JPH0733530B2 - Powder injection method - Google Patents

Powder injection method

Info

Publication number
JPH0733530B2
JPH0733530B2 JP3178909A JP17890991A JPH0733530B2 JP H0733530 B2 JPH0733530 B2 JP H0733530B2 JP 3178909 A JP3178909 A JP 3178909A JP 17890991 A JP17890991 A JP 17890991A JP H0733530 B2 JPH0733530 B2 JP H0733530B2
Authority
JP
Japan
Prior art keywords
powder
blowing
hopper
cutting
hoppers
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
JP3178909A
Other languages
Japanese (ja)
Other versions
JPH051307A (en
Inventor
久生 石井
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.)
Nippon Steel Corp
Original Assignee
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP3178909A priority Critical patent/JPH0733530B2/en
Publication of JPH051307A publication Critical patent/JPH051307A/en
Publication of JPH0733530B2 publication Critical patent/JPH0733530B2/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)
  • Manufacture Of Iron (AREA)
  • Blast Furnaces (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、高炉への微粉炭あるい
は微粉鉱石の搬送吹込をはじめとして、セメント等の粉
体(粉、粒またはこれらの混合体を示す)の連続搬送、
吹込方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to continuous feeding of powder such as cement (indicating powder, granules or a mixture thereof), including feeding and blowing of pulverized coal or fine ore into a blast furnace.
It concerns the blowing method.

【0002】[0002]

【従来の技術】例えば、高炉の微粉炭吹込を例にとる
と、図4に示す例においては、並列に配置された吹込ホ
ッパー2、2′を有し、微粉炭の切出量は、ロードセル
15、15′からの重量信号を圧力制御弁18、18′
に伝達し、吹込ホッパー2、2′内の圧力を増減するこ
とで制御される。
2. Description of the Related Art For example, taking pulverized coal blowing in a blast furnace as an example, in the example shown in FIG. 4, the blasting hoppers 2 and 2'arranged in parallel are provided, and the pulverized coal is cut out by a load cell. The weight signal from 15, 15 'is sent to the pressure control valve 18, 18'.
And is controlled by increasing or decreasing the pressure in the blow hoppers 2, 2 '.

【0003】この例において、吹込ホッパー2、2′の
切替え時の切出量の変動を抑制するには、吹込ホッパー
2、2′下部に接続されている固気濃度の高い高濃度配
管20内の抵抗と吹込ホッパー2、2′内の圧力、及び
高炉の送風圧を平衡させる必要があるが、これは容易で
はない。
In this example, in order to suppress the variation of the cutting amount when the blow hoppers 2, 2'are switched, the inside of the high concentration pipe 20 having a high solid gas concentration and connected to the lower portions of the blow hoppers 2, 2 '. It is necessary to balance the resistance of No. 1 with the pressure in the blow hoppers 2, 2'and the blowing pressure of the blast furnace, but this is not easy.

【0004】また、この配管20内は高固気濃度のた
め、搬送ガスとの混合部まで非常に高い圧損が発生する
ことから、吹込ホッパー2、2′には高圧力の供給構造
が必要となる。また、吹込ホッパー2、2′下部におい
て、流動化、攪拌が行われていないため、粉体の圧密化
が生じ、切出しが円滑ではなく、粒度偏析等の問題があ
り、均一な微粉炭と搬送空気との混合体を安定的に連続
的に切出し搬送することは困難である等の問題がある。
特に、吹込ホッパー2、2′を切替える場合の吹込量変
動の問題がある。
Further, since the inside of the pipe 20 has a high solid gas concentration, a very high pressure loss occurs up to the mixing portion with the carrier gas. Therefore, the blow hoppers 2, 2'need to have a high pressure supply structure. Become. In addition, since fluidization and agitation are not performed in the lower part of the blow hoppers 2, 2 ', powder compaction occurs, cutting is not smooth, there is a problem of particle size segregation, etc. There is a problem that it is difficult to stably and continuously cut out and convey the mixture with air.
In particular, there is a problem of variation in the blowing amount when switching the blowing hoppers 2, 2 '.

【0005】一方、図5の例に於いては、貯蔵ホッパー
1と中間ホッパー22、及び吹込ホッパー2が直列に配
置され、吹込量はロードセル15からの重量信号を吹込
ホッパー2下部に設置している回転式粉体供給装置21
に伝達し、その回転数を増減することで切出量が制御さ
れている。
On the other hand, in the example of FIG. 5, the storage hopper 1, the intermediate hopper 22, and the blow hopper 2 are arranged in series, and the blow amount is set by the weight signal from the load cell 15 below the blow hopper 2. Revolving powder feeder 21
The cut-out amount is controlled by transmitting it to and increasing / decreasing its rotation speed.

