JPS60187353A - Control of discharge amount of foreign matter - Google Patents

Control of discharge amount of foreign matter

Info

Publication number
JPS60187353A
JPS60187353A JP4053584A JP4053584A JPS60187353A JP S60187353 A JPS60187353 A JP S60187353A JP 4053584 A JP4053584 A JP 4053584A JP 4053584 A JP4053584 A JP 4053584A JP S60187353 A JPS60187353 A JP S60187353A
Authority
JP
Japan
Prior art keywords
foreign matter
coal
mill
hot gas
amount
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
JP4053584A
Other languages
Japanese (ja)
Inventor
正昭 木下
永山 脩也
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP4053584A priority Critical patent/JPS60187353A/en
Publication of JPS60187353A publication Critical patent/JPS60187353A/en
Pending legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

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】 本発明は石炭粉砕装置における異物排出量調節方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the amount of foreign matter discharged in a coal pulverizer.

石炭を微粉砕する目的で、石炭の乾燥、粉砕、分級を行
なうと共に、異物(埋戻中の他の比重の大きい鉱物又は
石炭に混入してくる岩石、鉄片等)の自動排出を行なう
リングローラ式粉砕機においては、異物除去は重大であ
る。
A ring roller that dries, crushes, and classifies the coal for the purpose of finely pulverizing the coal, and also automatically discharges foreign matter (other minerals with high specific gravity during backfilling, or rocks, iron pieces, etc. mixed into the coal). In a type crusher, foreign matter removal is critical.

一般的に埋戻中には10〜30%の灰分が含有されてお
り、中でもSin、及びfree S i OLはミル
粉砕部の摩耗を促進させる。また供給される石炭に混入
している硬い岩石及び鉄片等も同様な弊害がある。この
為これ等の異物のミル粉砕部での滞留を極力避けると共
に、早期にミル外部へ排出する必要がある(常に少量の
排出は必要)。
Generally, backfilling contains 10 to 30% ash, and among them, Sin and free Si OL accelerate wear of the mill grinding part. Also, hard rocks, iron pieces, etc. mixed in the supplied coal have similar adverse effects. For this reason, it is necessary to prevent these foreign substances from accumulating in the grinding section of the mill as much as possible, and to discharge them to the outside of the mill as soon as possible (a small amount must always be discharged).

前記異物の自動排出機能に於いて、熱ガス吹上げロ開ロ
面積が一定のためミル負荷(石炭処理N)が変化した場
合、異物と共に多量の石炭を排出することがあり、異物
処理上及び省資源上無駄が多くなり好ましくなかった。
In the automatic discharge function of foreign matter, the open area of the hot gas blasting chamber is constant, so if the mill load (coal processing N) changes, a large amount of coal may be discharged together with foreign matter. This was not desirable in terms of resource conservation as it resulted in a lot of waste.

ここで第1図〜第4図について、石炭の微粉砕の一般的
な作用を説明すると、先ず図において1はバウル、2は
減速部、3は給炭管、4はロール、5は熱ガス入口、6
は熱ガス吹上げ口、7は転向ベーン、8は偏向ベーン、
9は微粉搬出口、10は内部円錐管、11はミル下部、
12は主軸、13はスクレーパである。
Here, to explain the general operation of fine pulverization of coal with reference to Figures 1 to 4, first, in the figure, 1 is a bowl, 2 is a reduction section, 3 is a coal feed pipe, 4 is a roll, and 5 is a hot gas entrance, 6
is a hot gas blow-off port, 7 is a turning vane, 8 is a deflection vane,
9 is a fine powder outlet, 10 is an internal conical tube, 11 is a mill lower part,
12 is a main shaft, and 13 is a scraper.

さてバウル1は別途設置されたモータで減速部2を介し
て回転している(通常、大型35RPM〜小型90RP
M)。石炭(埋戻)は給炭管3からバウル1上へ投入さ
れる。投入された石炭は、バウル1の回転による遠心力
でバウル外周方向へ送られ、ロール4との間に挟まれて
粉砕される。
Now, the bowl 1 is rotated by a separately installed motor via a speed reducer 2 (normally 35RPM for large size to 90RPM for small size).
M). Coal (backfilling) is charged onto the bowl 1 from the coal feed pipe 3. The introduced coal is sent toward the outer periphery of the bowl by the centrifugal force caused by the rotation of the bowl 1, and is crushed between the bowls and the rolls 4.

この時、ロール4はバウル1の回転力により従動(回転
)する。
At this time, the roll 4 is driven (rotated) by the rotational force of the bowl 1.

