JP3115687B2 - Coal crusher and water injection control method thereof - Google Patents

Coal crusher and water injection control method thereof

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Publication number
JP3115687B2
JP3115687B2 JP04071256A JP7125692A JP3115687B2 JP 3115687 B2 JP3115687 B2 JP 3115687B2 JP 04071256 A JP04071256 A JP 04071256A JP 7125692 A JP7125692 A JP 7125692A JP 3115687 B2 JP3115687 B2 JP 3115687B2
Authority
JP
Japan
Prior art keywords
coal
water injection
water
feed pipe
tube wall
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 - Fee Related
Application number
JP04071256A
Other languages
Japanese (ja)
Other versions
JPH05269394A (en
Inventor
幸男 高橋
直機 藤原
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 Power Ltd
Original Assignee
Babcock Hitachi KK
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Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP04071256A priority Critical patent/JP3115687B2/en
Publication of JPH05269394A publication Critical patent/JPH05269394A/en
Application granted granted Critical
Publication of JP3115687B2 publication Critical patent/JP3115687B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は石炭粉砕装置に関し、特
に石炭粉砕機への石炭供給時の閉塞トラブルを未然に防
止しプラントの円滑な運転を可能とする石炭粉砕装置お
よび該石炭粉砕装置への注水量制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coal crusher, and more particularly to a coal crusher and a coal crusher capable of preventing a blockage trouble at the time of coal supply to a coal crusher and enabling a smooth operation of a plant. And a method for controlling the amount of injected water.

【0002】[0002]

【従来の技術】火力発電用の大型ボイラ、一般産業用の
ボイラなど石炭を微粉砕した粉末状の石炭(以下、微粉
炭と称する)を燃料として使用するボイラがある。図4
は石炭を粉砕するための従来装置として、竪型ボ−ルミ
ルと称される石炭粉砕装置を示す。粉砕される石炭Cは
粉砕装置本体1の給炭管8内を落下して粉砕部に到る。
粉砕部は加圧装置4によって押圧力を加えられた上部固
定輪6と、駆動装置15によって回転する下部転輪9
と、上部固定輪6と下部転輪9との間に配置されて下部
転輪9の回転に伴って転動する複数個の粉砕用ボ−ル7
とから形成される。粉砕部に到った石炭は下部転輪9の
回転により生ずる遠心力によって粉砕用ボ−ル7の位置
に移動して粉砕される。粉砕された石炭は空気口17か
ら供給される空気(通常は石炭の乾燥をも行うために高
温空気とする)により粉砕装置本体1内を上昇する。粉
砕された石炭を含有する気流は、分級器11の入口に設
置した旋回羽根12により旋回気流となり、大径の粒子
は分級器11内を下降して粉砕部に落下して再粉砕さ
れ、微粉炭は気流と共に微粉炭管13に流入し、図示し
ない微粉炭バ−ナに気流搬送される。
2. Description of the Related Art There are boilers which use powdered coal (hereinafter, referred to as pulverized coal) as a fuel, such as a large boiler for thermal power generation and a boiler for general industry, which are obtained by pulverizing coal. FIG.
In the drawings, there is shown a conventional apparatus for pulverizing coal, a coal pulverization apparatus called a vertical ball mill. The pulverized coal C falls in the coal feed pipe 8 of the pulverizing apparatus main body 1 and reaches the pulverizing section.
The crushing unit includes an upper fixed wheel 6 to which a pressing force is applied by a pressing device 4 and a lower rolling wheel 9 which is rotated by a driving device 15.
And a plurality of crushing balls 7 arranged between the upper fixed wheel 6 and the lower wheel 9 and rolling with the rotation of the lower wheel 9.
And formed from The coal reaching the pulverizing section is moved to the position of the pulverizing ball 7 by the centrifugal force generated by the rotation of the lower rolling wheel 9 and pulverized. The pulverized coal rises in the pulverizer main body 1 by air supplied from the air port 17 (usually, high-temperature air is also used for drying the coal). The air stream containing the pulverized coal is turned into a swirling air stream by the swirling blades 12 installed at the entrance of the classifier 11, and the large-diameter particles fall down in the classifier 11 and fall into the pulverizing section to be re-pulverized. The charcoal flows into the pulverized coal pipe 13 together with the airflow, and is conveyed to the pulverized coal burner (not shown) by the airflow.