【0006】この例では、吹込ホッパーは1基のため切
替え時の切出量の変動は配慮しなくてもよいが、中間ホ
ッパー22から吹込ホッパー2に微粉炭を投入する時間
帯は切り出しと充填が同時に行われており、真の切出量
の把握が困難であり、また、吹込ホッパー2下部におい
て、微粉炭の圧密化が生じる懸念もあり、切出しが必ず
しも円滑ではなく、均一な微粉炭と搬送空気との混合体
を安定的に連続的に切出し搬送することは困難である等
の問題がある。
[0006] In this example, since there is only one blowing hopper, it is not necessary to consider the variation in the amount of cutting at the time of switching, but during the time when the pulverized coal is charged from the intermediate hopper 22 to the blowing hopper 2, cutting and filling are performed. Since it is difficult to grasp the true amount of cutting, and there is a concern that the pulverized coal will be compacted in the lower part of the blowing hopper 2, the cutting is not always smooth and a uniform pulverized coal is obtained. There is a problem that it is difficult to stably and continuously cut out and convey the mixture with the conveying air.

【0007】粉体の切出部には機械式切出機構を採用し
ているため、搬送空気との混合部までの圧損は高濃度配
管を有する図4の例に比べ少なくて済み、吹込ホッパー
2には高圧力の供給構造を必要としないが、中間ホッパ
ー22を有することにより、各設備を構成支持するステ
ーション架構が大きく、建設コストがかさむという問題
もある(特開昭61−266507号公報、特開昭61
−153214号公報)。
Since a mechanical cutting mechanism is used for the powder cutting portion, the pressure loss to the mixing portion with the carrier air is smaller than that in the example of FIG. 4 having the high concentration pipe, and the blowing hopper is used. 2 does not require a high pressure supply structure, but since it has the intermediate hopper 22, it has a problem that a station frame for supporting and supporting each equipment is large and construction cost is high (Japanese Patent Laid-Open No. 61-266507). , JP-A-61
No. 153214).

【0008】[0008]

【発明が解決しようとする課題】本発明は、粉体吹込ホ
ッパーの下部における粉体の流動化、攪拌を促進して切
出しの円滑化を図り、かつ粉体と搬送ガスとの混合を均
一化し、この混合体の切出し量の変動を抑制しながら連
続的に搬送吹込みできる低コストの粉体吹込方法を提供
する。特に、複数の粉体吹込ホッパーを用い、これを円
滑に切替えて、粉体を長時間に亘って安定した吹込量で
連続的に搬送吹込みができる粉体吹込方法を提供する。
SUMMARY OF THE INVENTION According to the present invention, the fluidization and agitation of the powder in the lower part of the powder blowing hopper are promoted to facilitate the cutting, and the mixing of the powder and the carrier gas is made uniform. Provided is a low-cost powder blowing method capable of continuously carrying and blowing while suppressing the variation in the cut-out amount of the mixture. In particular, the present invention provides a powder blowing method in which a plurality of powder blowing hoppers are used and smoothly switched, and the powder can be continuously conveyed and blown at a stable blowing amount for a long time.

【0009】[0009]

