JPH09141116A - Vibration estimation device of crusher and control device based on vibration estimation of crusher - Google Patents
Vibration estimation device of crusher and control device based on vibration estimation of crusherInfo
- Publication number
- JPH09141116A JPH09141116A JP30164295A JP30164295A JPH09141116A JP H09141116 A JPH09141116 A JP H09141116A JP 30164295 A JP30164295 A JP 30164295A JP 30164295 A JP30164295 A JP 30164295A JP H09141116 A JPH09141116 A JP H09141116A
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- Japan
- Prior art keywords
- crusher
- vibration
- crushed
- estimated value
- value
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- 239000000463 material Substances 0.000 claims description 33
- 239000002994 raw material Substances 0.000 claims description 24
- 239000012159 carrier gas Substances 0.000 claims description 17
- 238000012937 correction Methods 0.000 claims description 12
- 239000011362 coarse particle Substances 0.000 claims description 10
- 238000005259 measurement Methods 0.000 claims description 8
- 238000010298 pulverizing process Methods 0.000 claims description 8
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- 230000003134 recirculating effect Effects 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 230000006870 function Effects 0.000 description 36
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- 238000011156 evaluation Methods 0.000 description 2
- 230000012447 hatching Effects 0.000 description 2
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- 230000002829 reductive effect Effects 0.000 description 2
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- PXFBZOLANLWPMH-UHFFFAOYSA-N 16-Epiaffinine Natural products C1C(C2=CC=CC=C2N2)=C2C(=O)CC2C(=CC)CN(C)C1C2CO PXFBZOLANLWPMH-UHFFFAOYSA-N 0.000 description 1
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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、粉砕機の振動予測
装置および粉砕機の振動予測に基づく制御装置に係わ
り、現在の運転状態およびその周囲の運転状態において
発生する振動の大きさの分布を予測することにより、粉
砕機の負荷応答性、生産物粒径を確保しつつ、閾値を超
える振動の発生を回避した運転操作を可能とし、プラン
トの安定した運用を実現するに好適な粉砕機の振動予測
装置および振動予測に基づく制御装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vibration prediction device for a crusher and a control device based on the vibration prediction for a crusher, and determines the distribution of the magnitude of vibration generated in the current operating condition and its surrounding operating conditions. By predicting, the load response of the crusher and the product particle size are secured, while enabling the operation operation that avoids the occurrence of vibration exceeding the threshold value, and the crusher suitable for realizing stable operation of the plant. The present invention relates to a vibration prediction device and a control device based on the vibration prediction.
【0002】[0002]
【従来の技術】図10は従来技術による粉砕機とその制
御装置である。被粉砕原料1は指令信号3に従ってフィ
ーダ2により、粉砕機上部に設けられたホッパ4より粉
砕機に投入されて保有手段(回転円板)5上に落下し、
後述する分級手段により発生する粗粒の再循環流10と
混合し、被粉砕物6となる。2. Description of the Related Art FIG. 10 shows a conventional crusher and its control device. The raw material 1 to be crushed is fed into the crusher by the feeder 2 according to the command signal 3 from the hopper 4 provided on the upper part of the crusher, and drops onto the holding means (rotating disc) 5,
It is mixed with the recirculation flow 10 of coarse particles generated by the classifying means described later to form the pulverized material 6.
【0003】被粉砕物6は、保有手段5の回転により発
生する遠心力により、保有手段5の中心部より外周方向
へと移動し、保有手段5と粉砕ローラ7との間で圧砕さ
れ、保有手段5の外周より吹き上げる搬送気体8により
吹き上げられる。吹き上げられた被粉砕物は、粉砕機上
部に位置し、回転羽根を原動機で回転させる回転式分級
機9により旋回を与えられ、粒径が大なる粒子は遠心力
を受けて再循環流10を形成する。一方、粒径が小さな
粒子は回転式分級器9をすり抜けて粉砕機生産物11と
なり、需要先へと搬送される。The object to be crushed 6 is moved from the central portion of the holding means 5 toward the outer peripheral direction by the centrifugal force generated by the rotation of the holding means 5, is crushed between the holding means 5 and the crushing roller 7, and is held. The carrier gas 8 is blown up from the outer periphery of the means 5. The object to be pulverized blown up is located at the upper part of the pulverizer and is swirled by the rotary classifier 9 in which the rotary blades are rotated by the prime mover, and the particles having a large particle size are subjected to centrifugal force to generate the recirculation flow 10. Form. On the other hand, the particles having a small particle diameter pass through the rotary classifier 9 to become a crusher product 11, which is conveyed to a customer.
【0004】回転式分級器は、回転羽根の回転数を制御
することにより鋭敏な分級特性を得ることが可能である
ため、生産物粒径に対する要求が厳しい用途において
は、近年、一般的に採用されている。分級手段として
は、この他に固定されたベーンにより旋回を与える固定
式分級器等があるが、ベーンの角度を制御することによ
り分級特性を調整することが可能であり、機能としては
回転式分級器と同様に考えればよい。Since the rotary classifier can obtain sensitive classification characteristics by controlling the number of rotations of the rotary blades, it has been generally adopted in recent years in applications where the product particle size is strictly required. Has been done. In addition to this, as a classification means, there is a fixed type classifier that gives a swirl by a fixed vane, but it is possible to adjust the classification characteristics by controlling the angle of the vane, and the function is a rotary type classification. You can think in the same way as a container.
【0005】また、搬送用気体8の供給量は、搬送用気
体供給路途中に設けた調整手段(ダンパ)12により調
整する。従来技術による粉砕機の制御は、一般に被粉砕
原料1の供給量に応じて分級特性指令信号13、加圧力
指令信号14、搬送気体供給量指令信号15を加減する
構成である。Further, the supply amount of the carrier gas 8 is adjusted by an adjusting means (damper) 12 provided on the way of the carrier gas supply path. The control of the crusher according to the prior art is generally configured to adjust the classification characteristic command signal 13, the pressing force command signal 14, and the carrier gas supply amount command signal 15 according to the supply amount of the crushed raw material 1.
【0006】ここでフィーダ指令信号3は、多くの場
合、粉砕機生産物11の流量が需要先の要求量に一致す
るように加減され、粉砕機生産物11の流量がオンライ
ン計測可能な場合は、その計測値と需要先の要求量の偏
差のPI(比例積分式)調節により与えればよい。とこ
ろが、多くの場合、粉砕機生産物11の流量はオンライ
ン計測が困難であるから、該流量と因果関係のある需要
先の状態量を用いて同様の目的を達成する。例えば被粉
砕原料として石炭、需要先として微粉炭焚きドラムボイ
ラを考えると、ドラムボイラの発生蒸気圧力は、粉砕機
よりバーナに供給される微粉炭流量と直接的な因果関係
を有するから、該蒸気圧力の目標値に対する偏差のPI
調節によりフィーダ指令信号3を加減すればよい。Here, in many cases, the feeder command signal 3 is adjusted so that the flow rate of the crusher product 11 matches the demand amount of the customer, and when the flow rate of the crusher product 11 can be measured online. , PI (proportional integral formula) adjustment of the deviation between the measured value and the demanded amount of the customer. However, in many cases, it is difficult to measure the flow rate of the crusher product 11 online, and therefore, the same purpose is achieved by using the state quantity of the demand destination having a causal relationship with the flow rate. For example, considering coal as a raw material to be crushed and a pulverized coal burning drum boiler as a demand destination, the generated steam pressure of the drum boiler has a direct causal relationship with the pulverized coal flow rate supplied to the burner from the pulverizer. PI of deviation from target value of pressure
The feeder command signal 3 may be adjusted by the adjustment.
【0007】分級特性指令信号13は、関数要素16に
より、一般に粉砕機は高負荷運転で粉砕機生産物11の
粗粒が増加する傾向にあるため、被粉砕原料1の供給量
が増加するとともにより強い旋回力を与えて粗粒の捕集
効率を向上させる方向で与えられる。加圧力指令信号1
4は関数要素17により、粉砕機の粉砕能力は加圧力の
増加とともに向上することに基づき、被粉砕原料1の供
給量に応じて増加する方向で与えられる。The classification characteristic command signal 13 has a tendency to increase coarse particles of the crusher product 11 due to the function element 16 in the high load operation of the crusher, so that the supply amount of the raw material 1 to be crushed increases. It is given in the direction of giving a stronger turning force to improve the collection efficiency of coarse particles. Pressure command signal 1
4 is given by the function element 17 in the direction of increasing according to the supply amount of the raw material 1 to be ground, based on the fact that the crushing capacity of the crusher is improved with the increase of the pressing force.
【0008】搬送気体供給量指令信号15は、関数要素
18により、生成される粉砕機生産物11を搬送するに
充分な輸送能力を与えるため、被粉砕物1の供給量に応
じて増加する方向で与えられる。昨今は、需要先の要求
により、低負荷運転時に一層の生産物の細粒化を求めら
れるなど、関数要素16、17、18の設定法について
上記のように画一的には論じにくいが、指令信号13、
14、15が被粉砕物1の供給量の関数となる点は共通
している。The carrier gas supply amount command signal 15 has a function element 18 which provides a sufficient transportation capacity for conveying the crusher product 11 to be produced, and therefore the carrier gas supply amount command signal 15 increases in accordance with the supply amount of the object to be crushed 1. Given in. These days, it is difficult to discuss the setting method of the function elements 16, 17, and 18 uniformly as described above, such as demanding further refinement of the product at the time of low load operation due to the demand of the customer. Command signal 13,
It is common that 14 and 15 are functions of the supply amount of the object to be ground 1.
【0009】一般に、粉砕機においては、低負荷運転時
に、正常運転時の数倍から数十倍もの非常に大きな振幅
の振動が発生することがある。このような激しい振動が
継続すると、当該粉砕機が破損する恐れがあり、その発
生、または発生の可能性を事前に検知する手段が求めら
れている。上述の激しい振動は、これまでの研究から粉
砕ローラ7の自励振動と考えられており、発生のメカニ
ズムは次のように考えられている。Generally, in a crusher, a vibration with a very large amplitude, which is several times to several tens times that of normal operation, may occur during low load operation. If such violent vibration continues, the crusher may be damaged, and means for detecting the occurrence or possibility of occurrence of the crusher in advance is required. The above-mentioned violent vibration is considered to be the self-excited vibration of the crushing roller 7 based on the studies so far, and the mechanism of occurrence is considered as follows.
【0010】前述のように、負荷調整はフィーダ2によ
る被粉砕原料供給量を加減することにより行なうため、
低負荷時においては、被粉砕原料供給量が少なくなり、
これに伴ない、保有手段5上の被粉砕物6が減少する。
このため、粉砕ローラ7の粉砕能力に余裕が生じ、相対
的に、粉砕ローラ7と保有手段5の間の被粉砕物の層が
薄くなるとともに、被粉砕物の粒径分布は粒径の細かい
方向に移行する。このため、被粉砕物の層内での摩擦係
数が低下し、該被粉砕物層内で滑りが生じる。その結
果、粉砕ローラ7が大きく振動し自励振動を引き起こ
す。As described above, the load is adjusted by adjusting the feed amount of the raw material to be pulverized by the feeder 2,
When the load is low, the amount of raw material to be crushed decreases,
Along with this, the crushed material 6 on the holding means 5 decreases.
Therefore, the crushing capacity of the crushing roller 7 has a margin, the layer of the crushed object between the crushing roller 7 and the holding means 5 becomes relatively thin, and the particle size distribution of the crushed object is small. Move in the direction. For this reason, the friction coefficient in the layer of the crushed material is lowered, and slippage occurs in the layer of the crushed object. As a result, the crushing roller 7 vibrates greatly and causes self-excited vibration.
【0011】前記炭層内での滑りは、粉砕ローラ7を保
有手段5に押しつけるローラ加圧力が大であるほど、発
生しやすい傾向にあることが知られている。このため、
低負荷時においては、激しい振動の発生を防ぐため、あ
らかじめローラ加圧力を減ずることが考えられる。しか
しながら、ローラ加圧力の減少は、粉砕ローラの粉砕能
力低下を招き、粉砕機の負荷応答性(粉砕原料供給量の
変化に対する、粉砕機生産物生成量の追従性)が悪化す
る。このため、前述のように需要先がドラムボイラであ
る場合など、粉砕機の負荷応答性がプラント全体の負荷
応答性を左右するような用途においては、可能な限りロ
ーラ加圧力を大きくしたいという要求がある。It is known that slippage in the coal seam tends to occur as the pressing force of the crushing roller 7 against the holding means 5 increases. For this reason,
When the load is low, it is conceivable to reduce the roller pressure in advance in order to prevent the occurrence of severe vibration. However, the reduction of the pressure applied to the roller causes a reduction in the pulverization ability of the pulverization roller, and the load response of the pulverizer (the ability to follow the production amount of the pulverizer product with respect to the change in the feed amount of the pulverizing material) is deteriorated. Therefore, as mentioned above, in cases where the load response of the crusher influences the load response of the entire plant, such as when the demand destination is a drum boiler, as described above, there is a demand to increase the roller pressure as much as possible. There is.
【0012】従来技術では、実機での試運転を実施し、
通常の運転範囲で粉砕機生産物粒径分布、負荷応答性が
要求を満足し、閾値を超える振動が発生しない運転操作
となるよう関数要素16、17、18の最終調整を行な
っていた。また、検出器19で粉砕機振動を、検出器2
0で粉砕機差圧を、検出器21で粉砕機に供給する搬送
用気体の温度を、検出器22で粉砕機出口の搬送気体の
温度を計測し、粉砕機内部の異常監視に利用していた。[0012] In the prior art, a trial run with an actual machine is carried out,
The function elements 16, 17 and 18 were finally adjusted so that the particle size distribution of the crusher product and the load responsiveness satisfy the requirements in the normal operation range, and the operation is such that vibration exceeding the threshold does not occur. Further, the detector 19 detects vibration of the crusher and the detector 2
The differential pressure of the crusher is 0, the temperature of the carrier gas supplied to the crusher by the detector 21 and the temperature of the carrier gas at the outlet of the crusher are measured by the detector 22, and they are used for abnormality monitoring inside the crusher. It was
【0013】[0013]
【発明が解決しようとする課題】従来技術では、前述の
ように実機の試運転時に閾値を超える振動が発生しない
操作条件(操作量の組み合わせ)を求めて関数要素1
6、17、18を設定していた。したがって、粉砕機の
構造、被粉砕原料の性状(粉砕性、etc.)が試運転時の
条件と同じであれば従来技術においても閾値を超える振
動を生じることはない。In the prior art, as described above, the function element 1 is obtained by obtaining the operation condition (combination of operation amounts) at which the vibration exceeding the threshold does not occur during the test operation of the actual machine.
6, 17, and 18 were set. Therefore, if the structure of the crusher and the properties of the raw material to be crushed (crushability, etc.) are the same as the conditions at the time of test operation, vibration exceeding the threshold value will not occur even in the conventional technique.
【0014】しかしながら、例えば、供給される被粉砕
原料の性状が変動する場合には、性状の変動に伴って、
閾値を超える振動が生じる操作条件の範囲が変わり、試
運転時には安全であった操作条件が閾値を超える振動が
発生する領域に含まれてしまうことがある。このような
場合、従来技術では、関数要素の設定は固定であるた
め、この変動に対処できず閾値を超える振動が発生する
場合が生ずる。特に、石炭焚きボイラに微粉炭を供給す
る粉砕機の場合、粉砕原料である石炭は、その銘柄(主
として産地で定まる)によって性状が大きく異なること
が知られている。However, for example, when the properties of the material to be pulverized to be supplied are changed, the changes in the properties cause
The range of operation conditions in which vibration exceeding the threshold value occurs changes, and the operation condition that was safe at the time of test operation may be included in the region in which vibration exceeding the threshold value occurs. In such a case, in the related art, since the setting of the function element is fixed, it may not be possible to cope with this variation and vibration exceeding the threshold value may occur. In particular, in the case of a crusher that supplies pulverized coal to a coal-fired boiler, it is known that the coal, which is a raw material for pulverization, has greatly different properties depending on its brand (mainly determined by the place of origin).
【0015】この点に対して、従来技術では、当該プラ
ントで使用する石炭銘柄が複数ある場合、それぞれの銘
柄ごとに試運転を実施し、関数発生器16、17、18
それぞれについて銘柄別に専用の設定を用意し、現時点
で当粉砕機に供給している石炭に対応する設定に切り替
えて使用している。ところが、この場合でも次のような
問題が残る。On the other hand, in the prior art, when there are a plurality of coal brands used in the plant, a trial run is carried out for each brand and the function generators 16, 17, 18 are carried out.
Each brand has its own dedicated setting, and it is used by switching to the setting that corresponds to the coal currently supplied to this crusher. However, even in this case, the following problems remain.
【0016】第1に従来技術では、同一粉砕原料銘柄内
での性状のばらつきへの対応が困難である。一般に石炭
のような天然に産出する固体原料は、同一の銘柄であっ
ても比較的大きな性状のばらつきがある。例えば、同一
銘柄の石炭であっても、ロットによる石炭粉砕性(HG
I)のばらつきが2割にもなることがある。粉砕性が変
動すると、粉砕ローラ7に要求され粉砕能力が相対的に
変動し、これに伴って被粉砕物保有量、被粉砕物粒径分
布も変動する。また、炭層内の滑りの発生のしやすさ
も、粉砕性に強い相関があることが知られている。この
ため、従来の石炭銘柄別の固定的な対応では十分である
とは言いがたい。First, in the prior art, it is difficult to deal with variations in properties within the same brand of pulverized raw material. In general, naturally occurring solid raw materials such as coal have relatively large variations in properties even with the same brand. For example, even if coals of the same brand are used, coal crushability (HG
The variation of I) may be 20%. When the crushability changes, the crushing ability required of the crushing roller 7 also changes relatively, and along with this, the amount of crushed material held and the particle size distribution of the crushed object also change. It is also known that the easiness of slippage in the coal seam has a strong correlation with the pulverizability. Therefore, it cannot be said that the conventional fixed measures for each coal brand are sufficient.
【0017】第2に従来技術では、複数の銘柄の粉砕原
料が混合されて供給される場合に、対応することが困難
である。複数の銘柄の粉砕材料が混合されたものが粉砕
機に供給される場合、混合する粉砕原料の銘柄、それぞ
れの混合率の組み合わせは膨大となり、あらゆる条件下
で閾値を超える振動の発生を回避とするよう関数発生要
素16、17、18を設定することは困難である。Secondly, it is difficult for the prior art to deal with the case where a plurality of brands of crushed raw materials are mixed and supplied. When a mixture of crushed materials of multiple brands is supplied to the crusher, the combination of the brands of crushed raw materials to be mixed and the respective mixing ratios will be huge, and it is possible to avoid the occurrence of vibrations that exceed the threshold under all conditions. It is difficult to set the function generating elements 16, 17, and 18 to do so.
【0018】第3に従来技術では、過渡状態への対応が
困難である。従来技術は、良好な運転が実現される操作
量の組み合わせを試験によって求めるものである。定常
状態においては、粉砕機の内部状態量は操作量の組み合
わせにより一意に定まる(石炭性状一定を仮定)。しか
し、過渡状態においては、たとえ同じ操作量であっても
内部状態が異なる場合があり得る。例えば、粉砕原料投
入量が増加する過程と、減少する過程では、全く異なる
内部状態となる。このため、急速な負荷変化時などで
は、粉砕機の内部状態が、試運転時の試験範囲を逸脱し
やすく、閾値を超える振動が発生する場合があった。Thirdly, it is difficult for the prior art to deal with a transient state. The conventional technique seeks a combination of manipulated variables that achieves good driving by a test. In the steady state, the internal state quantity of the crusher is uniquely determined by the combination of manipulated variables (assuming constant coal properties). However, in the transient state, the internal state may be different even if the manipulated variable is the same. For example, the internal state is completely different in the process of increasing the pulverized raw material input amount and the process of decreasing it. For this reason, when the load changes rapidly, the internal state of the crusher is likely to deviate from the test range during the test run, and vibration exceeding the threshold value may occur.
【0019】従来技術の問題点は、結局、次のように集
約される。 (1)振動と密接な関係にある粉砕機内部状態量(被粉
砕物保有量、被粉砕物粒径分布等)をオンラインで知る
手段が提供されていない。 (2)粉砕機に供給されている被粉砕原料の性状を、オ
ンラインで知る手段が提供されていない。 (3)前記粉砕機内部状態量、および被粉砕物性状で定
まる粉砕機の状態空間内での、現時点の粉砕機状態から
見た、激しい振動発生領域の方向、および距離を知る手
段が提供されていないために、振動回避のために必要充
分な補正操作の方向、大きさが求められない。The problems of the prior art are eventually summarized as follows. (1) There is no means for knowing online the amount of internal state of the crusher (amount of crushed object, particle size distribution of crushed object, etc.) that is closely related to vibration. (2) There is no means for knowing the properties of the raw material to be pulverized supplied to the pulverizer online. (3) A means is provided for knowing the direction and distance of a violent vibration generation region as seen from the current state of the crusher in the crusher state space determined by the crusher internal state quantity and the property of the crushed material. Therefore, the direction and size of the correction operation necessary and sufficient for avoiding vibration cannot be obtained.
【0020】本発明は、上記問題点を解決し、特に被粉
砕原料の性状が頻繁にかわるプラントにおいても安定運
用を実現する粉砕機の振動予測装置および粉砕機の振動
予測に基づく制御装置を提供するためになされたもので
ある。The present invention provides a vibration prediction device for a crusher and a control device based on the vibration prediction of the crusher, which solves the above problems and realizes stable operation especially in a plant where the properties of the material to be crushed frequently change. It was made to do.
【0021】[0021]
【課題を解決するための手段】上記目的を達成するため
本願で特許請求する発明は以下のとおりである。 (1)粉砕機内の水平面内を回転する被粉砕物の保有手
段と、該保有手段に押圧されつつ回転し該保有手段とと
もに被粉砕物の粉砕手段を構成する複数個の粉砕ローラ
と、該粉砕手段を通過した被粉砕物の粗粒分を保有手段
へ再循環させるとともに微粒分を粉砕機生産物として取
出すための分級手段と、該分級手段の分級特性の調整手
段と、粉砕機差圧を計測する手段とを有する粉砕機の振
動予測装置において、現時点の粉砕機への操作量計測値
と、前回計算時点における粉砕機状態量推定値と、粉砕
機が保有する被粉砕原料性状の前回計算時点における推
定値に基づき、現時点での粉砕機状態量推定値を算出す
る第一の演算手段と、第一の演算手段で算出した一以上
の粉砕機状態量推定値と、該状態量の計測値との一致状
況とを用い、粉砕機が当該計算時点で保有する被粉砕物
の性状を推定する第二の演算手段と、第一の演算手段で
算出した当該粉砕機の状態量の一部または全部と、該粉
砕機の操作量の一部または全部とで構成する多次元空間
における現時点での座標を中心とする一定範囲での粉砕
機振動の大きさの予測値の分布を算出する第三の演算手
段とを備えたことを特徴とする粉砕機の振動予測装置。The invention claimed in this application to achieve the above object is as follows. (1) Holding means for crushing an object to be crushed that rotates in a horizontal plane in a crusher; a plurality of crushing rollers that rotate while being pressed by the holding means to constitute crushing means for the object to be crushed; The coarse particles of the material to be crushed that has passed through the means are recirculated to the holding means and the fine particles are taken out as a crusher product, a means for adjusting the classification characteristics of the classifying means, and a crusher differential pressure In the vibration prediction device of the crusher that has a means for measuring, the measured value of the amount of operation to the crusher at the present time, the estimated value of the crusher state amount at the time of the previous calculation, and the previous calculation of the property of the crushed raw material held by the crusher Based on the estimated value at the time point, a first calculation means for calculating the current estimated value of the pulverizer state quantity, one or more estimated values of the crusher state quantity calculated by the first arithmetic means, and measurement of the state quantity Grind by using the matching status with the value A second calculating means for estimating the property of the crushed object held at the time of the calculation, a part or all of the state amount of the crusher calculated by the first calculating means, and the operation amount of the crusher. And a third arithmetic means for calculating the distribution of the predicted value of the vibration magnitude of the crusher in a certain range centered on the current coordinates in the multidimensional space formed by part or all Vibration prediction device for crushers.
【0022】(2)粉砕機内で回転する被粉砕物の保有
手段と、加圧手段により該保有手段に押圧されつつ回転
し、保有手段とともに被粉砕物の粉砕手段を構成する複
数個の粉砕ローラと、該粉砕手段を通過した被粉砕物の
粗粒分を前記保有手段へ再循環させるとともに微粒分を
粉砕機生産物として排出するための分級手段とを有し、
粉砕機への被粉砕原料供給指令信号に基づき、粉砕機へ
の原料供給量を調整する手段、前記分級手段の分級特性
を調整する手段、粉砕手段の加圧力を調整する手段およ
び粉砕機への搬送気体供給量調整手段とを備えた粉砕機
の振動予測装置において、現時点の粉砕機への被粉砕原
料の供給量と、粉砕ローラを保有手段に押付けるローラ
加圧力と、分級手段の分級特性を定める分級特性指令信
号と、搬送気体供給量信号15と、前回計算時点の粉砕
機の被粉砕物保有量推定値と、被粉砕物の粉砕性推定値
とを用いて、現時点の粉砕機の被粉砕物保有量推定値
と、保有手段上の被粉砕物粒径分布推定値と、被粉砕物
保有量推定値に基づく粉砕機の粉砕機差圧推定値とを算
出する第一の演算手段を、第一の演算手段で算出した粉
砕機差圧推定値と該粉砕機差圧実測値との偏差に基づ
き、現時点の被粉砕物の粉砕性を算出する第二の演算手
段と、第一の演算手段で算出した現在の粉砕機の被粉砕
物保有量推定値と、保有手段上の被粉砕物粒径分布推定
値と、第二の演算で算出した被粉砕物の粉砕性推定値
と、現時点のローラ加圧力とに基づいて、この4変数に
より構成される粉砕機の状態空間において、現時点の粉
砕機状態を中心とする一定範囲の粉砕機状態空間内にお
ける粉砕機振動の大きさの予測値の分布を算出する第三
の演算手段とを備えたことを特徴とする粉砕機の振動予
測装置。(2) Holding means for rotating the crushed object in the crusher, and a plurality of crushing rollers that rotate while being pressed by the holding means by the pressurizing means and constitute crushing means for the crushed object together with the holding means. And a classification means for recirculating the coarse particles of the material to be crushed that has passed through the crushing means to the holding means and discharging the fine particles as a crusher product,
Based on the crushed raw material supply command signal to the crusher, means for adjusting the amount of raw material supplied to the crusher, means for adjusting the classification characteristics of the classifying means, means for adjusting the pressing force of the crushing means and the crusher In a vibration predicting device of a crusher equipped with a carrier gas supply amount adjusting means, a current supply amount of a material to be crushed to a crusher, a roller pressing force for pressing a crushing roller against a holding means, and a classification characteristic of a classifying means. Of the pulverizer at the present time by using the classification characteristic command signal that determines the value, the carrier gas supply amount signal 15, the estimated value of the pulverized object possessed by the pulverizer at the time of the previous calculation, and the estimated pulverizability of the pulverized object. First computing means for calculating an estimated value of the crushed material holding amount, an estimated value of the crushed object particle size distribution on the holding means, and an estimated value of the crusher differential pressure of the crusher based on the estimated crushed object holding amount value And the estimated value of the crusher differential pressure calculated by the first calculation means and Based on the deviation from the measured value of the crusher differential pressure, the second calculation means for calculating the crushability of the crushed object at the present time, and the current estimated value of the crushed object held by the crusher calculated by the first calculating means. , The crushing constituted by these four variables, based on the particle size distribution estimated value of the object to be crushed on the holding means, the pulverizability estimated value of the object to be crushed calculated by the second operation, and the roller pressing force at the present time. In the state space of the machine, a third arithmetic means for calculating the distribution of the predicted value of the magnitude of the crusher vibration in the crusher state space within a certain range centering on the current crusher state is provided. Vibration prediction device for crushers.
