JPS6197052A - Device for drying and grinding coal - Google Patents

Device for drying and grinding coal

Info

Publication number
JPS6197052A
JPS6197052A JP22092484A JP22092484A JPS6197052A JP S6197052 A JPS6197052 A JP S6197052A JP 22092484 A JP22092484 A JP 22092484A JP 22092484 A JP22092484 A JP 22092484A JP S6197052 A JPS6197052 A JP S6197052A
Authority
JP
Japan
Prior art keywords
pulverized coal
drying
coal
pneumatic
air
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
JP22092484A
Other languages
Japanese (ja)
Inventor
三浦 祥正
沖上 昇
善利 関口
邦夫 佐々木
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen 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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP22092484A priority Critical patent/JPS6197052A/en
Publication of JPS6197052A publication Critical patent/JPS6197052A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、微粉炭燃焼ボイラシステムにおける石炭乾燥
・粉砕装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a coal drying and pulverizing device in a pulverized coal combustion boiler system.

従来の技術 従来の石炭乾燥・粉砕装置は、外部から供贅された粗炭
を粉砕して微粉炭とし、外部から供給された乾燥・気送
用空気により前記微粉炭を乾燥しかつ微粉炭燃焼ボイラ
に搬送する構造でめった。
BACKGROUND OF THE INVENTION Conventional coal drying and pulverizing equipment pulverizes coarse coal supplied from the outside into pulverized coal, dries the pulverized coal using drying and pneumatic air supplied from the outside, and burns the pulverized coal. This happened because of the structure that transports it to the boiler.

発明が解決しようとする問題点 上記従来構成によれば、石炭乾燥・粉砕装置内の旧法気
送用空気の空塔速度は乾燥・気送用空気の量によって決
定され、供給粗炭の量を下げた場合でも、微粉炭浮遊の
最小空塔速度を維持するため、乾燥・気送用空気の量を
大幅に低減することができず、乾燥・気送用空気と微粉
炭との重量比(以下rA/CJと記す)の値をあ″り低
くすることができなかった。特に小型の石炭乾燥・粉砕
装置では、A/Cを小さくすると装置の圧損が増大し、
微粉炭が装置内に過充填されて、装置の振動が発生する
等、異常運転となり、A/Cの低い運転操作が難しかっ
た。一方、微粉炭の燃焼について考えると、A/Cがで
きるだけ小さい方が燃焼の安定性やNOxの抑制面から
都合が良く、この点で石炭乾燥・粉砕装置の要求と相反
してお9、微粉炭燃焼ボイラシステムとしての操作性(
特にタウンダウン)が悪かった。
Problems to be Solved by the Invention According to the above-mentioned conventional configuration, the superficial velocity of the old method pneumatic air in the coal drying/pulverizing device is determined by the amount of drying/pneumatic air, and the amount of raw coal to be supplied is determined by the amount of drying/pneumatic air. Even if the air volume is lowered, the amount of air for drying and pneumatics cannot be significantly reduced in order to maintain the minimum superficial velocity for floating pulverized coal, and the weight ratio of air for drying and pneumatics to pulverized coal ( It was not possible to reduce the value of rA/CJ (hereinafter referred to as rA/CJ) too low. Especially in small coal drying and pulverizing equipment, reducing the A/C increases the pressure drop in the equipment.
The equipment was overfilled with pulverized coal, causing abnormal operation such as vibration of the equipment, making it difficult to operate the equipment at low A/C. On the other hand, when considering the combustion of pulverized coal, it is convenient to have the A/C as small as possible in terms of stability of combustion and suppression of NOx. Operability as a charcoal-fired boiler system (
Town Down) was especially bad.

また、石炭乾燥・粉砕装置の負荷変動による異常運転を
防止するため、微粉炭を一時貯えるヒン方式を採用した
システムが従来存在していたが、この場合、微粉炭の捕
集、貯炭設備の付加が必要であシ、更に微粉炭貯炭に対
する安全対策上、■2吹き込み設備の付加等、コストア
ップの要因となっていた。
In addition, in order to prevent abnormal operation due to load fluctuations in the coal drying/pulverizing equipment, there has been a system that uses a hinge system to temporarily store pulverized coal. In addition, due to safety measures for storing pulverized coal, additional blowing equipment (2) was required, which increased costs.