【課題を解決するための手段】本発明の要旨は、粉体貯
蔵ホッパーの下方に複数の粉体吹込ホッパーを並列に配
置して、粉体貯蔵ホッパーから粉体をこの複数の粉体吹
込ホッパーに交互に充填し、その下部に設置した攪拌機
能を備えた粉体供給装置を介して粉体搬送管に切出し、
搬送ガスと混合して搬送し吹込む粉体吹込方法におい
て、粉体充填後の粉体吹込ホッパーからの粉体切出しの
開始と共に該粉体吹込ホッパー内の粉体重量と圧力を測
定し、重量の変化に応じて圧力を調整すると共に、粉体
供給装置の攪拌力を調整して粉体を流動化させ、切出量
の変動を抑制しながら搬送管に切出し吹込むことを特徴
とする粉体の吹込方法である。また、この際、粉体吹込
ホッパーからの粉体切出しの開始に合せて粉体貯蔵ホッ
パーから粉体未充填の粉体吹込ホッパーへの充填を開始
し、該粉体吹込ホッパー内の粉体重量を測定し、所定値
になった時充填を終了し、粉体切出し中の粉体吹込ホッ
パーからの切出しが終了する前に圧力を所定値に維持す
ると共に、粉体供給装置で攪拌力を付与して粉体を流動
化状態に維持し、前記粉体吹込ホッパーからの切出しの
終了に合せて切出しを開始することにより、複数の粉体
吹込ホッパーを切替えて搬送管に粉体を連続的に切出し
て吹込むことを特徴とする粉体吹込方法である。
DISCLOSURE OF THE INVENTION The gist of the present invention is to arrange a plurality of powder blowing hoppers in parallel below a powder storage hopper, and to transfer powder from the powder storage hopper to the plurality of powder blowing hoppers. Alternately, and cut into a powder conveying pipe through a powder supply device equipped with a stirring function installed in the lower part,
In the powder blowing method in which the powder is mixed with the carrier gas and blown, the powder weight and the pressure in the powder blow hopper are measured together with the start of the powder cutting from the powder blow hopper after the powder filling. The powder is characterized by adjusting the pressure according to changes in the powder, adjusting the stirring force of the powder supply device to fluidize the powder, and cutting and blowing the powder into the carrier pipe while suppressing fluctuations in the cutting amount. It is a method of blowing the body. In addition, at this time, in accordance with the start of the cutting of the powder from the powder blowing hopper, the filling of the powder storage hopper into the powder unfilled powder blowing hopper is started, and the weight of the powder in the powder blowing hopper is started. Is measured, the filling is completed when it reaches a predetermined value, the pressure is maintained at a predetermined value before the cutting from the powder blowing hopper during powder cutting is completed, and the stirring force is applied by the powder feeding device. Then, the powder is kept in a fluidized state, and the cutting is started at the end of the cutting from the powder blowing hopper, so that the plurality of powder blowing hoppers are switched and the powder is continuously transferred to the conveying pipe. It is a powder blowing method characterized by cutting and blowing.

【0010】[0010]

【作用・実施例】以下に、本発明を図1に示す実施例に
基づいて説明する。
OPERATION / EXAMPLES The present invention will be described below based on the embodiments shown in FIG.

【0011】本実施例は、高炉への微粉炭吹込みに適用
した場合であって、粉体貯蔵ホッパー1の下方に並列配
置した2基の粉体吹込ホッパー2、2′を切替えて、高
炉への微粉炭の吹込みを連続的かつ安定的に行うもので
ある。
This embodiment is applied to the injection of pulverized coal into a blast furnace, and two powder injection hoppers 2 and 2'arranged in parallel below the powder storage hopper 1 are switched to change the blast furnace. The pulverized coal is continuously and stably blown into it.

【0012】微粉炭Cの貯蔵ホッパー1の下方に並列に
配設した2基の粉体吹込ホッパー2、2′は、それぞれ
充填弁3A、3A′、充填弁3B、3B′を備えた充填
管3、3′によって粉体貯蔵ホッパー1の下部に連結さ
れている。粉体吹込ホッパー2、2′の下部に、攪拌翼
を備えた回転式粉体供給装置4、4′が設けられてい
る。この粉体供給装置4、4′の下部には切出口があ
り、この切出口は切出弁5A、5A′、切出弁5B、5
B′を備えた切出管5、5′によって高炉への粉体搬送
管6に連結されている。
The two powder blowing hoppers 2 and 2'arranged in parallel below the storage hopper 1 for the pulverized coal C are filling pipes provided with filling valves 3A, 3A 'and filling valves 3B, 3B', respectively. It is connected to the lower part of the powder storage hopper 1 by 3, 3 '. Below the powder blowing hoppers 2, 2 ', rotary powder feeding devices 4, 4'having a stirring blade are provided. There is a cutout port in the lower part of the powder supply device 4, 4 ', and these cutout ports are cutout valves 5A, 5A', cutout valves 5B, 5
It is connected to the powder conveying pipe 6 to the blast furnace by cutting pipes 5 and 5'provided with B '.

【0013】また、粉体吹込ホッパー2、2′には、吹
込ホッパー2、2′内の圧力を調整するための加圧ガス
吹込管7、7′が取付けられており、圧力計P、P′に
よる吹込ホッパー2、2′内の圧力値に応じて加圧ガス
吹込調整弁8、8′を制御して加圧ガス吹込管7、7′
からの加圧ガス吹込流量を制御し、粉体吹込ホッパー
2、2′内の圧力を所定値に維持する。
The powder blowing hoppers 2 and 2'are provided with pressurized gas blowing pipes 7 and 7'for adjusting the pressure in the blowing hoppers 2 and 2 ', and the pressure gauges P and P are provided. The pressurized gas blowing control valves 8 and 8'are controlled according to the pressure values in the blowing hoppers 2 and 2'by means of the pressurized gas blowing pipes 7 and 7 '.
The flow rate of the pressurized gas blown from is controlled to maintain the pressure in the powder blowing hoppers 2, 2'at a predetermined value.

