JP2711774B2 - Operating method of vertical mill - Google Patents

Operating method of vertical mill

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Publication number
JP2711774B2
JP2711774B2 JP18023892A JP18023892A JP2711774B2 JP 2711774 B2 JP2711774 B2 JP 2711774B2 JP 18023892 A JP18023892 A JP 18023892A JP 18023892 A JP18023892 A JP 18023892A JP 2711774 B2 JP2711774 B2 JP 2711774B2
Authority
JP
Japan
Prior art keywords
raw material
rotary table
material layer
power value
set range
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
Application number
JP18023892A
Other languages
Japanese (ja)
Other versions
JPH05329392A (en
Inventor
敏光 末原
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.)
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 JP18023892A priority Critical patent/JP2711774B2/en
Publication of JPH05329392A publication Critical patent/JPH05329392A/en
Application granted granted Critical
Publication of JP2711774B2 publication Critical patent/JP2711774B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • 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】本発明は回転テーブルと粉砕ロー
ラとの協働により,石灰石,スラグ,クリンカ,セメン
ト原料や化学品などの原料を粉砕する竪型粉砕機の運転
方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of operating a vertical grinder for grinding raw materials such as limestone, slag, clinker, cement raw materials and chemicals by cooperation of a rotary table and a grinding roller.

【0002】[0002]

【従来の技術】石灰石やスラグ,セメント原料などの原
料を細かく粉砕し粉体とする粉砕機の一種として,図6
に示すように,回転テーブルと粉砕ローラとを備えた竪
型粉砕機1が広く用いられている。この種の粉砕機は,
円筒状ケーシング15の下部において定速モータ2Kに
より減速機2で駆動されて低速回転する円盤状の回転テ
ーブル3Aと,その上面外周部を円周方向へ等分する箇
所に油圧などで圧接されて従動回転する複数個の粉砕ロ
ーラ4とを備えている。
2. Description of the Related Art As one type of crusher for finely pulverizing raw materials such as limestone, slag, and cement raw material into powder, FIG.
As shown in FIG. 1, a vertical pulverizer 1 having a rotary table and a pulverizing roller is widely used. This kind of crusher is
A disk-shaped rotary table 3A, which is driven by the speed reducer 2 by the constant speed motor 2K and is rotated at a low speed at the lower portion of the cylindrical casing 15, is pressed against a portion equally dividing the outer peripheral portion of the upper surface in the circumferential direction by hydraulic pressure or the like. And a plurality of crushing rollers 4 that are driven and rotated.

【0003】粉砕ローラ4はケーシング15に回転軸6
によって揺動自在に軸支されたアーム5とアーム7を介
して油圧シリンダ9のピストンロッド10に連結されて
おり,油圧シリンダ9を作動させることにより,粉砕ロ
ーラ4を回転テーブル3A上に押圧して原料への粉砕圧
力を与えている。3Bは回転テーブル3Aの外周縁に設
けられ原料層厚を調整するダムリング,14は回転テー
ブル3A周囲のガス吹上用環状空間通路,14Aはガス
供給路,13は羽根13Aにより粉砕された原料を分級
する回転セパレータ,16はガスと共に製品を取出す排
出口,17は原料投入シュートである。
The crushing roller 4 has a rotating shaft 6
The arm 5 is pivotally supported by an arm 5 and is connected to a piston rod 10 of a hydraulic cylinder 9 via an arm 7. By operating the hydraulic cylinder 9, the grinding roller 4 is pressed onto the rotary table 3 </ b> A. To give the grinding pressure to the raw material. 3B is a dam ring provided on the outer periphery of the rotary table 3A to adjust the thickness of the raw material layer, 14 is an annular space passage for gas blowing around the rotary table 3A, 14A is a gas supply path, and 13 is a raw material pulverized by the blade 13A. A rotary separator for classification, 16 is an outlet for taking out the product together with the gas, and 17 is a raw material input chute.

