JP2001246276A - Installation for pulverizing coal - Google Patents
Installation for pulverizing coalInfo
- Publication number
- JP2001246276A JP2001246276A JP2000062162A JP2000062162A JP2001246276A JP 2001246276 A JP2001246276 A JP 2001246276A JP 2000062162 A JP2000062162 A JP 2000062162A JP 2000062162 A JP2000062162 A JP 2000062162A JP 2001246276 A JP2001246276 A JP 2001246276A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- hot air
- pulverizing
- air duct
- duct
- 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
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- Crushing And Grinding (AREA)
- Disintegrating Or Milling (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は石炭粉砕機に係り、
緊急停止後粉砕機内の残炭を系内に残すことなく安全に
排出するのに好適な石炭粉砕設備に関する。TECHNICAL FIELD The present invention relates to a coal crusher,
The present invention relates to a coal crushing facility suitable for safely discharging remaining coal in a crusher after an emergency stop without leaving it in the system.
【0002】[0002]
【従来の技術】石炭直接燃焼システムにおいて、石炭微
粉砕設備は、石炭を粉砕する微粉炭機(以下、ミルと称
する)、粉砕された石炭を乾燥及び搬送するための熱空
気を導入する熱空気ダクト、微粉炭機に石炭(原炭)を
供給する給炭機、粉砕され乾燥された微粉炭をバーナに
供給する輸送管、から成る。2. Description of the Related Art In a direct coal combustion system, a coal pulverizing facility includes a pulverized coal mill (hereinafter referred to as a mill) for pulverizing coal, and hot air for introducing hot air for drying and conveying the pulverized coal. It consists of a duct, a coal feeder for supplying coal (raw coal) to the pulverized coal machine, and a transport pipe for supplying pulverized and dried pulverized coal to the burner.
【0003】図5は前記微粉炭機が用いられた石炭焚き
ボイラの典型的なフローを示す。図示するように、石炭
焚きボイラでは、燃焼用空気Aは押込み通風機1を通過
後に一次空気Bと二次空気Cとに分けられる。さらに、
一次空気Bは、一次空気押込通風機4を通過後に、直
接、微粉炭機5へ送られる冷空気と、空気予熱器3を通
って過熱される熱空気とに分けられる。そして、冷空気
と熱空気は微粉炭機の手前で混合され、微粉炭機5の入
口温度が所定の温度になるようにコントロールされてい
る。また、二次空気Cは、蒸気式空気予熱器2および空
気予熱器3を通って過熱されたのち、ボイラ8へ送られ
る。FIG. 5 shows a typical flow of a coal-fired boiler using the pulverized coal machine. As shown in the figure, in the coal-fired boiler, the combustion air A is divided into primary air B and secondary air C after passing through the forced draft fan 1. further,
The primary air B is divided into cold air which is directly sent to the pulverized coal machine 5 after passing through the primary air pusher 4 and hot air which is superheated through the air preheater 3. Then, the cold air and the hot air are mixed before the pulverized coal machine, and the inlet temperature of the pulverized coal machine 5 is controlled to be a predetermined temperature. The secondary air C is sent to the boiler 8 after being superheated through the steam-type air preheater 2 and the air preheater 3.
【0004】一方、石炭Dは石炭バンカ6より給炭機7
を介して微粉炭機5内に供給され、微粉炭機5によって
粉砕される。粉砕された石炭は一次空気Bによりボイラ
8のバーナ26へ搬送され、ボイラ8内で二次空気Cに
よって燃焼する。On the other hand, coal D is supplied from coal bunker 6 to coal feeder 7
And is supplied into the pulverized coal machine 5 through the pulverized coal machine 5 to be pulverized. The pulverized coal is transported to the burner 26 of the boiler 8 by the primary air B, and is burned in the boiler 8 by the secondary air C.
【0005】図5において、9は集塵機、10は脱硝装
置、11は誘引通風機、12は脱硫装置、13は煙突で
ある。In FIG. 5, reference numeral 9 denotes a dust collector, 10 denotes a denitration device, 11 denotes an induction ventilator, 12 denotes a desulfurization device, and 13 denotes a chimney.