【発明が解決しようとする課題】[Problems to be solved by the invention]

【0003】上述構成の粉砕装置において、給炭管8の
下部を中心として石炭の付着事故が何件か報告されてお
り、この給炭管8の閉塞事故は通常、つぎの原因によっ
て生ずる。すなわち、石炭は可燃物である炭分以外に鉱
物質(通常、灰分と称している)を含んでおり、特に、
選炭の過程で排出されるスラッジ炭と称される低品位炭
には多くの灰分が含まれている。さらに、スラッジ炭の
灰分にはカオリナイトもしくはマスコバイトといった粘
土分を多量に含むケ−スが多い。周知のように粘土分は
水で湿らせた状態のものを乾燥させると強く固着、固化
する性質を有するので、粘土分を含む石炭もこの性質を
有することになる。
[0003] In the pulverizing apparatus having the above-mentioned structure, several incidents of coal adhesion have been reported mainly in the lower part of the coal feed pipe 8, and the clogging accident of the coal feed pipe 8 is usually caused by the following causes. That is, coal contains mineral matter (usually called ash) in addition to combustible coal,
Low-grade coal called sludge coal discharged in the process of coal preparation contains a lot of ash. Furthermore, the sludge coal ash contains many cases containing a large amount of clay such as kaolinite or muscovite. As is well known, clay has a property of firmly fixing and solidifying when dried in a state of being moistened with water, so that coal containing a clay also has this property.

【0004】通常、これらのスラッジ炭の大半は炭鉱廃
棄物として廃棄される。しかし、スラッジの一部はカロ
リ−調整のために、高品質炭(高カロリ−炭)に混合さ
れる場合がある。スラッジ炭を混合した石炭でなくと
も、炭田の土質として粘土分を含有する石炭も比較的多
い。前述のように粘土分は水で湿らせた状態のものを乾
燥させると強く固着、固化する性質を有するので、粘土
分を含む石炭もこの性質を有することになる。
[0004] Usually, most of these sludge coals are disposed of as coal mine waste. However, a part of the sludge may be mixed with high quality coal (high calorie coal) for calorie control. Even if it is not coal mixed with sludge charcoal, there are relatively many coals that contain clay as soil of coal fields. As described above, since the clay component has a property of firmly fixing and solidifying when dried in a state of being moistened with water, the coal containing the clay component also has this property.

【0005】石炭は通常、湿った状態で粉砕装置本体
に供給され、給炭管8の下部で熱空気によって乾燥せし
められるが、この石炭の灰分中に粘土分が含まれている
と給炭管8の下部内壁で乾燥し、粘土分が付着する。付
着層が徐々に成長して、最終的には給炭管8の閉塞、使
用不能といった事態に至る。
[0005] Coal is usually wet in a crushing apparatus main body 1 in a wet state.
The coal is dried by hot air at the lower part of the coal feed pipe 8, but if the ash of this coal contains clay, it dries on the lower inner wall of the coal feed pipe 8 and the clay adheres. The adhesion layer gradually grows, and eventually leads to a situation in which the coal feed pipe 8 is blocked or unusable.

【0006】こういった問題点を解決する手段として、
下部転輪9に掻き取り刃を取付けて下部転輪の回転を利
用して給炭管8の内壁を掻き取ったり、他の動力源を利
用して、掻き取り作業を行う装置が提案されている。し
かし、これらの装置は掻き取り刃自体に石炭、特に粘土
分が付着するなどのために、充分な効果を挙げることが
できていない。
As a means for solving these problems,
A device has been proposed in which a scraping blade is attached to the lower rolling wheel 9 to scrape the inner wall of the coal feed pipe 8 by using the rotation of the lower rolling wheel, or to perform a scraping operation by using another power source. I have. However, these devices have not been able to provide a sufficient effect because coal, particularly clay, adheres to the scraping blade itself.

【0007】また、他の手段として付着した石炭層を掻
き取る代わりに、予め注水管2および注水孔3を通じて
給炭管8の内壁に水を流下させ、給炭管8の下部におい
ても粘土分が乾燥、固化しないようにする方法が提案さ
れ、効果を挙げている。しかしこの方法は、石炭の付
着、固化を防止できる反面、粉砕装置に対して水を供給
することは石炭の乾燥とは反対の操作であるから、分級
器11の分級能率が低下したり、微粉炭の燃焼性が低下
するなどの問題点が生ずる。
As another means, instead of scraping off the coal layer that has adhered, water is allowed to flow in advance on the inner wall of the coal feed pipe 8 through the water injection pipe 2 and the water injection hole 3, and the clay content is also formed below the coal feed pipe 8. Has been proposed to prevent drying and solidification, which has been effective. However, while this method can prevent the adhesion and solidification of coal, supplying water to the pulverizer is an operation opposite to the drying of coal, so that the classification efficiency of the classifier 11 decreases, Problems such as a decrease in the flammability of charcoal occur.

【0008】従って本発明の目的は、上記した従来技術
の、給炭管の閉塞を防止するための水量が多すぎると分
級器における分級効率の低下、微粉炭の燃焼性の低下、
水の蒸発熱によるボイラの熱損失の増加などの問題点を
解決するため、給炭管に対する石炭の付着を効果的に防
止可能で、石炭の分級効率の低下や微粉炭の燃焼性の低
下などのない石炭粉砕装置および該石炭粉砕装置の注水
量の制御方法を提供するにある。
[0008] Accordingly, an object of the present invention is to reduce the classification efficiency of the classifier when the amount of water for preventing blockage of the coal feed pipe is too large, the flammability of pulverized coal, and the like.
In order to solve the problems such as increase in heat loss of the boiler due to heat of water evaporation, it is possible to effectively prevent coal from adhering to the coal feed pipe, decrease coal classification efficiency, decrease pulverized coal flammability, etc. It is an object of the present invention to provide a coal pulverizing apparatus without the above and a method for controlling the water injection amount of the coal pulverizing apparatus.

【0009】[0009]

【課題を解決するための手段】本発明によれば、石炭を
粉砕部に供給する給炭管の上部に、注水ポンプおよび注
水弁を介して供給される注水を前記給炭管の内壁面に流
下させる注水孔を設け 石炭粉砕装置において前記
炭管管壁温度を検出する管壁温度検出器を設け、該
壁温度検出器からの管壁温度検出信号と予め設定した
壁温度設定信号との比較結果に基づいて前記注水弁の開
度を制御する演算装置を設けた、石炭粉砕装置が提供さ
れる。
According to the present invention, a water injection pump and a water injection pump are provided above a coal feed pipe for supplying coal to a pulverizing section.
The water supplied through the water valve flows to the inner wall of the coal pipe.
Oite coal pulverizer provided with a water injection hole for Do, the tube wall temperature detector for detecting the wall temperature of the Kyusumikan provided, preset the tube wall temperature detection signal from the tube wall temperature detector opening of the injection valve based on the comparison result between the tube wall temperature setting signal
A coal crusher provided with a computing device for controlling the degree is provided.

【0010】さらに本発明によれば、石炭を粉砕部に供
給する給炭管の内壁面に石炭付着防止用の注水を行う
炭粉砕装置の注水量制御方法において、前記給炭管
壁温度に基づいて前記注水量を制御する、石炭粉砕装置
の注水量制御方法が提供される。この場合、前記管壁温
度を正常時の管壁温度と比較して、大の場合には前記注
水量を増加させ、小の場合には前記注水量を減少させ
る。
[0010] Further, according to the present invention, the water injection rate control method for stone <br/> coal pulverizing apparatus which performs injection of coal antiadhesive coal on the inner wall surface of the supplied coal feed pipe to the grinding unit, the coal feed A method for controlling a water injection amount of a coal crusher, wherein the water injection amount is controlled based on a pipe wall temperature of the pipe is provided. In this case, the tube wall temperature
Temperature compared to the normal tube wall temperature.
Increase the amount of water and, if small, decrease the amount of water injected
You.

