JPS6066011A - Feeder for pulverized coal - Google Patents

Feeder for pulverized coal

Info

Publication number
JPS6066011A
JPS6066011A JP17408683A JP17408683A JPS6066011A JP S6066011 A JPS6066011 A JP S6066011A JP 17408683 A JP17408683 A JP 17408683A JP 17408683 A JP17408683 A JP 17408683A JP S6066011 A JPS6066011 A JP S6066011A
Authority
JP
Japan
Prior art keywords
air
hot air
pulverized coal
pulverized
coal
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
JP17408683A
Other languages
Japanese (ja)
Inventor
Mitsuru Ikeda
充 池田
Noribumi Ishida
紀文 石田
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.)
Ube Corp
Original Assignee
Ube 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP17408683A priority Critical patent/JPS6066011A/en
Publication of JPS6066011A publication Critical patent/JPS6066011A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To adjust the quantity of air fed to a combustion apparatus, and to improve combustion efficiency by mounting a vent port discharging one part of hot air into atmospheric air in a piping connecting a pulverized coal-hot air mixture discharge port for a pulverizer and the combustion apparatus. CONSTITUTION:A valve, an opening thereof can be adjusted freely, is fitted between a fan 17 in a piping 15 and an ejector 10, a vent port 19 for discharging one part of hot air into atmospheric air, and the quantity of air toward a combustion apparatus 18 through the ejector 10 is adjusted by opening and closing the valve. When the quantity of air at a comparatively low temperature fed to the combustion apparatus 18 is too much and the ratio A/C of the air to pulverized coal is too large, A/C can be reduced when the valve for the vent port 19 is opened and one part of hot air is made to escape into atmospheric air.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は粉砕機で粉砕した微粉炭を粉砕時の乾燥用熱風
とともに空気圧で燃焼装置へ供給する粉砕微粉炭供給装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a pulverized pulverized coal supply device that supplies pulverized coal pulverized by a pulverizer to a combustion device using air pressure together with hot air for drying during pulverization.

〔従来技術〕[Prior art]

石炭やセメント、化学品などの粒体を細かく粉砕し微粉
化する粉砕機の熱風供給口部には、粉砕機内に熱風を送
入しかつその熱風によシ粉砕機で粉砕された微粉体を乾
燥して機外へ排出する熱風装置が付設されることが多い
。そして、この種の粉砕機を石炭の粉砕に用いる場合に
は、熱風装置の作用で排出された微粉炭を微粉炭ホッパ
にいったん貯留することをせず、この粉砕機に供給装置
を介して燃焼装置を直結し、微粉炭と熱風との混合体を
空気圧で燃焼装置へ供給することがしばしば行なわれる
The hot air supply port of the pulverizer, which finely grinds and pulverizes granules such as coal, cement, and chemicals, is equipped with hot air that is fed into the pulverizer, and the fine powder that has been pulverized by the pulverizer is passed through the hot air. A hot air device is often attached to dry and discharge the air outside the machine. When this type of pulverizer is used for pulverizing coal, the pulverized coal discharged by the action of the hot air device is not stored in the pulverized coal hopper, but is instead sent to the pulverizer through the supply device for combustion. It is often the case that the apparatus is directly connected and a mixture of pulverized coal and hot air is supplied pneumatically to the combustion apparatus.

ところが従来の供給装置においては、粉砕機と燃焼装置
とが、ファンとサイクロン等を備えた配管で直結されて
お少例えば80℃のように低温の粉砕機からのエアは、
微粉炭を運ぶのに充分なだけ多量に用いられているが、
その全量が微粉炭ととも処燃焼装置へ送シ込まれるので
、低温のエア量の過多によシ燃焼効率が大幅に低下する
という不具合があった。特許ハードグローブ指数で表示
される粉砕性の悪い石炭を粉砕する場合には、エア量と
粉炭量との比率A/Cが大きくなる上に、粉砕性が悪い
とこれを見込んで大型の粉砕機が採用されることになり
、エア量を極度に低下させることができなくなってこの
ためにA/Cの値がさらに大きくなシ燃焼効率をますま
す低下させていた。
However, in conventional supply devices, the crusher and combustion device are directly connected by piping equipped with a fan and cyclone, etc., and the air from the crusher at a low temperature of, for example, 80°C, is
Although it is used in large enough quantities to transport pulverized coal,
Since the entire amount of the pulverized coal is sent to the treatment combustion equipment, there is a problem in that the combustion efficiency is significantly reduced due to an excessive amount of low-temperature air. When crushing coal with poor crushability as indicated by the patented hard glove index, the ratio A/C between the amount of air and the amount of pulverized coal increases, and if the crushability is poor, a large crusher is required. was adopted, making it impossible to reduce the amount of air to an extreme extent, and as a result, the A/C value was further reduced, further reducing the combustion efficiency.

