JP2673844B2 - Automatic operation method of vertical crusher - Google Patents

Automatic operation method of vertical crusher

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Publication number
JP2673844B2
JP2673844B2 JP3331086A JP33108691A JP2673844B2 JP 2673844 B2 JP2673844 B2 JP 2673844B2 JP 3331086 A JP3331086 A JP 3331086A JP 33108691 A JP33108691 A JP 33108691A JP 2673844 B2 JP2673844 B2 JP 2673844B2
Authority
JP
Japan
Prior art keywords
raw material
value
layer thickness
set value
rotary table
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
JP3331086A
Other languages
Japanese (ja)
Other versions
JPH05104011A (en
Inventor
忠之 古閑
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 JP3331086A priority Critical patent/JP2673844B2/en
Publication of JPH05104011A publication Critical patent/JPH05104011A/en
Application granted granted Critical
Publication of JP2673844B2 publication Critical patent/JP2673844B2/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自動
運転方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an automatic operation method of a vertical crusher for crushing raw materials such as limestone, slag, clinker, cement raw materials and chemicals in cooperation with a rotary table and a pulverizing 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5
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 materials 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,粉砕機の回転テーブル3A上に落
下した原料が首尾よく粉砕ローラ4へ当接して噛込まれ
るためには,原料に適度の摩擦係数が必要であり,表面
がつるつるした滑らかな性状を有する摩擦係数の小さな
原料の場合には粉砕ローラ4を回転テーブル3Aに向け
て強く押し付けても両者の間に介在する原料は脇へ逃げ
て有効な粉砕力を原料に与えることができない。こうし
た摩耗係数の小さな原料は概ね含有水分が少ないので,
予め原料含有水分を適正な値に調整することによって摩
耗係数を上昇させねばならない。こうした原料含有水分
が少なく摩擦係数の小さい原料のうち,特に比較的被粉
砕性の悪い物性を有する原料を超微粉砕する場合には,
ミル振動が頻発することが多く,振動値(振幅)が特に
大きい場合には機器の損傷や運転不能に陥って止むなく
運転休止に追い込まれることがあった。
In the conventional vertical crusher as described above, in order for the raw material dropped onto the rotary table 3A of the crusher to be successfully brought into contact with the crushing roller 4 and to be bitten, the raw material is required. In the case of a material having a small friction coefficient and a smooth and smooth surface, even if the grinding roller 4 is strongly pressed against the rotary table 3A, the material interposed therebetween is not The material cannot escape to the side and give effective crushing power to the raw material. Raw materials with a low wear coefficient generally contain little moisture,
The wear coefficient must be increased by adjusting the moisture content of the raw material to an appropriate value in advance. Among such raw materials with low moisture content and low coefficient of friction, especially when ultrafine grinding is performed on raw materials having relatively poor grindability,
Mill vibration often occurs frequently, and when the vibration value (amplitude) is particularly large, the equipment may be damaged or become inoperable, and the operation may be stopped without stopping.

【0007】このように運転中ミル振動値が通常の値で
ある片振幅50μmよりもはるかに大きな値となり,し
かもこの状態が継続するときには,早急にミル振動値を
低下させるための何らかの措置を講じなければならな
い。その手段としては,たとえば,粉砕機へ供給する原
料を一時的に減少させるとか,ミル通風量を増加させ
る,あるいは,原料に水分を加える,ミル運転を停止す
る等の対応策がとられていた。しかしながら,原料の供
給量減少やミル運転休止は処理能力の低下を招き,ミル
通風量の増加は製品の粒度が粗大化して製品品質が低下
し,水分添加による摩擦係数の改善は製品水分が増加し
て製品品質の悪化を招くなどいずれも2次的な悪影響を
与えることになっていた。本発明の方法においては,運
転中大きな振動が発生しても,自動的にかつ簡便に遠隔
操作でこれを低減する操作を行なおうとするものであ
る。
As described above, during the operation, the mill vibration value becomes much larger than the normal value of the half amplitude of 50 μm, and when this state continues, some measures are taken to reduce the mill vibration value immediately. There must be. As measures for this, for example, countermeasures such as temporarily reducing the amount of raw material supplied to the crusher, increasing the amount of air flowing through the mill, adding water to the raw material, and stopping the operation of the mill have been taken. . However, a decrease in the supply of raw materials and a stoppage of the mill operation lead to a decrease in the processing capacity. An increase in the amount of air flow through the mill results in a coarsening of the product particle size, resulting in a decrease in the product quality. All of these have a secondary adverse effect, for example, resulting in deterioration of product quality. In the method of the present invention, even if a large vibration is generated during operation, an operation to reduce the large vibration is automatically and simply performed by remote control.

