JPH0440068B2 - - Google Patents
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- Publication number
- JPH0440068B2 JPH0440068B2 JP58041861A JP4186183A JPH0440068B2 JP H0440068 B2 JPH0440068 B2 JP H0440068B2 JP 58041861 A JP58041861 A JP 58041861A JP 4186183 A JP4186183 A JP 4186183A JP H0440068 B2 JPH0440068 B2 JP H0440068B2
- Authority
- JP
- Japan
- Prior art keywords
- crushed
- control device
- signal
- hydraulic
- differentiator
- 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
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- Crushing And Grinding (AREA)
- Disintegrating Or Milling (AREA)
Description
【発明の詳細な説明】
本発明はバウルミル等に応用できる竪形粉砕装
置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a vertical crushing device that can be applied to bowl mills and the like.
従来のこの種の竪形粉砕装置は、通常、第1図
に示すように構成されている。同図において1は
基礎上に立設された竪形粉砕装置のケーシング、
2は同ケーシング1の頂壁中央に、その軸心がケ
ーシング1の中心と合致するように配設された被
粉砕物供給管、3はケーシング1の底部中央に設
置された受台(図示せず)上に回転自在に支承さ
れ、かつ図示省略の駆動源によつて回転駆動され
る摺鉢状受皿(バウル)で、同受皿3は、その回
転中心がケーシング1の中心と合致するように配
置される。 A conventional vertical crushing device of this type is usually constructed as shown in FIG. In the figure, 1 is the casing of a vertical crusher installed on the foundation;
Reference numeral 2 denotes a material supply pipe to be crushed, which is arranged at the center of the top wall of the casing 1 so that its axis coincides with the center of the casing 1, and 3 is a pedestal (not shown) installed at the center of the bottom of the casing 1. (b) is a mortar-shaped saucer (baul) rotatably supported on the top and rotationally driven by a drive source (not shown); Placed.
4は前記摺鉢状受皿3の外周縁部上面に、後述
する押圧手段により圧接されながら同摺鉢状受皿
3の回転に伴なつて回転するように、その支持軸
5の先端に回転自在に軸支された載頭円錐状の粉
砕用ローラで、支持軸5の基部はケーシング1の
側壁の外側適所に図示の如く固設された支持部材
11に支軸9を介して同支軸9を中心として上下
に揺動可能に支持されており、また同基部には図
示の如くレバー10が連設されている。 4 is rotatably attached to the tip of the support shaft 5 so as to be pressed against the upper surface of the outer peripheral edge of the mortar-shaped saucer 3 by a pressing means described later and rotate as the mortar-shaped saucer 3 rotates. The base of the support shaft 5 is connected via a support shaft 9 to a support member 11 which is fixed at a proper position outside the side wall of the casing 1 as shown in the figure. It is supported so as to be able to swing up and down at the center, and a lever 10 is connected to the base as shown in the figure.
12は前記粉砕用ローラ4を摺鉢状受皿3の外
周縁部上面に圧接するための押圧手段で、同押圧
手段によりローラ4はレバー10を介して支軸9
を中心として摺鉢状受皿3の外周縁部上面に圧接
されるようになつており、同押圧手段としては粉
砕装置の粉砕容量が小さい場合には一般に圧縮ば
ねが用いられるが、粉砕容量が大きくなるにつれ
て、ローラ4の摺鉢状受皿3への圧接力も大きく
する必要があるため、通常、油圧装置が用いられ
る。なお、前記ローラ4とこれに付帯する部材
は、ケーシング1の周方向に沿つて等間隔毎に複
数組(通常2〜4組)配設される。 Reference numeral 12 denotes a pressing means for pressing the crushing roller 4 against the upper surface of the outer peripheral edge of the mortar-shaped saucer 3;
is pressed against the upper surface of the outer periphery of the mortar-shaped saucer 3, and a compression spring is generally used as the pressing means when the crushing capacity of the crushing device is small, but when the crushing capacity is large. As the pressure increases, it is necessary to increase the pressing force of the roller 4 against the mortar-shaped saucer 3, so a hydraulic device is usually used. Note that a plurality of sets (usually 2 to 4 sets) of the rollers 4 and the members attached thereto are arranged at regular intervals along the circumferential direction of the casing 1.
6はケーシング1における前記摺鉢状受皿3の
若干下方の側壁に配設された熱ガス導入管で、同
熱ガス導入管6は図示省略の熱空気源または熱ガ
ス源に接続されており、同熱ガス導入管6からケ
ーシング内に導入される熱空気または熱ガスは、
摺鉢状受皿3の外周端面とケーシング1の側壁内
周面との間隙を上昇気流となつて上昇するように
なつている。 Reference numeral 6 denotes a hot gas introduction pipe disposed on the side wall of the casing 1 slightly below the mortar-shaped saucer 3, and the hot gas introduction pipe 6 is connected to a hot air source or a hot gas source (not shown), The hot air or hot gas introduced into the casing from the isothermal gas introduction pipe 6 is
The air flows upward through the gap between the outer circumferential end surface of the mortar-shaped saucer 3 and the inner circumferential surface of the side wall of the casing 1 as an upward air current.
7は図示の如くケーシング1内に配設された粗
粉分離器、8は微粉出口管をそれぞれ示し、被粉
砕物供給機13により被粉砕物供給管2を介して
ケーシング1内に導入された被粉砕物は、回転中
の摺鉢状受皿3上面の中心部付近に供給される
が、同被粉砕物は回転する摺鉢状受皿3の遠心力
によつて同摺鉢状受皿3の外周縁部上面に移動
し、押圧手段12で同外周縁部上面に圧接されて
いる粉砕用ローラ4で圧縮粉砕されたのち、同外
周縁部上面から同摺鉢状受皿3の外周方向へ投げ
出される。 7 is a coarse powder separator disposed in the casing 1 as shown in the figure, and 8 is a fine powder outlet pipe, which is introduced into the casing 1 via the pulverized material feeder 13 through the pulverized material supply pipe 2. The material to be crushed is supplied near the center of the upper surface of the rotating mortar-shaped tray 3, and the material to be crushed is pushed out of the mortar-shaped tray 3 by the centrifugal force of the rotating mortar-shaped tray 3. It moves to the upper surface of the peripheral edge, is compressed and crushed by the crushing roller 4 that is pressed against the upper surface of the outer peripheral edge by the pressing means 12, and is then thrown out from the upper surface of the outer peripheral edge toward the outer circumference of the mortar-shaped saucer 3. .
このようにして圧縮粉砕されて摺鉢状受皿3の
外周方向へ放出される粉砕物は、熱ガス導入管6
からの熱空気または熱ガスの上昇気流に乗つて、
熱空気または熱ガスにより乾燥されながら上昇し
て上方の粗粉分離器7内に入り、ここで微粉と粗
粉に分離され、微粉は微粉出口管8から空気また
はガスとともに外部に排出され、また粗粉は下方
の摺鉢状受皿3上に落下し、被粉砕物供給管2か
ら新たに供給される被粉砕物とともに粉砕され
る。以上の操作の繰返えしで、被粉砕物は所望の
微粉状に粉砕される。 The pulverized material thus compressed and pulverized and discharged toward the outer circumference of the mortar-shaped saucer 3 is transferred to the hot gas introduction pipe 6.
Riding the updraft of hot air or hot gas from
It rises while being dried by hot air or hot gas and enters the upper coarse powder separator 7, where it is separated into fine powder and coarse powder, and the fine powder is discharged to the outside together with air or gas from the fine powder outlet pipe 8. The coarse powder falls onto the mortar-shaped saucer 3 below and is crushed together with the crushed material newly supplied from the crushed material supply pipe 2. By repeating the above operations, the material to be crushed is crushed into a desired fine powder.
さて前記の如く説明した従来の竪形粉砕装置に
おいて、その粉砕容量が小さく、粉砕用ローラ4
の押圧手段として圧縮ばねを用いている場合は格
別問題はないが、その粉砕容量が大きく、粉砕用
ローラ4の押圧手段として油圧装置を用いている
場合は、同油圧装置の油圧を、通常粉砕装置の負
荷率に無関係な一定値、すなわち粉砕装置の最大
負荷に必要な値に設定する方法もしくは粉砕用ロ
ーラ4と摺鉢状受皿3の間の被粉砕物の層の厚さ
に応じた油圧に制御する方法のいずれかが採用さ
れて来た。 Now, in the conventional vertical crusher described above, its crushing capacity is small, and the crushing roller 4
There is no particular problem if a compression spring is used as the pressing means for the crushing roller 4, but if the crushing capacity is large and a hydraulic device is used as the pressing means for the crushing roller 4, the hydraulic pressure of the hydraulic device is usually A method of setting a constant value regardless of the load factor of the device, that is, a value required for the maximum load of the crushing device, or a method of setting oil pressure according to the thickness of the layer of the material to be crushed between the crushing roller 4 and the mortar-shaped receiver 3. One of the methods of controlling this has been adopted.
しかし前者の方法によると、粉砕装置の部分負
荷時には、必要以上の圧接力が粉砕用ローラ4と
摺鉢状受皿3の外周縁部上面に作用し、被粉砕物
が過度に微粉砕される傾向となるばかりでなく、
粉砕装置の消費動力が負荷の減少に見合うだけ減
少せず不経済であるという欠点があつた。 However, according to the former method, when the crushing device is partially loaded, a pressure contact force that is more than necessary acts on the upper surface of the outer peripheral edge of the crushing roller 4 and the mortar-shaped receiver 3, and the material to be crushed tends to be excessively pulverized. Not only is it
There was a drawback that the power consumption of the crushing device did not decrease commensurately with the decrease in load, making it uneconomical.
一方後者の方法においては、前記の欠点は改善
されたものの、被粉砕物の供給量が急激に変動し
た場合には、これに伴ない粉砕用ローラ4と摺鉢
状受皿3の間の被粉砕物の層の厚さが変動し、油
圧が変化されるまでには時間遅れがあるため、粉
砕装置としての負荷応答性が悪いという欠点があ
つた。 On the other hand, in the latter method, although the above-mentioned drawbacks have been improved, when the supply amount of the material to be crushed changes rapidly, the amount of material to be crushed between the crushing roller 4 and the mortar-shaped receiver 3 is affected. Since the thickness of the material layer fluctuates and there is a time delay before the oil pressure is changed, the crushing device had the disadvantage of poor load response.
本発明は前記従来の欠点を解消するために提案
されたもので、垂直駆動軸周りに回転している摺
鉢状受皿と、これと協調して被粉砕物を粉砕する
複数個の粉砕用ローラと、同ローラを押圧する油
圧シリンダと、前記受皿上に被粉砕物を供給機に
より供給する被粉砕物供給管と、前記ローラを受
皿に押付ける押圧手段とを有する竪形粉砕装置に
おいて、前記被粉砕物供給機は、被粉砕物供給機
駆動用可変速モータにより回転駆動制御され、同
可変速モータは回転数制御装置により制御され、
かつ同回転数制御装置は電子式油圧制御装置と電
気的に接続されており、同電子式油圧制御装置は
函数発生器、微分器、リミツタ、コンパレータで
構成されると共に、同函数発生器と微分器は、前
記回転数制御装置に電気的に接続され、かつ同函
数発生器及びリミツタの出力の合流部とコンパレ
ータの間に油圧トランスミツタを配設し、かつ同
コンパレータは信号発信器を介して電磁弁に電気
的に接続されており、前記回転数制御装置により
出力された被粉砕物供給量の制御信号が前記電子
式油圧制御装置への入力信号となつて、前記函数
発生器及び微分器に入り、同函数発生器では前記
ローラの押圧手段を構成する油圧シリンダ内の油
圧が予め設定された函数に基づいて所定のレベル
に保持されるような指令を出力し、前記微分器で
は、前記回転数制御装置の変化速度に応じた信号
が出され、この信号がリミツタの入力信号となる
ようにすることにより、前記押圧手段の押圧力を
被粉砕物の供給量とその変化速度とに基づいて制
御するようにし、負荷応答性を改善した竪形粉砕
装置を提供せんとするものである。 The present invention was proposed to solve the above-mentioned conventional drawbacks, and includes a mortar-shaped tray rotating around a vertical drive shaft, and a plurality of crushing rollers that cooperate with the mortar-shaped tray to crush the object to be crushed. and a hydraulic cylinder for pressing the roller, a material supply pipe for supplying the material to be crushed onto the receiving tray by a feeder, and a pressing means for pressing the roller against the receiving tray. The material to be crushed feeder is rotationally controlled by a variable speed motor for driving the material to be crushed, and the variable speed motor is controlled by a rotation speed control device,
The rotation speed control device is electrically connected to an electronic hydraulic control device, and the electronic hydraulic control device is composed of a function generator, a differentiator, a limiter, and a comparator, and also has a function generator and a differentiator. A hydraulic transmitter is electrically connected to the rotation speed control device, and a hydraulic transmitter is disposed between a confluence of the outputs of the function generator and the limiter and a comparator, and the comparator is connected to the rotation speed control device through a signal transmitter. It is electrically connected to the electromagnetic valve, and a control signal for the supply amount of the material to be crushed outputted by the rotation speed control device becomes an input signal to the electrohydraulic control device, and the function generator and the differentiator are connected to the electromagnetic valve. The function generator outputs a command to maintain the hydraulic pressure in the hydraulic cylinder constituting the pressing means for the roller at a predetermined level based on a preset function, and the differentiator outputs a command to maintain the hydraulic pressure in the hydraulic cylinder constituting the pressing means for the roller at a predetermined level based on a preset function. A signal corresponding to the rate of change of the rotational speed control device is output, and by making this signal serve as an input signal to the limiter, the pressing force of the pressing means can be controlled based on the supply amount of the material to be crushed and the rate of change thereof. It is an object of the present invention to provide a vertical crushing device that improves load response.