【0004】このような竪型粉砕機において,回転テー
ブルの中央部へ原料投入シュート17で供給された原料
は,回転テーブル3Aの回転によりテーブル半径方向の
遠心力を受けて回転テーブル3A上を滑るときに回転テ
ーブル3Aにより回転方向の力を受け,回転テーブル3
Aとの間で滑って回転テーブル3Aの回転数よりいくら
か遅い回転を行なう。以上2つの力,すなわち,半径方
向と回転方向の力とが合成され,原料は回転テーブル3
A上を渦巻状の軌跡を描いて回転テーブル3Aの外周部
へ移動する。この外周部には,ローラが圧接されて回転
しているので,渦巻線を描いた原料は粉砕ローラ4と回
転テーブル3Aとの間へローラ軸方向とある角度をなす
方向から進入して噛込まれて粉砕される。
In such a vertical pulverizer, the raw material supplied to the center of the rotary table by the raw material charging chute 17 receives the centrifugal force in the table radial direction by the rotation of the rotary table 3A and slides on the rotary table 3A. When a force in the rotating direction is received by the rotating table 3A,
A slides with A and makes a rotation somewhat slower than the rotation speed of the turntable 3A. The above two forces, that is, the force in the radial direction and the force in the rotational direction are synthesized, and the raw material is
A moves to the outer periphery of the turntable 3A in a spiral locus on A. Since a roller is pressed against this outer peripheral portion and rotated, the raw material describing the spiral enters the crushing roller 4 and the rotary table 3A from a direction forming an angle with the roller axis direction and is caught. Rarely crushed.

【0005】一方,ケーシング15の基部にはグクトに
よって空気,あるいは熱風などのガスが導かれており,
このガスが回転テーブル3Aの外周面とケーシングの内
周面との間の環状空間部14から吹き上がることによ
り,粉砕された微粉体はガスに同伴されてケーシング1
5内を上昇し,上部に位置するセパレータ13の羽根1
3Aにより分級作用を受け,所定粒度の製品はガスと共
に排出口16から排出され次の工程へ送られる。
On the other hand, a gas such as air or hot air is guided to the base of the casing 15 by guguto.
This gas blows up from the annular space 14 between the outer peripheral surface of the turntable 3A and the inner peripheral surface of the casing, so that the pulverized fine powder accompanies the gas and the casing 1
5, the blades 1 of the separator 13 located above.
The product having the predetermined particle size is subjected to the classification action by 3A, and is discharged together with the gas from the outlet 16 and sent to the next step.

【0006】[0006]

【発明が解決しようとする課題】上記のごとき従来の竪
型粉砕機においては,粉砕機内へ投入する原料の供給量
は竪型粉砕機へ導入されるガスの入口側圧力と出口側圧
力との差圧が一定となるように制御されており,運転中
の回転テーブル上の原料層厚とは無関係であった。とこ
ろが,竪型粉砕機においては,粉砕される原料の種類と
原料供給量と粉砕ローラの緊張油圧と回転テーブル上の
原料層厚には密接な関係があり,粉砕産物の粉末度を所
望の粉末度に維持しつつ,かつ,竪型粉砕機の処理能力
をその型番で可能なかぎり向上し,その結果極めて低い
電力原単位を達成するという粉砕効率の高い運転を実施
するためには,竪型粉砕機の主動力機である回転テーブ
ル駆動用の電動機を,許容する定格出力で常時使用する
ことが必須である。そのうえさらに安定連続運転を継続
するためには,粉砕中の原料の種類に適合した原料層厚
で粉砕を持続することが重要である。しかしながら,電
力値と原料層厚という刻々の実測値を監視しながらこれ
らを望ましい設定範囲に維持するために竪型粉砕機の各
粉砕条件を変更し制御するという運転方法はこれまで十
分に確立されていなかった。
In the conventional vertical crusher as described above, the amount of the raw material supplied into the crusher depends on the inlet pressure and the outlet pressure of the gas introduced into the vertical crusher. The differential pressure was controlled to be constant, and was independent of the thickness of the raw material layer on the rotating table during operation. However, in a vertical mill, there is a close relationship between the type of raw material to be ground and the amount of raw material supplied, the tension hydraulic pressure of the grinding roller, and the thickness of the raw material layer on the rotary table. In order to perform the operation with high grinding efficiency while maintaining the temperature at the same time and improving the processing capacity of the vertical grinding machine as much as It is essential to always use the rotating table drive motor, which is the main power unit of the crusher, with an allowable rated output. In addition, in order to maintain stable and continuous operation, it is important to continue grinding with a raw material layer thickness suitable for the type of raw material being ground. However, the operation method of changing and controlling each crushing condition of the vertical crusher so as to maintain the desired set range while monitoring the instantaneous measured values of the power value and the raw material layer thickness has been well established. I didn't.