一方、石炭の乾燥及び微粉炭の分級、搬送に使われる熱
ガスはミル下部の熱ガス人口5から送入される。熱ガス
は主にバウル周囲に特に設けられた熱ガス吹上げ口6 
〈適音円周」二に2〜4個所)から吹出され(一部はバ
ウル周囲の隙間から流出)転向ベーン7により、はぼ9
0°方向(中心側に)を変換し、バウル上面の粉砕炭中
の微粉(一部粗粉を含む)をバウル」二の粉砕炭層より
分離(−次分級)し、ミル−に部へIM送する。
On the other hand, hot gas used for drying coal and classifying and transporting pulverized coal is sent from hot gas port 5 at the bottom of the mill. Hot gas is mainly supplied through hot gas blow-off ports 6 specially installed around the bowl.
The air is blown out from 2 to 4 places on the circumference of the bowl (some of it flows out from the gap around the bowl), and the deflection vane 7 causes the air to reach the bow 9.
The direction is changed to 0° (toward the center), and the fine powder (including some coarse powder) in the pulverized coal on the upper surface of the bowl is separated from the pulverized coal layer on the second bowl (-order classification) and transferred to the mill. send

微粉を含む熱ガスは、ミル上部で更に90゜(水平方向
となる)方向を変換すると共に、偏向ベーン8により水
平方向旋回流に流れを変えて微粉炭粒子に遠心力を与え
、微粉と粗粉を分離(二次分級)し、微粉はミルトップ
中央搬出口9からボイラ又は微粉炭貯蔵設備等へ熱ガス
により搬送される。また粗粉ば内部円錐管10によりバ
ウル上に回収され再び粉砕される。なお、偏向ベーン角
度は、ミル出口の微粉度調整のため、通常ミル外部から
調節可能となっている。
The hot gas containing fine powder is further changed in direction by 90 degrees (horizontal direction) at the top of the mill, and the deflection vane 8 changes the flow into a horizontal swirling flow to apply centrifugal force to the pulverized coal particles, separating the fine powder and coarse particles. The powder is separated (secondary classification), and the fine powder is transported by hot gas from the central outlet 9 of the mill top to a boiler or pulverized coal storage facility. The coarse powder is collected onto a bowl by the internal conical tube 10 and ground again. Note that the deflection vane angle can usually be adjusted from outside the mill in order to adjust the fineness of the mill outlet.

石炭中の異物(石炭より比重の大きいもの、石炭は0.
3〜0,4)は、前記熱ガス吹上げ口6からミル下部1
1へ落下し、主軸12に取付けられたスクレーバ13に
よりミル下部開口部から自動的にミル外部へ排出される
。なお、ミル風量は石炭粉砕及びミル本体振動上、負荷
に応じ適正に変化させる必要がある。従って前記熱ガス
吹上げ流速が負荷により変化する。
Foreign matter in coal (things with a higher specific gravity than coal, coal is 0.
3 to 0, 4) are from the hot gas blow-off port 6 to the mill lower part 1.
1, and is automatically discharged to the outside of the mill from the lower opening of the mill by a scraper 13 attached to the main shaft 12. Note that the mill air volume needs to be changed appropriately depending on the load for coal crushing and mill body vibration. Therefore, the flow rate of hot gas blowing up changes depending on the load.

本発明はミルの全負荷域に於いて適度な異物の排出を行
ない、石炭の排出を抑制して無駄を少なくし、ミル運転
上の経済性を向上することを目的とするものである。
The object of the present invention is to appropriately discharge foreign matter in the entire load range of the mill, suppress coal discharge, reduce waste, and improve the economical efficiency of mill operation.

従来異物排出量に関与する因子として、経験的に石炭性
状(粉砕性指数、灰分%)、粉砕部摩耗度、石炭処理量
、原炭粒径等が考えられていた。
Conventionally, coal properties (crushability index, ash content %), grinding part wear degree, coal throughput, raw coal particle size, etc. have been considered empirically as factors related to the amount of foreign matter discharged.

今回、異物排出量のデータを採取する機会に、たまたま
熱ガス量の変化で異物排出量が変化することが分かり、
第7図のようなデータを採取することが出来た。第7図
から分かるように、異物排出量(異物排出率0.02%
以上では殆どが石炭)は熱ガス吹上げ速度支配であり、
熱ガス量一定の場合、熱ガス吹上げ面積を小さくすれば
異物排出量は減少する。
This time, when I had the opportunity to collect data on the amount of foreign matter discharged, I happened to find that the amount of foreign matter discharged changes with changes in the amount of hot gas.
We were able to collect data as shown in Figure 7. As can be seen from Figure 7, the amount of foreign matter discharged (foreign matter discharge rate 0.02%
In the above, most of coal) is dominated by the hot gas blowing speed,
When the amount of hot gas is constant, the amount of foreign matter discharged can be reduced by reducing the hot gas blowing area.

そこで本発明者等は、逆にミル負荷が下がり、風量が少
なくなる時、吹上げ面積を小さくすればよいことに着目
して本発明を発明するに至ったものである。即ち、本発
明はこの吹−ヒげ面積をミル運転中外部から調節出来る
ように、して、異物排出量を常に適度になるように自由
に調節することを可能にした異物排出量調節方法を提供
せんとするものである。
Therefore, the present inventors have developed the present invention by focusing on the fact that when the mill load decreases and the air volume decreases, the blowing area can be reduced. That is, the present invention provides a method for adjusting the amount of foreign matter discharged, which makes it possible to adjust the blow-whisker area from the outside during mill operation, thereby making it possible to freely adjust the amount of foreign matter discharged so that the amount of foreign matter discharged is always appropriate. This is what we intend to provide.

