JPH01168362A - How to control the amount of coal output from a vertical mill - Google Patents
How to control the amount of coal output from a vertical millInfo
- Publication number
- JPH01168362A JPH01168362A JP32628987A JP32628987A JPH01168362A JP H01168362 A JPH01168362 A JP H01168362A JP 32628987 A JP32628987 A JP 32628987A JP 32628987 A JP32628987 A JP 32628987A JP H01168362 A JPH01168362 A JP H01168362A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- vane
- amount
- coal feed
- feed amount
- 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.)
- Pending
Links
Landscapes
- Crushing And Grinding (AREA)
- Disintegrating Or Milling (AREA)
Abstract
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は竪ミルの出炭量制御方法に関するものである。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for controlling the amount of coal produced in a vertical mill.
[従来の技術]
第5図は竪ミルの一例を示すもので、本体ケーシング1
の中央上部に設けられた石炭投入管2から投入された原
料石炭aを、モータ3によって回転する粉砕臼4を有し
た粉砕テーブル5と、前記粉砕臼4に押付けるように設
けられた粉砕ローラ6との間に供給して粉砕を行い、粉
砕によって生じた微粉炭を1次空気供給ロア及びエアポ
ート8を介して下側から導入される1次空気すにより本
体ケーシング1内を浮遊上昇させ、上部に設けられた分
離ベーン9、エジェクトシュート10及び導出管11か
らなる粗粉分離器12により粗粉Cを分離して所要の微
粉度の微粉炭dとした後、燃料管13を介して微粉炭燃
焼ボイラ等のバーナに供給するようにしている。[Prior art] Fig. 5 shows an example of a vertical mill, in which the main body casing 1
A crushing table 5 having a crushing mill 4 rotated by a motor 3, and a crushing roller provided to press the raw coal a input from a coal input pipe 2 provided at the upper center of the mill against the crushing mill 4. 6 to carry out pulverization, and cause the pulverized coal produced by the pulverization to float upward in the main body casing 1 by the primary air introduced from the lower side via the primary air supply lower and the air port 8, A coarse powder separator 12 consisting of a separation vane 9, an eject chute 10, and a discharge pipe 11 provided at the upper part separates the coarse powder C into pulverized coal d of the required fineness, and then the fine powder is passed through a fuel pipe 13. It is supplied to burners such as charcoal-fired boilers.
第6.7図は前記分離ベーン9の詳細を示すもので、エ
ジェクトシュートlOの上部に設けた固定リング14に
、周方向に所要の間隔を有してベーン15を回転自在に
取付け、且つ該各ベーン15と一体に形成したベーンア
ーム16の相互間を接続ロッド17により順次連結し、
又ハンドル18によって回転するようにした駆動軸19
を設け、且つ該駆動軸19に固定したレバー20と前記
ベーンアーム16の1つとを連結杆2Iにて連結し、前
記ハンドル18の作動により、すべてのベーン15の開
度を同時に調整することができるようにしている。Fig. 6.7 shows details of the separation vane 9, in which the vane 15 is rotatably attached to the fixing ring 14 provided at the upper part of the eject chute 10 at a required interval in the circumferential direction. The vane arms 16 formed integrally with each vane 15 are successively connected to each other by a connecting rod 17,
Also, a drive shaft 19 rotated by a handle 18.
A lever 20 fixed to the drive shaft 19 and one of the vane arms 16 are connected by a connecting rod 2I, and the opening degrees of all the vanes 15 can be adjusted simultaneously by operating the handle 18. That's what I do.
上記した竪ミルにおいては、竪ミルの試運転時にベーン
15の開度をハンドル18を介して手動により設定し、
その後はベーン開度を一定にした状態において、1次空
気供給ロアから1次空気すを供給し、図示しない石炭供
給装置から石炭投入管2を介して供給される石炭aの量
を変えることにより、燃料管13から導出される微粉炭
dの出炭量を調整するようにしている。In the vertical mill described above, the opening degree of the vane 15 is manually set via the handle 18 during a test run of the vertical mill.
Thereafter, with the vane opening degree constant, primary air is supplied from the primary air supply lower, and the amount of coal a supplied from the coal supply device (not shown) via the coal input pipe 2 is changed. , the amount of pulverized coal d drawn out from the fuel pipe 13 is adjusted.