【0007】[0007]

【課題を解決するための手段】以上の課題を解決するた
めに,本発明においては,原料輸送用の可変速コンスタ
ントフィード・ウェアを備え,可変速の回転テーブルを
有し,かつ,原料層厚を測定するレーザ変位計とプログ
ラマブル操作器を備えた竪型粉砕機において,運転中の
回転テーブル駆動用の可変速電動機の出力電力値ならび
に原料層厚の実測値を予め設定した設定範囲と比較し,
電力値が設定範囲に達しないときにはその不足量に比例
して原料供給量を増加するとともに原料供給増加比率に
見合う回転テーブル回転数の増加を行ない,電力値が設
定範囲を超過するときには,その超過量に逆比例して原
料供給量を減少するとともに原料供給減少比率に見合う
回転テーブル回転数の減少を行ない,電力値が設定範囲
内で,かつ,原料層厚が設定範囲より低いとき粉砕ロー
ラの緊張油圧を低減するか,および/または回転テーブ
ル回転数を減少し,電力値が設定範囲内で,かつ,原料
層厚が設定範囲より高いとき粉砕ローラの緊張油圧を増
加するか,および/または回転テーブル回転数を増加
し,電力値および原料層厚がともに設定範囲内にあると
きにはこれまでの運転状態を維持するという運転方法を
採用した。
In order to solve the above problems, the present invention comprises a variable-speed constant feed ware for transporting raw materials, a variable-speed rotary table, and a raw material layer thickness. In a vertical pulverizer equipped with a laser displacement gauge and a programmable actuator for measuring the output, the output power value of the variable speed motor for driving the rotary table during operation and the measured value of the raw material layer thickness are compared with the preset setting range. ,
When the electric power value does not reach the set range, the raw material supply amount is increased in proportion to the shortage, and the rotation speed of the turntable is increased in proportion to the raw material supply increase ratio. The amount of raw material supplied is reduced in inverse proportion to the amount, and the number of revolutions of the rotary table is reduced in proportion to the raw material supply reduction ratio. When the power value is within the set range and the raw material layer thickness is lower than the set range, the grinding roller Reducing the tension hydraulic pressure and / or reducing the rotation speed of the rotary table, and increasing the tension hydraulic pressure of the grinding roller when the power value is within the set range and the raw material layer thickness is higher than the set range, and / or An operation method was adopted in which the number of revolutions of the turntable was increased, and when the electric power value and the thickness of the raw material layer were both within the set ranges, the operation state was maintained.

【0008】[0008]

【作用】本発明の竪型粉砕機の運転方法においては,刻
々測定される運転中の回転テーブル駆動用(ミル用)の
可変速電動機の電力値と原料層厚の実測値がプログラマ
ブル操作器へ入力され,粉砕原料の種類および使用して
いる竪型粉砕機の型番を考慮して設定された所望の電力
値と原料層厚を維持するように,緊張油圧や原料供給量
やミル用電動機の回転数(すなわち,回転テーブルの回
転数)を制御する。
In the operation method of the vertical crusher according to the present invention, the power value of the variable speed motor for driving the rotary table (for the mill) and the actually measured value of the raw material layer thickness which are measured every moment are supplied to the programmable actuator. The tension hydraulic pressure, the amount of raw material supplied, and the electric motor The number of revolutions (that is, the number of revolutions of the turntable) is controlled.

【0009】[0009]

【実施例】以下図面に基づいて本発明の実施例について
詳細に説明する。図1〜図5は本発明の実施例に係り,
図1は竪型粉砕機のフローシート,図2は竪型粉砕機の
制御ブロック線図,図3は竪型粉砕機の制御系統図,図
4は竪型粉砕機の要部縦断面図,図5はレーザ変位計の
原理図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the drawings. 1 to 5 relate to an embodiment of the present invention.
1 is a flow sheet of a vertical crusher, FIG. 2 is a control block diagram of the vertical crusher, FIG. 3 is a control system diagram of the vertical crusher, FIG. FIG. 5 is a principle diagram of the laser displacement meter.

【0010】図において,1は竪型粉砕機,2Aは回転
テーブル駆動用の可変速電動機,2Bは可変速電動機2
A用のコントローラ,9Aは粉砕ローラ4緊張用の油圧
シリンダ9の油圧ユニット,60は原料コンベヤ,70
は原料ホッパ,80はコンスタントフィード・ウェア,
80aは同用可変速電動機,80bはコンスタントフィ
ード・ウェア80の秤量機,90は集塵装置,100は
吸引ファン,130はレーザ変位計,150はプログラ
マブル操作器であり,プログラマブル操作器150に
は,図2に示すように,内部に比較器,設定器,制御器
(調節器と操作器),増幅器が収納されている。竪型粉
砕機1本体の各機器は従来技術で説明したとおりのもの
であり,その説明を省略する。
In the drawing, 1 is a vertical mill, 2A is a variable speed motor for driving a rotary table, and 2B is a variable speed motor 2
Controller A, 9A is a hydraulic unit of the hydraulic cylinder 9 for tensioning the crushing roller 4, 60 is a raw material conveyor, 70
Is raw material hopper, 80 is constant feed wear,
80a is the same variable speed motor, 80b is a weighing machine of the constant feedware 80, 90 is a dust collector, 100 is a suction fan, 130 is a laser displacement meter, 150 is a programmable operation device, and 150 is a programmable operation device. As shown in FIG. 2, a comparator, a setting device, a controller (a controller and an operating device), and an amplifier are housed therein. Each device of the main body of the vertical crusher 1 is as described in the prior art, and the description thereof will be omitted.

【0011】次にレーザ変位計130について説明する
と,図4,図5に示すように,粉砕ローラ4に接続され
る油圧シリンダ9のピストンロッド9aにはサポートを
介して測定板90が固設され,この測定板90に対向し
てレーザ変位計130が油圧シリンダ90の側面に取付
けられ,刻々変化する原料層厚Bに対応する距離Aが測
定される。図5はレーザ変位計130の原理を示したも
ので,センサ部の光源からのレーザ光が測定板90へ斜
めに入射し,測定板90の表面で反射した後集光レンズ
を通過してイメージセンサへ結像する。測定範囲Wを移
動する測定板の位置に応じてイメージセンサ上の結像も
移動し,これをイメージセンサドライバでキャッチして
電気信号の形で表示部へ送られディジタルまたはアナロ
グの出力信号がプログラマブル操作器150へ伝送され
る。
Next, a description will be given of the laser displacement meter 130. As shown in FIGS. 4 and 5, a measuring plate 90 is fixed to a piston rod 9a of a hydraulic cylinder 9 connected to the crushing roller 4 via a support. A laser displacement gauge 130 is attached to the side surface of the hydraulic cylinder 90 so as to face the measuring plate 90, and a distance A corresponding to the raw material layer thickness B that changes every moment is measured. FIG. 5 shows the principle of the laser displacement meter 130. The laser light from the light source of the sensor section is obliquely incident on the measuring plate 90, is reflected on the surface of the measuring plate 90, and then passes through the condensing lens. An image is formed on the sensor. The image formed on the image sensor also moves in accordance with the position of the measurement plate moving in the measurement range W. This is caught by the image sensor driver and sent to the display unit in the form of an electric signal, and the digital or analog output signal is programmable. It is transmitted to the operation device 150.

【0012】次に,プログラマブル操作器150の作動
について説明する。図2に示すように,タイマで設定さ
れた時間間隔毎に刻々測定されるミル用可変速電動機電
力計2Cおよびレーザ変位計130の測定結果が電気信
号に変換されてプログラマブル操作器150へ入力され
る。この2つの情報(電力値と原料層厚)と予め設定器
に入力されている設定値とを比較器で比較し,設定値の
範囲を逸脱している場合には,制御器を介して粉砕ロー
ラに負荷する油圧力を変更して電力値と原料層厚の改善
を図り,次いで可変速電動機2Aの回転数を制御して回
転テーブル3Aの回転数を増減する。設定値には基準電
力値,基準原料層厚を入れておく。制御器は調節器と操
作器とから構成され,調節器は電力値や原料層厚の測定
値と設定値との差異に応じて緊張油圧やコンスタントフ
ィード・ウェア駆動用可変速電動機の回転数や回転テー
ブル駆動用(ミル用)可変速電動機の回転数の増減の幅
を指示するもので,その制御動作には比例動作(P動
作),積分動作(I動作),微分動作(D動作),比例
積分動作(PI動作),比例微分動作(PD動作)等,
原料水分の変化の状況に応じて使い分けることができ
る。なお,原料供給量はコンスタントフィード・ウェア
80の秤量機80bの測定値を時間単位に積算すること
により得られる。上記の基準電力値や基準原料層厚は1
点でなく,ある幅を持たせたもので,電力値の場合は定
格の上下10%までとし,原料層厚は原料の種類,型
番,粉末度を考慮し決定する。
Next, the operation of the programmable controller 150 will be described. As shown in FIG. 2, the measurement results of the variable speed motor wattmeter 2C for mill and the laser displacement meter 130, which are measured every time interval set by the timer, are converted into electric signals and input to the programmable controller 150. You. These two information (power value and raw material layer thickness) are compared with a set value input to the setter in advance by a comparator, and if the set value is out of the range, it is crushed via the controller. The power value and the raw material layer thickness are improved by changing the oil pressure applied to the rollers, and then the rotation speed of the variable speed motor 2A is controlled to increase or decrease the rotation speed of the turntable 3A. The reference power value and reference material layer thickness are set in the set values. The controller is composed of a controller and an operating device. The controller adjusts the tension and the speed of the variable speed motor for driving the constant feed wear according to the difference between the set value and the measured value of the electric power value or raw material layer thickness. It instructs the range of increase / decrease of the number of revolutions of the variable speed motor for driving the rotary table (for the mill). The control operation includes proportional operation (P operation), integration operation (I operation), differentiation operation (D operation), Proportional integration operation (PI operation), proportional differentiation operation (PD operation), etc.
It can be used properly according to the situation of the change of the raw material moisture. The raw material supply amount is obtained by integrating the measured values of the weighing machine 80b of the constant feed ware 80 in units of time. The above reference power value and reference material layer thickness are 1
It is not a point but a certain width. In the case of power value, it is up to 10% above and below the rating, and the thickness of the raw material layer is determined in consideration of the type, model number, and fineness of the raw material.

【0013】操作器はこの調節器からの指示に基づいて
油圧ユニット9Aまたは可変速電動機2Aや可変速電動
機80aへ動作指令を伝達する。図中の矢印のついた線
は信号の流れを示す。
The operating device transmits an operation command to the hydraulic unit 9A or the variable speed motor 2A or the variable speed motor 80a based on an instruction from the controller. The line with the arrow in the figure indicates the signal flow.

【0014】これらのプログラマブル操作器150の制
御系統の流れは,図3に示すとおりである。すなわち,
運転中タイマによって指示された時間間隔で,ミル用可
変速電動機2Aの電力値と原料層厚が測定され,電力値
が設定範囲以下のときにはその不足量に比例して予め設
定器に入力した比率で原料供給量を増加するとともにこ
れに見合って原料層厚が増加しないようミル用可変速電
動機2Aの回転数を追従増加し原料層厚をもとの高さに
維持する。一方,電力値が設定範囲以上となり過負荷の
状態になったとき安定運転が危惧されるので,その超過
量に逆比例して予め定められた比率にしたがって原料供
給量を低減し,ミル用可変速電動機2Aの回転数を追従
減少し原料層厚を維持する。このようにして,電力値が
設定範囲内にあり原料層厚が設定範囲より低いときには
緊張油圧を予め定めた比率にしたがって低減し,タイマ
で設定した時間後に再び原料層厚の実測値と設定範囲を
比較し,それでもなお低いときには回転テーブルの回転
数を減少する。逆に原料層厚が設定範囲より高いときに
は緊張油圧を増加したあと,タイマ設定時間後に同様に
実測値と設定範囲を比較して,なお高いときには回転テ
ーブルの回転数を増加する。電力値も原料層厚もともに
設定範囲内のときにはそのまま運転を続行する。
The flow of the control system of the programmable controller 150 is as shown in FIG. That is,
The power value and raw material layer thickness of the variable speed electric motor for mill 2A are measured at the time intervals specified by the timer during operation, and when the power value is below the set range, the ratio input to the setter in advance in proportion to the shortage. Then, the rotation speed of the variable speed electric motor for mill 2A is increased to keep the raw material layer thickness at the original height so that the raw material supply amount is increased and the raw material layer thickness is not increased accordingly. On the other hand, when the power value exceeds the set range and the system is overloaded, stable operation is feared. Therefore, the amount of raw material supplied is reduced in inverse proportion to the excess amount according to a predetermined ratio, and the mill speed is reduced. The number of rotations of the electric motor 2A is reduced to maintain the thickness of the raw material layer. In this way, when the electric power value is within the set range and the raw material layer thickness is lower than the set range, the tension oil pressure is reduced according to a predetermined ratio, and after the time set by the timer, the actual measured value of the raw material layer thickness and the set range are again set. And if it is still low, reduce the number of revolutions of the turntable. Conversely, when the raw material layer thickness is higher than the set range, the tension oil pressure is increased, and after the timer set time, the measured value is similarly compared with the set range. When both the electric power value and the raw material layer thickness are within the set ranges, the operation is continued as it is.

【0015】このようにして,動作変更したあとタイマ
による一定時間経過後,再び電力値やレーザ変位計13
0による原料層厚測定値と設定値とを比較し,設定値を
越えたときには上に述べた操作を繰返す。電力値の設定
値は前述のように定格値のプラスマイナス10%程度と
し,原料層厚の設定値は原料の種類や粉砕機の型番,製
品粒度によって異なり一概に決められないが,軟い原料
や型番の大きな粉砕機,製品粒度の粗いときほど設定層
厚は大きくなる。運転実績やテストランによって状況を
把握し適正な値を選定するとよい。
In this way, after the operation is changed, after the elapse of a certain time by the timer, the electric power value and the laser displacement
The measured value of the raw material layer thickness according to 0 is compared with the set value, and when the set value is exceeded, the above operation is repeated. As described above, the set value of the electric power value is about ± 10% of the rated value, and the set value of the raw material layer thickness depends on the type of raw material, the model of the crusher, and the product particle size, and cannot be determined unconditionally. The set layer thickness increases as the size of the pulverizer or the size of the product increases. It is advisable to grasp the situation based on operation results and test runs and select an appropriate value.

【0016】以上のようなフィードバック機構を有する
自動制御を実施することにより,電力値が急に増大した
り,運転中に供給原料の含有水分が急に低下(または増
大)して粉砕効率が低下したり,噛込みが悪くなってミ
ル振動が増大した状態になっても,上記の操作によって
原料供給量や原料層厚が改善され,原料の噛込みが再び
良くなってもとの安定した運転状態にもどすことができ
る。
By performing the automatic control having the above-described feedback mechanism, the power value increases suddenly, or the water content of the feed material suddenly decreases (or increases) during operation, and the grinding efficiency decreases. Even if the milling vibrations increase due to poor biting, the above operation improves the raw material supply amount and the raw material layer thickness, and the raw material bite is improved again to maintain the stable operation. You can return to the state.

【0017】[0017]

【発明の効果】以上の説明から明らかなように,本発明
の竪型粉砕機の運転方法では,運転中のミル用可変速電
動機(回転テーブル駆動用)の電力値と原料層厚の実測
値を刻々監視し,各々設定した範囲に収まるように緊張
油圧や原料供給量や回転テーブル回転数を適正に制御す
ることにより,十分な処理能力を得ながら安定連続運転
を実施できる。したがって,運転操作性や生産効率が著
しく向上する。
As is apparent from the above description, in the method of operating the vertical pulverizer of the present invention, the electric power value of the variable speed electric motor for the mill (for driving the rotary table) and the actually measured values of the raw material layer thickness are used. By constantly controlling the tension hydraulic pressure, the raw material supply amount, and the rotation table rotation speed so as to fall within the set ranges, stable continuous operation can be performed while obtaining a sufficient processing capacity. Therefore, driving operability and production efficiency are significantly improved.

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

【図1】本発明の実施例を示す竪型粉砕機のフローシー
トである。
FIG. 1 is a flow sheet of a vertical crusher showing an embodiment of the present invention.

【図2】本発明の実施例に係る竪型粉砕機の制御ブロッ
ク線図である。
FIG. 2 is a control block diagram of a vertical mill according to an embodiment of the present invention.

【図3】本発明の実施例に係る竪型粉砕機の制御系統図
である。
FIG. 3 is a control system diagram of a vertical mill according to an embodiment of the present invention.

【図4】本発明の実施例に係る竪型粉砕機の要部縦断面
図である。
FIG. 4 is a vertical sectional view of a main part of a vertical pulverizer according to an embodiment of the present invention.

【図5】本発明の実施例に係るレーザ変位計の原理図で
ある。
FIG. 5 is a principle diagram of the laser displacement meter according to the embodiment of the present invention.

【図6】従来の竪型粉砕機の全体縦断面図である。FIG. 6 is an overall vertical sectional view of a conventional vertical crusher.

【符号の説明】 1 竪型粉砕機 2 減速機 2A 可変速電動機 2B コントローラ 2C 電力計 2K 定速モータ 3A 回転テーブル 4 粉砕ローラ 5 アーム 6 回転軸 9 油圧シリンダ 9A 油圧ユニット 15 ケーシング 60 原料コンベヤ 70 原料ホッパ 80 コンスタントフィード・ウェア 80a 可変速電動機 80b 秤量機 90 集塵装置 100 吸引ファン 130 レーザ変位計 150 プログラマブル操作器[Description of Signs] 1 Vertical crusher 2 Reducer 2A Variable speed motor 2B Controller 2C Power meter 2K Constant speed motor 3A Rotary table 4 Crush roller 5 Arm 6 Rotary shaft 9 Hydraulic cylinder 9A Hydraulic unit 15 Casing 60 Raw material conveyor 70 Raw material Hopper 80 Constant feed wear 80a Variable speed motor 80b Weighing machine 90 Dust collector 100 Suction fan 130 Laser displacement meter 150 Programmable actuator