〔発明の概要〕[Summary of the invention]

本発明は以上のような点に鑑みなされたもので。 The present invention was made in view of the above points.

粉砕機の微粉炭・熱風混合体排出口と燃焼装置とを接続
する配管内に、熱風の一部を大気中へ放出するベントロ
を設けるととKよシ、燃焼装置へ送給されるエア量を調
節することを可能にして燃焼効率の向上を計った粉砕微
粉炭供給装置を提供するものである。以下1本発明の実
施例を図面に基づいて詳細に説明する。
If a vent is installed in the piping that connects the pulverized coal/hot air mixture outlet of the crusher and the combustion device to release a portion of the hot air into the atmosphere, the amount of air sent to the combustion device can be reduced. The purpose of the present invention is to provide a pulverized pulverized coal supply device that improves combustion efficiency by making it possible to adjust the combustion efficiency. EMBODIMENT OF THE INVENTION Below, one embodiment of the present invention will be described in detail based on the drawings.

〔実施例〕〔Example〕

図は本発明に係る粉砕微粉炭供給装置の実施例を示す概
要構成図であって、粉砕機1には、原料としての粒状炭
を投入するバンカ2と、そのシャッタ3を開くこと如よ
シ落下する粒状炭を搬送して粉砕機1のシュート入口へ
供給するコンベア式の給炭機4とが付設されている。粉
砕機1は水平状の回転テーブルの中心部へシュートから
供給された粒状炭を回転テーブルとその外周部上面に圧
接されて従動回転するローラとの間で粉砕するものであ
って、粉砕された微粒炭は回転テーブルの下方からその
周囲を通って吹き上げる熱風によつ昇するように構成さ
れている。5は熱風発生装置であシ、6は粉砕機1と図
示しない熱風発生装置との間を連結するエアダクトであ
る。
The figure is a schematic configuration diagram showing an embodiment of the pulverized pulverized coal supply device according to the present invention. A conveyor-type coal feeder 4 that conveys falling granular coal and supplies it to the chute entrance of the crusher 1 is attached. The pulverizer 1 pulverizes granulated coal supplied from a chute to the center of a horizontal rotary table between the rotary table and a roller that is pressed against the upper surface of its outer periphery and rotates drivenly. The granulated coal is configured to be lifted up by hot air blown from below the rotary table through its surroundings. 5 is a hot air generator, and 6 is an air duct connecting the crusher 1 and the hot air generator (not shown).

以上のように構成された粉砕機1の微粉炭・熱風混合体
排出ロアには、ダクト8が接続されており、その他端は
、バッグフィルタを備え混合体を微粉炭と熱風とに分離
する微粉炭捕集装置9に接続されている。符号10で示
すものはエゼクタであってこれと微粉炭捕集装置9の微
粉炭排出口11との間は配管12によって接続されてお
シ、この配管12内には、エアの通過を阻止するエアロ
ツク機構13が設けられている。また、微粉炭捕集装置
9の熱風排出口14とエゼクタ10との間は配管15に
よって接続されてお公、この配管15内には、管路を開
閉するパルプ16と、熱風をエゼクタ10へ向って送給
するファン17とが設けられている。さらにエゼクタ1
0はキルンやボイラ等の燃焼装置18のバーナ18aと
接続されてお夛、配管12内を送られて来た微粉炭が配
管15からの熱風圧でバーナへ供給されて燃焼するよし
に構成されている。そして配管15のファン17とエゼ
クタ10との間には、開度調節自在なパルプを備え熱風
の一部を大気中へ放出するためのベントロ19が設けら
れておシ、パルプを開閉することKよシエゼクタ10を
経て燃焼装置18へ向うエア量が調節されるように構成
されている。なお、燃焼装置18へは例えば300〜4
00 ”Oの高温の二次空気を送入し燃焼効率を高める
ようになっている。
A duct 8 is connected to the pulverized coal/hot air mixture discharge lower of the pulverizer 1 configured as described above, and the other end is equipped with a bag filter to separate the pulverized coal and hot air mixture into pulverized coal and hot air. It is connected to the charcoal collection device 9. Reference numeral 10 denotes an ejector, and this ejector is connected to the pulverized coal discharge port 11 of the pulverized coal collection device 9 by a pipe 12, and there is a pipe 12 that prevents air from passing through. An aerodynamic mechanism 13 is provided. Further, the hot air outlet 14 of the pulverized coal collection device 9 and the ejector 10 are connected by a pipe 15. Inside the pipe 15, there is a pulp 16 for opening and closing the pipe, and a pulp 16 for directing the hot air to the ejector 10. A fan 17 is provided to feed the air. Furthermore, ejector 1
0 is connected to a burner 18a of a combustion device 18 such as a kiln or boiler, and the pulverized coal sent through the pipe 12 is supplied to the burner by hot air pressure from the pipe 15 and is combusted. ing. Between the fan 17 of the pipe 15 and the ejector 10, there is provided a vent 19 which is equipped with pulp whose opening degree can be adjusted freely and which discharges a portion of the hot air into the atmosphere. The amount of air flowing to the combustion device 18 via the evacuator 10 is adjusted. In addition, for example, 300 to 4
00" high temperature secondary air is introduced to increase combustion efficiency.