【0011】管壁温度検出器は給炭管の内壁、外壁また
は給炭管の内壁に隣接して配置してよく、水が流れてい
るかどうか、石炭の微粉が管壁に付着していないかどう
か、を温度を監視することによって検知し、付着防止用
給水の給水量をこれに基づいて制御する。
The pipe wall temperature detector may be arranged adjacent to the inner wall, outer wall or inner wall of the coal feed pipe, and whether or not water is flowing, whether or not fine coal powder adheres to the pipe wall. Is detected by monitoring the temperature, and the supply amount of the adhesion preventing supply water is controlled based on this.

【0012】[0012]

【作用】水は加熱されると温度が上昇するが、所定の雰
囲気圧力の下では該圧力により定まる温度以上に温度が
上昇することはなく、この温度において加えた熱は水の
蒸発潜熱として消費される。この水の物性により、給炭
管の内壁に付着した石炭が湿っているときは、圧力によ
って定まる温度を超えて上昇することはない。本発明は
これを利用して付着防止用水の量の適正化を行うもので
あり、破砕装置への注水量を必要最小限度にすることが
できるのみでなく、注水装置の異常を早期に発見するこ
とができる。
Although the temperature of water rises when heated, the temperature does not rise above a temperature determined by the pressure under a predetermined atmospheric pressure, and the heat added at this temperature is consumed as latent heat of evaporation of water. Is done. Due to the physical properties of this water, when the coal adhering to the inner wall of the coal feed pipe is wet, it does not rise above the temperature determined by the pressure. The present invention utilizes this to optimize the amount of anti-adhesion water and not only can minimize the amount of water injected into the crushing device to the minimum necessary, but also finds an abnormality in the water injection device at an early stage. be able to.

【0013】[0013]

【実施例】図1は本発明の実施例である石炭粉砕装置の
概略図であり、図4の従来技術と対応する部品は同一参
照数字で示され、これは、粉砕装置本体1、注水管2、
注水孔3、加圧装置4、管壁温度検出器である熱電対
5、上部固定輪6、粉砕用ボ−ル7、給炭管8、下部転
輪9、分級器11、旋回羽根12、微粉炭管13、駆動
装置15、注水器16、空気口17を含み、さらに、演
算装置10、CRT画面14、注水弁である弁18、注
水ポンプ19、管壁温度検出信号20、管壁温度設定信
号21も示されている。
FIG. 1 is a schematic view of a coal pulverizing apparatus according to an embodiment of the present invention. Parts corresponding to those of the prior art shown in FIG. 4 are designated by the same reference numerals. 2,
A water injection hole 3, a pressurizing device 4, a thermocouple 5, which is a tube wall temperature detector , an upper fixed wheel 6, a crushing ball 7, a coal feed tube 8, a lower rolling wheel 9, a classifier 11, a rotating blade 12, It includes a pulverized coal pipe 13, a driving device 15, a water injector 16, an air port 17, and further includes a computing device 10, a CRT screen 14, a valve 18 as a water injection valve, a water injection pump 19, a tube wall temperature detection signal 20, a tube wall temperature. The setting signal 21 is also shown.

【0014】図1について説明する前に、発明者等が行
った実験デ−タについて図2、図3を参照して説明す
る。図2は図3に示すように給炭管の外部から熱電対挿
入用の孔を設け、その中にシ−ス熱電対を挿入し、給炭
管の内壁から3mmの位置の管壁部の温度を測定し、給
炭管の長手方向の温度分布として示したものであって、
給炭管の内壁に給炭中の微粉が付着していない場合は管
壁の温度は給炭管の下部に向って上昇しているが、10
0℃以下である。
Before describing FIG. 1, experimental data performed by the inventors will be described with reference to FIGS. FIG. 2 shows a case in which a thermocouple insertion hole is provided from the outside of the coal feed pipe as shown in FIG. The temperature was measured and shown as a temperature distribution in the longitudinal direction of the coal feed pipe,
When the fine powder in the coal feed is not attached to the inner wall of the coal feed pipe, the temperature of the pipe wall rises toward the lower part of the coal feed pipe.
0 ° C. or less.