[発明が解決しようとする問題点]
しかし、上記従来装置においては、分離ベーン9のベー
ン15の開度は試運転時に手動で設定し、出炭量の調整
は石炭投入管2を介してミルに供給する石炭aの投入量
を変えることのみによって行っているために、第8図破
線で示すようなユニット負荷変動による出炭要求があっ
ても、石炭aの投入から粉砕されて微粉炭となり、1次
空気すによって搬送され更に粗粉分離器12を介して導
出されるまでに時間が掛り、よって実線で示すように実
出炭量に大きな遅れが生じる問題を有していた。[Problems to be Solved by the Invention] However, in the conventional device described above, the opening degree of the vane 15 of the separation vane 9 is manually set during the test run, and the amount of coal output is adjusted by entering the mill via the coal input pipe 2. Since this is done only by changing the input amount of coal a to be supplied, even if there is a demand for coal output due to unit load fluctuations as shown by the broken line in Figure 8, coal a is pulverized from the input and becomes pulverized coal. It takes time for the coal to be conveyed by the primary air chamber and further to be drawn out through the coarse powder separator 12, which has the problem of causing a large delay in the actual amount of coal produced, as shown by the solid line.
本発明は、上記従来の問題点に着目してなしたもので、
竪ミルにおけるユニット負荷変動時の出炭要求に対する
実出炭量の追従性の向上を図ることを目的としている。The present invention was made by focusing on the above-mentioned conventional problems.
The purpose of this project is to improve the follow-up ability of the actual coal output amount to the coal output request when the unit load fluctuates in a vertical mill.
[問題点を解決するための手段]
本発明は、上記技術的課題を解決しようとしたもので、
竪ミルの粗粉分離器における分離ベーンのベーン開度を
調節する駆動装置を設け、ユニット負荷変動時の負荷変
化率に応じて前記駆動装置を作動して前記ベーン開度を
調節することにより出炭量を制御することを特徴とする
竪ミルの出炭量制御方法、に係るものである。[Means for solving the problems] The present invention attempts to solve the above technical problems, and
A drive device is provided to adjust the vane opening of the separation vane in the coarse powder separator of the vertical mill, and the drive device is operated to adjust the vane opening in accordance with the load change rate when the unit load fluctuates. The present invention relates to a method for controlling the amount of coal output from a vertical mill, which is characterized by controlling the amount of coal.
[作 用]
従って、本発明では、ユニット負荷変動時に、ミルに供
給する石炭量を調節することにより行う出炭要求に対す
る実出炭量の変化の遅れを、分離ベーンのベーン開度を
調節することにより補正して、実出炭量を出炭要求に追
従させる。[Function] Therefore, in the present invention, when the unit load fluctuates, the delay in the change in the actual amount of coal output in response to the coal output request, which is performed by adjusting the amount of coal supplied to the mill, is adjusted by adjusting the vane opening degree of the separation vane. By correcting this, the actual amount of coal produced can be made to follow the demand for coal production.
[実 施 例コ 以下本発明の実施例を図面を参照しつつ説明する。[Implementation example] Embodiments of the present invention will be described below with reference to the drawings.
第1図は本発明の方法を実施する装置の一例を示すもの
で、第5図と同一符号を付したものは同一物を表わして
いる。FIG. 1 shows an example of an apparatus for carrying out the method of the present invention, and the same reference numerals as in FIG. 5 represent the same parts.
図示するように、前記駆動軸19を駆動装置22により
動力で回転するようにし、更に出炭要求信号23を石炭
供給装置24に導入してミルに供給する石炭aの供給量
を制御すると共に、前記出炭要求信号23を制御装置2
5に入力し、該制御装置25からの制御指令26により
前記駆動装置22を制御するよう構成する。As shown in the figure, the drive shaft 19 is rotated by power from a drive device 22, and a coal output request signal 23 is introduced into a coal supply device 24 to control the amount of coal a supplied to the mill. The coal output request signal 23 is transmitted to the control device 2.
5, and the drive device 22 is controlled by a control command 26 from the control device 25.
第2図及び第3図は駆動装置22の例を示すもので、第
2図はモータ27の回転軸に設けたウオーム軸28を駆
動軸19に設けたウオームホイール29に噛合して、モ
ータ27の駆動により駆動軸19を回転させるようにし
た方式を示し、又第3図はシリンダ30のシリンダロッ
ド31を駆動軸19に設けたレバー32に連結して、シ
リンダ30の伸縮により駆動軸19の回転を行うように
した方式を示している。2 and 3 show an example of the drive device 22. In FIG. 2, a worm shaft 28 provided on the rotating shaft of the motor 27 is meshed with a worm wheel 29 provided on the drive shaft 19, and the motor 27 FIG. 3 shows a system in which a cylinder rod 31 of a cylinder 30 is connected to a lever 32 provided on the drive shaft 19, and the expansion and contraction of the cylinder 30 rotates the drive shaft 19. This shows a method for performing rotation.