以上のように構成された粉砕機とこれで粉砕された微粒
炭の供給装置との動作を説明する。バンカ2へ粒状炭を
供給してシャッタ3を開くと、粒状炭は落下して給炭機
4で搬送され、粉砕機1のシュートへ供給される。供給
された粒状炭はシュート内を回転テーブルの中心部に落
下し、回転テーブルとその外周部に圧接されなから従動
回転するローラとの間へ噛込まれて粉砕される。回転テ
ーブル1の下方へはエアダクト6を経て熱風が供鉛七引
−イ私h との教服値五回餅テーブル1の円鏝とケーシ
ングとの間の環状空間部から吹き上がるので、粉砕され
た微粉炭は熱風によりて乾燥されながら熱風との混合体
となって排出ロアから排出される。この混合体がダクト
8を通りて微粉炭捕集装置9へ送給されると、微粉炭と
熱風とに分離され、微粉炭は排出口11から排出されて
配管12内をエアロツク機構を介しエゼクタ10へ向う
The operation of the pulverizer configured as above and the supply device for pulverized coal pulverized by the pulverizer will be explained. When granular coal is supplied to the bunker 2 and the shutter 3 is opened, the granular coal falls, is conveyed by the coal feeder 4, and is supplied to the chute of the crusher 1. The supplied granular charcoal falls through the chute to the center of the rotary table, is not pressed against the rotary table and its outer periphery, and is then caught between the rotary table and a driven rotating roller to be pulverized. Hot air blows downward from the rotary table 1 through the air duct 6 and from the annular space between the circular trowel of the table 1 and the casing, causing the lead to be crushed. The pulverized coal is dried by the hot air and is mixed with the hot air and discharged from the discharge lower. When this mixture is sent to the pulverized coal collection device 9 through the duct 8, it is separated into pulverized coal and hot air, and the pulverized coal is discharged from the discharge port 11 and passed through the pipe 12 through the air mechanism to the ejector. Head to 10.

また排出口14から排出された熱風は、パルプ16を開
くことによシフアン1Tでエゼクタ10へ送給される。
Further, the hot air discharged from the discharge port 14 is sent to the ejector 10 by the air blower 1T by opening the pulp 16.

このときの熱風は例えば80°Cのように比較的低温で
あシこのようにしてエゼクタ10へは微粉炭と圧力を有
する熱風とが送給されるので、微粉炭は熱風の風圧によ
ってこれとともに燃焼装置17のバーナ18aに供給さ
れて燃焼する。
The hot air at this time is relatively low temperature, for example, 80°C.The pulverized coal and the hot air under pressure are thus fed to the ejector 10, so the pulverized coal is transported along with the hot air by the pressure of the hot air. It is supplied to the burner 18a of the combustion device 17 and burned.

但しこのときの熱風は例えば80゛Cのように比較的に
低温であ夛、この熱風が多過ぎると、燃焼装置1Bでの
燃焼効率が低下する。
However, the hot air at this time is relatively low temperature, for example, 80°C, and if there is too much of this hot air, the combustion efficiency in the combustion device 1B will decrease.

燃焼装置18へ送給される比較的低温のエア量が多過ぎ
てこれと微粉炭との比率A/Cが大き過ぎる場合には、
ベントロ19のパルプを開いて熱風の一部を大気中へ逃
がしてやれば、A/Cを小さくすることができる。この
場合、粉砕機1から排出する微粉炭の量に応じて熱風の
量も異なシ、シたがうてそれに応じてA/Cも異なるが
、A/Cは通常、重量比で1.5〜4とする。そして1
例えば粉砕機1からの排出風量の70%をベントロ19
から逃がして残シを燃焼装置18のバーナ18mへ送シ
、燃焼装置18へ供給してりる300〜400’Cの二
次空気とともに燃焼装置18で微粉炭を効率よく燃焼さ
せる。
If the amount of relatively low temperature air fed to the combustion device 18 is too large and the ratio A/C of this and pulverized coal is too large,
The A/C can be reduced by opening the pulp of the vent 19 and allowing some of the hot air to escape into the atmosphere. In this case, the amount of hot air varies depending on the amount of pulverized coal discharged from the crusher 1, and the A/C also differs depending on the case, but the A/C is usually 1.5 by weight. ~4. and 1
For example, 70% of the exhaust air volume from the crusher 1 is transferred to the ventilator 19.
The remaining residue is sent to the burner 18m of the combustion device 18, and the pulverized coal is efficiently burned in the combustion device 18 together with the secondary air of 300 to 400'C supplied to the combustion device 18.