【0023】(3)粉砕機内で水平に回転する被粉砕物
の保有手段と、加圧手段により該保有手段に押圧されつ
つ回転し保有手段とともに被粉砕物の粉砕手段を構成す
る粉砕ローラと、該粉砕手段を通過した被粉砕物の粗粒
分を前記保有手段に再循環させるとともに微粒分を粉砕
機外に排出するための分級手段と、該分級手段の分級特
性の調整手段と、粉砕機差圧を計測する手段とを有する
粉砕機の振動予測装置において、粉砕機の動特性モデル
を用い、現時点の当該粉砕機への被粉砕原料供給量と、
粉砕ローラを前記保有手段に押圧するローラ加圧力と、
分級特性指令信号、前回計算時点の被粉砕物保有量推定
値と、被粉砕物の粉砕性推定値とを用いて、現時点の粉
砕機内被粉砕物保有量推定値と、保有手段上の被粉砕物
粒径分布推定値とを算出し、さらに被粉砕物保有量推定
値に基づき粉砕機差圧推定値とを算出する第一の演算手
段と、前記粉砕機差圧推定値と該差圧実測値との偏差か
ら現時点の被粉砕物の粉砕性を推定する第二の演算手段
と、ローラ加圧力と被粉砕物保有量推定値と、保有手段
上の被粉砕物粒径分布推定値と、被粉砕物の粉砕性推定
値と、逐次学習する過去の振動発生履歴に基づいて、現
時点の粉砕機状態量を中心とする一定範囲の粉砕機状態
量空間内における振動の大きさの予測値の分布を算出す
る第三の演算手段とを備えたことを特徴とする粉砕機の
振動予測装置。 (4)(1)〜(3)のいずれか記載の粉砕機振動予測
装置によって算出された振動予測値分布に基づきローラ
加圧力補正信号と、分級特性補正信号を算出する手段
と、上記算出された上記補正信号に基づき粉砕機のロー
ラ加圧力と分級手段の分級特性を調整する手段とを設け
たことを特徴とする粉砕機の振動予測に基づく制御装
置。(3) Holding means for the object to be crushed which horizontally rotates in the crusher, and a crushing roller which rotates while being pressed by the holding means by the pressing means and constitutes a crushing means for the object to be crushed together with the holding means. Classifying means for recirculating the coarse particles of the material to be crushed that has passed through the crushing means to the holding means and discharging fine particles to the outside of the crusher, means for adjusting the classification characteristics of the classifying means, and a crusher In a vibration predicting device for a crusher having a means for measuring a differential pressure, a dynamic characteristic model of the crusher is used, and a raw material supply amount to be crushed to the crusher at the present time,
A roller pressing force for pressing the crushing roller against the holding means,
Using the classification characteristic command signal, the estimated value of the crushed object holding amount at the time of the previous calculation, and the crushability estimated value of the crushed object, the current estimated value of the crushed object held amount in the crusher and the crushed object on the holding means A first calculation means for calculating the particle size distribution estimated value and further for calculating the pulverizer differential pressure estimated value based on the pulverized material holding amount estimated value; the pulverizer differential pressure estimated value and the differential pressure actual measurement A second calculation means for estimating the pulverizability of the pulverized material at the present time from the deviation from the value, the roller pressing force and the pulverized material holding amount estimated value, the pulverized material particle size distribution estimated value on the holding means, Based on the estimated crushability of the crushed object and the history of past vibrations that are successively learned, the predicted value of the magnitude of vibration in the crusher state quantity space within a certain range centered on the current crusher state quantity A vibration predicting apparatus for a crusher, comprising: a third calculating means for calculating a distribution. (4) Means for calculating the roller pressing force correction signal and the classification characteristic correction signal based on the vibration predicted value distribution calculated by the crusher vibration prediction device according to any one of (1) to (3), and the above calculation. A controller based on vibration prediction of a crusher, characterized in that it is provided with means for adjusting the roller pressure of the crusher and the classification characteristics of the classifying means based on the correction signal.
【0024】本発明は、振動発生に強い相関があるとさ
れる、粉砕機の内部状態量(例えば、被粉砕物保有量、
被粉砕物粒径分布)と粉砕機操作量(例えば、粉砕圧力
ローラ加圧力)、および被粉砕物の性状(例えば、被粉
砕物粉砕性)による多次元状態空間を想定し、該多次元
状態空間内での当該粉砕機実機に発生する振動の大きさ
(振幅)の分布を、オンラインで学習、参照する手段を
与えるものである。According to the present invention, the amount of internal state of the crusher (for example, the amount of crushed material retained, which is considered to have a strong correlation with the vibration generation,
Assuming a multidimensional state space based on the crushed object particle size distribution), the crusher operation amount (for example, crushing pressure roller pressure), and the crushed object property (for example, crushed object crushability), the multidimensional state is assumed. It provides a means for learning and referring to the distribution of the magnitude (amplitude) of the vibration generated in the actual crusher machine in the space online.
【0025】ところが、粉砕機実機においては、内部状
態量の多くはオンラインで計測することが困難である。
そこで、本発明では、必要な粉砕機内部状態量を粉砕機
の動特性モデル算出する。動特性モデルでの粉砕機内部
状態量算出には、被粉砕物の性状(例えば粉砕性)のよ
うに、確定していない量(以下未知パラメータと呼ぶ)
が存在し、計算誤差の原因となる。これに対処するた
め、本発明では、粉砕機実機において計測可能、かつ代
表的な粉砕機内部状態に強い相関性をもつ量(例えば粉
砕機差圧、粉砕機動力)を動特性モデルにおいて推定
し、該推定値の当該実測値との偏差がなくなるよう、未
知パラメータを逐次同定する構成をとる。However, in the actual crusher, it is difficult to measure most of the internal state quantities online.
Therefore, in the present invention, the required crusher internal state quantity is calculated as a dynamic characteristic model of the crusher. In calculating the internal state quantity of the crusher using the dynamic characteristic model, the undetermined quantity (hereinafter referred to as unknown parameter) such as the property of the crushed object (eg, crushability)
Exists, which causes a calculation error. In order to deal with this, in the present invention, an amount that can be measured in an actual crusher machine and has a strong correlation with a typical crusher internal state (for example, crusher differential pressure, crusher power) is estimated in a dynamic characteristic model. , The unknown parameters are sequentially identified so that there is no deviation between the estimated value and the actual measured value.
