JPH09206614A - Control method of pressing force of roller mill - Google Patents
Control method of pressing force of roller millInfo
- Publication number
- JPH09206614A JPH09206614A JP2132496A JP2132496A JPH09206614A JP H09206614 A JPH09206614 A JP H09206614A JP 2132496 A JP2132496 A JP 2132496A JP 2132496 A JP2132496 A JP 2132496A JP H09206614 A JPH09206614 A JP H09206614A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- crushing
- roller
- roller mill
- pressing force
- 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.)
- Granted
Links
- 238000003825 pressing Methods 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims description 10
- 239000003245 coal Substances 0.000 claims abstract description 67
- 239000011362 coarse particle Substances 0.000 abstract description 7
- 238000000227 grinding Methods 0.000 abstract description 6
- 238000007599 discharging Methods 0.000 abstract description 3
- 238000010586 diagram Methods 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 238000010298 pulverizing process Methods 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 3
- 229910052683 pyrite Inorganic materials 0.000 description 3
- 239000011028 pyrite Substances 0.000 description 3
- 238000005096 rolling process Methods 0.000 description 3
- 239000004568 cement Substances 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Crushing And Grinding (AREA)
- Disintegrating Or Milling (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、石炭、セメントク
リンカ、化学製品の原料等を粉砕するローラミルの粉砕
部に加える圧力を制御するローラミルの加圧力制御方法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a roller mill pressure control method for controlling the pressure applied to a crushing section of a roller mill for crushing coal, cement clinker, raw materials for chemical products and the like.
【0002】[0002]
【従来の技術】石炭、セメント原料、素材原料等の塊状
物を細かく粉砕する粉砕機の1つとして、回転する粉砕
テーブルと、その上で自転する粉砕ローラとを備えたロ
ーラミルがある。このようなローラミルを図2により説
明する。2. Description of the Related Art As one of pulverizers for finely pulverizing lumps such as coal, cement raw materials and raw material raw materials, there is a roller mill having a rotating pulverizing table and a pulverizing roller which rotates on the pulverizing table. Such a roller mill will be described with reference to FIG.
【0003】図2は石炭を粉砕する竪型のローラミルの
概略構成を示す図である。この図で、1はケーシング、
2は図示しないモータの回転軸、3は回転軸2の回転を
減速する減速機、4は減速機3に連結された図示しない
垂直回転軸に固定されて回転する粉砕テーブル、41は
粉砕テーブル4の上面円周上に形成された粉砕レース面
である。5は粉砕ローラであり、粉砕レース面41と接
触し、粉砕テーブルの回転により自転する。6は粉砕ロ
ーラ5を回転自在に支持するローラブラケット、7は下
加圧フレーム、8は上加圧フレーム、9は下加圧フレー
ムと上加圧フレームとの間に介在するスプリング、10
はローラピボットである。ローラブラケット6はローラ
ピボット10を介して下加圧フレーム7に支持される。FIG. 2 is a diagram showing a schematic structure of a vertical roller mill for crushing coal. In this figure, 1 is a casing,
Reference numeral 2 is a rotary shaft of a motor (not shown), 3 is a speed reducer for reducing the rotation of the rotary shaft 2, 4 is a crushing table which is fixedly rotated on a vertical rotary shaft (not shown) connected to the speed reducer 3, and 41 is a crushing table 4. Is a crushing race surface formed on the circumference of the upper surface of. A crushing roller 5 is in contact with the crushing race surface 41 and rotates by the rotation of the crushing table. 6 is a roller bracket for rotatably supporting the crushing roller 5, 7 is a lower pressure frame, 8 is an upper pressure frame, 9 is a spring interposed between the lower pressure frame and the upper pressure frame, 10
Is a roller pivot. The roller bracket 6 is supported by the lower pressing frame 7 via the roller pivot 10.
【0004】12は油圧シリンダ、13は油圧シリンダ
のロッド、14はリンク、15は上加圧フレーム8とリ
ンク14とを連結するピン、16はロッド13とリンク
14とを連結するピンである。油圧シリンダ12のロッ
ド13を伸縮させることにより、上加圧フレーム8、ス
プリング9、下加圧フレーム7、ローラピボット10、
ローラブラケット6を介して粉砕ローラ5に加わる圧力
が調整される。18は回転分級器、19は給炭機、20
は給炭機19から供給される石炭を粉砕テーブル4へ導
く供給管である。Reference numeral 12 is a hydraulic cylinder, 13 is a rod of the hydraulic cylinder, 14 is a link, 15 is a pin for connecting the upper pressurizing frame 8 and the link 14, and 16 is a pin for connecting the rod 13 and the link 14. By expanding and contracting the rod 13 of the hydraulic cylinder 12, the upper pressure frame 8, the spring 9, the lower pressure frame 7, the roller pivot 10,
The pressure applied to the crushing roller 5 via the roller bracket 6 is adjusted. 18 is a rotary classifier, 19 is a coal feeder, 20
Is a supply pipe for guiding the coal supplied from the coal feeder 19 to the crushing table 4.
【0005】給炭機19からの石炭が、供給管20を通
って粉砕テーブル4の中心部へ供給されると、この供給
された石炭は粉砕テーブル4の回転による遠心力により
粉砕テーブル4の外周部へ移動し、粉砕レース面41と
粉砕ローラとの間に噛み込まれて粉砕される。一方、ケ
ーシング1の底部には図示しないダクトにより熱風が導
かれ、この熱風は、矢印Wに示すように粉砕テーブル4
の外側とケーシング1の内側との間から上方へ吹き上げ
られ、粉砕後の石炭を乾燥させながら上部へ輸送する。
輸送された石炭粉のうち粗いものは途中で落下し(一次
分級)、その他の石炭粉はさらに上昇して回転分級器1
8へ達し、ここで再度分級され(二次分級)、所定の粒
径以下の石炭粉は、例えばボイラの微粉炭バーナ又は微
分貯蔵ビンへ送られ、所定の粒径以上の石炭粉は粉砕テ
ーブル4へ落下せしめられ、新たに供給された石炭とと
もに再度粉砕される。このように、粉砕と分級が繰り返
される。When the coal from the coal feeder 19 is supplied to the center of the crushing table 4 through the supply pipe 20, the supplied coal is rotated by the centrifugal force of the rotation of the crushing table 4 and the outer periphery of the crushing table 4 is rotated. And is crushed by being caught between the crushing race surface 41 and the crushing roller. On the other hand, hot air is guided to the bottom of the casing 1 by a duct (not shown), and this hot air is, as shown by an arrow W, the crushing table 4
Is blown upward from between the outside of the casing and the inside of the casing 1, and the pulverized coal is dried and transported to the upper part.
Coarse of the transported coal powder falls on the way (primary classification), and other coal powder further rises to the rotary classifier 1.
No. 8 is reached and the particles are classified again (secondary classification), and the coal powder having a predetermined particle size or less is sent to, for example, a pulverized coal burner of a boiler or a differential storage bin, and the coal powder having a predetermined particle size or more is crushed on a crushing table. It is made to fall to No. 4, and is crushed again with the newly supplied coal. In this way, crushing and classification are repeated.
【0006】[0006]
【発明が解決しようとする課題】ところで、上記ローラ
ミルにおいては、石炭供給を停止すると、粉砕ローラ5
の下の炭層の厚さが刻々薄くなり、かつ、給炭されてい
るときより炭層粒子は細かくなるため、摩擦抵抗が小さ
くなって粉砕ローラ5が滑り易くなり、粉砕ローラ5の
転動が不安定となり、これにより自励振動が発生する場
合がある。このような自励振動を回避するため、従来、
例えば実開昭62−95742号公報に示されるよう
に、粉砕ローラへの荷重を減少させて転動を安定させる
手段や、ローラミル内の石炭を粗粒の状態でもローラミ
ル外へ排出させて転動を安定させるため分級能力を減少
させる手段等が採用されていた。By the way, in the above roller mill, when the coal supply is stopped, the crushing roller 5
Since the thickness of the coal layer underneath becomes smaller and the particles of the coal layer become finer than when the coal is being fed, the friction resistance becomes small and the crushing roller 5 becomes slippery, so that the crushing roller 5 does not roll. It becomes stable, which may cause self-excited vibration. In order to avoid such self-excited vibration, conventionally,
For example, as disclosed in Japanese Utility Model Laid-Open No. 62-95742, a means for stabilizing the rolling by reducing the load on the crushing roller, or rolling the coal in the roller mill by discharging it to the outside of the roller mill even in a coarse particle state. In order to stabilize the, the method of reducing the classification ability was adopted.
【0007】しかし、これらの手段は、いずれも石炭が
粗粒の状態で排出されるので、パイライト量の増加、N
OX や未燃分の増加を生じるという問題を生じていた。
又、石炭の粉砕に限らず他の被粉砕物の粉砕において
も、その被粉砕物が微粉で排出されるべきところ粗粒で
排出されるのは好ましくない。However, in all of these means, since coal is discharged in the state of coarse particles, the amount of pyrite increases and N
An increase in the O X and unburned had caused the problem arises.
Further, not only in the case of crushing coal but also in the case of crushing other objects to be crushed, it is not preferable that the objects to be crushed should be discharged in the form of fine powder and coarse particles.
【0008】本発明の目的は、上記従来技術における課
題を解決し、被粉砕物を粗粒で排出することなく、自励
振動の発生を防止することができるローラミルの加圧力
制御方法を提供することにある。An object of the present invention is to solve the above-mentioned problems in the prior art and to provide a method for controlling the pressure of a roller mill which can prevent the occurrence of self-excited vibration without discharging the crushed material in coarse particles. Especially.
【0009】[0009]
【課題を解決するための手段】上記の目的を達成するた
め、本発明は、回転する粉砕テーブルと、この粉砕テー
ブルに対向する粉砕ローラと、この粉砕ローラに圧力を
加える加圧手段とを備え、この加圧手段により前記粉砕
ローラに圧力を加えた状態で前記粉砕テーブルと前記粉
砕ローラとの間で被粉砕物を粉砕するローラミルにおい
て、前記被粉砕物の供給停止後からの残炭処理領域で、
前記加圧手段により、前記粉砕ローラに加える圧力を前
記被粉砕物の供給停止時における圧力より高くして前記
ローラミルを運転するようにしたことを特徴とする。To achieve the above object, the present invention comprises a rotating crushing table, a crushing roller facing the crushing table, and a pressing means for applying pressure to the crushing roller. In a roller mill for crushing an object to be crushed between the crushing table and the crushing roller in a state where pressure is applied to the crushing roller by the pressurizing means, a residual coal treatment area after the supply of the object to be crushed is stopped. so,
It is characterized in that the pressure applying means makes the pressure applied to the crushing roller higher than the pressure when the supply of the object to be crushed is stopped to operate the roller mill.
【0010】[0010]
【発明の実施の形態】以下、本発明を図示の実施の形態
に基づいて説明する。図1は本発明の実施の形態に係る
ローラミルの加圧力制御方法を説明する図である。図1
の(a)はロールミルに対する石炭の供給量を示す図で
あり、横軸に時間、縦軸に給炭量がとってある。図1の
(b)は粉砕ローラ5に加わる加圧力の変化を示す図で
あり、横軸に時間、縦軸に加圧力がとってある。ローラ
ミルを低負荷領域で運転している状態では石炭供給量は
少なく、粉砕ローラ5に加わる加圧力も低い。この運転
状態から、時刻t1 において石炭の供給を停止すべくそ
の操作を行なうと、図1の(a)に示すように給炭量は
時間とともに減少してゆき、かつ、給炭量が少なくなる
ので、粉砕ローラ5の加圧力も図1の(b)に示すよう
に減少してゆき、時刻t2 に到って石炭の供給量が最低
(最低給炭量)となり、加圧力も最低となる。続いて、
時刻t3 で石炭供給停止指令が出力されると、石炭の供
給は0になり、ローラミルの運転は残炭処理領域に入
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the illustrated embodiments. FIG. 1 is a diagram illustrating a method for controlling a pressing force of a roller mill according to an embodiment of the present invention. FIG.
(A) is a diagram showing the amount of coal supplied to the roll mill, in which the horizontal axis represents time and the vertical axis represents the coal supply amount. FIG. 1B is a diagram showing changes in the pressing force applied to the crushing roller 5, where the horizontal axis represents time and the vertical axis represents the pressing force. When the roller mill is operating in the low load region, the amount of coal supplied is small and the pressure applied to the crushing roller 5 is also low. From this operating state, when the operation is performed to stop the coal supply at time t 1 , the coal supply amount decreases with time as shown in (a) of FIG. 1 and the coal supply amount decreases. Therefore, the pressing force of the crushing roller 5 also decreases as shown in FIG. 1 (b), and the supply amount of coal becomes the minimum (minimum coal supply amount) at time t 2 and the pressing force also becomes the minimum. Becomes continue,
When the coal supply stop command is output at time t 3 , the supply of coal becomes 0, and the operation of the roller mill enters the residual coal treatment area.
【0011】さきに述べたように、従来のローラミルで
は、上記残炭処理領域の運転において、粉砕ローラ5の
加圧力を減少させ、又は分級能力を減少させて粉砕ロー
ラ5の転動の安定を図る。しかし、本実施の形態では、
時刻t3 における石炭供給停止指令が出力されてから時
刻t4 でローラミルが停止されるまでの残炭処理領域の
運転において、図1の(b)に示すように粉砕ローラ5
の加圧力をほぼ時間に比例して増加させてゆく。As described above, in the conventional roller mill, in the operation of the residual coal treatment area, the pressing force of the pulverizing roller 5 is reduced or the classification ability is reduced to stabilize the rolling of the pulverizing roller 5. Try. However, in the present embodiment,
In the operation of the residual coal treatment area from the time the coal supply stop command is output at time t 3 to the time the roller mill is stopped at time t 4 , as shown in FIG.
The pressing force of is increased almost in proportion to time.
【0012】残炭処理領域における加圧力の上限は、粉
砕時の加圧力(粉砕する石炭量に合わせて調整された加
圧力)の30%〜300 %とすることが望ましい。即ち、30
%未満では必要とする粉砕能力を得ることができない
し、又、300 %を超えると粉砕能力が大きくなり過ぎて
微粉も細かくなり過ぎ、かつ、炭層も薄くなり過ぎて振
動を生じ易くなるからである。The upper limit of the pressing force in the residual coal treatment region is preferably 30% to 300% of the pressing force during crushing (pressing force adjusted according to the amount of coal to be crushed). That is, 30
If it is less than 100%, the required crushing ability cannot be obtained, and if it exceeds 300%, the crushing ability becomes too large and the fine powder becomes too fine, and the coal bed becomes too thin, and vibration easily occurs. is there.
【0013】このように、残炭処理領域で加圧力を増大
させてゆくことにより、粉砕ローラ5の粉砕能力が大き
くなり、ローラミル内の石炭を早く微粉砕し、これを熱
風Wによりローラミル外に迅速に排出できる。即ち、自
励振動を発生するおそれのある残炭処理領域を迅速に通
過することができるので、自励振動の発生を抑えること
ができる。さらに、従来方法のように粉砕ローラ5の加
圧力を減少させ、又は分級能力を減少させることはない
ので、ローラミル外へ排出される石炭の粒度を高めるこ
とができ、従来方法に比較してパイライト量の増加、N
OX や未燃分の増加を大幅に抑えることができる。As described above, by increasing the pressure in the residual coal treatment area, the crushing ability of the crushing roller 5 is increased, the coal in the roller mill is quickly pulverized, and the coal is pulverized by the hot air W to the outside of the roller mill. Can be discharged quickly. That is, since it is possible to quickly pass through the residual coal treatment region where self-excited vibration may occur, it is possible to suppress the occurrence of self-excited vibration. Further, unlike the conventional method, the pressing force of the crushing roller 5 is not reduced or the classification ability is not reduced, so that the particle size of the coal discharged to the outside of the roller mill can be increased, and the pyrite is compared to the conventional method. Increase in quantity, N
O X and the increase of unburned fuel can be suppressed significantly.