【0008】[0008]

【課題を解決するための手段】以上のような課題を解決
するために,本発明の竪型粉砕機の自動運転方法におい
ては,原料を輸送する秤量機を具備した可変速のコンス
タントフィード・ウェアを備え,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へ押圧する油圧手段を備え,回
転テーブル中央部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,
ケーシングに振動計を装着するとともに,運転中におけ
る回転テーブルと粉砕ローラ間の原料層厚を測定する層
厚計を備え,前記油圧手段の油圧力を変更し,前記コン
スタントフィード・ウェアの供給量を増減する制御装置
を備えた竪型粉砕機において,運転中刻々測定される振
動計および層厚計の指示値と予め設定した設定値とを比
較し,前記油圧手段の油圧力や前記コンスタントフィー
ド・ウェアの原料供給量を次の各工程の操作手順により
調整する竪型粉砕機の自動運転方法とした。 振動計の指示値と設定値とを比較し,指示値が設定
値よりも大きいとき層厚計の指示値と設定値(原料層厚
適正範囲)とを比較し,原料層厚指示値が設定値を下回
るとき,その程度に応じて油圧力を減少させる第1工程 振動計の指示値が設定値よりも大きく,かつ,原料
層厚指示値が設定値を上回るとき,その程度に応じて油
圧力を増加させる第2工程 振動計の指示値が設定値より大きく,かつ,原料層
厚指示値が設定範囲内のとき,原料供給量を減少させる
第3工程 振動計の指示値が設定値よりも小さく,かつ,原料
供給量の指示値が定格原料供給量を下回るとき,原料供
給量を増加する第4工程 振動計の指示値が設定値よりも小さく,かつ,原料
供給量の指示値が定格原料供給量を上回るとき,現状の
油圧力ならびに原料供給量を保持する第5工程
In order to solve the above problems, in the method for automatically operating a vertical crusher according to the present invention, a variable speed constant feed ware equipped with a weighing machine for transporting raw materials is used. And a plurality of rotatable crushing rollers arranged on the upper surface of the outer periphery of the rotary table, and a hydraulic means for pressing the crushing rollers against the rotary table. A vertical crusher that crushes between the crushing roller and the peripheral surface,
The casing is equipped with a vibrometer and is equipped with a bed thickness gauge for measuring the material bed thickness between the rotary table and the crushing roller during operation. The hydraulic pressure of the hydraulic means is changed to adjust the supply amount of the constant feed ware. In a vertical crusher equipped with a control device that increases and decreases, the indicated values of the vibrometer and layer thickness meter, which are measured every moment during operation, are compared with preset values, and the oil pressure of the hydraulic means and the constant feed The vertical crusher was automatically operated by adjusting the raw material supply amount of the ware according to the operation procedure of each of the following steps. The indicated value of the vibrometer is compared with the set value, and when the indicated value is larger than the set value, the indicated value of the layer thickness meter is compared with the set value (the proper range of the raw material layer thickness) to set the raw material layer indicated value. When the value is below the value, the first step of decreasing the oil pressure according to the degree is greater than the set value of the vibrometer, and when the raw material layer thickness indication value is above the set value, the oil pressure is reduced according to the degree. 2nd step to increase the pressure When the indicated value of the vibrometer is larger than the set value and the raw material layer thickness indicated value is within the set range, the 3rd step to decrease the feed rate of the raw material is less than the set value. Is smaller than the rated feedstock feed rate and the raw material feedrate is less than the set value. Maintains the current hydraulic pressure and raw material supply when the rated raw material supply is exceeded The fifth step to do