」1記において、ユニット負荷変化時、出炭要求信号2
3が石炭供給装置24に導入されてミルへの石炭aの供
給量が変更されると共に、出炭要求信号23が制御装置
25に入力され、該制御装置25による制御指令2Bに
より分離ベーン9のベーン開度がユニット負荷変化率に
応じて制御される。” 1, when the unit load changes, the coal output request signal 2
3 is introduced into the coal supply device 24 to change the supply amount of coal a to the mill, and at the same time, the coal output request signal 23 is input to the control device 25, and the control device 25 controls the separation vane 9 according to the control command 2B. The vane opening degree is controlled according to the unit load change rate.
これにより、ベーン15の開度に応じた微粉度の微粉炭
dが燃料管13を介して導出されることにより出炭量が
直ちに制御され、よって第4図に示すように実出炭量を
出炭要求に近付けて制御することが可能となる。As a result, pulverized coal d having a fineness corresponding to the opening degree of the vane 15 is led out through the fuel pipe 13, and the amount of coal produced is immediately controlled, so that the actual amount of coal produced is controlled as shown in FIG. It becomes possible to control the coal output closely.
このとき、ベーン15の調整はミルに供給される石炭a
の供給量の変化による出炭量の変化を見ながら(予め計
測しておく)行う。又、この制御は出炭量の増、減のい
ずれの場合も実施できる。At this time, the adjustment of the vane 15 is based on the coal a supplied to the mill.
This is done while observing changes in the amount of coal produced due to changes in the amount of coal supplied (measured in advance). Further, this control can be performed whether the amount of coal produced is increased or decreased.
尚、本発明は上記実施例にのみ限定されるものではなく
、ベーン開度の調節を自動で行うための駆動方式は種々
変更し得ること、その池水発明の要旨を逸脱しない範囲
内において種々変更し得ること、等は勿論である。It should be noted that the present invention is not limited to the above-mentioned embodiments, and that the drive system for automatically adjusting the vane opening degree can be modified in various ways without departing from the gist of the invention. Of course, there are things that can be done.
[発明の効果]
上記したように、本発明の竪ミルの出炭量制御方法によ
れば、ユニット負荷変動時に、ミルに供給する石炭量を
調節することによる出炭要求に対する実出炭量の変化の
遅れを、分離ベーンのベーン開度を調節することにより
補正し、これにより実出炭量を出炭要求に追従させて正
確に制御することができる優れた効果を奏し得る。[Effects of the Invention] As described above, according to the method for controlling the amount of coal output from a vertical mill of the present invention, when the unit load fluctuates, the actual amount of coal output can be controlled in response to the coal output request by adjusting the amount of coal supplied to the mill. The delay in change is corrected by adjusting the vane opening degree of the separation vane, thereby producing an excellent effect in which the actual coal production amount can be accurately controlled to follow the coal production request.
第1図は本発明の方法を実施する装置の一例を示す説明
図、第2図は第1図における駆動装置の一例を示す説明
図、第3図は第2図の他の例を示す説明図、第4図は本
発明におけるベーン開度及び出炭量と時間の関係を示す
線図、第5図は従来のミルの一例を示す説明図、第6図
は従来の粗粉分離機の一例を示す説明図、第7図は第6
図の平面図、第8図は従来のベーン開度及び出炭量と時
間の関係を示す線図である。
■は本体ケーシング、2は石炭投入管、7は1次空気供
給口、9は分離ベーン、10はエジェクトシュート、1
2は粗粉分離器、13は燃料管、14は固定リング、1
5はベーン、1Bはベーンアーム、17は接続ロッド、
19は駆動軸、20はレバー、21は連結杆、22は駆
動装置、23は出炭量要求信号、24は石炭供給装置、
25は制御装置、27はモータ、28はウオーム軸、2
9はウオームホイール、30はシリンダ、31はシリン
ダロッド、32はレバーを示す。FIG. 1 is an explanatory diagram showing an example of a device for implementing the method of the present invention, FIG. 2 is an explanatory diagram showing an example of the drive device in FIG. 1, and FIG. 3 is an explanatory diagram showing another example of the drive device in FIG. 2. Figure 4 is a diagram showing the relationship between the vane opening degree and coal output amount in the present invention and time, Figure 5 is an explanatory diagram showing an example of a conventional mill, and Figure 6 is a diagram showing the relationship between the vane opening degree and coal output amount and time in the present invention. An explanatory diagram showing an example, Fig. 7 is the 6th
The plan view of the figure and FIG. 8 are diagrams showing the relationship between the conventional vane opening degree, coal output amount, and time. ■ is the main body casing, 2 is the coal input pipe, 7 is the primary air supply port, 9 is the separation vane, 10 is the eject chute, 1
2 is a coarse powder separator, 13 is a fuel pipe, 14 is a fixing ring, 1
5 is a vane, 1B is a vane arm, 17 is a connecting rod,
19 is a drive shaft, 20 is a lever, 21 is a connecting rod, 22 is a drive device, 23 is a coal output request signal, 24 is a coal supply device,
25 is a control device, 27 is a motor, 28 is a worm shaft, 2
9 is a worm wheel, 30 is a cylinder, 31 is a cylinder rod, and 32 is a lever.