【0014】ここで、上記のように残炭処理領域で加圧
力を増大させることにより、当該領域での処理期間にロ
ーラミルの出炭特性が急速に上昇することが予測された
が、例えばローラミルからの石炭がボイラに供給される
場合、ボイラ側への影響(ボイラ主蒸気圧力偏差等)は
ほとんどないこと、さらに、粉砕ローラ5と粉砕テーブ
ル4とがメタルタッチ状態となったときの機械振動も無
視できることが確認された。Here, it was predicted that by increasing the pressure in the residual coal treatment region as described above, the coal milling characteristics of the roller mill would rapidly increase during the treatment period in that region. When the coal is supplied to the boiler, there is almost no influence on the boiler side (boiler main steam pressure deviation, etc.), and further, mechanical vibration when the crushing roller 5 and the crushing table 4 are in a metal touch state. It was confirmed that it can be ignored.
【0015】なお、上記実施の形態の説明において、ロ
ーラミルによる被粉砕物として石炭を例示して説明した
が、石炭以外の物体に対して適用することができるのは
当然である。又、残炭処理領域における加圧力の増加の
態様は、直線的な増加に限ることはなく、ローラミルの
構造的な条件や被粉砕物の物性等を考慮して適宜の態様
に設定することができる。In the above description of the embodiment, coal was used as an example of the object to be crushed by the roller mill, but it goes without saying that it can be applied to objects other than coal. Further, the mode of increase of the pressing force in the residual coal treatment area is not limited to the linear increase, and may be set to an appropriate mode in consideration of the structural conditions of the roller mill, the physical properties of the material to be ground, and the like. it can.
【0016】[0016]
【発明の効果】以上述べたように、本発明では、ローラ
ミルの残炭処理領域で、粉砕ローラに加える圧力を被粉
砕物の供給停止時における圧力より高くするようにした
ので、ローラミル内の石炭を早く微粉砕してローラミル
外に迅速に排出でき、自励振動を発生するおそれのある
残炭処理領域を迅速に通過することができ、自励振動の
発生を抑えることができる。さらに、従来方法のように
粉砕ローラの加圧力を減少させ、又は分級能力を減少さ
せることはないので、粗粒が排出されることはない。そ
して、ボイラに使用するローラミルの場合、ローラミル
外へ排出される石炭は微粒であるので、従来方法に比較
してパイライト量の増加や、NOX や未燃分の増加を大
幅に抑えることができる。As described above, in the present invention, the pressure applied to the crushing roller in the residual coal treatment area of the roller mill is set to be higher than the pressure when the supply of the material to be crushed is stopped. Can be quickly finely pulverized and quickly discharged to the outside of the roller mill, can quickly pass through the residual coal treatment region where self-excited vibration may occur, and suppress the occurrence of self-excited vibration. Further, since the pressing force of the crushing roller or the classification ability is not reduced unlike the conventional method, coarse particles are not discharged. In the case of a roller mill for use in a boiler, the coal is discharged to the outside of the roller mill is because it is fine, can be compared with the conventional method increases and pyrite amount, remarkably suppressed the increase of the NO X and unburned combustibles .
【図1】本発明の実施の形態に係るローラミルの加圧力
制御方法を説明する図である。FIG. 1 is a diagram illustrating a method for controlling a pressing force of a roller mill according to an embodiment of the present invention.
【図2】石炭を粉砕する竪型のローラミルの概略構成を
示す図である。FIG. 2 is a diagram showing a schematic configuration of a vertical roller mill for crushing coal.
