JPH0673636B2 - Pulverizer - Google Patents
PulverizerInfo
- Publication number
- JPH0673636B2 JPH0673636B2 JP60188829A JP18882985A JPH0673636B2 JP H0673636 B2 JPH0673636 B2 JP H0673636B2 JP 60188829 A JP60188829 A JP 60188829A JP 18882985 A JP18882985 A JP 18882985A JP H0673636 B2 JPH0673636 B2 JP H0673636B2
- Authority
- JP
- Japan
- Prior art keywords
- mill
- coal
- baul
- bawl
- 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.)
- Expired - Lifetime
Links
- 239000003245 coal Substances 0.000 claims description 47
- 230000002093 peripheral effect Effects 0.000 claims description 12
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 7
- 229910052683 pyrite Inorganic materials 0.000 description 7
- 239000011028 pyrite Substances 0.000 description 7
- 238000010926 purge Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000007613 slurry method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Landscapes
- Crushing And Grinding (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、竪形バウルミル、粉砕機(セメント製造用な
ど)等に利用できる微粉砕機に関するものである。TECHNICAL FIELD The present invention relates to a vertical crusher, a fine crusher that can be used as a vertical crusher, a crusher (for cement production, etc.), and the like.
(従来の技術) 石炭焚きボイラの石炭の粉砕、供給機械であるミルは、
予備機を含め複数台を装備されており、ボイラの部分負
荷を得るためにミルの台数を増減するのが普通である。
さらに近年では、石炭をDSS(Daily Start and Stop)
化、すなわち発電所においては、電力需要が減る夜間に
ボイラを停止、電力需要が増える昼間に備えて、朝ボイ
ラを点火、始動、運転する要求があり、ミルの発停が必
要となっている。特にボイラを起動して通常運転状態に
するには、ミルの始動から石炭粉砕までの時間を極力短
くすべきであるが、従来は下記の様なミル停止及びスタ
ンバイ状態であり、無理であった。(Prior Art) A mill that is a crushing and feeding machine for coal in a coal-fired boiler,
It is equipped with multiple units including the standby unit, and it is common to increase or decrease the number of mills to obtain the partial load of the boiler.
Furthermore, in recent years, coal has been converted to DSS (Daily Start and Stop).
In other words, in the power plant, there is a demand to stop the boiler at night when power demand decreases and to ignite, start, and operate the boiler in the morning in preparation for daytime when power demand increases, and it is necessary to start and stop the mill. . In particular, in order to start the boiler and put it into a normal operation state, the time from the start of the mill to the crushing of coal should be as short as possible, but in the past, it was impossible because of the following mill stop and standby states. .
(1).ミルを停止する時には、第1図の竪形バウルミ
ルで説明すると、同ミルの給炭管4からの石炭供給をま
ず停止し、ミル内の石炭をできるだけ燃焼させた後空気
入口管8から大量の空気をミル内に吹かし、バウル1上
にある残炭をボイラに送って燃焼させるか、またはパイ
ライト室10に落していた。しかし、どうしてもバウル上
にかなりの石炭が残留していた。(1). When the mill is stopped, it will be explained with reference to the vertical baul mill shown in FIG. 1. First, the coal supply from the coal feeding pipe 4 of the mill is stopped, the coal in the mill is burned as much as possible, and then a large amount of air is fed from the air inlet pipe 8. Air was blown into the mill and the residual coal on Baul 1 was sent to a boiler for combustion or dropped into the pyrite chamber 10. However, there was a considerable amount of coal remaining on the Baul.
(2).バウル上にかなりの残炭があるため、バウル内
雰囲気を空気にて冷却すると同時に、残炭から発生する
可燃性のガスをミル内からパージしないとこの残炭に着
火し、爆発の危険性があった。(2). Since there is a considerable amount of residual coal on the baul, the atmosphere inside the baul must be cooled with air, and at the same time flammable gas generated from the residual coal must be purged from the mill to ignite the residual coal and cause an explosion hazard. there were.
(3).前記(2)項のためにバウル、ロールやケーシ
ングなどは、運転中に得た熱量を冷空気に放出してしま
うため、次第に温度が下がってしまった。従って、停止
中のミルを再起動する際は、ミル内部が冷えているた
め、熱空気を入れ内部を加熱して石炭を投入するまでの
時間が必要であった。(3). Because of the above item (2), the temperature of the cowl, roll, casing, and the like gradually decreases because the amount of heat obtained during operation is released to the cold air. Therefore, when restarting the stopped mill, since the inside of the mill is cold, it took time until hot air was introduced to heat the inside and to add coal.