【0014】そして、粉体供給装置4、4′内の攪拌翼
上部には、粉体供給装置4、4′内の微粉炭を流動化す
るための複数のガス吹出口を有する流動化ガス吹込管
9、9′が取付けられており、これから粉体供給装置
4、4′内に加圧ガスを吹込んで、ここで微粉炭を流動
状態に維持する。10、10′は流動化ガス吹込調整弁
である。
In the upper part of the stirring blades in the powder feeders 4 and 4 ', a fluidizing gas blower having a plurality of gas outlets for fluidizing the pulverized coal in the powder feeders 4 and 4'. Tubes 9 and 9'are attached, from which pressurized gas is blown into the powder feeders 4 and 4 ', where the pulverized coal is maintained in a fluidized state. Reference numerals 10 and 10 'are fluidizing gas injection control valves.

【0015】また、この粉体供給装置4、4′の切出口
近傍に、搬送補助ガス吹込管11、11′が取付けられ
ており、切出口から微粉炭を切り出す際に、加圧ガスを
吹き込んで微粉炭の切出し・搬送を補助する。12、1
2′は搬送補助ガス開閉弁である。
Further, conveyance assisting gas blowing pipes 11 and 11 'are attached near the cutouts of the powder supply devices 4 and 4', and a pressurized gas is blown when the pulverized coal is cut out from the cutouts. Assists in the cutting and transportation of pulverized coal. 12, 1
2'is a transfer auxiliary gas on-off valve.

【0016】各粉体吹込ホッパー2、2′の上部は排圧
弁13、13′を備えた排圧管14、14′によって粉
体貯蔵ホッパー1上部と連結し、粉体吹込ホッパー2、
2′内の圧力と粉体貯蔵ホッパー1の圧力を調整できる
ようになっている。
The upper part of each powder blowing hopper 2, 2'is connected to the upper part of the powder storage hopper 1 by a pressure exhaust pipe 14, 14 'equipped with a pressure relief valve 13, 13', and the powder blowing hopper 2,
The pressure in 2'and the pressure in the powder storage hopper 1 can be adjusted.

【0017】粉体吹込ホッパー2、2′内の微粉炭の重
量を測定するためのロードセル15、15′での重量測
定値は、供給制御装置16、16′に送信され、供給制
御装置16、16′により駆動装置M、M′の駆動を制
御し、攪拌翼の回転を制御すると共に、粉体吹込ホッパ
ー2、2′内の刻々変化する重量を測定し、切替制御装
置17に入力し演算処理してこの測定値が所定値になっ
たら供給制御装置17を介して各種弁の開閉を制御して
粉体吹込ホッパー2、2′間の切替えが行われる。
The weight measurement values at the load cells 15, 15 'for measuring the weight of the pulverized coal in the powder blowing hoppers 2, 2'are transmitted to the supply control devices 16, 16', and the supply control device 16, 16 'controls the driving of the driving devices M, M', controls the rotation of the stirring blades, measures the momentarily changing weight in the powder blowing hoppers 2, 2 ', and inputs it to the switching control device 17 for calculation. When the measured value reaches a predetermined value after processing, the opening / closing of various valves is controlled via the supply controller 17 to switch between the powder blowing hoppers 2 and 2 '.