4 粉砕テーブル 5 粉砕ローラ 6 ローラブラケット 7 下加圧フレーム 8 上加圧フレーム 12 油圧シリンダ 41 粉砕レース面 4 Grinding Table 5 Grinding Roller 6 Roller Bracket 7 Lower Pressure Frame 8 Upper Pressure Frame 12 Hydraulic Cylinder 41 Grinding Race Surface
───────────────────────────────────────────────────── フロントページの続き (72)発明者 金本 浩明 広島県呉市宝町3番36号 バブコツク日立 株式会社呉研究所内 (72)発明者 廻 信康 広島県呉市宝町3番36号 バブコツク日立 株式会社呉研究所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Hiroaki Kanemoto Inventor Hiroaki Kane City 3-36 Takaracho, Kure City, Hiroshima Babkotuku Hitachi Co., Ltd. Kure Research Institute (72) Nobuyasu Makoto 36-36 Takaracho, Kure City, Hiroshima Prefecture Babkotsu Hitachi Stock Company Kure Institute
Claims (4)
ブルに対向する粉砕ローラと、この粉砕ローラに圧力を
加える加圧手段とを備え、この加圧手段により前記粉砕
ローラに圧力を加えた状態で前記粉砕テーブルと前記粉
砕ローラとの間で被粉砕物を粉砕するローラミルにおい
て、前記被粉砕物の供給停止後からの残炭処理領域で、
前記加圧手段により、前記粉砕ローラに加える圧力を前
記被粉砕物の供給停止時における圧力より高くして前記
ローラミルを運転するようにしたことを特徴とするロー
ラミルの加圧力制御方法。1. A rotating crushing table, a crushing roller facing the crushing table, and a pressurizing means for applying a pressure to the crushing roller. In a state in which a pressure is applied to the crushing roller by the pressurizing means. In a roller mill for crushing an object to be crushed between the crushing table and the crushing roller, in a residual coal treatment area after the supply of the object to be crushed is stopped,
A method for controlling a pressing force of a roller mill, wherein the pressurizing means makes the pressure applied to the crushing roller higher than the pressure when the supply of the crushed object is stopped to operate the roller mill.
前記粉砕ローラに加える圧力は、時間にほぼ比例して増
加させることを特徴とするローラミルの加圧力制御方
法。2. The pressure control method for a roller mill according to claim 1, wherein the pressure applied to the crushing roller in the residual coal treatment region is increased substantially in proportion to time.
前記粉砕ローラに加える圧力の上限は、前記ローラミル
の加圧力の30%乃至300 %であることを特徴とするロー
ラミルの加圧力制御方法。3. The pressure control method for a roller mill according to claim 1, wherein the upper limit of the pressure applied to the crushing roller in the residual coal treatment area is 30% to 300% of the pressure applied to the roller mill. .
圧シリンダであることを特徴とするローラミルの加圧力
制御方法。4. The pressing force control method for a roller mill according to claim 1, wherein the pressurizing means is a hydraulic cylinder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP02132496A JP3681458B2 (en) | 1996-02-07 | 1996-02-07 | Roller mill pressure control method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP02132496A JP3681458B2 (en) | 1996-02-07 | 1996-02-07 | Roller mill pressure control method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09206614A true JPH09206614A (en) | 1997-08-12 |
JP3681458B2 JP3681458B2 (en) | 2005-08-10 |
Family
ID=12051975
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP02132496A Expired - Fee Related JP3681458B2 (en) | 1996-02-07 | 1996-02-07 | Roller mill pressure control method |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2019217454A (en) * | 2018-06-19 | 2019-12-26 | 三菱日立パワーシステムズ株式会社 | Vertical mill |
CN118634976A (en) * | 2024-08-15 | 2024-09-13 | 中慧农牧股份有限公司 | An intelligent control system for feed crusher |
-
1996
- 1996-02-07 JP JP02132496A patent/JP3681458B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2019217454A (en) * | 2018-06-19 | 2019-12-26 | 三菱日立パワーシステムズ株式会社 | Vertical mill |
CN118634976A (en) * | 2024-08-15 | 2024-09-13 | 中慧农牧股份有限公司 | An intelligent control system for feed crusher |
Also Published As
Publication number | Publication date |
---|---|
JP3681458B2 (en) | 2005-08-10 |
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