(発明が解決しようとする問題点) 本発明は従来の粉砕機におけるバウル上の残炭の問題点
を解決しようとするものである。(Problems to be Solved by the Invention) The present invention is intended to solve the problem of residual coal on the baul in a conventional crusher.
(問題点を解決するための手段) このため本発明は、バウル上の被粉砕物をロールで粉砕
する粉砕機において、ノズル吹出口をバウル外周側縁部
近傍に位置させ、給炭を止めた後のミル停止前にバウル
粉砕面の外周縁部に向けて空気を噴射するノズルを設
け、ノズル外周側の残炭を吹き上げてバウル外側に吹き
飛ばすようにしてなるもので、これを問題点解決のため
の手段とするものである。(Means for Solving the Problems) Therefore, in the present invention, in the crusher for crushing the object to be crushed on the baul by the roll, the nozzle outlet is located in the vicinity of the outer peripheral side edge portion of the bawl and the coal feeding is stopped. Before stopping the subsequent mill, a nozzle is provided to inject air toward the outer peripheral edge of the crushing surface of the baul, and the residual coal on the outer peripheral side of the nozzle is blown up and blown off to the outside of the baul. It is a means to
(作用) ノズル吹出口から、バウル粉砕面の外周縁部に向けて給
炭を止めた後のミル停止前に圧縮空気を噴射すると、ノ
ズル外周側の残炭は吹き上がると同時に遠心力によって
バウルの外側に吹き飛ばされるため、ミル停止中の保温
又は加温ができ、ミルを急速起動可能な状態に維持でき
る。(Operation) If compressed air is injected from the nozzle outlet toward the outer peripheral edge of the crushing surface of the baul and before the mill is stopped, the residual coal on the outer peripheral side of the nozzle blows up and at the same time the centrifugal force causes baul. Since it is blown to the outside of the mill, it can be kept warm while the mill is stopped or heated, and the mill can be maintained in a state in which it can be rapidly started.
(実施例) 以下本発明の実施例を図面について説明すると、第1図
〜第3図は本発明の実施例を示し、第1図の竪形バウル
ミルにおけるバウル1上面の詳細斜視図を第2図に示
す。先ず第1図において1はバウル、2はロール、3は
竪主軸、4は給炭管、5はロール軸、6はセパレータ、
7は微粉炭管、8は入口管、9はケーシング、10はパイ
ライト室、11はスクレーパである。(Embodiment) Hereinafter, an embodiment of the present invention will be described with reference to the drawings. FIGS. 1 to 3 show an embodiment of the present invention, and a detailed perspective view of an upper surface of a bawl 1 in a vertical bawl mill of FIG. Shown in the figure. First, in FIG. 1, 1 is a cowl, 2 is a roll, 3 is a vertical shaft, 4 is a coal feeding pipe, 5 is a roll shaft, 6 is a separator,
7 is a pulverized coal pipe, 8 is an inlet pipe, 9 is a casing, 10 is a pyrite chamber, and 11 is a scraper.
さてあらかじめ適当な粒径に粉砕された石炭粒は、給炭
管4を通ってバウル上に落下し供給される。バウル1の
回転軸である竪主軸3は、減速歯車(図示しない)を介
して電動機(図示しない)により駆動されている。回転
しているバウル1と、軸5がケーシング9に固定されて
いるロール2との間に石炭をかみ込むことにより、同石
炭が粉砕される。この間、空気入口管8から流入する熱
空気によって石炭は乾燥され、さらに粉砕、乾燥を繰り
返す。そして、セパレータ6にて粗粒を分級し、もとの
バウル1上に戻し再度粉砕する。The coal particles previously crushed to an appropriate particle size are supplied by dropping through the coal feeding pipe 4 and onto the baul. The vertical main shaft 3, which is the rotating shaft of the bawl 1, is driven by an electric motor (not shown) via a reduction gear (not shown). By biting coal between the rotating bawl 1 and the roll 2 having the shaft 5 fixed to the casing 9, the coal is crushed. During this time, the coal is dried by the hot air flowing in from the air inlet pipe 8, and further crushing and drying are repeated. Then, the coarse particles are classified by the separator 6, returned to the original bowl 1 and pulverized again.
一方分級された微粉は、微粉炭管7内をこの熱空気によ
って搬送され、ボイラで燃焼させられる。バウル上で粉
砕できない固い物質、例えば石炭中のパイライト成分
は、バウル1の窪みからバウル1の遠心力等ではみ出
し、バウル1の下部にあるパイライト室10に落下する。
このパイライト成分は、竪主軸3と共に回転するスクレ
ーパ11によりパイライトホッパー等の容器に移され、水
にてスラリー状にされて搬送、処理される。On the other hand, the classified fine powder is conveyed by the hot air in the fine coal pipe 7 and burned in the boiler. A hard substance that cannot be crushed on the bawl, for example, a pyrite component in coal, protrudes from the recess of the baul 1 by the centrifugal force of the baul 1 and falls into the pyrite chamber 10 below the baul 1.