【0006】また、微粉炭機5は図6に示すように構成
されている。図示するように、微粉炭機5へは給炭管1
4を介して平均直径2〜70mm程度の石炭Dが供給さ
れ、粉砕テーブル16上へ落下する。粉砕テーブル16
は減速機32を介して電動機17に連結されており、2
0〜40rpmで回転している。また、粉砕テーブル1
6に取付けられた粉砕輪19上にある粉砕ローラ18に
は、外部の加圧装置20より粉砕荷重が加えられてお
り、この粉砕ローラ18は粉砕輪19の回転に伴って回
転する。そして、粉砕テーブル16に落下した石炭Dは
遠心力により粉砕輪19と回転中の粉砕ローラ18の間
へ搬送され、この間を通過するときに粉砕されてスロー
ト21上部へ送られる。[0006] The pulverized coal machine 5 is configured as shown in FIG. As shown in FIG.
4, coal D having an average diameter of about 2 to 70 mm is supplied and falls onto the crushing table 16. Grinding table 16
Is connected to the electric motor 17 through the speed reducer 32,
It is rotating at 0 to 40 rpm. Also, grinding table 1
A crushing load is applied to a crushing roller 18 on a crushing wheel 19 attached to 6 by an external pressing device 20. The crushing roller 18 rotates with the rotation of the crushing wheel 19. Then, the coal D that has dropped on the crushing table 16 is transported by a centrifugal force between the crushing wheel 19 and the rotating crushing roller 18, crushed when passing through the space, and sent to the upper part of the throat 21.
【0007】一方、150〜300℃前後に過熱された
一次空気Bは、熱空気ダクト29、チャンバ22を通り
均一にスロート21へ供給され、スロート上部で粉砕さ
れた石炭を乾燥しながら搬送する。粉砕された石炭のう
ち比較的細かい粒子は、この一次空気Bにより搬送され
て、ベーン23を経て分級機24へ送られる。また、粗
い粒子は空気流速の低下に伴い気流から分離され、再び
粉砕テーブル16へ戻される(これを一次分級とい
う)。分級機24内では旋回流により石炭粒子に遠心力
が働き、比較的粗い粒子は分級機24内を落下しホッパ
25より、再び粉砕テーブル16へ戻される(これを二
次分級という)。そして、微粒子のみ送炭管15を通っ
てバーナ26へ供給される。On the other hand, the primary air B superheated to about 150 to 300 ° C. is uniformly supplied to the throat 21 through the hot air duct 29 and the chamber 22, and conveys the pulverized coal at the upper part of the throat while drying. Relatively fine particles of the pulverized coal are conveyed by the primary air B and sent to the classifier 24 via the vane 23. Further, the coarse particles are separated from the airflow as the air flow velocity decreases, and returned to the pulverizing table 16 again (this is referred to as primary classification). In the classifier 24, centrifugal force acts on the coal particles due to the swirling flow, and relatively coarse particles fall down in the classifier 24 and are returned to the crushing table 16 from the hopper 25 again (this is referred to as secondary classification). Then, only the fine particles are supplied to the burner 26 through the coal feeding pipe 15.
【0008】また、石炭中の異物(石、鉄片等)はスロ
ート21を通過する熱せられた一次空気Bに対して落下
し、パイライトプロー(スクレイパーとも称される)2
7によりパイライトボックス28に蓄えられ一定時間毎
に外部へ排出される。即ち、異物は、回転するパイライ
トプローによって掻き集められてパイライトボックスに
収容される。Further, foreign matters (stones, iron pieces, etc.) in the coal fall on the heated primary air B passing through the throat 21, and the pyrite probe (also called a scraper) 2
7 and is discharged to the outside at regular intervals. That is, the foreign matter is raked up by the rotating pyrite probe and stored in the pyrite box.