【0009】[0009]

【作用】本発明の竪型粉砕機の自動運転方法において
は,竪型粉砕機のケーシングに装着した振動計で計測さ
れる振動値と運転中の回転テーブルと粉砕ローラ間の原
料層厚を測定する層厚計の計測値とを,各々予め設定さ
れた振動値や基準層厚値(基準層厚範囲)と比較して,
適正な振動値を越えたりあるいは基準層厚範囲を逸脱し
たときに制御装置により指令を発して,粉砕ローラの油
圧手段の油圧力を変更して原料層厚の不適正に起因する
振動発生現象を抑制し鎮静化する。また,原料層厚が適
正範囲であるにも拘らず振動レベルが設定値以上に高い
ときには止むを得ず一時的に原料供給量を減らすが,振
動が基準値以下に収まれば原料供給量を増加して元の状
態に復帰する。
In the automatic operation method of the vertical crusher of the present invention, the vibration value measured by the vibrometer attached to the casing of the vertical crusher and the raw material layer thickness between the rotating table and the crushing roller during operation are measured. The measured value of the layer thickness gauge to be compared with the preset vibration value and reference layer thickness value (reference layer thickness range),
When the vibration exceeds the appropriate vibration value or deviates from the reference layer thickness range, a command is issued by the control device to change the hydraulic pressure of the hydraulic means of the crushing roller to prevent the occurrence of vibration due to the inadequate raw material layer thickness. Suppress and calm. Moreover, although the material layer thickness is within the proper range, when the vibration level is higher than the set value, it is unavoidable to temporarily reduce the raw material supply amount, but if the vibration falls below the reference value, the raw material supply amount increases. Then it returns to the original state.

【0010】[0010]

【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4は本発明の実施例に係る竪
型粉砕機を示し,図1はフローシート,図2は制御装置
のブロック線図,図3は制御系統図,図4は層厚計の概
略説明用縦断面図である。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,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は層厚計,14
0は振動計,150は制御装置であり,制御装置150
には,図2に示すように,内部に設定器,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。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the drawings. 1 to 4 show a vertical pulverizer according to an embodiment of the present invention, FIG. 1 is a flow sheet, FIG. 2 is a block diagram of a control device, FIG. 3 is a control system diagram, and FIG. It is a longitudinal section for outline explanation. In the figure, 1 is a vertical crusher, 2A is a variable speed electric motor for driving a rotary table, 60 is a raw material conveyor, 70 is a raw material hopper, 80 is constant feed ware, 80a is a variable speed electric motor for the same, and 80b is the same.
Is a constant feed ware 80 weighing machine, 90 is a dust collector, 100 is a suction fan, 130 is a layer thickness gauge, 14
0 is a vibrometer, 150 is a control device, and the control device 150
As shown in FIG. 2, a setter, a controller (regulator and operator), and an amplifier are housed inside. Vertical crusher 1
Each device of the main body is as described in the related art, and its description is omitted.

【0011】次に層厚計130について説明すると,図
4に示すように,運転中刻々変動する原料層厚の変化に
対応して上下動する粉砕ローラ4の動きを回転軸6回り
に回動するアーム5の動きとして把握し,その変位は変
位変換器として,たとえば,差動変圧器を応用した層厚
計130で測定する。すなわち,図に示すように1次コ
イルEと2次コイルA,Bとの間に磁性体で作られたコ
アCを入れ,1次コイルAに一定の交流電圧Eを励磁
しておき,アーム5とロッドRを介して連結して前後進
させると,コアCの移動によって2次コイルAと2次コ
イルBに対するリアクタンスが変化し,両者の誘起電圧
とEに差を生じて出力電位差Eが得られ,これ
よりコアCの変位が測定できる。
Next, the layer thickness meter 130 will be described. As shown in FIG. 4, the movement of the pulverizing roller 4 which moves up and down in response to a change in the material layer thickness that fluctuates during operation is rotated about the rotation axis 6. The displacement is measured by a layer thickness gauge 130 to which a differential transformer is applied, for example, as a displacement converter. That is, as shown in the figure, a core C made of a magnetic material is inserted between the primary coil E and the secondary coils A and B, and a constant AC voltage E P is excited in the primary coil A, When the arm 5 and the rod R are connected and moved forward and backward, the reactance with respect to the secondary coil A and the secondary coil B changes due to the movement of the core C, and a difference occurs between the induced voltages E A and E B of the two. The output potential difference E O is obtained, and the displacement of the core C can be measured from this.