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 原料輸送用の可変速コンスタントフィー
ド・ウェアを備え,可変速の回転テーブルの外周部上面
に複数個の回転自在な粉砕ローラを配置し,該粉砕ロー
ラを該回転テーブル上面へ緊張する油圧シリンダを備
え,回転テーブルに供給した原料を回転テーブル上面と
粉砕ローラ周面との間で粉砕する竪型粉砕機であって,
かつ,回転テーブル上の原料層厚を測定するレーザ変位
計およびプログラマブル操作器を備えた竪型粉砕機にお
いて,運転中の回転テーブル駆動用の可変速電動機の出
力電力値ならびに原料層厚の実測値を予め設定した設定
範囲と比較し,電力値が設定範囲に達しないときにはそ
の不足量に比例して原料供給量を増加するとともに原料
供給増加比率に見合う回転テーブル回転数の増加を行な
い,電力値が設定範囲を超過するときには,その超過量
に逆比例して原料供給量を減少するとともに原料供給減
少比率に見合う回転テーブル回転数の減少を行ない,電
力値が設定範囲内で,かつ,原料層厚が設定範囲より低
いとき粉砕ローラの緊張油圧を低減するか,および/ま
たは回転テーブル回転数を減少し,電力値が設定範囲内
で,かつ,原料層厚が設定範囲より高いとき粉砕ローラ
の緊張油圧を増加するか,および/または回転テーブル
回転数を増加し,電力値および原料層厚がともに設定範
囲内にあるときにはこれまでの運転状態を維持する竪型
粉砕機の運転方法。
1. A variable speed constant feed ware for transporting raw materials, a plurality of rotatable crushing rollers arranged on an upper surface of an outer peripheral portion of a variable speed rotary table, and tensioning the crushing roller to the upper surface of the rotary table. A vertical cylinder having a hydraulic cylinder for grinding the raw material supplied to the rotary table between the upper surface of the rotary table and the peripheral surface of the grinding roller.
In a vertical grinding machine equipped with a laser displacement gauge for measuring the thickness of the raw material layer on the rotary table and a programmable controller, the output power value of the variable speed motor for driving the rotary table during operation and the measured value of the raw material layer thickness Is compared with a preset setting range, and when the power value does not reach the setting range, the amount of raw material supplied is increased in proportion to the shortage, and the number of rotations of the rotary table is increased in accordance with the raw material supply increasing ratio. Exceeds the set range, the feed rate is reduced in inverse proportion to the excess amount, and the rotation speed of the turntable is reduced in proportion to the feed rate reduction rate. If the thickness is lower than the set range, reduce the tension oil pressure of the grinding roller and / or reduce the number of revolutions of the rotary table so that the power value is within the set range and When the pressure is higher than the set range, the tension hydraulic pressure of the crushing roller is increased and / or the number of revolutions of the rotary table is increased. When both the electric power value and the raw material layer thickness are within the set range, the vertical operating state is maintained. Operating method of the mold crusher.
JP18023892A 1992-05-29 1992-05-29 Operating method of vertical mill Expired - Lifetime JP2711774B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18023892A JP2711774B2 (en) 1992-05-29 1992-05-29 Operating method of vertical mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18023892A JP2711774B2 (en) 1992-05-29 1992-05-29 Operating method of vertical mill

Publications (2)

Publication Number Publication Date
JPH05329392A JPH05329392A (en) 1993-12-14
JP2711774B2 true JP2711774B2 (en) 1998-02-10

Family

ID=16079786

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18023892A Expired - Lifetime JP2711774B2 (en) 1992-05-29 1992-05-29 Operating method of vertical mill

Country Status (1)

Country Link
JP (1) JP2711774B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102580840A (en) * 2012-03-07 2012-07-18 广西贺州市科隆粉体有限公司 Automatic feeding controller of milling system

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102012106554A1 (en) 2012-07-19 2014-05-15 Thyssenkrupp Resource Technologies Gmbh Method and plant for comminuting regrind with a roller mill
JP7080970B2 (en) * 2018-05-18 2022-06-06 三菱重工業株式会社 Crushing device and control method of crushing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102580840A (en) * 2012-03-07 2012-07-18 广西贺州市科隆粉体有限公司 Automatic feeding controller of milling system

Also Published As

Publication number Publication date
JPH05329392A (en) 1993-12-14

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