【0009】一方、微粉炭機5が緊急停止(以下、トリ
ップと称する)すると、微粉炭機5内を循環する石炭が
粉砕テーブル16と粉砕輪19に堆積し、一部はスロー
ト21を通過し、チャンバ22に堆積する。堆積した残
炭Fは放置すると自然発火し、時には火災の発生につな
がる場合があり、また、ある時にはおき燃焼(発熱状
態)を起こし、次の起動時に熱空気を供給したときにま
き上げられ、炭じん爆発を起こす恐れがあるため、トリ
ップ後、微粉炭機5内を不活性(イナート)とし、電動
機17のみを単独でまわして、粉砕テーブ16、粉砕輪
19上の残炭は遠心力によりスロート21よりチャンバ
22内に落下させ、パイライトプロー27にてパイライ
トボックス28に集めて系外へ排出する(スワールと称
する)。ここで、スワールとは、トリップ時にミルに石
炭と空気を供給しない状態で、ミル内の残炭を排出する
ためミルを回転稼働させることを云う。On the other hand, when the pulverized coal machine 5 is stopped in an emergency (hereinafter referred to as a trip), the coal circulating in the pulverized coal machine 5 accumulates on the pulverizing table 16 and the pulverizing wheel 19, and a part passes through the throat 21. , Deposited in the chamber 22. The deposited residual coal F ignites spontaneously if left unattended, and may sometimes lead to the occurrence of a fire. In addition, at some point, the remaining coal will burn (heat generation state), and will be picked up when hot air is supplied at the next startup, After the trip, after the trip, the inside of the pulverized coal machine 5 is made inert (inert), and only the electric motor 17 is turned alone to remove the residual coal on the grinding table 16 and the grinding wheel 19 by centrifugal force. It is dropped into the chamber 22 from the throat 21 and collected in a pyrite box 28 by a pyrite probe 27 and discharged out of the system (referred to as a swirl). Here, the swirl means that the mill is rotated to discharge residual coal in the mill without supplying coal and air to the mill during a trip.
【0010】しかし、パイライトプロー27は周速数m
/秒で回転するため、チャンバ22内に落下してくる石
炭及び堆積石炭は遠心力により、熱空気ダクト29側へ
押し出されるか、又ははね飛ばされ堆積する(G)こと
がある。これを放置しておくと、上述したと同様に自燃
発火が原因で重大な事故につながる可能性をもってい
る。However, the pyrite probe 27 has a peripheral speed of several meters.
Because of the rotation at the speed of / sec, the coal and the deposited coal falling into the chamber 22 may be pushed out toward the hot air duct 29 side by the centrifugal force or may be splashed and deposited (G). If left unchecked, there is a possibility that serious accidents may occur due to self-combustion, as described above.
【0011】また、スワール時にはチャンバ22内の冷
却及び洗浄も兼ねて注水することがあり、残炭(F)と
水の混合物がパイライトプロー27により押し出されて
熱空気ダクト29に沿って昇り、水平部まで達すること
がある。During swirling, water is sometimes injected to cool and clean the inside of the chamber 22, and a mixture of residual coal (F) and water is pushed out by the pyrite probe 27 and rises along the hot air duct 29 to be horizontal. Department.
【0012】[0012]
【発明が解決しようとする課題】上記従来技術は、ミル
スワール時に回転するミルパイライトプロー27にて熱
空気ダクト側に遠心力にて飛散させられた残炭(G)、
または粉砕輪からスロートを介して落下する石炭がパイ
ライトプローによって打出されて熱空気ダクト29側に
飛散して、熱空気ダクト29側の特に水平部に堆積する
ことがある。この堆積石炭は次のミル運転までに熱空気
ダクト29の予熱の助けも加わり自燃発火し、おき燃焼
状態となり、次のミル起動時に新鮮な熱空気が供給され
たとき飛散し、最悪の場合粉じん爆発を起こす危険性が
ある。The above-mentioned prior art is based on residual coal (G) which is scattered by centrifugal force to the hot air duct side by a mill pyrite probe 27 rotating at the time of mill swirl,
Alternatively, the coal falling from the grinding wheel through the throat may be driven out by the pyrite probe and scattered to the hot air duct 29 side, and may be deposited on the hot air duct 29 side, particularly in a horizontal portion. The deposited coal ignites itself with the help of the preheating of the hot air duct 29 before the next mill operation, and becomes a burning state. It scatters when fresh hot air is supplied at the next start of the mill, and in the worst case, dust. Risk of explosion.
【0013】また、スワール後、いちいち残炭の有無を
確認し取除くことは、次のミル運転スケジュールに影響
を及ぼし、ボイラ負荷制限にもなりうる。[0013] In addition, after the swirl, confirming the presence or absence of residual coal one by one affects the next mill operation schedule, and can also limit the boiler load.
【0014】石炭の熱空気ダクト側への石炭飛散防止策
として、図4に示すように、じゃま板30を設ける方法
もあるが局部的には効果があるものの、すべての飛散炭
Gを取除くには至らない。また、ダクト29に沿って上
昇するものに対しては効果がない。また、熱空気ダクト
に石炭が飛散しても石炭が堆積しないような角度及び高
さを取ることも考えられるが配置上、大きなスペースが
必要となり、必ずしも根本的解決にはならない。As a countermeasure for preventing coal from being scattered to the hot air duct side, there is a method of providing a baffle plate 30 as shown in FIG. 4, but it is effective locally but removes all scattered coal G. Does not reach. In addition, there is no effect on an object rising along the duct 29. In addition, it is conceivable to take an angle and a height such that coal does not accumulate even if the coal is scattered in the hot air duct, but a large space is required in arrangement, and this is not necessarily a fundamental solution.
【0015】本発明の目的は、スワール時にミル側と熱
空気ダクト側への石炭堆積・飛散を完全に防止すること
にある。An object of the present invention is to completely prevent coal deposition and scattering on the mill side and hot air duct side during swirl.
【0016】[0016]
【課題を解決するための手段】前記課題を解決するため
に、本発明は次のような構成を採用する。In order to solve the above problems, the present invention employs the following configuration.
【0017】駆動源で回転させられる粉砕輪と前記粉砕
輪の回転に伴い回転する粉砕ローラにより石炭を粉砕す
る微粉炭機と、前記微粉炭機で粉砕された石炭を乾燥及
び空気搬送するための熱空気を導入する熱空気ダクト
と、を備えた石炭微粉砕設備であって、通常運転時には
前記熱空気ダクトから前記微粉炭機へ熱空気を支障無く
供給するとともに、石炭微粉砕設備の停止時に前記微粉
炭機から飛散する石炭を前記熱空気ダクト側に浸入させ
ないように前記熱空気ダクトの通路を略閉鎖するダンパ
を前記熱空気ダクトに設け、前記ダンパの近傍に飛散石
炭を洗浄する注水装置を設けた石炭微粉砕設備。A pulverizer for pulverizing coal by a pulverizing wheel rotated by a driving source and a pulverizing roller rotating with rotation of the pulverizing wheel; and a pulverizer for drying and pneumatically conveying the pulverized coal by the pulverizer. A hot air duct for introducing hot air, and a coal pulverizing facility comprising, during normal operation, hot air is supplied from the hot air duct to the pulverized coal machine without hindrance, and when the coal pulverizing facility is stopped. A damper for closing the passage of the hot air duct in the hot air duct so as to prevent coal scattered from the pulverized coal machine from entering the hot air duct side, and a water injection device for washing the scattered coal near the damper. Coal pulverization equipment equipped with.
【0018】また、前記石炭微粉砕設備において、前記
熱空気ダクトは、水平部ダクトと傾斜部ダクトと経て前
記微粉炭機に連結され、前記ダンパは、前記水平部ダク
トと傾斜部ダクトの境界近傍に設置する石炭微粉砕設
備。Further, in the coal pulverizing facility, the hot air duct is connected to the pulverizer through a horizontal duct and an inclined duct, and the damper is located near a boundary between the horizontal duct and the inclined duct. Coal crushing equipment to be installed in
【0019】[0019]
【発明の実施の形態】本発明の実施形態に係る石炭微粉
砕設備について、図1及び図2を用いて以下説明する。
図1は本発明の実施形態に係る石炭微粉砕設備の隔離ダ
ンパの構成と注水構成を示す。図1において、ダンパ5
0は熱空気ダクト29内に設置されており、通常の微粉
炭機5運転中は熱空気Bの流れを阻害しないように回動
されており、スワール時に外部にあるアクチュエータ5
1によりダンパ50は回動され、熱空気ダクト29は微
粉炭機5側と隔離する。また、ダンパ廻りに洗浄水の注
水部52を設けて、熱空気側に飛散した石炭を洗浄する
ようにする。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A coal pulverizing facility according to an embodiment of the present invention will be described below with reference to FIGS.
FIG. 1 shows a configuration of an isolation damper and a water injection configuration of a coal pulverization facility according to an embodiment of the present invention. In FIG.
Numeral 0 is installed in the hot air duct 29 and is rotated so as not to hinder the flow of the hot air B during the operation of the normal pulverized coal machine 5.
1, the damper 50 is rotated, and the hot air duct 29 is isolated from the pulverized coal machine 5 side. Further, a washing water injection section 52 is provided around the damper to wash the coal scattered to the hot air side.
【0020】ダンパ50は、通常運転中は熱空気ダクト
29に平行に設置してあり(開)、スワール開始時にア
クチュエータ51によって閉状態にされる。スワール開
始により微粉炭機5側より飛散してくる石炭はダンパ5
0と衝突し、熱空気ダクト29の斜面に落下する。熱空
気ダクト29とダンパ51下部の間にはすき間Hが設け
られており、ダクト上流側には注水部52があり、ダク
ト斜面上の石炭は、その傾斜面形状と注水によりチャン
バ22内に押しもどされ、パイライトプロー27によ
り、パイライトボックス28内に排出することができ
る。The damper 50 is installed parallel to the hot air duct 29 during normal operation (open), and is closed by the actuator 51 at the start of swirl. Coal scattered from the pulverized coal machine 5 due to the start of the swirl
It collides with 0 and falls on the slope of the hot air duct 29. A gap H is provided between the hot air duct 29 and the lower part of the damper 51, and a water injection part 52 is provided on the upstream side of the duct. Coal on the slope of the duct is pushed into the chamber 22 by the shape of the slope and water injection. It is returned and can be discharged into the pyrite box 28 by the pyrite probe 27.
【0021】本実施形態のダンパ50の構成と配置によ
り、飛散した石炭はここで落下してこれ以上ダクト上流
側にはいかない。Due to the configuration and arrangement of the damper 50 of the present embodiment, the scattered coal falls here and does not go further upstream of the duct.
【0022】また、ダンパ下部にはすき間Hを設け、ダ
クト上流側から洗浄水を流すのでダクト斜面の石炭を残
すことなくチャンバ側へ流すことができる。Further, a gap H is provided below the damper, and the washing water flows from the upstream side of the duct, so that the coal on the slope of the duct can be flown to the chamber side without leaving.
【0023】次に、本発明の他の実施形態に係る石炭微
粉砕設備の隔離ダンパと注水構成を図2に示す。本実施
形態のダンパは昇降形式のギロチンダンパ53であり、
ダンパ53側に洗浄水をかけるようにしたものである。
通常運転中はダンパ53は最上昇しており熱空気の通過
に支障のない構造であり、スワール時にはダンパは下降
して微粉炭機からの飛散石炭がダンパと衝突してダクト
の水平部に浸入しないようにしている。Next, FIG. 2 shows an isolation damper and a water injection structure of a coal pulverizing facility according to another embodiment of the present invention. The damper of the present embodiment is a guillotine damper 53 of a lifting type,
The cleaning water is applied to the damper 53 side.
During normal operation, the damper 53 is at its highest position and has a structure that does not hinder the passage of hot air.During swirl, the damper descends and scattered coal from the pulverized coal machine collides with the damper and enters the horizontal part of the duct. I try not to.