【0015】一方、給炭管の内壁に微粉の付着層が形成
されると、水は付着層の表面を流れるために、給炭管を
直接に冷却することができなくなり、給炭管の内壁から
僅かに(約3mm)離れた位置の温度は図2の(b)に
示すように、粉砕装置に供給した空気により加熱されて
100℃を超える。すなわち、このことを利用し給炭管
の管壁の温度を測定して給炭管の内壁への微粉の付着状
況を知ることが可能となり、本発明はこれを利用するも
のである。
On the other hand, if an adhesion layer of fine powder is formed on the inner wall of the coal feed pipe, water cannot flow directly on the surface of the adhesion layer, and thus cannot be directly cooled. As shown in FIG. 2 (b), the temperature at a position slightly (about 3 mm) away from is higher than 100 ° C. by the air supplied to the pulverizer. That is, by utilizing this fact, it becomes possible to measure the temperature of the pipe wall of the coal feed pipe to know the state of adhesion of the fine powder to the inner wall of the coal feed pipe, and the present invention utilizes this.

【0016】図1において、粉砕される石炭Cは粉砕装
置本体1の給炭管8内を落下して、粉砕部に至る。粉砕
部は、加圧装置4により圧力を加えられる上部固定輪6
と、駆動装置15によって回転駆動される下部転輪9
と、上部固定輪6と下部転輪9との間に配置され下部転
輪9の回転に伴って転動する粉砕用ボ−ル7とから形成
される。粉砕部に到った石炭は、下部転輪9の回転によ
り生ずる遠心力によって粉砕用ボ−ル7の位置に移動し
て粉砕される。粉砕された石炭は空気口17から供給さ
れる空気(通常は石炭の乾燥をも行うために高温空気と
する)により粉砕装置本体1内を上昇する。粉砕された
石炭を含有する気流は、分級器11の入口に設置した旋
回羽根12により旋回気流となり、大径の粒子は分級器
11内を下降して粉砕部に落下して再粉砕され、微粉炭
は気流と共に微粉炭管13に流入し図示しない微粉炭バ
−ナに気流搬送される。
In FIG. 1, the coal C to be pulverized falls in the coal feed pipe 8 of the pulverizer main body 1 and reaches the pulverizing section. The pulverizing unit includes an upper fixed wheel 6 to which pressure is applied by the pressurizing device 4.
And the lower wheel 9 rotationally driven by the driving device 15
And a grinding ball 7 disposed between the upper fixed wheel 6 and the lower wheel 9 and rolling with the rotation of the lower wheel 9. The coal that has reached the pulverizing section is moved to the position of the pulverizing ball 7 by the centrifugal force generated by the rotation of the lower rolling wheel 9 and pulverized. The pulverized coal rises in the pulverizer main body 1 by air supplied from the air port 17 (usually, high-temperature air is also used for drying the coal). The air stream containing the pulverized coal is turned into a swirling air stream by the swirling blades 12 installed at the entrance of the classifier 11, and the large-diameter particles fall down in the classifier 11 to fall into the pulverizing section and are re-pulverized. The charcoal flows into the pulverized coal pipe 13 together with the airflow, and is conveyed by airflow to a pulverized coal burner (not shown).

【0017】微粉が給炭管8の内壁に付着することを防
止するための水(以下、付着防止用注水と称する)は
注水管2により注水器16に入り、注水孔3から給炭管
8内に入り、内壁を流下する。給炭管8の長手方向に配
置され、給炭管8の壁内部に挿入された複数の熱電対5
によって給炭管8の管壁温度を測定する。また、給炭管
8の円周方向にも熱電対5を配置し、この円周方向に配
置した熱電対5によって円周方向の管壁の温度分布を測
定し、円周方向の水の流下量の均一性を監視する。
Water for preventing the fine powder from adhering to the inner wall of the coal feed pipe 8 (hereinafter referred to as water for preventing adhesion) enters the water injector 16 through the water injection pipe 2 and flows through the water injection hole 3 into the coal feed pipe. 8 and flow down the inner wall. Arranged in the longitudinal direction of coal feed pipe 8
And a plurality of thermocouples 5 inserted inside the wall of the coal feed pipe 8.
To measure the wall temperature of the coal feed pipe 8. A thermocouple 5 is also arranged in the circumferential direction of the coal feed pipe 8, and the temperature distribution of the pipe wall in the circumferential direction is measured by the thermocouple 5 arranged in the circumferential direction. Monitor volume uniformity.