Claims (1)
度を調節する駆動装置を設け、ユニット負荷変動時の負
荷変化率に応じて前記駆動装置を作動して前記ベーン開
度を調節することにより出炭量を制御することを特徴と
する竪ミルの出炭量制御方法。1) Providing a drive device for adjusting the vane opening degree of the separation vane in the coarse powder separator of the vertical mill, and adjusting the vane opening degree by operating the drive device according to the rate of change in load when the unit load fluctuates. A method for controlling the amount of coal produced in a vertical mill, characterized by controlling the amount of coal produced by a vertical mill.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32628987A JPH01168362A (en) | 1987-12-23 | 1987-12-23 | How to control the amount of coal output from a vertical mill |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32628987A JPH01168362A (en) | 1987-12-23 | 1987-12-23 | How to control the amount of coal output from a vertical mill |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01168362A true JPH01168362A (en) | 1989-07-03 |
Family
ID=18186107
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32628987A Pending JPH01168362A (en) | 1987-12-23 | 1987-12-23 | How to control the amount of coal output from a vertical mill |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01168362A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110164653A1 (en) * | 2010-01-07 | 2011-07-07 | General Electric Company | Thermal inspection system and method incorporating external flow |
CN102802800A (en) * | 2009-06-22 | 2012-11-28 | 巴布科克和威尔科克斯能量产生集团公司 | System for controlling coal flow in a coal pulverizer |
CN105642407A (en) * | 2016-03-02 | 2016-06-08 | 河南省少林重型机器有限公司 | Vertical grinding mill |
-
1987
- 1987-12-23 JP JP32628987A patent/JPH01168362A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102802800A (en) * | 2009-06-22 | 2012-11-28 | 巴布科克和威尔科克斯能量产生集团公司 | System for controlling coal flow in a coal pulverizer |
US20110164653A1 (en) * | 2010-01-07 | 2011-07-07 | General Electric Company | Thermal inspection system and method incorporating external flow |
CN105642407A (en) * | 2016-03-02 | 2016-06-08 | 河南省少林重型机器有限公司 | Vertical grinding mill |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS5836632B2 (en) | Power plant pulverizer control device | |
CN113385294A (en) | Energy-saving control method for reducing coal grinding unit consumption of medium-speed coal mill by adjusting speed change of rare earth motor | |
JPH01168362A (en) | How to control the amount of coal output from a vertical mill | |
US5875977A (en) | Technique for improving the response time of pulverized coal boilers | |
JPH0731898A (en) | Coal pulverizer fitted with rotary type classifier and operating method therefor | |
CN208948386U (en) | Membrane pump feeding speed-regulating system and sand mill feed system | |
JP3763155B2 (en) | Mill coal supply control device | |
US4602744A (en) | Method of controlling a grinding roller mill | |
JPS6316984B2 (en) | ||
JPH02253861A (en) | Method for controlling fineness of pulverized coal in a vertical mill | |
JPH04334563A (en) | Control device for coal feed amount from coal mill | |
CN109264411A (en) | Membrane pump feeding speed-regulating system and sand mill feed system | |
US3467036A (en) | Steam generator and coal pulverizing apparatus | |
JPH01270956A (en) | Method for controlling rotational speed of rotary type classifier of vertical mill | |
JPH0361089B2 (en) | ||
SU973160A1 (en) | Method of automatic control of drum ball mill | |
CN212943445U (en) | Pulverized coal separator automatically regulated folds to baffle device | |
JP2003311170A (en) | Mill control unit for coarse powder separation vane opening | |
SU606621A1 (en) | System of automatic control of the material-desintegration process in grate-free hammer mill | |
JPS60207823A (en) | Pulverized coal/air ratio adjustment device for pulverized coal manufacturing equipment | |
JPH08252476A (en) | Mill coal output characteristic correction device | |
JPH01203058A (en) | Vertical mill | |
JPH01315354A (en) | Method for controlling feed rate in roller mill | |
SU814463A1 (en) | Apparatus for regulating mill charge with source materials | |
JPS62162818A (en) | Mill control method in pulverized-coal-firing boiler |