以下本発明の実施例を図面について説明する
と、第2図乃至第4図は本発明の実施例を示す。
先ず第2図において、1は粉砕装置のケーシン
グ、2は被粉砕物供給管、3は摺鉢状受皿、4は
粉砕用ローラ、5はその支持軸、6は熱ガス導入
管、7は粗粉分離器、8は微粉出口管、9は前記
ローラ4の支持軸5の基部の支軸、10はレバ
ー、11は支持部材、13は被粉砕物供給機、1
4は同駆動用可変速モータで、それら各部材の構
成、作用および相互の関係構造は、前記第1図に
示す従来装置におけるものとほぼ同様であり、同
一の符号で示してある。 Embodiments of the present invention will be described below with reference to the drawings. FIGS. 2 to 4 show embodiments of the present invention.
First, in Fig. 2, 1 is a casing of the crushing device, 2 is a supply pipe for the material to be crushed, 3 is a mortar-shaped saucer, 4 is a crushing roller, 5 is its support shaft, 6 is a hot gas introduction pipe, and 7 is a rough A powder separator, 8 is a fine powder outlet pipe, 9 is a support shaft at the base of the support shaft 5 of the roller 4, 10 is a lever, 11 is a support member, 13 is a material feeder to be crushed, 1
Reference numeral 4 denotes a variable speed motor for driving the same, and the structure, function, and mutual relationship of each of these members are substantially the same as those in the conventional device shown in FIG. 1, and are designated by the same reference numerals.
Aは前記支持部材11に図示の如く装着され、
前記粉砕用ローラ4を摺鉢状受皿3の外周縁部上
面に圧接するための押圧機構で、同押圧機構Aは
第3図に示す如く構成されている。第3図におい
て20は油圧シリンダ、21はピストン、22は
ピストンロツドで、それらのシリンダ20、ピス
トン21およびピストンロツド22で油圧装置を
形成している。 A is attached to the support member 11 as shown in the figure,
This is a pressing mechanism for pressing the crushing roller 4 against the upper surface of the outer peripheral edge of the mortar-shaped saucer 3, and the pressing mechanism A is constructed as shown in FIG. 3. In FIG. 3, 20 is a hydraulic cylinder, 21 is a piston, and 22 is a piston rod, and these cylinder 20, piston 21, and piston rod 22 form a hydraulic system.
23は被粉砕物供給機駆動用可変速モータ14
の回転数制御装置であり、24及び25は同制御
装置23の制御信号をそれぞれ可変速モータ14
及び電子式油圧制御装置26に伝達する電線、2
7は油圧配管、28は油圧トランスミツタ、29
は同油圧トランスミツタ28と前記電子式油圧制
御装置26とを結ぶ電線、30は電子式油圧制御
装置26と信号発信器31を結ぶ電線、Vは同信
号発信器31からの電気信号で作動する電磁四方
弁、32は図示省略の油圧ポンプから電磁四方弁
Vを介して前記油圧配管27に圧油を供給する配
管、33は電磁四方弁Vから油圧ポンプの吸込口
に連通されたタンク(図示せず)への戻油配管、
34は圧油配管27に図示の如く付設されたアキ
ユムレータをそれぞれ示す。 23 is a variable speed motor 14 for driving the material feeder to be crushed.