【0018】これらの熱電対5によって検知した管壁温
度検出信号20は演算装置10に取込まれ、CRT画面
14上に温度分布として表示される。運転員によって
の温度分布を監視するとともに、演算装置10によっ
て、予めインプットした正常時の管壁温度設定信号21
(温度パタ−ン)と比較、演算を行って、正常時の温度
パタ−ンとの最大温度差を求める。温度差が予め設定し
た許容値以上であった場合、演算装置10から信号を発
生して(運転員の操作によることも可能である)注水用
の弁18を開き、注水量を増加させる。円周方向の温度
パタ−ンについても、同様に予めインプットした正常時
の温度パタ−ンと比較、演算を行って温度差が予め設定
した許容値以上であった場合に警報を発生して運転員に
注意する。円周方向の温度パタ−ンの異常は注水圧力の
低下、注水孔3のつまり、その他の種々の要因によって
生ずるので、運転員の現場点検、補修を必要とすること
が多い。
The tube wall temperature detection signal 20 detected by the thermocouple 5 is taken into the arithmetic unit 10 and displayed on the CRT screen 14 as a temperature distribution. The operator thus monitors the temperature distribution of this <br/>, by the arithmetic unit 10
The normal setting of the tube wall temperature setting signal 21
(Temperature pattern), and a calculation is performed to determine the maximum temperature difference from the normal temperature pattern. If the temperature difference is equal to or greater than a preset allowable value, a signal is generated from the arithmetic unit 10 (which can be operated by an operator) to open the water injection valve 18 to increase the water injection amount. Similarly, the temperature pattern in the circumferential direction is compared with the normal temperature pattern input in advance and calculated, and if the temperature difference is equal to or greater than a predetermined allowable value, an alarm is generated and the operation is performed. Watch out for members. An abnormality in the temperature pattern in the circumferential direction is caused by a decrease in the injection pressure and a clogging of the injection hole 3, that is, due to various other factors.

【0019】[0019]

【発明の効果】上記のように本発明によれば、破砕装置
への注水量を必要最小限度にすることができるのみでな
く、注水装置の異常を早期に発見することができる。
As described above, according to the present invention, not only can the amount of water injected into the crushing device be minimized, but also an abnormality in the water injection device can be detected at an early stage.

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

【図1】本発明による石炭粉砕装置の概略断面図。FIG. 1 is a schematic sectional view of a coal crusher according to the present invention.

【図2】本発明による方法で測定した給炭管の温度分布
の例を示す図。
FIG. 2 is a diagram showing an example of a temperature distribution of a coal feed pipe measured by the method according to the present invention.

【図3】図2に示す温度分布を測定するために配置した
熱電対の取付けを示す図。
FIG. 3 is a view showing attachment of a thermocouple arranged for measuring the temperature distribution shown in FIG. 2;

【図4】従来技術の石炭粉砕装置の一例を示す図。FIG. 4 is a diagram showing an example of a conventional coal crusher.

【符号の説明】[Explanation of symbols]

1…粉砕装置本体 2…注水管 3…注水孔 4…加圧装置 5…熱電対 6…上部固定輪 7…粉砕用ボ−ル 8…給炭管 …下部転輪 10…演算装置 11…分級器 12…旋回羽根 13…微粉炭管 14…CRT画面 15…駆動装置 16…注水器 17…空気口 18…弁 19…注水ポンプ 20…管壁温度検出信号 21…管壁温度設定信号 DESCRIPTION OF SYMBOLS 1 ... Pulverizer main body 2 ... Injection pipe 3 ... Injection hole 4 ... Pressurizer 5 ... Thermocouple 6 ... Upper fixed wheel 7 ... Pulverizing ball 8 ... Coal supply pipe 9 ... Lower wheel 10 ... Computing device 11 ... Classifier 12 ... Swirl vane 13 ... Pulverized coal pipe 14 ... CRT screen 15 ... Driver 16 ... Water injector 17 ... Air port 18 ... Valve 19 ... Injection pump 20 ... Tube wall temperature detection signal 21 ... Tube wall temperature setting signal

