JPS62276318A - Mill outlet temperature control method - Google Patents

Mill outlet temperature control method

Info

Publication number
JPS62276318A
JPS62276318A JP12056786A JP12056786A JPS62276318A JP S62276318 A JPS62276318 A JP S62276318A JP 12056786 A JP12056786 A JP 12056786A JP 12056786 A JP12056786 A JP 12056786A JP S62276318 A JPS62276318 A JP S62276318A
Authority
JP
Japan
Prior art keywords
mill
coal
flow rate
primary air
temperature
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
Application number
JP12056786A
Other languages
Japanese (ja)
Inventor
Ichiro Tashiro
田代 一郎
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.)
IHI Corp
Original Assignee
IHI 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 IHI Corp filed Critical IHI Corp
Priority to JP12056786A priority Critical patent/JPS62276318A/en
Publication of JPS62276318A publication Critical patent/JPS62276318A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To enable a temperature at a mill outlet to be held at a given value, by a method wherein a flow rate of primary air to a mill is regulated according to a moisture content of coal fed to the mill. CONSTITUTION:An amount of coal stored in a coal feeder 1 is controlled through the working of a coal feed amount regulating device 10 by means of a mill master instruction 9 by feedbacking a weighing signal from a weighing machine 11, mounted to the coal feeder 1, to a subtractor 12. A coal feed instruction from the subtractor 12 produces a primary air flow rate instruction 14 by means of a function converter 13, and a flow rate signal from a flow meter 16, mounted to the inlet of a mill 2, is fedback to a subtractor 17 to feed primary air according to the instruction 14. A moisture content of coal previously fed to the mill 2 is measured, a change in temperature at the outlet of the mill due to the coal is read by means of a temperature detector 21. The temperature at the outlet of the mill is restored to a specified value, and an increase in a primary air flow rate required for maintenance of the temperature is measured, and a primary air flow rate set by the air flow rate instruction 14 is increased by means of an increase instruction device 19.

Description

【発明の詳細な説明】 3、発明の詳細な説明 [産業上の利用分野] 本発明は竪形ミルのミル出口温度制御方法に関するもの
である。
Detailed Description of the Invention 3. Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a method for controlling the mill outlet temperature of a vertical mill.

[従来の技術] 竪形微粉炭ミルの場合、給炭量がミルマスター指令によ
って調整され、且つ上記給炭量に応じて、ミルへの微粉
炭搬送用1次空気の流量が制御されるようになっている
[Prior Art] In the case of a vertical pulverized coal mill, the amount of coal fed is adjusted by a mill master command, and the flow rate of primary air for conveying pulverized coal to the mill is controlled according to the amount of coal fed. It has become.

[発明が解決しようとする問題点] しかし、上記従来方式においては、給炭量に応じて1次
空気流量を変化させるのみであるため、例えば湿分の多
い石炭が給炭されたような場合、ミル出口温度(ミル内
温度)が低下して石炭の粉砕性が低下し、安定した運用
が出来なくなる問題を有していた。
[Problems to be Solved by the Invention] However, in the conventional method described above, the primary air flow rate is only changed depending on the amount of coal fed, so for example, when coal with a high moisture content is fed, However, there was a problem in that the mill outlet temperature (mill internal temperature) decreased and the coal pulverization properties deteriorated, making stable operation impossible.

本発明は、上記従来の問題点に着目してなしたもので、
ミルに湿分の大きな石炭が供給されるとき、1次空気流
量を増加して供給熱量を確保することによりミル出口温
度をキープすることを目的とする。
The present invention was made by focusing on the above-mentioned conventional problems.
When coal with high moisture content is supplied to the mill, the purpose is to maintain the mill outlet temperature by increasing the primary air flow rate and ensuring the amount of heat supplied.

[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、
竪形微粉炭ミルに供給される石炭の供給量に応じて調整
される前記ミルへの1次空気流量を、ミルに供給する石
炭の湿分に応じて加減することにより、ミル出口温度を
所定温度に保持することを特徴とするミル出口温度制御
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
By adjusting the primary air flow rate to the vertical pulverized coal mill, which is adjusted according to the amount of coal supplied to the mill, according to the moisture content of the coal supplied to the mill, the mill outlet temperature can be maintained at a predetermined value. The present invention relates to a mill outlet temperature control method characterized by maintaining the temperature at a certain temperature.

[作   用] 従って、本発明では、ミルに供給される1次空気流量を
、ミルに供給される石炭の湿分を検出して、その湿分量
に応じて変化させることにより、ミル出口温度を所定の
規定温度範囲内に維持することができる。
[Function] Therefore, in the present invention, the mill outlet temperature can be adjusted by detecting the moisture content of the coal supplied to the mill and changing the primary air flow rate supplied to the mill according to the moisture content. It can be maintained within a predetermined specified temperature range.

[実 施 例] 以下本発明の実施例を図面を参照しつつ説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.