24 and 25 are control signals of the control device 23 and are respectively connected to the variable speed motor 14.
and an electric wire transmitting to the electronic hydraulic control device 26, 2
7 is a hydraulic pipe, 28 is a hydraulic transmitter, 29
is an electric wire connecting the hydraulic transmitter 28 and the electronic hydraulic control device 26, 30 is an electric wire connecting the electronic hydraulic control device 26 and the signal transmitter 31, and V is activated by an electric signal from the signal transmitter 31. An electromagnetic four-way valve, 32 is a pipe for supplying pressure oil from a hydraulic pump (not shown) to the hydraulic pipe 27 via the electromagnetic four-way valve V, and 33 is a tank (see figure) connected from the electromagnetic four-way valve V to the suction port of the hydraulic pump. oil return piping to (not shown),
Reference numeral 34 indicates an accumulator attached to the pressure oil pipe 27 as shown in the figure.
第4図は前記電子式油圧制御装置26の主要な
構成部材の一例をブロツク線図で示しているが、
同図に示す如く同電子式油圧制御装置26は、函
数発生器35、微分器36、リミツタ37、コン
パレータ38等で構成されており、函数発生器3
5と微分器36が電線25を介して前記モータ回
転数制御装置23に、また函数発生器35及びミ
リツタ37の出力の合流部とコンパレータ38の
間に電線29を介して前記油圧トランスミツタ2
8が、なおまたコンパレータ38が信号発信器3
1を介して電磁四方弁Vにそれぞれ電気的に接続
されていて、電子式油圧制御回路を形成してい
る。 FIG. 4 shows an example of the main components of the electronic hydraulic control device 26 in a block diagram.
As shown in the figure, the electronic hydraulic control device 26 is composed of a function generator 35, a differentiator 36, a limiter 37, a comparator 38, etc.
5 and a differentiator 36 are connected to the motor rotation speed control device 23 via an electric wire 25, and to the hydraulic transmitter 2 via an electric wire 29 between a confluence of the outputs of the function generator 35 and the millimeter 37 and a comparator 38.
8, and the comparator 38 is also the signal transmitter 3
1 to the electromagnetic four-way valves V, forming an electronic hydraulic control circuit.
そして被粉砕物供給機駆動用可変速モータ14
の回転数制御装置23より出力された被粉砕物供
給量の制御信号は、電線25を介して電子式油圧
制御装置26への入力信号となり、函数発生器3
5及び微分器36内へ入るようになつている。 And a variable speed motor 14 for driving the material feeder to be crushed.
The control signal for the supply amount of the material to be crushed output from the rotation speed control device 23 becomes an input signal to the electronic hydraulic control device 26 via the electric wire 25, and
5 and into the differentiator 36.
また、前記函数発生器35では、被粉砕物所要
供給量に相当するモータ回転数制御装置23の出
力信号に対して、前記油圧シリンダ20内の油圧
が、予かじめ設定された函数に基づいて所定のレ
ベルに保持されるような指令が出力される。一
方、微分器36では、前記回転数制御装置23の
出力信号の微分量、即ち変化速度に応じた信号が
出力され、この信号はリミツタ37の入力信号と
なる。リミツタ37は、前記入力信号に対し、上
限値及び下限の設定を行ない出力する。 Further, the function generator 35 controls the hydraulic pressure in the hydraulic cylinder 20 based on a preset function in response to the output signal of the motor rotation speed control device 23 corresponding to the required supply amount of the material to be crushed. A command is output to maintain it at a predetermined level. On the other hand, the differentiator 36 outputs a signal corresponding to the amount of differentiation of the output signal of the rotational speed control device 23, that is, the rate of change, and this signal becomes an input signal to the limiter 37. The limiter 37 sets an upper limit and a lower limit for the input signal and outputs the set value.
函数発生器35とリミツタ37のそれぞれの出
力信号の和は油圧トランスミツタ28からの信号
と比較され、その間にある限度以上の差異がある
と、コンパレータ38を通過して油圧増減の指令
を、前記信号発信器31に送り、同信号発信器3
1の作動で油圧配管7上の電磁四方弁Vを作動せ
しめることにより、油圧シリンダ20内の油圧を
適当に制御するようになつている。 The sum of the respective output signals of the function generator 35 and the limiter 37 is compared with the signal from the hydraulic transmitter 28, and if there is a difference between them by more than a certain limit, the sum is passed through the comparator 38 and a command to increase or decrease the hydraulic pressure is sent to the signal from the hydraulic transmitter 28. The signal is sent to the signal transmitter 31, and the signal transmitter 3
1 operates the electromagnetic four-way valve V on the hydraulic piping 7, thereby appropriately controlling the oil pressure in the hydraulic cylinder 20.
以上の如く本発明の特徴とする点は、被粉砕物
供給機駆動用可変速モータ14の回転数のフイー
ドバツク信号(スピード発信器SX)を函数発生
器35に入力し、その出力と油圧トランスミツタ
28が発生する油圧の実測値をコンパレータ38
で比較演算し、信号発信器31で油圧荷重装置内
にある電磁弁Vにチヤージ、デイスチヤージの指
令を行い、粉砕用ローラ4の押圧力を制御するよ
うにした点である。 As described above, the present invention is characterized by inputting the feedback signal (speed transmitter SX) of the rotation speed of the variable speed motor 14 for driving the material feeder to the function generator 35, and transmitting the output and the hydraulic transmitter. The actual measured value of the oil pressure generated by 28 is sent to the comparator 38.
The difference is that the signal transmitter 31 issues commands for charge and discharge to the electromagnetic valve V in the hydraulic load device, thereby controlling the pressing force of the crushing roller 4.
次に作用を説明する。先ず本装置の運転を開始
すると、被粉砕物供給管2からケーシング1内に
導入された被粉砕物は、粉砕用ローラ4と摺鉢状
受皿3の外周縁部上面との間で粉砕されたのち、
熱ガス導入管6からの熱ガスによつて乾燥されな
がらケーシング1内を上昇し、粗粉分離器7で粗
粉と微粉に分離され、微粉は微粉出口管8から外
部へ排出され、また粗粉は摺鉢状受皿3上に落下
し、被粉砕物供給管2からの新たな被粉砕物とと
もに再粉砕されることは前記従来装置と同様であ
る。 Next, the action will be explained. First, when the operation of this device is started, the material to be crushed introduced into the casing 1 from the material supply pipe 2 is crushed between the crushing roller 4 and the upper surface of the outer peripheral edge of the mortar-shaped saucer 3. after,
It rises inside the casing 1 while being dried by the hot gas from the hot gas introduction pipe 6, and is separated into coarse powder and fine powder by the coarse powder separator 7. The fine powder is discharged to the outside from the fine powder outlet pipe 8, and the coarse powder is The powder falls onto the mortar-shaped tray 3 and is re-pulverized together with the new material to be ground from the material supply pipe 2, as in the conventional apparatus.
被粉砕物の供給量が一定の場合には、被粉砕物
供給機駆動モータ制御装置23の出力信号は一定
値となるため、微分器36の出力信号は0とな
り、従つて油圧シリンダ20内の油圧は、函数発
生器35にて予め設定された函数に基づいて保持
されるように指令信号が発せられる。 When the supply amount of the material to be crushed is constant, the output signal of the material feeder drive motor control device 23 is a constant value, so the output signal of the differentiator 36 is 0, and therefore the output signal in the hydraulic cylinder 20 is A command signal is issued by a function generator 35 to maintain the oil pressure based on a preset function.
この指令信号は、油圧トランスミツタ28から
の信号と比較され、それらの間にある限度以上の
差異があると、コンパレータ38を経て油圧増減
の指令を信号発信器31に送り、同信号発信器3
1の指令で油圧配管7に介装された電磁四方弁V
を作動させて油圧シリンダ20内の油圧を制御す
る。従つて油圧シリンダ20のピストンロツド2
2による粉砕用ローラ4の摺鉢状受皿3の外周縁
部上面に対する圧接力は、被粉砕物の供給量に応
じた値に制御される。 This command signal is compared with the signal from the hydraulic transmitter 28, and if there is a difference between them that exceeds a certain limit, a command to increase or decrease the hydraulic pressure is sent to the signal transmitter 31 via the comparator 38.