本発明は上記問題を全て解消した上次乾燥・粉砕装置を
提供することを目的とする。
An object of the present invention is to provide an upper drying/pulverizing device that solves all of the above problems.

問題を解決するための手段 上記問題を解決するため、本発明の上次乾燥・粉砕装置
は、粗炭と乾燥・気送用空気とが供給されかつ前記粗炭
を粉砕して微粉炭とするミル本体と、前記乾燥・気送用
空気に混入して前記ミル本体の外部へ搬送された前記微
粉炭を回収するサイクロンとを@えた構成としたもので
ろる。
Means for Solving the Problems In order to solve the above-mentioned problems, the primary drying/pulverizing device of the present invention is provided with crude coal and drying/air blowing air, and pulverizes the coarse coal into pulverized coal. The mill may have a structure including a mill body and a cyclone for recovering the pulverized coal mixed with the drying/air blowing air and conveyed to the outside of the mill body.

作   用 上記構成において、ミル本体で得られた微粉炭は、乾燥
・気送用空気により乾燥かつ搬送され、サイクロンで回
収されて微粉炭燃焼ボイラに供給される。したがって、
ミル本体からの気送微粉炭のA/Cは大きくても、サイ
クロンから欽粉炭燃焼ホイラに供給される気送微粉炭の
A/Cは充分小さくでき、微粉炭燃焼ボイラの燃焼の安
定性の向上とミル本体の異常運転の防止とを同時に実現
できる。
Operation In the above configuration, the pulverized coal obtained in the mill body is dried and conveyed by drying and pneumatic air, collected by a cyclone, and supplied to the pulverized coal combustion boiler. therefore,
Even if the A/C of the pneumatic pulverized coal from the mill body is large, the A/C of the pneumatic pulverized coal supplied from the cyclone to the pulverized coal combustion boiler can be sufficiently small, which improves the combustion stability of the pulverized coal combustion boiler. It is possible to simultaneously achieve improvement and prevention of abnormal operation of the mill body.

実施例 以下、本発明の一実施例を図面に基づいて説明する。Example Hereinafter, one embodiment of the present invention will be described based on the drawings.

図において、(1)はミル本体、(2)はサイクロン、
(3)はプロア、(4)は粗炭を前記ミル本体(1)に
供給するための粗炭供給管、(5)は乾燥・気送用空気
を前記ミル本体(1)に供給するための乾燥・気送用空
気供給管、(6)は前記ミル本体(1)と前記サイクロ
ン(2)とを接続する低濃度気送微粉炭搬送管、(7)
は#記すイクロン(2)の下端に接続された高濃度気送
微粉炭搬送管、(8)は前記プロア(3)を介して前記
サイクロン(2)の上端部と前記ミル本体(IJとを接
続する極低濃度気送微粉炭返送管である。
In the figure, (1) is the mill body, (2) is the cyclone,
(3) is a proa, (4) is a raw coal supply pipe for supplying raw coal to the mill body (1), and (5) is for supplying drying and pneumatic air to the mill body (1). (6) is a low concentration pneumatic pulverized coal conveying pipe connecting the mill main body (1) and the cyclone (2); (7) is a drying/pneumatic air supply pipe;
(8) is a high concentration pneumatic pulverized coal conveying pipe connected to the lower end of the cyclone (2) marked with #, and (8) is a pipe that connects the upper end of the cyclone (2) and the mill main body (IJ) through the proar (3). This is the extremely low concentration pneumatic pulverized coal return pipe to be connected.

以下、上記構成における作用について説明する。The effects of the above configuration will be explained below.