The pyrite component is transferred to a container such as a pyrite hopper by a scraper 11 that rotates together with the vertical spindle 3, and is made into a slurry with water to be conveyed and processed.
第2図及び第3図における13は残炭を示す。この残炭13
はミルが停止する前には給炭を止めるため、次第に薄く
なると同時に遠心力によってバウル1の周近くに堆積し
た状態になる。なお、ロール2には図示しないストッパ
ー機構が装備されており、ロール2とバウル1とのクリ
アランスを一定以上に保っているため、残炭がある程度
薄くなれば石炭は粉砕されない。従って給炭を止め、バ
ウル1上の残炭13をできるだけ粉砕した後の残炭層の形
状は、ほぼ第3図の様になっている。バウル1の皿の端
の内側に、第2図、第3図で示す様な空気噴射ノズル12
を取付け、残炭13の外周側に圧縮空気を噴射すると、残
炭は吹き上がると同時に遠心力によってバウル外側に飛
ばされる。そこではパージ空気14を吹き上げており、微
粉はこのパージ空気14により搬送されて微粉炭管7を通
り、図示しないボイラにて燃焼させられる。一方粒径の
大きい石炭はパージ空気では浮力が得られないため、パ
イライト室10に落ち、水スラリー方式等で処理される。13 in FIGS. 2 and 3 indicates residual coal. This charcoal 13
Since the coal supply is stopped before the mill stops, it gradually becomes thinner and at the same time it is in a state of being accumulated near the circumference of the baul 1 by centrifugal force. Since the roll 2 is equipped with a stopper mechanism (not shown) to keep the clearance between the roll 2 and the bawl 1 at a certain level or more, the coal will not be crushed if the residual coal becomes thin to some extent. Therefore, the shape of the residual coal layer after stopping the coal supply and crushing the residual coal 13 on the baul 1 as much as possible is almost as shown in FIG. Inside the end of the bowl of the bowl 1, an air injection nozzle 12 as shown in FIG. 2 and FIG.
Is attached, and when compressed air is injected to the outer peripheral side of the residual coal 13, the residual coal is blown up and, at the same time, is blown to the outside of the baul by the centrifugal force. There, the purge air 14 is blown up, and the fine powder is conveyed by the purge air 14, passes through the fine coal powder pipe 7, and is burned in a boiler (not shown). On the other hand, since coal having a large particle size cannot obtain buoyancy with purge air, it falls into the pyrite chamber 10 and is treated by a water slurry method or the like.
(発明の効果) 以上詳細に説明した如く本発明は、ノズル吹出口をバウ
ル外周側縁部近傍に位置させ、給炭を止めた後のミル停
止前にバウル粉砕面の外周縁部に向けて空気を噴射する
ノズルを設け、ノズル外周側の残炭を吹き上げてバウル
外側に吹き飛ばす。従ってミル停止前にミル内残炭の大
部分であるバウル上のものをミル外に効率的及び安全に
処理できるため、従来の様にミル内を冷空気にてパージ
する必要はなく、ミルの空気入口及びミル出口近くの微
粉炭管に設けられている出口弁を閉鎖することにより、
ミル内部を密閉状態にすることができる。このことでミ
ル運転中に温まったミルの各部品、特にバウルを保温す
るので、ミル再起動時に給炭を即開始し、加温、乾燥に
続き粉砕可能となる。従って従来よりもミルの起動時間
を短縮できるなお、ミル停止中にミル内部を加熱できる
熱風がボイラなどから供給できれば、ミル内部をこの熱
風を使って常時保温(加温)しておく方法は、特に長期
停止ミルの急速起動には有効であることは言うまでもな
い(少量の熱風を空気入口管8から入れ、ミル内部を加
温した後微粉炭管からボイラに燃焼用空気として送風す
る)。またミル内部で石炭堆積が予想される場所も、同
様に別に設けた空気噴射ノズルで残炭処理する。(Effects of the Invention) As described in detail above, according to the present invention, the nozzle outlet is located in the vicinity of the outer peripheral edge of the bawl, and is directed toward the outer peripheral edge of the baul crushing surface before stopping the mill after stopping the coal feeding. A nozzle that injects air is provided, and the residual coal on the outer peripheral side of the nozzle is blown up and blown outside the bawl. Therefore, before the mill is stopped, most of the residual coal in the mill, which is on the baul, can be efficiently and safely treated outside the mill, so there is no need to purge the inside of the mill with cold air as in the past. By closing the outlet valve provided in the pulverized coal pipe near the air inlet and mill outlet,
The inside of the mill can be sealed. As a result, each part of the mill that has been warmed during the operation of the mill, especially the bawl, is kept warm, so that when the mill is restarted, coal feeding is started immediately, and after heating and drying, crushing is possible. Therefore, the start-up time of the mill can be shortened compared to the past.If hot air that can heat the inside of the mill while the mill is stopped can be supplied from the boiler, etc., the method of keeping the inside of the mill warm (warming) at all times is It is needless to say that it is particularly effective for the rapid start of the long-term stop mill (a small amount of hot air is introduced from the air inlet pipe 8 to heat the inside of the mill and then blown as combustion air from the pulverized coal pipe to the boiler). Also, at places where coal accumulation is expected inside the mill, residual air is similarly treated with a separate air injection nozzle.