An electromagnetic four-way valve V installed in the hydraulic piping 7 according to the command of 1.
is operated to control the oil pressure in the hydraulic cylinder 20. Therefore, the piston rod 2 of the hydraulic cylinder 20
The pressing force of the crushing roller 4 against the upper surface of the outer peripheral edge of the mortar-shaped tray 3 by the crushing roller 2 is controlled to a value corresponding to the supply amount of the material to be crushed.
一方被粉砕物の供給量が急激に変化する場合に
は、供給量の変化速度に応じた出力信号が微分器
36より発せられ、函数発生器35の出力信号に
加算された後、油圧トランスミツタ28からの信
号と比較され、以下の制御が行なわれる。 On the other hand, when the supply amount of the material to be crushed changes rapidly, an output signal corresponding to the rate of change in the supply amount is generated from the differentiator 36, and after being added to the output signal of the function generator 35, the output signal is sent to the hydraulic transmitter. It is compared with the signal from 28 and the following control is performed.
この結果、被粉砕物の供給量が増加する場合に
は、油圧は予め設定された圧力より高く、また同
供給量が減少する場合には、油圧は予め設定され
た圧力より低く制御される。 As a result, when the supply amount of the material to be crushed increases, the oil pressure is controlled to be higher than the preset pressure, and when the same supply amount decreases, the oil pressure is controlled to be lower than the preset pressure.
以上詳細に説明した如く本発明装置は構成され
ており、被粉砕物の供給量が一定の場合には、油
圧シリンダによる粉砕用ローラの受皿に対する押
圧力は、被粉砕物の供給量に応じた値に制御さ
れ、また被粉砕物の供給量が急激に変化する場合
には、油圧シリンダの油圧は予め設定された圧力
より高く、更に供給量が減少する場合には、油圧
は予め設定された圧力より低く制御される。以上
の如く粉砕装置の負荷増加時には、粉砕用ローラ
の摺鉢状受皿の外周縁部上面への圧接力が高めに
制御されるため、粉砕能力が向上し、粉砕装置出
口の製品量が直ちに増加するため、負荷増加の要
求に極めて短時間に応答できる。 The apparatus of the present invention is configured as explained in detail above, and when the amount of the material to be crushed is constant, the pressing force of the crushing roller against the tray by the hydraulic cylinder is proportional to the amount of the material to be crushed. When the feed rate of the material to be crushed changes rapidly, the oil pressure of the hydraulic cylinder is higher than the preset pressure, and when the feed rate further decreases, the oil pressure is higher than the preset pressure. Controlled below pressure. As described above, when the load on the crushing device increases, the pressure of the crushing roller against the upper surface of the outer peripheral edge of the mortar-shaped tray is controlled to be high, so the crushing capacity improves and the amount of product at the outlet of the crushing device increases immediately. Therefore, it is possible to respond to requests for load increases in an extremely short time.
また粉砕装置の負荷減少時には、前記圧接力が
低めに制御されるので、粉砕能力が低下し、粉砕
装置出口の製品量が直ちに減少するため負荷減少
の要求に極めて短時間に応答できる。なお、本発
明において制御装置23の出力信号の代りに、被
粉砕物供給量の信号を使用しても同様な効果が期
待できる。 Furthermore, when the load on the crusher is reduced, the pressing force is controlled to be low, so the crushing capacity is reduced and the amount of product at the outlet of the crusher is immediately reduced, so that a request for load reduction can be responded to in an extremely short time. Incidentally, in the present invention, the same effect can be expected even if the signal of the supply amount of the material to be crushed is used instead of the output signal of the control device 23.
第1図は従来の竪形粉砕装置の1例を示す正面
断面図、第2図は本発明の実施例を示す竪形粉砕
装置の正面断面図、第3図は第2図における油圧
装置のシステム図、第4図は第3図における電気
回路図である。
図の主要部分の説明、2……被粉砕物供給管、
3……摺鉢状受皿、4……粉砕用ローラ、A……
押圧機構(押圧手段)、20……油圧シリンダ
(油圧装置)、21……ピストン、22……ピスト
ンロツド、23……被粉砕物供給機駆動モータ制
御装置、28……油圧トランスミツタ、35……
函数発生器、36……微分器。
FIG. 1 is a front sectional view showing an example of a conventional vertical crushing device, FIG. 2 is a front sectional view of a vertical crushing device showing an embodiment of the present invention, and FIG. 3 is a front sectional view of the hydraulic system shown in FIG. The system diagram, FIG. 4, is an electrical circuit diagram in FIG. 3. Explanation of the main parts of the diagram, 2...Pipe for supplying the material to be crushed,
3... Mortar-shaped saucer, 4... Grinding roller, A...