【0024】洗浄水52はダクト側にも注水されるの
で、付着性の高い石炭が飛散してきた場合でもダクトへ
の石炭の付着を防止できると共に、ダクトの傾斜面への
注水によって(図2の上図は最下段の注水状態を示す)
傾斜面での残炭もなくなり、自燃発火に対しての危険が
なくなること、及びダンパスライド面とダクト面との間
に水を流すので両面の間に石炭が狭まることによるダン
パの駆動が阻害されることがなくなる。Since the washing water 52 is also injected into the duct side, it is possible to prevent the coal from adhering to the duct even when highly adhesive coal is scattered, and to inject water into the inclined surface of the duct (see FIG. 2). (The upper figure shows the water injection state at the bottom.)
There is also no residual coal on the inclined surface, and there is no danger of self-ignition, and since the water flows between the sliding surface of the damper and the duct surface, the drive of the damper due to the narrowing of coal between both surfaces is impeded. No more.
【0025】以上説明したように、本発明の実施形態に
係る石炭微粉砕設備によれば、次のような構成と機能を
奏するものである。即ち、スワール時にミルと熱空気ダ
クト側とを完全に隔離できるように、通常運転中は、何
の障害もなく熱空気を供給できるように、開閉可能なダ
ンパを熱空気ダクトに設置し、且つダンパで受け止めら
れた石炭を洗浄する注水設備を設置するものである。As described above, according to the coal pulverizing equipment according to the embodiment of the present invention, the following configuration and function are provided. That is, in order to completely isolate the mill and the hot air duct side during swirling, during normal operation, an openable / closable damper is installed in the hot air duct so that hot air can be supplied without any obstacles, and A water injection facility will be installed to wash the coal received by the damper.
【0026】熱空気ダクトに設置されたダンパは、通常
運転時には開状態にあり、熱空気は自由にミル側に流入
する。一方、スワール時にはダンパを閉とする。それに
よってミル側から飛散する石炭はダンパによって受け止
められ、熱空気ダクト下面(斜面)に落下する。落下し
た石炭は、洗浄水によってミル側に流され、パイライト
ボックスより外部に排出させられるので、熱空気ダクト
への石炭の堆積はなくなるので、石炭の自燃発火はなく
ミルを安全に運転することができる。The damper installed in the hot air duct is open during normal operation, and the hot air freely flows into the mill. On the other hand, at the time of swirl, the damper is closed. Thereby, the coal scattered from the mill side is received by the damper and falls to the lower surface (slope) of the hot air duct. The fallen coal is flushed to the mill side by the washing water and discharged to the outside from the pyrite box, so there is no coal accumulation in the hot air duct.Therefore, there is no self-ignition of coal and the mill can be operated safely. it can.
【0027】[0027]
【発明の効果】本発明によれば、スワール時に熱空気ダ
クトへの石炭の飛散堆積を防止できるので、熱空気ダク
トでの石炭の自燃発火、おき燃焼を防止できる。そのこ
とにより、次のミル起動時に熱空気が供給された時の石
炭飛散による炭じん爆発を防止でき、ミルを安全に運用
することができる。According to the present invention, the coal can be prevented from being scattered and deposited on the hot air duct during swirl, so that the self-combustion of the coal and the ignitable combustion of the coal in the hot air duct can be prevented. As a result, it is possible to prevent coal dust explosion due to coal scattering when hot air is supplied at the next start of the mill, and to operate the mill safely.
【0028】また、おき燃焼が起っているところへ点検
等でマンホールを開けたとき新鮮な空気が供給されると
火災に発展することもあり得るが、これを防止すること
ができる。In addition, when fresh air is supplied when a manhole is opened for inspection or the like at a place where flammable combustion occurs, a fire may develop, but this can be prevented.
【0029】更に、熱空気ダクト内に熱空気の流れを乱
すことなく設置するため、圧力損失も最小にかつ、熱空
気ダクトを高くしかつ傾斜角度も小さくでき、配置上コ
ンパクトになり、スペース上節約できる。Further, since the hot air duct is installed in the hot air duct without disturbing the flow, the pressure loss can be minimized, and the hot air duct can be made high and the inclination angle can be made small. Can save.
【図1】本発明の実施形態に係る石炭微粉砕設備の隔離
ダンパの構成と注水構成を示す図である。FIG. 1 is a diagram showing a configuration of a separation damper and a water injection configuration of a coal pulverization facility according to an embodiment of the present invention.