【0012】次に,制御装置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振動計140および層厚計130,
秤量機80bの測定結果が電気信号に変換されて制御装
置150へ入力される。この3つの情報(振動値と原料
層厚と原料供給量)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油圧シリンダ9(図5に図示)の
油圧ユニット(図示せず)を制御して粉砕ローラ4の押
圧力(油圧力)を増減する。設定値には基準振動レベ
ル,基準原料層厚ならびに定格回転数(コンスタントフ
ィード・ウェア駆動用可変速電動機)を入れておく。制
御器は調節器と操作器とから構成され,調節器は振動値
や原料層厚の測定値と設定値との差異に応じて油圧シリ
ンダ9の油圧力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。調節器は,以上のほか,振動
の設定値に対する測定値の越え方に応じて原料供給量を
減少させる幅を指示する役割も有する。
Next, the operation of the control device 150 will be described. As shown in FIG. 2, the vibrometer 140 and the layer thickness meter 130, which are measured at every time interval set by the timer,
The measurement result of the weighing machine 80b is converted into an electric signal and input to the control device 150. The three pieces of information (vibration value, raw material layer thickness, and raw material supply amount) are compared with set values input to the setter in advance by a comparator. The hydraulic unit (not shown) of the hydraulic cylinder 9 (shown in FIG. 5) is controlled via the controller to increase or decrease the pressing force (oil pressure) of the crushing roller 4. The set values include the reference vibration level, reference material layer thickness, and rated speed (variable speed motor for constant feed wear drive). The controller is composed of a controller and an operating device. The controller indicates the range of increase and decrease of the hydraulic pressure of the hydraulic cylinder 9 according to the difference between the measured value of the vibration value or the raw material layer thickness and the set value. 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. Can be used properly depending on. In addition to the above, the controller also has a role of indicating a width of decreasing the raw material supply amount in accordance with how the measured value exceeds the set value of the vibration.

【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 operation unit transmits an operation command to the hydraulic unit and the variable speed electric motor 80a based on the instruction from the controller. The line with the arrow in the figure indicates the signal flow.

【0014】これらの制御装置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,振動値と原料層厚が測
定され,振動実測値が基準振動レベル(たとえば片振幅
50μm)より大きいときには,原料層厚が設定範囲よ
り低いとき油圧力を減少し,設定範囲より高いときには
油圧力を増加させる。原料層厚が適正範囲にあるにも拘
らず振動レベルが高いときにはこの事態を回避するため
一時的に原料供給量を減少させる。また,振動レベルが
基準レベル以内で原料供給量が定格に満たないときには
原料供給量を増加する。
The flow of the control system of these control devices 150 is as shown in FIG. That is, the vibration value and the raw material layer thickness are measured at the time interval designated by the running timer, and when the measured actual vibration value is larger than the reference vibration level (for example, one-sided amplitude is 50 μm), when the raw material layer thickness is lower than the set range, Decrease the pressure and increase the hydraulic pressure when it is higher than the set range. When the vibration level is high even though the raw material layer thickness is within the appropriate range, the raw material supply amount is temporarily reduced to avoid this situation. When the vibration level is within the reference level and the raw material supply amount is less than the rated value, the raw material supply amount is increased.