Pressing mechanism (pressing means), 20... Hydraulic cylinder (hydraulic device), 21... Piston, 22... Piston rod, 23... Crushed material feeder drive motor control device, 28... Hydraulic transmitter, 35...
Function generator, 36...differentiator.
Claims (1)
と、これと協調して被粉砕物を粉砕する複数個の
粉砕用ローラと、同ローラを押圧する油圧シリン
ダと、前記受皿上に被粉砕物を供給機により供給
する被粉砕物供給管と、前記ローラを受皿に押付
ける押圧手段とを有する竪形粉砕装置において、
前記被粉砕物供給機は、被粉砕物供給機駆動用可
変速モータにより回転駆動制御され、同可変速モ
ータは回転数制御装置により制御され、かつ同回
転数制御装置は電子式油圧制御装置と電気的に接
続されており、同電子式油圧制御装置は函数発生
器、微分器、リミツタ、コンパレータで構成され
ると共に、同函数発生器と微分器は、前記回転数
制御装置に電気的に接続され、かつ同函数発生器
及びリミツタの出力の合流部とコンパレータの間
に油圧トランスミツタを配設し、かつ同コンパレ
ータは信号発信器を介して電磁弁に電気的に接続
されており、前記回転数制御装置により出力され
た被粉砕物供給量の制御信号が前記電子式油圧制
御装置への入力信号となつて、前記函数発生器及
び微分器に入り、同函数発生器では前記ローラの
押圧手段を構成する油圧シリンダ内の油圧が予め
設定された函数に基づいて所定のレベルに保持さ
れるような指令を出力し、前記微分器では、前記
回転数制御装置の変化速度に応じた信号が出さ
れ、この信号がリミツタの入力信号となるように
することにより、前記押圧手段の押圧力を被粉砕
物の供給量とその変化速度とに基づいて制御する
ことを特徴とする竪形粉砕装置。1. A mortar-shaped tray rotating around a vertical drive shaft, a plurality of crushing rollers that cooperate with this to crush the material to be crushed, a hydraulic cylinder that presses the rollers, and a container to be crushed on the tray. In a vertical crushing device having an object supply pipe for supplying objects by a feeder, and a pressing means for pressing the roller against a receiving tray,
The rotation of the material feeder to be crushed is controlled by a variable speed motor for driving the material to be crushed, the variable speed motor is controlled by a rotation speed control device, and the rotation speed control device is an electronic hydraulic control device. The electronic hydraulic control device is composed of a function generator, a differentiator, a limiter, and a comparator, and the function generator and the differentiator are electrically connected to the rotation speed control device. and a hydraulic transmitter is disposed between the confluence of the outputs of the function generator and the limiter and the comparator, and the comparator is electrically connected to the solenoid valve via the signal transmitter, and the A control signal for the feed rate of the material to be crushed outputted by the numerical control device becomes an input signal to the electronic hydraulic control device and enters the function generator and the differentiator, and the function generator controls the pressing means for the roller. The differentiator outputs a command to maintain the oil pressure in a hydraulic cylinder constituting a predetermined level at a predetermined level based on a preset function, and the differentiator outputs a signal corresponding to the rate of change of the rotation speed control device. A vertical crushing apparatus characterized in that the pressing force of the pressing means is controlled based on the supply amount of the material to be crushed and the rate of change thereof by making this signal serve as an input signal to a limiter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4186183A JPS59169543A (en) | 1983-03-14 | 1983-03-14 | Vertical type crusher |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4186183A JPS59169543A (en) | 1983-03-14 | 1983-03-14 | Vertical type crusher |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59169543A JPS59169543A (en) | 1984-09-25 |
| JPH0440068B2 true JPH0440068B2 (en) | 1992-07-01 |
Family
ID=12620025
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4186183A Granted JPS59169543A (en) | 1983-03-14 | 1983-03-14 | Vertical type crusher |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59169543A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5835311Y2 (en) * | 1979-10-29 | 1983-08-09 | 三菱重工業株式会社 | Hydraulic bowl mill load control device |
-
1983
- 1983-03-14 JP JP4186183A patent/JPS59169543A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59169543A (en) | 1984-09-25 |
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