粗炭供給管(4)を通ってミル本体(IJに供給された
粗炭は、ミル本体(1)によジ粉砕されて微粉炭にされ
る。この微粉炭は、乾燥・気送用空気供給管(5)を通
ってミル本体(1)へ供給される乾燥・気送用空気によ
シ乾燥されかつ低濃度気送微粉戻搬送管(6)を通って
サイクロン(2)に搬送される。なお乾燥・気送用空気
は、酸素の重量比が12%以下であることが望ましく、
微粉炭の水分が多い琳合は通常の空気でもよい。サイク
ロン(2)では、乾燥・気送用空気に混入した微粉炭が
回収され、この微粉炭は高濃度気送微粉炭搬送管(7)
を通って図外の微粉炭燃焼ボイラに供給される。一般に
、サイクロン(2)は10μm以上の粒径の微粉炭を捕
集できるので、はとんど全部の微粉炭が回収される。一
方、サイクロン(2)により微粉炭を回収された乾燥・
気送用空気は、プロア(3)により、極低濃度気送微粉
炭返送管(8)を通ってミル本体(1)に返送され、乾
燥・気送用。
The raw coal supplied to the mill body (IJ) through the raw coal supply pipe (4) is ground into pulverized coal by the mill body (1).This pulverized coal is It is dried by the drying/pneumatic air supplied to the mill body (1) through the supply pipe (5), and is transported to the cyclone (2) through the low concentration pneumatic fine powder return transport pipe (6). It is desirable that the weight ratio of oxygen in the drying/pneumatic air is 12% or less.
Ordinary air may be used for pulverized coal with a high moisture content. In the cyclone (2), the pulverized coal mixed in the drying/pneumatic air is collected, and this pulverized coal is transferred to the high concentration pneumatic pulverized coal conveying pipe (7).
It is supplied to a pulverized coal combustion boiler (not shown) through the pulverized coal combustion boiler. Generally, the cyclone (2) can collect pulverized coal with a particle size of 10 μm or more, so almost all of the pulverized coal is recovered. On the other hand, the pulverized coal collected by the cyclone (2) is dried and
The pneumatic air is returned to the mill body (1) by the proa (3) through the extremely low concentration pneumatic pulverized coal return pipe (8) for drying and pneumatic feeding.

空気供給管(5)からの乾燥・気送用空気と混合し、微
粉度を乾燥させかつ搬送する。
It is mixed with drying and pneumatic air from the air supply pipe (5) to dry the fineness and convey it.

このように、サイクロン(2)によシ微粉次を回収して
高濃度気送微粉炭として微粉炭燃焼ボイラに供給するの
で、ミル本体(1)から搬出される低濃度気送微粉炭の
A/’C値に関係なく、充分〜で値の小さい気送微粉炭
を微粉炭燃焼ボイラに供給でき、したがって燃焼の安定
性の向上とミル本体の異常運転の防止とを同時に実現で
きる。すなわち、°低負荷時においても、ミル本体(1
)に充分な量の乾燥・気送用空気を供給できるので、乾
燥・気送用空気の量が少ないために政粉炭をミル本体(
1)内に過充填させてミル本体(υの振動を発生させて
しまう等の異常運転を生じることがない。また、燃焼に
供する高濃度気送微粉炭のルで値は、粗炭供給管(4)
を通ってミル本体(1)に供給される粗炭の量と乾燥・
気送用空気供給管(5)を通ってミル本体(1)K供給
される乾燥・気送用空気の量とKよって自由に制御可能
であシ、低負荷時においてもA/C値2未満の運転が可
能である。
In this way, the cyclone (2) collects the fine powder and supplies it to the pulverized coal combustion boiler as high concentration pneumatic pulverized coal, so that the A of the low concentration pneumatic pulverized coal carried out from the mill body (1) is reduced. Regardless of the /'C value, pneumatic pulverized coal with a sufficiently low value can be supplied to the pulverized coal combustion boiler, and therefore, it is possible to simultaneously improve combustion stability and prevent abnormal operation of the mill body. In other words, even under low load, the mill body (1
Since the amount of air for drying and pneumatics is small, powdered coal can be supplied to the mill body (
1) Overfilling the mill body (υ) will not cause abnormal operation such as vibration.In addition, the value of the high concentration pneumatic pulverized coal used for combustion is (4)
The amount of raw coal supplied to the mill body (1) through the
The amount of drying and pneumatic air supplied to the mill body (1) through the pneumatic air supply pipe (5) and K can be freely controlled, and the A/C value is 2 even at low loads. It is possible to operate under