【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,再び振動計140による振動値
や層厚計130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。
振動値の設定値は片振幅50μm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。
After changing the operation in this way, after a lapse of a certain time by the timer, the vibration value by the vibrometer 140 and the raw material layer thickness measured value by the layer thickness meter 130 are compared again with the set value, and the set value is exceeded. Sometimes the above-mentioned operation is repeated.
The set value of the vibration value is about 50 μm per side amplitude, and the set value of the raw material layer thickness depends on the type of raw material, the model number of the crusher, and the product grain size, and cannot be determined in a general way. The coarser the grain size, the greater the set layer thickness. 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,振動値が急に増大した
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振
動値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 feedback mechanism as described above, the vibration value suddenly increases, or the moisture content of the feed material suddenly decreases (or increases) during operation, and the grinding efficiency decreases. Even if the vibration value increases due to poor biting, the raw material supply amount and the raw material layer thickness are improved by the above operation, and the raw material biting 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
の方法では,運転中何らかの原因によって振動値が大き
くなっても,自動的に,かつ,遠隔操作で,粉砕ローラ
の回転テーブルへの押圧力を調整して原料層厚を変更し
たり,あるいは原料供給量を一時的に減少させて振動を
鎮静化させることができる。また,振動が規定範囲内に
収まったあと自動的に原料供給量が復帰するので,粉砕
効率の低下が防止され,長期連続安定運転の継続が可能
となり,メインテナンス性と生産効率が向上する。
As is apparent from the above description, according to the method of the present invention, even if the vibration value becomes large due to some cause during operation, the rotary table of the crushing roller is automatically and remotely operated. The pressing force can be adjusted to change the raw material layer thickness, or the raw material supply amount can be temporarily reduced to suppress the vibration. In addition, after the vibration falls within the specified range, the raw material supply amount is automatically restored, so that the reduction of crushing efficiency is prevented, continuous long-term stable operation is possible, and the maintainability and production efficiency are 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調湿装置お
よび制御装置の制御ブロック線図である。
FIG. 2 is a control block diagram of a humidity control device and a control device of the vertical pulverizer according to the 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層厚計の概略説明図であ
る。
FIG. 4 is a schematic explanatory diagram of a layer thickness gauge according to an embodiment of the present invention.

【図5】従来の竪型粉砕機の全体縦断面図である。FIG. 5 is an overall vertical sectional view of a conventional vertical crusher.

【符号の説明】[Explanation of symbols]

1 竪型粉砕機 2 減速機 2A 電動機 2B コントローラ 3A 回転テーブル 4 粉砕ローラ 5 アーム 6 回転軸 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 層厚計 140 振動計 150 制御装置 A 2次コイル B 2次コイル C コア E 1次コイル R ロッド 1 Vertical Grinder 2 Reducer 2A Electric Motor 2B Controller 3A Rotary Table 4 Grinding Roller 5 Arm 6 Rotating Shaft 15 Casing 60 Raw Material Conveyor 70 Raw Material Hopper 80 Constant Feed Ware 80a Variable Speed Electric Motor 80b Weighing Machine 90 Dust Collector 100 Suction Fan 130 layer thickness meter 140 vibrometer 150 controller A secondary coil B secondary coil C core E primary coil R rod