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B02C 15/00 - 15/16 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 7 , DB name) B02C 15/00-15/16

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】石炭を粉砕部に供給する給炭管の上部に、
注水ポンプおよび注水弁を介して供給される注水を前記
給炭管の内壁面に流下させる注水孔を設けた石炭粉砕装
置において前記給炭管管壁温度を検出する管壁温度
検出器を設け、該管壁温度検出器からの管壁温度検出信
号と予め設定した管壁温度設定信号との比較結果に基づ
いて前記注水弁の開度を制御する演算装置を設けたこと
を特徴とする石炭粉砕装置。
1. An upper part of a coal feed pipe for supplying coal to a pulverizing section,
Wherein the water injection is supplied via a water injection pump and injection valve
Oite coal pulverizer provided with a water injection hole for flow down the inner wall surface of the coal feed pipe, the tube wall temperature detector for detecting the wall temperature of the Kyusumikan provided, the tube wall from the tube wall temperature detector coal pulverizer characterized in that a computing device for controlling the opening of the water injection valve based on the comparison result between the tube wall temperature setting signal preset temperature detection signal.
【請求項2】石炭を粉砕部に供給する給炭管の内壁面に
石炭付着防止用の注水を行う石炭粉砕装置の注水量制御
方法において、前記給炭管管壁温度に基づいて前記
水量を制御することを特徴とする石炭粉砕装置の注水量
制御方法。
2. An inner wall surface of a coal feed pipe for supplying coal to a pulverizing section.
Water injection amount control of the coal pulverizer for performing injection of coal antiadhesive
In the method, the water injection amount control method of the coal mill, characterized by controlling the water injection amount based on the wall temperature of the Kyusumikan.
【請求項3】請求項2に記載の石炭粉砕装置の注水量制3. The amount of water injected into the coal crusher according to claim 2.
御方法において、前記管壁温度を正常時の管壁温度と比In the control method, the tube wall temperature is compared with a normal tube wall temperature.
較して、大の場合には前記注水量を増加させ、小の場合In comparison, when the size is large, the amount of water injection is increased.
には前記注水量を減少させることを特徴とする石炭粉砕Coal grinding characterized by reducing the amount of water injected
装置の注水量制御方法。How to control the amount of water injected into the device.
JP04071256A 1992-03-27 1992-03-27 Coal crusher and water injection control method thereof Expired - Fee Related JP3115687B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04071256A JP3115687B2 (en) 1992-03-27 1992-03-27 Coal crusher and water injection control method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04071256A JP3115687B2 (en) 1992-03-27 1992-03-27 Coal crusher and water injection control method thereof

Publications (2)

Publication Number Publication Date
JPH05269394A JPH05269394A (en) 1993-10-19
JP3115687B2 true JP3115687B2 (en) 2000-12-11

Family

ID=13455456

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04071256A Expired - Fee Related JP3115687B2 (en) 1992-03-27 1992-03-27 Coal crusher and water injection control method thereof

Country Status (1)

Country Link
JP (1) JP3115687B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100504373B1 (en) * 2000-12-29 2005-07-29 주식회사 포스코 Apparatus for controlling the temperature in the mill by using the fogging sprayer
KR100941483B1 (en) * 2003-05-02 2010-02-10 주식회사 포스코 Apparatus for spalling lump ore of caustic lime kiln
CN105750022B (en) * 2016-03-16 2017-12-26 南京博沃科技发展有限公司 A kind of medium-speed pulverizer of the grey desulfurizing device containing drop
JP7348778B2 (en) * 2019-09-04 2023-09-21 川崎重工業株式会社 Vertical roller mill

Also Published As

Publication number Publication date
JPH05269394A (en) 1993-10-19

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