なお不実施例のように、サイクロン(2)で微粉炭を回
収された乾燥・気送用空気をミル本体(υに返送して循
環使用するようにすれば、乾燥・気送用空気を有効利用
できるので好ましい。これは、特に酸素濃度を12重量
%以下とした特別な空気からなる乾燥・気送用空気を使
用している場合に有用である。
In addition, as in the non-implemented example, if the air for drying and pneumatics that collects the pulverized coal in the cyclone (2) is returned to the mill body (υ) and used for circulation, the air for drying and pneumatics can be effectively used. This is preferable because it can be used.This is particularly useful when drying and pneumatic air consisting of special air with an oxygen concentration of 12% by weight or less is used.

発明の詳細 な説明したように本発明によれば、従来のビン方式のも
のと比較して安価に製作できるものであシながら、負荷
変#IKよるミル本体の異常振動などの異常運転を引き
起こすことがないと共に、ミル本体の負荷変動に関係な
く常に一定のA/C値の気送微粉炭を燃焼に供すること
ができ、タウンダウンの大きな操作及びVCの小さな操
作を可能にできる。
DETAILED DESCRIPTION OF THE INVENTION As described in detail, although the present invention can be manufactured at a lower cost than the conventional bottle type, it causes abnormal operation such as abnormal vibration of the mill body due to load change #IK. In addition, pneumatic pulverized coal with a constant A/C value can always be used for combustion regardless of load fluctuations on the mill main body, and large town-down operations and small VC operations can be made possible.

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

図面は本発明の一夾施例における上次乾燥粉砕装置の全
体構成図である。 (1)・・・ミル本体、(2)・・・サイクロン代理人
    森   本   義   弘l・・・ミル本体 ?・・・γ(70ン
The drawing is an overall configuration diagram of an upper drying and pulverizing apparatus in one embodiment of the present invention. (1)...The mill body, (2)...Cyclone agent Yoshihiro Morimoto...The mill body? ...γ(70n

Claims (1)

【特許請求の範囲】[Claims] 1、粗炭と乾燥・気送用空気とが供給されかつ前記粗炭
を粉砕して微粉炭とするミル本体と、前記乾燥・気送用
空気に混入して前記ミル本体の外部へ搬送された前記微
粉炭を回収するサイクロンとを備えた石炭乾燥・粉砕装
置。
1. A mill body to which coarse coal and air for drying and pneumatics are supplied and which pulverizes the coarse coal into pulverized coal; A cyclone for recovering the pulverized coal.
JP22092484A 1984-10-19 1984-10-19 Device for drying and grinding coal Pending JPS6197052A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22092484A JPS6197052A (en) 1984-10-19 1984-10-19 Device for drying and grinding coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22092484A JPS6197052A (en) 1984-10-19 1984-10-19 Device for drying and grinding coal

Publications (1)

Publication Number Publication Date
JPS6197052A true JPS6197052A (en) 1986-05-15

Family

ID=16758681

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22092484A Pending JPS6197052A (en) 1984-10-19 1984-10-19 Device for drying and grinding coal

Country Status (1)

Country Link
JP (1) JPS6197052A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5932957A (en) * 1982-08-19 1984-02-22 株式会社トクヤマ Crushing method
JPS5942048A (en) * 1982-09-01 1984-03-08 川崎重工業株式会社 Crusher

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5932957A (en) * 1982-08-19 1984-02-22 株式会社トクヤマ Crushing method
JPS5942048A (en) * 1982-09-01 1984-03-08 川崎重工業株式会社 Crusher

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