以上の如く本発明によると、ミル停止時にミル内残炭を
完全にパージできるので、ミル停止中の保温又は加温が
でき、ミルを急速起動可能な状態に維持できる。従って
本発明は、バウルミルの急速起動の方法として大変有効
であり、従来のものに比べ、ミル1機につき約5分間の
起動時間の短縮が可能(従来は30分位かかっていた)で
あり、1ボイラに6〜8台のミルがあるため、全体で30
分位の短縮が見込まれ、DSS運転の現状では、この30分
は貴重である。As described above, according to the present invention, the residual carbon in the mill can be completely purged when the mill is stopped, so that the temperature can be maintained or warmed while the mill is stopped, and the mill can be maintained in a state in which it can be rapidly started. Therefore, the present invention is very effective as a quick start method for a baul mill, and it is possible to reduce the start time for each mill by about 5 minutes (it took about 30 minutes in the past) as compared with the conventional method. Since there are 6 to 8 mills in one boiler, 30 in total
Quantiles are expected to be shortened, and in the current state of DSS operation, these 30 minutes are precious.
第1図は本発明の実施例を示す微粉炭機の1例である竪
型バウルミルの斜視図、第2図は第1図における要部の
詳細斜視図、第3図は第2図のA〜A断面図である。 図の主要部分の説明 1……バウル 2……ロール 3……竪主軸 12……空気噴射ノズル 13……残炭FIG. 1 is a perspective view of a vertical type baul mill which is an example of a pulverized coal machine showing an embodiment of the present invention, FIG. 2 is a detailed perspective view of a main part in FIG. 1, and FIG. 3 is A of FIG. FIG. Description of main parts of the figure 1 …… Bowl 2 …… Roll 3 …… Vertical spindle 12 …… Air injection nozzle 13 …… Residual coal
───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉田 博久 長崎県長崎市飽の浦町1番1号 三菱重工 業株式会社長崎研究所内 (56)参考文献 実開 昭60−79548(JP,U) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hirohisa Yoshida 1-1 1-1 Atsunoura-machi, Nagasaki-shi, Nagasaki Mitsubishi Heavy Industries, Ltd. Nagasaki Research Institute (56) References: 60-79548 (JP, U)
Claims (1)
砕機において、ノズル吹出口をバウル外周側縁部近傍に
位置させ、給炭を止めた後のミル停止前にバウル粉砕面
の外周縁部に向けて空気を噴射するノズルを設け、ノズ
ル外周側の残炭を吹き上げてバウル外側に吹き飛ばすよ
うにしたことを特徴とする微粉砕機。1. A crusher for crushing an object to be crushed on a bawl with a roll, wherein a nozzle outlet is located near an outer peripheral side edge portion of the bawl, and the outside of the crushed surface of the bawl is stopped before stopping the mill after stopping the coal feeding. A fine pulverizer characterized in that a nozzle for injecting air toward the peripheral portion is provided, and residual coal on the outer peripheral side of the nozzle is blown up to be blown outside the bawl.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60188829A JPH0673636B2 (en) | 1985-08-28 | 1985-08-28 | Pulverizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60188829A JPH0673636B2 (en) | 1985-08-28 | 1985-08-28 | Pulverizer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6249953A JPS6249953A (en) | 1987-03-04 |
| JPH0673636B2 true JPH0673636B2 (en) | 1994-09-21 |
Family
ID=16230559
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60188829A Expired - Lifetime JPH0673636B2 (en) | 1985-08-28 | 1985-08-28 | Pulverizer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0673636B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4948285B2 (en) * | 2007-06-26 | 2012-06-06 | 中国電力株式会社 | How to restart pulverized coal supply equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6079548U (en) * | 1983-11-02 | 1985-06-03 | 株式会社神戸製鋼所 | Laura Mill |
-
1985
- 1985-08-28 JP JP60188829A patent/JPH0673636B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6249953A (en) | 1987-03-04 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |