとともに、該収容容器の切
出口部に切出粉体の搬送を補助するためのガスを吹き込
む構造を備えたことを特徴とする粉体供給装置。
Claim 1: Powder storage containers each equipped with stirring blades are provided at the bottom of a plurality of powder blowing hoppers arranged in parallel below a powder storage tank, and a powder storage container is provided for fluidizing the powder in the storage container. A powder supply device characterized by having a structure for constantly blowing gas and for blowing gas into the cut-out port of the storage container to assist in transporting the cut-out powder.
JP3167431A 1991-06-13 1991-06-13 Powder feeder Expired - Lifetime JPH07100545B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3167431A JPH07100545B2 (en) 1991-06-13 1991-06-13 Powder feeder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3167431A JPH07100545B2 (en) 1991-06-13 1991-06-13 Powder feeder

Publications (2)

Publication Number Publication Date
JPH04365725A true JPH04365725A (en) 1992-12-17
JPH07100545B2 JPH07100545B2 (en) 1995-11-01

Family

ID=15849583

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3167431A Expired - Lifetime JPH07100545B2 (en) 1991-06-13 1991-06-13 Powder feeder

Country Status (1)

Country Link
JP (1) JPH07100545B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3033363U (en) * 1996-07-09 1997-01-21 永田醸造機械株式会社 Disc type raw material supply device
KR101276781B1 (en) * 2010-12-14 2013-06-21 (주)디에스리퀴드 Automatic feeder preventing flux outlet from clogging for aluminum flux
JP2014214361A (en) * 2013-04-26 2014-11-17 新日鐵住金株式会社 Method of monitoring powdered coal supply installation and powdered coal supply installation for blast furnace
CN112978293A (en) * 2021-04-27 2021-06-18 成都光华科技发展有限公司 Superfine high-purity micropowder feeder capable of realizing uniform metering powder feeding

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53128876A (en) * 1977-04-13 1978-11-10 Mitsui Miike Mach Co Ltd Method for separating out pulverulent body of silo and its device
JPS63113021U (en) * 1987-01-17 1988-07-20

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53128876A (en) * 1977-04-13 1978-11-10 Mitsui Miike Mach Co Ltd Method for separating out pulverulent body of silo and its device
JPS63113021U (en) * 1987-01-17 1988-07-20

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3033363U (en) * 1996-07-09 1997-01-21 永田醸造機械株式会社 Disc type raw material supply device
KR101276781B1 (en) * 2010-12-14 2013-06-21 (주)디에스리퀴드 Automatic feeder preventing flux outlet from clogging for aluminum flux
JP2014214361A (en) * 2013-04-26 2014-11-17 新日鐵住金株式会社 Method of monitoring powdered coal supply installation and powdered coal supply installation for blast furnace
CN112978293A (en) * 2021-04-27 2021-06-18 成都光华科技发展有限公司 Superfine high-purity micropowder feeder capable of realizing uniform metering powder feeding
CN112978293B (en) * 2021-04-27 2023-09-15 成都光华科技发展有限公司 Superfine high-purity micropowder powder feeder capable of realizing uniform metering powder feeding

Also Published As

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