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 原料を輸送する秤量機を具備した可変速
のコンスタントフィード・ウェアを備え,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へ押圧する油圧手段
を備え,回転テーブル中央部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,ケーシングに振動計を装着するとともに,運
転中における回転テーブルと粉砕ローラ間の原料層厚を
測定する層厚計を備え,前記油圧手段の油圧力を変更
し,前記コンスタントフィード・ウェアの供給量を増減
する制御装置を備えた竪型粉砕機において,運転中刻々
測定される振動計および層厚計の指示値と予め設定した
設定値とを比較し,前記油圧手段の油圧力や前記コンス
タントフィード・ウェアの原料供給量を次の各工程の操
作手順により調整する竪型粉砕機の自動運転方法。 振動計の指示値と設定値とを比較し,指示値が設定
値よりも大きいとき層厚計の指示値と設定値(原料層厚
適正範囲)とを比較し,原料層厚指示値が設定値を下回
るとき,その程度に応じて油圧力を減少させる第1工程 振動計の指示値が設定値よりも大きく,かつ,原料
層厚指示値が設定値を上回るとき,その程度に応じて油
圧力を増加させる第2工程 振動計の指示値が設定値より大きく,かつ,原料層
厚指示値が設定範囲内のとき,原料供給量を減少させる
第3工程 振動計の指示値が設定値よりも小さく,かつ,原料
供給量の指示値が定格原料供給量を下回るとき,原料供
給量を増加する第4工程 振動計の指示値が設定値よりも小さく,かつ,原料
供給量の指示値が定格原料供給量を上回るとき,現状の
油圧力ならびに原料供給量を保持する第5工程
1. A variable speed constant feed ware equipped with a weighing machine for transporting raw materials, wherein a plurality of rotatable crushing rollers are arranged on an upper surface of an outer peripheral portion of the rotary table, and the crushing rollers are adapted to the rotary table. A vertical crusher equipped with a hydraulic means for pressing to the center of the rotary table to crush the raw material supplied between the upper surface of the rotary table and the peripheral surface of the crushing roller. A vertical crusher equipped with a layer thickness gauge for measuring the raw material layer thickness between the rotary table and the crushing roller, and a controller for changing the oil pressure of the hydraulic means to increase or decrease the supply amount of the constant feed ware. In the above, the indicated values of the vibrometer and the layer thickness gauge, which are measured every moment during operation, are compared with preset values, and the hydraulic pressure of the hydraulic means and the constant feed wear are compared. The automatic operation method of the vertical crusher which adjusts the raw material supply amount according to the operation procedure of the following steps. The indicated value of the vibrometer is compared with the set value, and when the indicated value is larger than the set value, the indicated value of the layer thickness meter is compared with the set value (the proper range of the raw material layer thickness) to set the raw material layer indicated value. When the value is below the value, the first step of decreasing the oil pressure according to the degree is greater than the set value of the vibrometer, and when the raw material layer thickness indication value is above the set value, the oil pressure is reduced according to the degree. 2nd step to increase the pressure When the indicated value of the vibrometer is larger than the set value and the raw material layer thickness indicated value is within the set range, the 3rd step to decrease the feed rate of the raw material is less than the set value. Is smaller than the rated feedstock feed rate and the raw material feedrate is less than the set value. Maintains the current hydraulic pressure and raw material supply when the rated raw material supply is exceeded The fifth step to do
JP3331086A 1991-10-15 1991-10-15 Automatic operation method of vertical crusher Expired - Lifetime JP2673844B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3331086A JP2673844B2 (en) 1991-10-15 1991-10-15 Automatic operation method of vertical crusher

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3331086A JP2673844B2 (en) 1991-10-15 1991-10-15 Automatic operation method of vertical crusher

Publications (2)

Publication Number Publication Date
JPH05104011A JPH05104011A (en) 1993-04-27
JP2673844B2 true JP2673844B2 (en) 1997-11-05

Family

ID=18239698

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3331086A Expired - Lifetime JP2673844B2 (en) 1991-10-15 1991-10-15 Automatic operation method of vertical crusher

Country Status (1)

Country Link
JP (1) JP2673844B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07328466A (en) * 1994-06-03 1995-12-19 Nittetsu Mining Co Ltd Roller mill, method of controlling feed quantity of raw material for the same and device therefor
US7690590B2 (en) * 2008-06-13 2010-04-06 Alstom Technology Ltd Electronically controlled journal loading system
JP5810542B2 (en) * 2011-02-09 2015-11-11 株式会社Ihi Biomass mill
MY171158A (en) 2011-10-20 2019-09-27 Ihi Corp Vertical roller mill
JP7062351B2 (en) * 2014-12-05 2022-05-06 株式会社Ihi Crusher
JP7069799B2 (en) * 2018-02-16 2022-05-18 株式会社Ihi Control device
CN116337501B (en) * 2023-05-26 2023-08-18 合肥中亚建材装备有限责任公司 Device and method for detecting pressure stability of moving material bed of inorganic nonmetallic material

Also Published As

Publication number Publication date
JPH05104011A (en) 1993-04-27

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