【図2】本発明の他の実施形態に係る石炭微粉砕設備の
隔離ダンパの構成と注水構成を示す図である。FIG. 2 is a diagram illustrating a configuration of a separation damper and a water injection configuration of a coal pulverization facility according to another embodiment of the present invention.
【図3】従来技術に係る熱空気ダンパに設けたじゃま板
の構成と配置を示す図である。FIG. 3 is a diagram showing a configuration and an arrangement of a baffle provided on a hot air damper according to the related art.
【図4】従来技術の石炭焚ボイラの系統を示す図であ
る。FIG. 4 is a diagram showing a system of a conventional coal-fired boiler.
【図5】従来技術の石炭微粉砕設備を示す図である。FIG. 5 is a view showing a conventional coal pulverizing facility.
5 微粉炭機 19 粉砕輪 21 スロート 22 チャンバ 27 パイライトプロー 29 熱空気ダクト 50 ダンパ 51 アクチュエータ 52 注水装置 53 ギロチンダンパ B 熱空気(一次空気) F 残炭 G 堆積炭 H 隙間 I パイライトプロー回転方向 Reference Signs List 5 Pulverized coal machine 19 Crushing wheel 21 Throat 22 Chamber 27 Pyrite pro 29 Hot air duct 50 Damper 51 Actuator 52 Water injection device 53 Guillotine damper B Hot air (primary air) F Residual coal G Deposited coal H Gap I Pyrite pro rotation direction
フロントページの続き (72)発明者 川本 義人 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 (72)発明者 田辺 武利 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 (72)発明者 長谷川 忠 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 Fターム(参考) 4D063 EE03 EE12 EE22 4D067 EE13 EE39 GA04 GB03 Continued on the front page (72) Inventor Yoshito Kawamoto 6-9 Takaracho, Kure-shi, Hiroshima Prefecture Inside Babcock Hitachi Kure Factory (72) Inventor Taketoshi Tanabe 6-9 Takaracho, Kure-shi Hiroshima Prefecture Inside Babcock Hitachi Kure Factory (72) Inventor Tadashi Hasegawa 6-9 Takara-cho, Kure City, Hiroshima Prefecture F-term in Babcock Hitachi, Ltd. Kure Plant (reference) 4D063 EE03 EE12 EE22 4D067 EE13 EE39 GA04 GB03
Claims (2)
砕輪の回転に伴い回転する粉砕ローラにより石炭を粉砕
する微粉炭機と、前記微粉炭機で粉砕された石炭を乾燥
及び空気搬送するための熱空気を導入する熱空気ダクト
と、を備えた石炭微粉砕設備であって、 通常運転時には前記熱空気ダクトから前記微粉炭機へ熱
空気を支障無く供給するとともに、石炭微粉砕設備の停
止時に前記微粉炭機から飛散する石炭を前記熱空気ダク
ト側に浸入させないように前記熱空気ダクトの通路を略
閉鎖するダンパを前記熱空気ダクトに設け、 前記ダンパの近傍に飛散石炭を洗浄する注水装置を設け
たことを特徴とする石炭微粉砕設備。1. A pulverized coal machine that pulverizes coal by a pulverizing wheel rotated by a driving source and a pulverizing roller that rotates with the rotation of the pulverizing wheel; and drying and pneumatically conveying the pulverized coal by the pulverized coal machine. A hot air duct for introducing hot air, for supplying hot air from the hot air duct to the pulverized coal machine without any problem during normal operation, A damper for substantially closing the passage of the hot air duct is provided in the hot air duct so that coal scattered from the pulverized coal machine does not enter the hot air duct side when stopped, and the scattered coal is washed in the vicinity of the damper. Coal pulverization equipment characterized by having a water injection device.