【0018】個々の粉体吹込ホッパーは、図2に示すよ
うに排圧、充填、加圧、待機、吹込(切出)操作を繰り
返すが、微粉炭吹込はNo.1粉体吹込ホッパー2とN
o.2粉体吹込ホッパー2′から交互に行われ、結果と
して微粉炭は切替時にも切出量の変動を抑制して粉体搬
送管6に定量でかつ連続的に切出され、搬送ガスと混合
状態で分配器を介して又は直接に高炉羽口から高炉炉内
に長時間に亘って定量でかつ連続的に吹込まれる。即
ち、図3に示すように、No.1粉体吹込ホッパー2か
ら吹込(切出)中にはNo.2粉体吹込ホッパー2′で
は排圧弁13′を開き、充填弁3A′、充填弁3B′を
開いて、粉体貯蔵ホッパー1から微粉炭Cをロードセル
15′による重量測定に基づいて一定レベルになるまで
充填する。
Each of the powder blowing hoppers repeats the discharge pressure, filling, pressurization, standby, and blowing (cutting) operations as shown in FIG. 1 powder blowing hopper 2 and N
o. 2 The powder blast hoppers 2'are alternately operated. As a result, the pulverized coal is restrained from changing the amount of cutting even at the time of switching, and is quantified and continuously cut into the powder conveying pipe 6 and mixed with the carrier gas. In this state, it is continuously blown into the blast furnace through the distributor or directly from the tuyere of the blast furnace in a constant amount for a long time. That is, as shown in FIG. No. 1 during blowing (cutting) from the powder blowing hopper 2. 2 In the powder blowing hopper 2 ′, the exhaust pressure valve 13 ′ is opened, the filling valve 3A ′ and the filling valve 3B ′ are opened, and the pulverized coal C from the powder storage hopper 1 is brought to a constant level based on the weight measurement by the load cell 15 ′. Fill until complete.

【0019】この時、加圧ガス吹込調整弁8′、流動化
ガス吹込調整弁10′、搬送補助ガス開閉弁12′は閉
じている。そして、排圧弁13′を閉じて加圧ガス吹込
管7′から加圧ガスを吹込んで、圧力計P′による圧力
測定に基づいて、その圧力を設定値に維持して待機状態
としておく。この時、No2.粉体吹込ホッパー2′の
切出弁5A′、切出弁5B′は閉じており、流動化ガス
吹込管9′の流動化ガス調整弁10′、および搬送補助
ガス吹込管11′の搬送補助ガス調整弁12′は閉じて
いる。
At this time, the pressurized gas injection adjusting valve 8 ', the fluidizing gas injection adjusting valve 10', and the transfer auxiliary gas on-off valve 12 'are closed. Then, the exhaust pressure valve 13 'is closed and the pressurized gas is blown from the pressurized gas blowing pipe 7', and the pressure is maintained at the set value based on the pressure measurement by the pressure gauge P'and kept in the standby state. At this time, No2. The cut-out valve 5A 'and the cut-out valve 5B' of the powder blowing hopper 2'are closed, the fluidizing gas adjusting valve 10 'of the fluidizing gas blowing pipe 9', and the feeding assistance of the feeding assistance gas blowing pipe 11 '. The gas regulating valve 12 'is closed.

【0020】吹込中のNo.1粉体吹込ホッパー2内は
加圧ガス吹込調整弁8を調整し一定の圧力に維持し、ロ
ードセル15による微粉炭重量に応じて回転式粉体供給
装置4の回転を制御しながら微粉炭の搬送管6への切出
しを行う。この時切出弁5A、5Bは開いている。
No. being blown 1 Inside the powder blowing hopper 2, the pressurized gas blowing adjusting valve 8 is adjusted to maintain a constant pressure, and while the rotation of the rotary powder feeding device 4 is controlled according to the weight of the pulverized coal by the load cell 15, Cut out to the carrier pipe 6. At this time, the cutoff valves 5A and 5B are open.

【0021】No.1粉体吹込ホッパー2内の微粉炭の
重量が減少して切替設定値に達した時点で、No.2粉
体吹込ホッパー2′からの吹込(切出)に切替えが行わ
れる。
No. No. 1 when the weight of the pulverized coal in the powder blowing hopper 2 decreased and reached the switching set value. 2 Switching to blowing (cutting) from the powder blowing hopper 2'is performed.

【0022】この切替えは、図3に示すように、No.
1粉体吹込ホッパー2のロードセル15からの重量信号
を受けて回転式粉体供給装置4の攪拌翼の回転数を一定
勾配で下げて行くと同時に、待機中のNo.2粉体吹込
ホッパー2′の切出弁5A′を開とし、一定時間後切出
弁5B′も開とし、回転式粉体供給装置4′の回転数を
一定勾配で上げて行くことで、切替えに伴う切出量の変
動を最小限にする。
This switching is performed as shown in FIG.
In response to a weight signal from the load cell 15 of the powder blowing hopper 2, the rotating speed of the stirring blade of the rotary powder feeding device 4 is lowered at a constant gradient, and at the same time, the waiting No. 2 By opening the cut-off valve 5A 'of the powder blowing hopper 2'and opening the cut-off valve 5B' after a fixed time, the rotational speed of the rotary powder feeder 4'is increased at a constant gradient, Minimize the variation in the cutting amount due to switching.