以下本発明の実施例を図面について説明すると、第5図
及び第6図は本発明の実施例を示し、図中14はダンパ
羽根、15はダンパ軸、16はダンパ軸ボス、17はレ
バー、18はレバー固定板、19は固定ボルトである。
Embodiments of the present invention will be described below with reference to the drawings. FIGS. 5 and 6 show embodiments of the present invention, in which 14 is a damper blade, 15 is a damper shaft, 16 is a damper shaft boss, 17 is a lever, 18 is a lever fixing plate, and 19 is a fixing bolt.

さて図面の実施例では、熱ガス吹上げ口6の一部に、ミ
ル外部からレバー17で自由に開閉出来るダンパ(ダン
パ羽根14、ダンパ軸15)を有し、ミル負荷に応じレ
バーI7を操作してダンパ開度を変え、常時異物の排出
量を適正に保つことが出来るようにしたものである。
In the embodiment shown in the drawings, a part of the hot gas blow-off port 6 has a damper (damper blades 14, damper shaft 15) that can be freely opened and closed by a lever 17 from outside the mill, and the lever I7 is operated according to the mill load. By changing the damper opening degree, the amount of foreign matter discharged can be maintained at an appropriate level at all times.

さて実際に実施する場合は、石炭の堆積がない、バウル
外周」二面の高さ以上にみだりに突起部が出ないこと(
石炭の衝突による摩耗に耐えない)、微粉炭により可動
部が固着しない、作動が確実である等を考慮する必要が
あるが、本発明によると前記各項目を満足できると共に
、無駄を少なくして、ミル運転上の経済性を向上させる
ことができる。
Now, when actually carrying out the implementation, it is necessary to make sure that there is no accumulation of coal and that no protrusions protrude beyond the height of the two sides of the outer periphery of the bowl (
It is necessary to take into consideration the following factors: (not withstand wear due to coal collisions), that movable parts do not stick due to pulverized coal, that operation is reliable, etc., but according to the present invention, each of the above items can be satisfied, and waste can be reduced. , the mill operating economy can be improved.

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

第1図は従来の石炭粉砕装置の正面断面図、第2図は第
1図のA−A断面図、第3図は第1図のB−B断面図、
第4図は第3図のC−C断面図、第5図は本発明の実施
例を示し、第3図のC−C断面に相当する断面図、第6
図はミルの外部におけるレバ一部分の正面図、第7図は
異物排出率と熱ガス吹上げ速度との関係を示す線図であ
る。 図の主要部分の説明 6−熱ガス吹上げ口 14−ダンパ羽根 15−ダンパ軸 16−ダンパ軸ボス 17− レバー 18− レバー固定板 特許出願人 三菱重工業株式会社
Fig. 1 is a front sectional view of a conventional coal crushing device, Fig. 2 is a sectional view taken along line A-A in Fig. 1, and Fig. 3 is a sectional view taken along line B-B in Fig. 1.
4 is a sectional view taken along the line C-C in FIG. 3, FIG.
The figure is a front view of a part of the lever outside the mill, and FIG. 7 is a diagram showing the relationship between the foreign matter discharge rate and the hot gas blowing speed. Description of the main parts of the diagram 6 - Hot gas blow-off port 14 - Damper blade 15 - Damper shaft 16 - Damper shaft boss 17 - Lever 18 - Lever fixing plate Patent applicant Mitsubishi Heavy Industries, Ltd.

Claims (1)

【特許請求の範囲】[Claims] ミル運転中に熱ガス吹上げロ開ロ面積をミル外部から調
節可能にして、常に適量の異物を排出可能にしたことを
特徴とする異物排出量調節方法。
A method for adjusting the amount of foreign matter discharged, characterized in that the hot gas blow-up opening area can be adjusted from outside the mill during operation of the mill, so that an appropriate amount of foreign matter can always be discharged.
JP4053584A 1984-03-05 1984-03-05 Control of discharge amount of foreign matter Pending JPS60187353A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4053584A JPS60187353A (en) 1984-03-05 1984-03-05 Control of discharge amount of foreign matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4053584A JPS60187353A (en) 1984-03-05 1984-03-05 Control of discharge amount of foreign matter

Publications (1)

Publication Number Publication Date
JPS60187353A true JPS60187353A (en) 1985-09-24

Family

ID=12583147

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4053584A Pending JPS60187353A (en) 1984-03-05 1984-03-05 Control of discharge amount of foreign matter

Country Status (1)

Country Link
JP (1) JPS60187353A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016068023A (en) * 2014-09-30 2016-05-09 三菱日立パワーシステムズ株式会社 Vertical roller mill

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58207953A (en) * 1982-05-31 1983-12-03 バブコツク日立株式会社 Crushing and sorting device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58207953A (en) * 1982-05-31 1983-12-03 バブコツク日立株式会社 Crushing and sorting device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016068023A (en) * 2014-09-30 2016-05-09 三菱日立パワーシステムズ株式会社 Vertical roller mill

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