JPH06335628A - Powder feeder - Google Patents

Powder feeder

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Publication number
JPH06335628A
JPH06335628A JP12884993A JP12884993A JPH06335628A JP H06335628 A JPH06335628 A JP H06335628A JP 12884993 A JP12884993 A JP 12884993A JP 12884993 A JP12884993 A JP 12884993A JP H06335628 A JPH06335628 A JP H06335628A
Authority
JP
Japan
Prior art keywords
rotor
particle
pressure
pipe
powder
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.)
Withdrawn
Application number
JP12884993A
Other languages
Japanese (ja)
Inventor
Yutaka Iida
豊 飯田
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP12884993A priority Critical patent/JPH06335628A/en
Publication of JPH06335628A publication Critical patent/JPH06335628A/en
Withdrawn legal-status Critical Current

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  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To prevent the damage due to the backflow of high pressure gas in a centrifugal powder feeder for feeding powder into a place under high pressure. CONSTITUTION:To predict the generation of backflow of high pressure gas in its early stage to the utmost, a pressure detector 14 is installed in the central part of a rotor 3. When the detected pressure exceeds the 1st restricted value, the revolution of the rotor 3 is increased to prevent the backflow. And when, what is worse, the pressure in the rotor does not stop rising and exceeds the 2nd restricted value, cutoff valves 2, 10, 13 installed in a particle feeding pipe 1, a particle discharge pipe 9 and a particle return pipe 12 are all closed respectively.

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、石炭ガス化複合発電プ
ラント,加圧流動床ボイラ,製鉄所の高炉等,粉体を高
圧下へ供給する粉体供給装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coal gasification combined cycle power plant, a pressurized fluidized bed boiler, a blast furnace in a steel mill, and the like, and a powder supply device for supplying powder under high pressure.

【0002】[0002]

【従来の技術】図4は、高圧下へ粉体を供給する従来の
遠心式粉体供給装置の一例を示す系統図である。粉体は
粒子供給管(1)によりロータ(3)の中心へ気流搬送
され、ロータの回転に伴う遠心力によりロータ中心から
放射状に伸びている通路(6)に圧密され、ノズル
(7)から高圧のケーシング(5)内に排出される。そ
して排出管(9)を経由して、ボイラ(11)等へ供給
される。またロータ内に供給される粒子の一部は、余剰
粒子として粒子戻り管(12)を経由して、粒子供給管
(1)の上流側へ戻される。なお、図中(4),(1
5)は軸受,(8)はモータ,(16)はロータ回転数
検出器である。
2. Description of the Related Art FIG. 4 is a system diagram showing an example of a conventional centrifugal powder feeder for feeding powder under high pressure. The powder is conveyed by air flow to the center of the rotor (3) by the particle supply pipe (1), is compacted by the centrifugal force accompanying the rotation of the rotor into the passage (6) radially extending from the center of the rotor, and is discharged from the nozzle (7). It is discharged into the high-pressure casing (5). Then, it is supplied to the boiler (11) and the like via the discharge pipe (9). Further, some of the particles supplied into the rotor are returned as excess particles to the upstream side of the particle supply pipe (1) via the particle return pipe (12). In addition, (4), (1
5) is a bearing, (8) is a motor, and (16) is a rotor speed detector.

【0003】[0003]

【発明が解決しようとする課題】前記のような遠心式粉
体供給装置においては、ロータを適正な回転数で回転さ
せることによって、高圧下への粉体の排出と粉体層によ
る圧力シールが可能となり、安全に運転できる。しかし
ながら、適切でない運転操作,制御装置の異常、あるい
はハード上の故障等により、ロータ回転数がケーシング
(5)の圧力に対して適切な範囲を下廻る場合には、高
圧ガスがロータ内通路(6)に充填されている粒子をロ
ータ中心側へ押し戻すため、粉体層によるシールが破
れ、いわゆる高圧から常圧へのガスの逆流が起きる。ガ
スが逆流すると、粒子供給管(1),粒子戻り管(1
2)等の常圧系統の機器が加圧状態にさらされるため、
装置の故障の原因となる。更にまた、粒子排出管(9)
がガス化炉,加圧流動床ボイラ等と接続されている場合
には、高温の燃焼ガスが逆流するという、安全上も大き
な問題となる可能性が生じる。
In the centrifugal powder feeder as described above, by rotating the rotor at an appropriate rotational speed, the powder is discharged under high pressure and the pressure is sealed by the powder layer. It becomes possible and can drive safely. However, when the rotor speed falls below an appropriate range with respect to the pressure of the casing (5) due to improper driving operation, abnormality of the control device, hardware failure, or the like, the high-pressure gas passes through the rotor internal passage ( Since the particles filled in 6) are pushed back toward the rotor center side, the seal due to the powder layer is broken, and so-called backflow of gas from high pressure to normal pressure occurs. When gas flows backward, particle supply pipe (1), particle return pipe (1)
Since the equipment of the normal pressure system such as 2) is exposed to the pressurized state,
It may cause equipment failure. Furthermore, the particle discharge pipe (9)
Is connected to a gasification furnace, a pressurized fluidized bed boiler, etc., there is a possibility that a high temperature combustion gas will flow back, which will be a serious safety problem.

【0004】[0004]

【課題を解決するための手段】本発明は、前記従来の課
題を解決するために、内部に複数の通路が放射状に設け
られたロータの中心部に粒子供給管を経て供給される粉
体を上記ロータの遠心力により高圧下へ排出し粒子排出
管を経て取出すとともに、余剰粒子を粒子戻り管を経て
上記粒子供給管の上流へ戻すようにした粉体供給装置に
おいて、上記ロータの中心部に圧力検出器を、上記粒子
供給管、上記粒子排出管および上記粒子戻り管に自動遮
断弁をそれぞれ設けるとともに、上記圧力検出器の検出
圧力に基づいて上記ロータの回転数を制御する手段およ
び上記検出圧力に基づいて上記自動遮断弁を全て閉じる
手段を設けたことを特徴とする粉体供給装置を提案する
ものである。
In order to solve the above-mentioned conventional problems, the present invention provides a powder supplied through a particle supply pipe to a central portion of a rotor having a plurality of passages radially provided therein. In the powder supply device configured to discharge under high pressure by the centrifugal force of the rotor and take out through the particle discharge pipe, and to return surplus particles to the upstream of the particle supply pipe through the particle return pipe, in the center of the rotor. A pressure detector is provided in each of the particle supply pipe, the particle discharge pipe, and the particle return pipe, and an automatic shutoff valve is provided, and means for controlling the rotation speed of the rotor based on the pressure detected by the pressure detector and the detection. The present invention proposes a powder supply device characterized in that means for closing all of the above-mentioned automatic shutoff valves based on pressure is provided.

【0005】[0005]

【作用】ロータ中心部の圧力は、遠心力が適正に作用し
ている間は、ほぼ常圧を保持しているが、逆流現象の発
生直前には、高圧のケーシング側からのリーク空気(或
は他の加圧媒体)量が増加して粒子戻り管内を通過する
空気の流速が増加するため、ロータ中心部の圧力が上昇
する。したがって、その圧力を監視していれば逆流の発
生を予知できる。
The pressure at the center of the rotor is maintained at almost normal pressure while the centrifugal force is working properly, but immediately before the occurrence of the backflow phenomenon, high pressure leak air (or The other pressurized medium) and the flow velocity of the air passing through the particle return pipe increases, so that the pressure at the center of the rotor rises. Therefore, if the pressure is monitored, the occurrence of backflow can be predicted.

【0006】そこで本発明では、その圧力の上昇を検知
してロータの回転数を増加させ、逆流を防止する。また
回転数を増加させてもロータ中心部の圧力が低下しない
場合、すなわち逆流の発生を防止できない場合には、粒
子供給管,粒子排出管,および粒子戻り管にそれぞれ設
けられた自動遮断弁を全て閉じることにより、逆流の影
響を最少限に抑え、装置全体の安全を確保する。
Therefore, in the present invention, the increase in the pressure is detected to increase the rotational speed of the rotor to prevent the backflow. If the pressure at the center of the rotor does not drop even if the number of rotations is increased, that is, if backflow cannot be prevented, the automatic shutoff valves provided in the particle supply pipe, the particle discharge pipe, and the particle return pipe should be used. By closing all of them, the influence of backflow is minimized and the safety of the entire device is ensured.

【0007】[0007]

【実施例】図1は本発明の一実施例を示す系統図であ
る。ロータ(3)の中心部に設けられた圧力検出器(1
4)の出力信号Pとロータ回転数検出器(16)の出力
信号N0 は演算器(17)に入力される。演算器(1
7)には予め図2に例示するような関数が登録されてお
り、入力信号に対して次の動作をする。
FIG. 1 is a system diagram showing an embodiment of the present invention. A pressure detector (1 provided at the center of the rotor (3)
The output signal P of 4) and the output signal N 0 of the rotor speed detector (16) are input to the calculator (17). Arithmetic unit (1
In 7), a function as illustrated in FIG. 2 is registered in advance, and the following operation is performed on the input signal.

【0008】 圧力信号Pがロータ回転数N0 に対す
る警報点1の設定圧P1 以下の場合、すなわち、P≦P
1 の場合は現状維持。
When the pressure signal P is equal to or lower than the set pressure P 1 at the alarm point 1 with respect to the rotor speed N 0 , that is, P ≦ P
In case of 1 , the current status is maintained.

【0009】 圧力信号Pが警報点1の設定圧P1
りも大きく警報点2の設定圧P2 以下の場合は、圧力P
がP1 以下になるまでロータ回転数を上げるよう、ロー
タ回転数制御信号Aを出力し、ロータ回転数制御装置
(18)へ入力する。
When the pressure signal P is larger than the set pressure P 1 at the alarm point 1 and equal to or less than the set pressure P 2 at the alarm point 2, the pressure P
The rotor rotation speed control signal A is output so as to increase the rotor rotation speed until is less than P 1, and is input to the rotor rotation speed control device (18).

【0010】 圧力信号Pが警報点2の設定圧P2
りも大きくなった場合は、遮断弁信号Bを出力して遮断
弁開閉装置(19)へ送り、粒子排出管,粒子供給管,
粒子戻り管の各自動遮断弁(2),(10),(13)
を閉操作する。
When the pressure signal P becomes larger than the set pressure P 2 at the alarm point 2, the shutoff valve signal B is output and sent to the shutoff valve opening / closing device (19), and the particle discharge pipe, the particle supply pipe,
Automatic shutoff valves (2), (10), (13) for the particle return pipe
Close.

【0011】図5は、前記図4により説明した従来の粉
体供給装置において、逆流が生じた場合のロータ中心の
圧力P,ロータ回転数N,各遮断弁(手動)の開閉状態
および粒子供給系上流側の圧力Pa の変化を示し、図3
は本実施例における同様な変化を示す。図3(a)はロ
ータ回転数増加により逆流が防止できた場合、図3
(b)はロータが機械的あるいは電気的に停止した場合
である。いずれの場合も、本実施例では従来システムと
比較して粒子供給系の圧力上昇が低く抑えられており、
安全な運転あるいは停止ができるようになっている。
FIG. 5 shows the conventional powder feeding apparatus described with reference to FIG. 4, in which the pressure P at the center of the rotor, the rotor speed N, the open / close state of each shutoff valve (manual), and the particle feeding when a backflow occurs. The change in pressure P a on the upstream side of the system is shown in FIG.
Shows a similar change in this embodiment. FIG. 3A shows the case where the backflow can be prevented by increasing the rotor rotation speed.
(B) is the case where the rotor is mechanically or electrically stopped. In any case, in this embodiment, the pressure increase of the particle supply system is suppressed to be low as compared with the conventional system,
You can drive or stop safely.

【0012】[0012]

【発明の効果】本発明においては、遠心式粉体供給装置
のロータ内圧力を監視し、高圧ガスの逆流が生じるのを
早い段階で察知して、ロータの回転数を上げたり、粒子
供給管,粒子排出管,粒子戻り管にそれぞれ設けられた
自動遮断弁を閉じたりすることにより、高圧ガスの逆流
による被害を最少限に抑えることができる。
According to the present invention, the internal pressure of the rotor of the centrifugal powder feeder is monitored, and it is detected at an early stage that a high-pressure gas backflow occurs. By closing the automatic shut-off valves provided in the particle discharge pipe and the particle return pipe, the damage due to the reverse flow of high-pressure gas can be minimized.

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

【図1】図1は本発明の一実施例に係る粉体供給装置を
示す系統図、
FIG. 1 is a system diagram showing a powder supply device according to an embodiment of the present invention,

【図2】図2は上記実施例における粉体圧警報設定の一
例を示す図である。
FIG. 2 is a diagram showing an example of a powder pressure alarm setting in the above embodiment.

【図3】図3は上記実施例における逆流防止時の挙動を
示す図である。
FIG. 3 is a diagram showing a behavior at the time of preventing backflow in the above embodiment.

【図4】図4は従来の粉体供給装置の一例を示す系統図
である。
FIG. 4 is a system diagram showing an example of a conventional powder supply device.

【図5】図5は上記従来の粉体供給装置において逆流が
生じた場合の挙動を示す図である。
FIG. 5 is a diagram showing a behavior when a backflow occurs in the above-mentioned conventional powder supply device.

【符号の説明】[Explanation of symbols]

(1) 粒子供給管 (2) 自動遮断弁 (3) ロータ (4) 軸受 (5) ケーシング (6) 粒子通路 (7) ノズル (8) モータ (9) 粒子排出管 (10) 自動遮断弁 (11) ボイラ (12) 粒子戻り管 (13) 自動遮断弁 (14) ロータ内圧力検出器 (15) 軸受 (16) ロータ回転数検出器 (17) 演算器 (18) ロータ回転数制御装置 (19) 遮断弁開閉装置 (1) Particle supply pipe (2) Automatic shutoff valve (3) Rotor (4) Bearing (5) Casing (6) Particle passage (7) Nozzle (8) Motor (9) Particle discharge pipe (10) Automatic shutoff valve ( 11) Boiler (12) Particle return pipe (13) Automatic shutoff valve (14) Rotor pressure detector (15) Bearing (16) Rotor speed detector (17) Computer (18) Rotor speed controller (19) ) Shut-off valve opening / closing device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 内部に複数の通路が放射状に設けられた
ロータの中心部に粒子供給管を経て供給される粉体を上
記ロータの遠心力により高圧下へ排出し粒子排出管を経
て取出すとともに、余剰粒子を粒子戻り管を経て上記粒
子供給管の上流へ戻すようにした粉体供給装置におい
て、上記ロータの中心部に圧力検出器を、上記粒子供給
管、上記粒子排出管および上記粒子戻り管に自動遮断弁
をそれぞれ設けるとともに、上記圧力検出器の検出圧力
に基づいて上記ロータの回転数を制御する手段および上
記検出圧力に基づいて上記自動遮断弁を全て閉じる手段
を設けたことを特徴とする粉体供給装置。
1. A powder which is supplied through a particle supply pipe to a central portion of a rotor having a plurality of radial passages inside is discharged under high pressure by centrifugal force of the rotor and is taken out through the particle discharge pipe. In the powder supply device configured to return excess particles to the upstream of the particle supply pipe through the particle return pipe, a pressure detector is provided at the center of the rotor, the particle supply pipe, the particle discharge pipe, and the particle return pipe. Each of the pipes is provided with an automatic shutoff valve, and means for controlling the rotational speed of the rotor based on the pressure detected by the pressure detector and means for closing all the automatic shutoff valves based on the detected pressure are provided. Powder supply device.
JP12884993A 1993-05-31 1993-05-31 Powder feeder Withdrawn JPH06335628A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12884993A JPH06335628A (en) 1993-05-31 1993-05-31 Powder feeder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12884993A JPH06335628A (en) 1993-05-31 1993-05-31 Powder feeder

Publications (1)

Publication Number Publication Date
JPH06335628A true JPH06335628A (en) 1994-12-06

Family

ID=14994904

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12884993A Withdrawn JPH06335628A (en) 1993-05-31 1993-05-31 Powder feeder

Country Status (1)

Country Link
JP (1) JPH06335628A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998012357A1 (en) * 1996-09-19 1998-03-26 Deutsche Voest-Alpine Industrieanlagenbau Gmbh Process for monitoring the operation of a device for feeding an abrasive medium by means of a fluid
EP1013778A1 (en) * 1998-12-22 2000-06-28 Der Grüne Punkt-Duales System Deutschland Aktiengesellschaft Method and apparatus for producing metal from metal ores

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998012357A1 (en) * 1996-09-19 1998-03-26 Deutsche Voest-Alpine Industrieanlagenbau Gmbh Process for monitoring the operation of a device for feeding an abrasive medium by means of a fluid
EP1013778A1 (en) * 1998-12-22 2000-06-28 Der Grüne Punkt-Duales System Deutschland Aktiengesellschaft Method and apparatus for producing metal from metal ores
US6231638B1 (en) 1998-12-22 2001-05-15 Der Grune Punkt - Dsd Duales System Deutschland Ag Process for producing metal from metal ores

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Legal Events

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Effective date: 20000801