【0023】No.1粉体吹込ホッパー2の回転式粉体
供給装置4の回転数が最小値になった時点で切出弁5A
を閉とし、一定時間後切出弁5Bを閉とし、回転式粉体
供給装置4を停止すると共に、加圧ガス吹込調整弁8、
流動化ガス吹込調整弁10、搬送補助ガス開閉弁12を
閉とし、微粉炭充填のための排圧に移行する。
No. 1 When the rotational speed of the rotary powder feeder 4 of the powder blowing hopper 2 reaches the minimum value, the cutoff valve 5A
Is closed, and the cut-out valve 5B is closed after a fixed time, the rotary powder supply device 4 is stopped, and the pressurized gas injection adjusting valve 8,
The fluidizing gas injection adjusting valve 10 and the transfer auxiliary gas on-off valve 12 are closed, and the exhaust pressure for filling the pulverized coal is transferred.

【0024】一方、No.2粉体吹込ホッパー2′の回
転式粉体供給装置4′の回転数が所定値に達した時点で
切出弁5A′を開とし、一定時間後切出弁5B′を開と
して切出しを開始する。
On the other hand, No. 2 When the number of rotations of the rotary powder feeder 4'of the powder blowing hopper 2'has reached a predetermined value, the cut-out valve 5A 'is opened, and after a certain period of time, the cut-out valve 5B' is opened to start cutting. To do.

【0025】このように、並列に配置した複数の粉体吹
込ホッパー2、2′を交互に切替えて、搬送管6への微
粉炭の切出量変動を抑制して安定的にし、高炉への微粉
炭の吹込を長時間に亘って安定的に行うことができ、高
炉操業の安定化を図ることができた。通常レベルの微粉
炭切出量(吹込量)の場合においては、切出量の変動幅
aは、従来方法による微粉炭吹込の場合に比し20%程
度小さくなった。
As described above, the plurality of powder blowing hoppers 2 and 2'arranged in parallel are alternately switched to suppress the fluctuation of the amount of pulverized coal cut into the carrier pipe 6 to stabilize the blast furnace. The pulverized coal could be blown in stably for a long time, and the blast furnace operation could be stabilized. In the case of the normal level pulverized coal cutting amount (blowing amount), the fluctuation range a of the cutting amount was about 20% smaller than that in the case of the pulverized coal blowing by the conventional method.

【0026】なお、各粉体吹込ホッパー2、2′の回転
式粉体供給装置4、4′における流動化ガス及び搬送補
助ガスの吹込みは、回転式粉体供給装置4、4′の回転
に対応して行うが、粉体吹込ホッパー2、2′への微粉
炭充填に伴う圧密化を抑制する意味から充填、待機の間
も行うことを考慮する。
In addition, the blowing of the fluidizing gas and the carrier auxiliary gas in the rotary powder feeders 4 and 4'of the powder blowing hoppers 2 and 2'rotates the rotary powder feeders 4 and 4 '. However, in order to suppress the consolidation due to the filling of the powder blowing hoppers 2, 2 ′ with the pulverized coal, it is considered that the filling and the waiting are also performed.

【0027】また、排圧、充填、加圧、待機、吹込およ
び切替のための所要操作は、ロードセル、圧力計からの
測定信号等をベースとして供給制御装置、切替え制御装
置によって予め設定された条件に沿って自動制御される
ものであり、適用対象によってこれらの設定条件は適宜
設定される。
The required operations for discharging, filling, pressurizing, waiting, blowing and switching are conditions preset by the supply control device and the switching control device based on measurement signals from the load cell and pressure gauge. Is automatically controlled in accordance with the above, and these setting conditions are appropriately set depending on the application target.

【0028】本実施例は高炉への微粉炭吹込に適用した
ものであるが、本発明はこれに限定するものではなく、
粉体を長時間に亘って安定して連続的に吹込む場合に適
用して効果を奏するものであり、微粉炭(含コークス
粉)、各種鉱石粉、セメント等の粉体等の吹込等にも適
用できる。
The present embodiment is applied to the injection of pulverized coal into the blast furnace, but the present invention is not limited to this.
It is effective when applied to the case where the powder is continuously and stably blown for a long time, and is effective for blowing powder such as pulverized coal (including coke powder), various ore powder, and cement. Can also be applied.

【0029】また、本実施例では、粉体貯蔵ホッパー1
基に対して粉体吹込ホッパーは2基としているが、これ
に限定するものではなく、粉体貯蔵ホッパー、粉体吹込
ホッパーの容量や吹込量、連続吹込量等に応じて基数、
容量等を決定する。
Further, in this embodiment, the powder storage hopper 1 is used.
The number of powder blowing hoppers is two, but the number of powder blowing hoppers is not limited to this, and the number of powder blowing hoppers, the number of powder blowing hoppers, the number of continuous blowing, and the like
Determine capacity etc.

【0030】[0030]

【発明の効果】本発明により、粉体の切出しを容易にす
ると共に、気流と微粉炭との混合を均一化して切出量の
安定化ができ、又、複数の粉体吹込ホッパー間の切替え
に伴う切出量の変動を小さくして、粉体を定量でかつ連
続的に供給することができる。
EFFECTS OF THE INVENTION According to the present invention, the cutting of powder can be facilitated, and the amount of cutting can be stabilized by homogenizing the mixing of air flow and pulverized coal, and switching between a plurality of powder blowing hoppers can be performed. It is possible to reduce the variation in the cutout amount due to the above and supply the powder in a fixed amount and continuously.

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

【図1】本発明の一実施例を示す側面説明図である。FIG. 1 is a side view illustrating an embodiment of the present invention.

【図2】2基の粉体吹込ホッパーの運転状態の説明図で
ある。
FIG. 2 is an explanatory diagram of an operating state of two powder blowing hoppers.

【図3】2基の粉体吹込ホッパーの回転式粉体供給装置
からの切出状態の説明図である。
FIG. 3 is an explanatory diagram of a state in which two powder blowing hoppers are cut out from the rotary powder feeding device.

【図4】従来の粉体供給装置を示す側面説明図である。FIG. 4 is an explanatory side view showing a conventional powder supply device.

【図5】従来の粉体供給装置を示す側面説明図である。FIG. 5 is a side view showing a conventional powder supply device.

【符号の説明】[Explanation of symbols]

1 粉体貯蔵ホッパー 2、2′ 粉体吹込ホッパー 3、3′ 充填管 3A、3A′ 充填弁 3B、3B′ 充填弁 4、4′ 回転式粉体供給装置 5、5′ 切出管 5A、5A′ 切出弁 5B、5B′ 切出弁 6 粉体搬送管 7、7′ 加圧ガス吹込管 8、8′ 加圧ガス吹込調整弁 9、9′ 流動化ガス吹込管 10、10′ 流動化ガス吹込調整弁 11、11′ 搬送補助ガス吹込管 12、12′ 搬送補助ガス開閉弁 13、13′ 排圧弁 14、14′ 排圧管 15、15′ ロードセル 16、16′ 供給制御装置 17 切替制御装置 18、18′ 圧力制御弁 19、19′ 制御装置 20 高濃度配管 21 回転式粉体供給装置 22 中間タンク 1 powder storage hopper 2, 2'powder blowing hopper 3, 3'filling pipe 3A, 3A 'filling valve 3B, 3B' filling valve 4, 4'rotary powder feeding device 5, 5'cutout pipe 5A, 5A 'Cutoff valve 5B, 5B' Cutout valve 6 Powder transfer pipe 7, 7'Pressurized gas injection pipe 8, 8'Pressurized gas injection control valve 9, 9 'Fluidizing gas injection pipe 10, 10' Flow Controlled gas injection valve 11, 11 'Transfer auxiliary gas injection pipe 12, 12' Transfer auxiliary gas on-off valve 13, 13 'Exhaust pressure valve 14, 14' Exhaust pressure pipe 15, 15 'Load cell 16, 16' Supply controller 17 Switching control Device 18, 18 'Pressure control valve 19, 19' Control device 20 High concentration pipe 21 Rotary powder feeder 22 Intermediate tank