図面は本発明の一例を示すもので、給炭機1からの石炭
が竪形微粉炭ミル2に供給されるようになっており、又
ミル2には、熱空気3と冷空気4を調整ダンパ5.6に
より所要温度に混合調整した1次空気7が1次空気流量
制御ダンパ8を介して供給されている。
The drawing shows an example of the present invention, in which coal from a coal feeder 1 is supplied to a vertical pulverized coal mill 2, and the mill 2 is supplied with hot air 3 and cold air 4. Primary air 7 mixed and adjusted to a required temperature by a damper 5.6 is supplied via a primary air flow rate control damper 8.

給炭機1の給炭量は、ミルマスター指令9により給炭量
調節装置10を介して行われ、又給炭機lに設けられた
計量機11の計量信号が引算器12にフィードバックさ
れて指令通りの給炭が行われるように制御されている。
The amount of coal fed into the coal feeder 1 is determined by a mill master command 9 via a coal feed amount adjustment device 10, and a measurement signal from a measuring device 11 provided in the coal feeder 1 is fed back to a subtracter 12. The system is controlled so that coal is fed as instructed.

又、前記引算器12からの給炭指令が関数変換器13に
より1次空気流量指令14となって前記流量制御ダンパ
8を作動する流量調節装置15に入力され、又前記ミル
2人口に設けられた流量計16からの流量信号が引算器
17にフィードバックされて前記1次空気流量指令14
通りの1次空気の供給が行われるように制御される。
Further, the coal feeding command from the subtractor 12 is converted into a primary air flow rate command 14 by a function converter 13 and is inputted to a flow rate adjustment device 15 that operates the flow rate control damper 8. The flow rate signal from the flowmeter 16 is fed back to the subtractor 17 and is then used as the primary air flow rate command 14.
The primary air supply is controlled to take place.

上記構成において、関数変換器13からの1次空気流量
指令14に、加算器18を介して1次空気流量を増加す
るように変更を加える(バイアスをかける)増加指令装
置19を設ける。
In the above configuration, an increase command device 19 is provided that changes (applies a bias) to the primary air flow rate command 14 from the function converter 13 via an adder 18 so as to increase the primary air flow rate.

又、前記1次空気7と微粉炭の搬送混合比(A/C−A
 IR/C0AL)については、前記流量調節装置15
に下限制限機能(ロー・リミッタ−)を備えて歯止めを
かける。図中20はボイラバーナ等に微粉炭を供給する
微粉炭管、21はミル出口温度検出計を示す。
Furthermore, the conveyance mixing ratio (A/C-A) of the primary air 7 and pulverized coal is
IR/C0AL), the flow rate adjustment device 15
It is equipped with a lower limit function (low limiter) to put a brake on it. In the figure, 20 indicates a pulverized coal pipe that supplies pulverized coal to a boiler burner, etc., and 21 indicates a mill outlet temperature detector.

前記増加指令装置19により1次空気流量を増加させる
量は、予めミル2に供給される石炭の湿分を計測してお
き、その湿分の石炭がミル2に供給された後のミル出口
温度の変化を温度検出計21で読み取っておき、上記ミ
ル出口温度を規定値まで戻してその温度を維持するのに
必要な1次空気流量の増加分を測定しておくことにより
求められる。又、上記1次空気7の増加は、石炭の湿分
%に応じて増加させるようにしたり、或いは湿分がある
値を越えたときに成る一定量を増加させるようにしても
良い。
The amount by which the primary air flow rate is increased by the increase command device 19 is determined by measuring the moisture content of coal supplied to the mill 2 in advance, and adjusting the mill outlet temperature after the moisture content of the coal is supplied to the mill 2. It is determined by reading the change in the temperature with the temperature detector 21, and measuring the increase in the primary air flow rate required to return the mill outlet temperature to the specified value and maintain that temperature. Furthermore, the amount of primary air 7 may be increased in accordance with the moisture percentage of the coal, or may be increased by a certain amount when the moisture content exceeds a certain value.

前記増加指令装置19からの増加指令がなくなると、1
次空気流量指令14による指令まで、1次空気流量が減
少される。
When the increase command from the increase command device 19 disappears, 1
The primary air flow rate is reduced until commanded by the secondary air flow command 14.

尚、本発明は上記実施例にのみ限定されるものではな(
、本発明の要旨を逸脱しない範囲内において種々変更を
加え得る。
It should be noted that the present invention is not limited only to the above embodiments (
However, various changes may be made without departing from the spirit of the invention.