なお、本実施例においては、微粉炭捕集装置9にバッグ
フィルタを設けたことによシ、微粉炭がファン17へ向
うことがなくその摩耗を防止することができ、摩耗対策
の不要な高効率のファン1Tを設置することができるの
で、単位当シミ気消費量を節減することができる。
In this embodiment, since the pulverized coal collection device 9 is provided with a bag filter, the pulverized coal does not flow toward the fan 17, thereby preventing the pulverized coal from being worn out. Since a high-efficiency fan 1T can be installed, the amount of air consumed per unit can be reduced.

〔発明の効果〕〔Effect of the invention〕

以上の説明によシ明らかなように、本発明によれば粉砕
微粉炭供給装置において、粉砕機の微粉炭・熱風混合体
排出口と、燃焼装置とを接続する配管内に、熱風の一部
を大気中へ放出するベントロを設けることによシ、正常
な石炭はもとよシ粉砕性の悪い石炭を粉砕して熱風で燃
焼装置へ送る場合でも熱風の送給量を自由に調節して粉
炭量に対するエア量を適量にすることができるので、こ
れが過多となることがなく燃焼効率が著しく向上する。
As is clear from the above description, in the pulverized pulverized coal supply device according to the present invention, a portion of the hot air is provided in the pipe connecting the pulverized coal/hot air mixture discharge port of the pulverizer and the combustion device. By installing a ventilator that discharges into the atmosphere, the amount of hot air supplied can be freely adjusted, even when pulverizing not only normal coal but also coal that has poor pulverization properties and sending it to the combustion equipment with hot air. Since the amount of air can be set to an appropriate amount relative to the amount of pulverized coal, the amount of air will not become excessive and the combustion efficiency will be significantly improved.

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

図は本発明に係る粉砕微粉炭供給装置の実施例を示す概
要構成図である。 1・・・・粉砕機、6・・・・エアダクト、7・・・・
微粉炭・熱風混合体排出口、8・・・・ダクト、9・・
・・微粉炭捕集装置、10・・・・エゼクタ、11・・
・・微粉炭排出口、12゜15・・・・配管、14・・
・・熱風排出口。 1T・・・・ファン、18・・・・燃焼装置、19・−
・・ベントロ。 特許出願人 宇部興産株式会社 代理人山川政樹(綺九1次)
The figure is a schematic configuration diagram showing an embodiment of the pulverized pulverized coal supply device according to the present invention. 1...Crusher, 6...Air duct, 7...
Pulverized coal/hot air mixture outlet, 8...Duct, 9...
...Pulverized coal collection device, 10...Ejector, 11...
...Pulverized coal discharge port, 12゜15...Piping, 14...
・Hot air outlet. 1T...Fan, 18...Combustion device, 19...-
... Ventro. Patent applicant: Ube Industries Co., Ltd. Agent Masaki Yamakawa (Kiku 1st)

Claims (1)

【特許請求の範囲】[Claims] 粉砕機の微粉炭・熱風混合体排出口と燃焼装置とを接続
する混合体分離供給用通路内に前記熱風の一部を大気中
へ放出するベントロを設けたことを特徴とする粉砕微粉
炭供給装置。
A pulverized pulverized coal supply characterized in that a vent for discharging a part of the hot air into the atmosphere is provided in a mixture separation and supply passage connecting a pulverized coal/hot air mixture discharge port of a pulverizer and a combustion device. Device.
JP17408683A 1983-09-22 1983-09-22 Feeder for pulverized coal Pending JPS6066011A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17408683A JPS6066011A (en) 1983-09-22 1983-09-22 Feeder for pulverized coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17408683A JPS6066011A (en) 1983-09-22 1983-09-22 Feeder for pulverized coal

Publications (1)

Publication Number Publication Date
JPS6066011A true JPS6066011A (en) 1985-04-16

Family

ID=15972403

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17408683A Pending JPS6066011A (en) 1983-09-22 1983-09-22 Feeder for pulverized coal

Country Status (1)

Country Link
JP (1) JPS6066011A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0225609A (en) * 1988-07-14 1990-01-29 Babcock Hitachi Kk Pulverized coal burner and pulverized coal combustion device with the same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5749728A (en) * 1980-09-08 1982-03-23 Onoda Cement Co Ltd Pulverized coal combustion device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5749728A (en) * 1980-09-08 1982-03-23 Onoda Cement Co Ltd Pulverized coal combustion device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0225609A (en) * 1988-07-14 1990-01-29 Babcock Hitachi Kk Pulverized coal burner and pulverized coal combustion device with the same

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