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 粉体貯蔵ホッパーの下方に複数の粉体吹
込ホッパーを並列に配置して、粉体貯蔵ホッパーから粉
体をこの複数の粉体吹込ホッパーに交互に充填し、その
下部に設置した攪拌機能を備えた粉体供給装置を介して
粉体搬送管に切出し、搬送ガスと混合して搬送し吹込む
粉体吹込方法において、粉体充填後の粉体吹込ホッパー
からの粉体切出しの開始と共に該粉体吹込ホッパー内の
粉体重量と圧力を測定し、重量の変化に応じて圧力を調
整すると共に、粉体供給装置の攪拌力を調整して粉体を
流動化させ、切出量の変動を抑制しながら搬送管に切出
し吹込むことを特徴とする粉体の吹込方法。
1. A plurality of powder blowing hoppers are arranged in parallel below a powder storage hopper, and powder is alternately charged into the plurality of powder blowing hoppers from the powder storage hopper and installed at a lower portion thereof. In the powder blowing method in which the powder is fed into the powder feeding pipe through the powder feeding device equipped with the agitating function, mixed with the feeding gas, and fed and blown, the powder is fed from the powder feeding hopper after the powder filling. The powder weight and pressure in the powder blowing hopper are measured at the same time as the start of the process, and the pressure is adjusted according to the change in the weight, and the stirring force of the powder supply device is adjusted to fluidize the powder and cut it. A method for injecting powder, characterized by cutting and injecting into a conveying pipe while suppressing fluctuations in the amount of ejection.
【請求項2】 粉体吹込ホッパーからの粉体切出しの開
始に合せて粉体貯蔵ホッパーから粉体未充填の粉体吹込
ホッパーへの充填を開始し、該粉体吹込ホッパー内の粉
体重量を測定し、所定値になった時充填を終了し、粉体
切出し中の粉体吹込ホッパーからの切出しが終了する前
に圧力を所定値に維持すると共に、粉体供給装置で攪拌
力を付与して粉体を流動化状態に維持し、前記粉体吹込
ホッパーからの切出しの終了に合せて切出しを開始する
ことにより、複数の粉体吹込ホッパーを切替えて搬送管
に粉体を連続的に切出して吹込むことを特徴とする請求
項1記載の粉体吹込方法。
2. The powder weight in the powder blowing hopper is started when the powder storing hopper starts filling the powder unfilled powder blowing hopper with the start of the cutting of the powder from the powder blowing hopper. Is measured, the filling is completed when it reaches a predetermined value, the pressure is maintained at a predetermined value before the cutting from the powder blowing hopper during powder cutting is completed, and the stirring force is applied by the powder feeding device. Then, the powder is kept in a fluidized state, and the cutting is started at the end of the cutting from the powder blowing hopper, so that the plurality of powder blowing hoppers are switched and the powder is continuously transferred to the conveying pipe. The powder blowing method according to claim 1, wherein the powder is blown out by cutting.
JP3178909A 1991-06-25 1991-06-25 Powder injection method Expired - Lifetime JPH0733530B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3178909A JPH0733530B2 (en) 1991-06-25 1991-06-25 Powder injection method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3178909A JPH0733530B2 (en) 1991-06-25 1991-06-25 Powder injection method

Publications (2)

Publication Number Publication Date
JPH051307A JPH051307A (en) 1993-01-08
JPH0733530B2 true JPH0733530B2 (en) 1995-04-12

Family

ID=16056798

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3178909A Expired - Lifetime JPH0733530B2 (en) 1991-06-25 1991-06-25 Powder injection method

Country Status (1)

Country Link
JP (1) JPH0733530B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001004030A1 (en) 1999-07-08 2001-01-18 Nkk Corporation Method and device for cutting out and transporting powder and granular material
JP2004010357A (en) * 2003-08-08 2004-01-15 Jfe Steel Kk Granular and powdery material intermittent discharge apparatus

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Publication number Priority date Publication date Assignee Title
JP2002013973A (en) * 2000-06-29 2002-01-18 Mitsubishi Heavy Ind Ltd Powder weighting device
KR100862813B1 (en) * 2002-07-25 2008-10-13 주식회사 포스코 Apparatus for injecting dust coal into blast furnace
KR100862773B1 (en) * 2002-07-29 2008-10-13 주식회사 포스코 Apparatus for controling pressure and air flow of feed hopper for feeding pulverizer coal
SG118271A1 (en) * 2004-06-11 2006-01-27 Jetsis Int Pte Ltd Uninterrupted abrasive fluid supply
KR101445520B1 (en) 2011-06-24 2014-09-29 와이케이케이 가부시끼가이샤 Slide fastener
JP2014522698A (en) 2011-07-20 2014-09-08 Ykk株式会社 Top stop of slider
US9138033B2 (en) 2013-03-14 2015-09-22 Ykk Corporation Top stop for slider

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001004030A1 (en) 1999-07-08 2001-01-18 Nkk Corporation Method and device for cutting out and transporting powder and granular material
JP2004010357A (en) * 2003-08-08 2004-01-15 Jfe Steel Kk Granular and powdery material intermittent discharge apparatus

Also Published As

Publication number Publication date
JPH051307A (en) 1993-01-08

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