て、 前記熱空気ダクトは、水平部ダクトと傾斜部ダクトと経
て前記微粉炭機に連結され、 前記ダンパは、前記水平部ダクトと傾斜部ダクトの境界
近傍に設置することを特徴とする石炭微粉砕設備。2. The coal pulverizing facility according to claim 1, wherein the hot air duct is connected to the pulverizer through a horizontal duct and an inclined duct, and the damper is inclined with the horizontal duct. Coal pulverization equipment, which is installed near the boundary of the duct.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000062162A JP2001246276A (en) | 2000-03-07 | 2000-03-07 | Installation for pulverizing coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000062162A JP2001246276A (en) | 2000-03-07 | 2000-03-07 | Installation for pulverizing coal |
Publications (1)
Publication Number | Publication Date |
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JP2001246276A true JP2001246276A (en) | 2001-09-11 |
Family
ID=18582207
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000062162A Pending JP2001246276A (en) | 2000-03-07 | 2000-03-07 | Installation for pulverizing coal |
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JP (1) | JP2001246276A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100483455B1 (en) * | 2002-08-05 | 2005-04-15 | 산양환경산업 주식회사 | Construction Waste Of Crusher Device A Fly Dust Removing For Joining A Spray |
JP2009006216A (en) * | 2007-06-26 | 2009-01-15 | Chugoku Electric Power Co Inc:The | Method of reactivating pulverized coal supply device |
KR100964307B1 (en) | 2008-10-22 | 2010-06-16 | 두산중공업 주식회사 | Pulverized Coal Burner |
JP2011104492A (en) * | 2009-11-16 | 2011-06-02 | Ihi Corp | Vertical mill |
KR101059543B1 (en) | 2009-09-30 | 2011-08-26 | 한국동서발전(주) | Pulverized coal inflow prevention device for conveying air duct in bowl mill |
JP2012127549A (en) * | 2010-12-14 | 2012-07-05 | Ihi Corp | Apparatus for discharging pyrite, and boiler facility |
KR101473060B1 (en) * | 2012-11-30 | 2014-12-15 | 한국서부발전 주식회사 | Preventing reversible type air duct for pulverizer |
JP2016002542A (en) * | 2014-06-19 | 2016-01-12 | 株式会社Ihi | Impurity and carbon residue discharger and method for discharging impurity and carbon residue |
JP2019084486A (en) * | 2017-11-06 | 2019-06-06 | 三菱日立パワーシステムズ株式会社 | Waste matter processor and pulverization system, and waste matter processing method |
WO2020158092A1 (en) * | 2019-01-31 | 2020-08-06 | 三菱日立パワーシステムズ株式会社 | Pulverizer, boiler system, and operation method for pulverizer |
-
2000
- 2000-03-07 JP JP2000062162A patent/JP2001246276A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100483455B1 (en) * | 2002-08-05 | 2005-04-15 | 산양환경산업 주식회사 | Construction Waste Of Crusher Device A Fly Dust Removing For Joining A Spray |
JP2009006216A (en) * | 2007-06-26 | 2009-01-15 | Chugoku Electric Power Co Inc:The | Method of reactivating pulverized coal supply device |
KR100964307B1 (en) | 2008-10-22 | 2010-06-16 | 두산중공업 주식회사 | Pulverized Coal Burner |
KR101059543B1 (en) | 2009-09-30 | 2011-08-26 | 한국동서발전(주) | Pulverized coal inflow prevention device for conveying air duct in bowl mill |
JP2011104492A (en) * | 2009-11-16 | 2011-06-02 | Ihi Corp | Vertical mill |
JP2012127549A (en) * | 2010-12-14 | 2012-07-05 | Ihi Corp | Apparatus for discharging pyrite, and boiler facility |
KR101473060B1 (en) * | 2012-11-30 | 2014-12-15 | 한국서부발전 주식회사 | Preventing reversible type air duct for pulverizer |
JP2016002542A (en) * | 2014-06-19 | 2016-01-12 | 株式会社Ihi | Impurity and carbon residue discharger and method for discharging impurity and carbon residue |
JP2019084486A (en) * | 2017-11-06 | 2019-06-06 | 三菱日立パワーシステムズ株式会社 | Waste matter processor and pulverization system, and waste matter processing method |
WO2020158092A1 (en) * | 2019-01-31 | 2020-08-06 | 三菱日立パワーシステムズ株式会社 | Pulverizer, boiler system, and operation method for pulverizer |
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