[発明の効果コ 上記したように、本発明のミル出口温度制御装置によれ
ば、給炭量に応じて供給されている1次空気流量を、ミ
ルに供給される石炭の湿分に応じて変化させることによ
り、湿分の大きな石炭が供給された際、ミル内温度が低
下して石炭の粉砕性が低下するといった問題を防止し、
ミルの安定した運用を可能にできる優れた効果を奏し得
る。
[Effects of the Invention] As described above, according to the mill outlet temperature control device of the present invention, the primary air flow rate that is being supplied according to the amount of coal fed can be adjusted according to the moisture content of the coal that is supplied to the mill. By changing this, when coal with high moisture content is supplied, the temperature inside the mill decreases and the pulverization of the coal decreases, which can be prevented.
It can produce excellent effects that enable stable operation of the mill.

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

図面は本発明の方法を実施する制御回路の構成を示す説
明図である。 1は給炭機、2は竪形微粉炭ミル、7は1次空気、8は
1次空気流量制御ダンパ、9はミルマスター指令、lO
は給炭量調節装置、11は計量機、12は引算器、13
は関数変換器、14は1次空気流量指令、15は流量調
節装置、16は流量計、17は引算器、18は加算器、
19は増加指令装置、21は温度検出計を示す。
The drawing is an explanatory diagram showing the configuration of a control circuit that implements the method of the present invention. 1 is a coal feeder, 2 is a vertical pulverized coal mill, 7 is primary air, 8 is a primary air flow rate control damper, 9 is a mill master command, lO
1 is a coal feeding amount adjustment device, 11 is a weighing machine, 12 is a subtracter, 13
is a function converter, 14 is a primary air flow rate command, 15 is a flow rate adjustment device, 16 is a flow meter, 17 is a subtracter, 18 is an adder,
19 is an increase command device, and 21 is a temperature detector.

Claims (1)

【特許請求の範囲】[Claims] 1)竪形微粉炭ミルに供給される石炭の供給量に応じて
調整される前記ミルへの1次空気流量を、ミルに供給す
る石炭の湿分に応じて加減することにより、ミル出口温
度を所定温度に保持することを特徴とするミル出口温度
制御方法。
1) By adjusting the primary air flow rate to the vertical pulverized coal mill according to the amount of coal supplied to the mill, depending on the moisture content of the coal supplied to the mill, the mill outlet temperature can be adjusted. A mill outlet temperature control method characterized by maintaining the temperature at a predetermined temperature.
JP12056786A 1986-05-26 1986-05-26 Mill outlet temperature control method Pending JPS62276318A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12056786A JPS62276318A (en) 1986-05-26 1986-05-26 Mill outlet temperature control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12056786A JPS62276318A (en) 1986-05-26 1986-05-26 Mill outlet temperature control method

Publications (1)

Publication Number Publication Date
JPS62276318A true JPS62276318A (en) 1987-12-01

Family

ID=14789501

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12056786A Pending JPS62276318A (en) 1986-05-26 1986-05-26 Mill outlet temperature control method

Country Status (1)

Country Link
JP (1) JPS62276318A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102666A (en) * 2004-10-06 2006-04-20 Babcock Hitachi Kk Mill and coal fired boiler provided with it
JP2008246407A (en) * 2007-03-30 2008-10-16 Ihi Corp Method and device for controlling air temperature at outlet of horizontal type mill
JP2020085305A (en) * 2018-11-21 2020-06-04 三菱日立パワーシステムズ株式会社 Pulverized coal drying system for coal pulverizer, pulverized coal drying method and pulverized coal drying program for the system, coal pulverizer and gasification combined power generation facility
CN113028441A (en) * 2021-03-17 2021-06-25 华北电力科学研究院有限责任公司 Coal mill outlet temperature adjusting method and device and storage medium
CN114534901A (en) * 2022-03-01 2022-05-27 华能上海石洞口发电有限责任公司 Coal mill primary air control logic optimization method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102666A (en) * 2004-10-06 2006-04-20 Babcock Hitachi Kk Mill and coal fired boiler provided with it
JP4638708B2 (en) * 2004-10-06 2011-02-23 バブコック日立株式会社 Mill device and coal fired boiler equipment provided with the same
JP2008246407A (en) * 2007-03-30 2008-10-16 Ihi Corp Method and device for controlling air temperature at outlet of horizontal type mill
JP2020085305A (en) * 2018-11-21 2020-06-04 三菱日立パワーシステムズ株式会社 Pulverized coal drying system for coal pulverizer, pulverized coal drying method and pulverized coal drying program for the system, coal pulverizer and gasification combined power generation facility
CN113028441A (en) * 2021-03-17 2021-06-25 华北电力科学研究院有限责任公司 Coal mill outlet temperature adjusting method and device and storage medium
CN113028441B (en) * 2021-03-17 2022-07-05 华北电力科学研究院有限责任公司 Coal mill outlet temperature adjusting method and device and storage medium
CN114534901A (en) * 2022-03-01 2022-05-27 华能上海石洞口发电有限责任公司 Coal mill primary air control logic optimization method
CN114534901B (en) * 2022-03-01 2022-11-11 华能上海石洞口发电有限责任公司 Coal mill primary air control logic optimization method

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