【0026】以下、粉砕機内部状態量として被粉砕物6
保有量、被粉砕物6粒径分布を、オンライン計測可能な
量として、被粉砕物6保有量と強い相関性をもつ粉砕機
差圧を、未知パラメータとして被粉砕物6粉砕性を採用
した場合を例にとり、具体的な計算手順を説明する。第
1の演算手段において、対象とする粉砕機実機の操作信
号、および前回の計算時点において固定した当該被粉砕
物粉砕性推定値を粉砕性仮定値として粉砕機の動特性モ
デルに与え、被粉砕物6保有量、被粉砕物6粒径分布な
どの粉砕機内部状態量推定値を求める。さらに、推定し
た被粉砕物6保有量に基づいて粉砕機差圧推定値を算出
する。Hereinafter, the crushed object 6 is defined as the internal state quantity of the crusher.
When the amount of possession and the particle size distribution of the object to be pulverized 6 can be measured online, the differential pressure of the pulverizer which has a strong correlation with the amount of the object to be pulverized 6 is adopted, and the object 6 pulverizability of the object to be pulverized is used as an unknown parameter. Taking the example as an example, a specific calculation procedure will be described. In the first computing means, the operation signal of the target crusher actual machine and the crushability estimated value of the crushed object fixed at the time of the previous calculation are given to the kinetic model of the crusher as a crushability assumed value, and the crushed object is crushed. Estimated values of the amount of internal state of the crusher, such as the amount of the object 6 held and the particle size distribution of the object 6 to be crushed are obtained. Further, the crusher differential pressure estimated value is calculated based on the estimated amount of the crushed object 6 held.
【0027】第2の演算手段において、第1の演算手段
によって算出した粉砕機差圧推定値の当該実測値に対す
る偏差に基づいて、被粉砕物6の粉砕性推定値を更新す
る。一般的に、粉砕機差圧の推定値が実測値よりも大で
ある場合(被粉砕物6保有量が実機よりも多いと推定す
ることに相当)は、粉砕性を過小(実際よりも割れにく
い)評価していると判断して、被粉砕物6粉砕性推定値
を増加方向に修正し、逆の場合も同様に作用する。The second computing means updates the pulverizability estimation value of the object to be pulverized 6 based on the deviation of the estimated pulverizer differential pressure value calculated by the first computing means from the actual measurement value. Generally, when the estimated value of the crusher differential pressure is larger than the actual measured value (equivalent to estimating that the crushed object 6 possession amount is larger than the actual machine), the pulverizability is too small (cracking is smaller than actual). It is judged that it is difficult to evaluate, and the estimated pulverizability of the pulverized material 6 is corrected in the increasing direction, and the same is true in the opposite case.
【0028】なお、第1の演算手段と第2の演算手段の
作動形態は、各計算時点において、上述の粉砕機差圧の
推定値と実測値の偏差が規定値以内となるまで収斂計算
を繰り返す場合と1回または規定回数で当該収束計算を
打ち切る場合がある。これらは、採用する計算機の計算
速度と各計算時点の時間間隔の兼ね合いで決定する。第
3の演算手段は、2つの機能をもつ。第1の機能は、振
動分布更新機能であり、現在の粉砕機振動計測値を、操
作量であるローラ加圧力、第1の演算手段で算出した被
粉砕物6保有量推定値、被粉砕物6粒径分布推定値、被
粉砕物6粉砕性推定値などの、粉砕機振動と強い相関性
を持つ量を軸として構成される。多次元空状態空間内の
現在の座標における実績値として記録する。この動作
を、粉砕機の運転中逐次行なうことにより、十分な時間
が経過した後には、図2に示すような該多次元状態空間
内での振動分布が得られる。第2の機能は、前記振動分
布の参照機能であり、当該条件を中心とする一定範囲
(図3のハッチングの範囲)の多次元状態空間内での当
該粉砕機での振動分布を参照し、当該範囲内の振動予測
分布として出力する。The operating forms of the first calculating means and the second calculating means are such that, at each calculation point, convergence calculation is performed until the deviation between the estimated value and the measured value of the crusher differential pressure is within a specified value. The convergence calculation may be repeated once or may be terminated once or a prescribed number of times. These are determined in consideration of the calculation speed of the computer used and the time interval at each calculation time point. The third calculation means has two functions. The first function is a vibration distribution updating function, and the current crusher vibration measurement value is the operation amount of the roller pressing force, the crushed object 6 estimated amount of the crushed object 6 calculated by the first calculating means, and the crushed object. It is configured with the amount having a strong correlation with the vibration of the crusher, such as the estimated value of 6 particle size distribution and the estimated value of 6 crushability of the object to be crushed. Record as the actual value at the current coordinates in the multidimensional empty state space. By sequentially performing this operation during the operation of the crusher, a vibration distribution in the multidimensional state space as shown in FIG. 2 can be obtained after a sufficient time has elapsed. The second function is a reference function of the vibration distribution, and refers to the vibration distribution in the crusher in a multidimensional state space within a certain range (hatched range in FIG. 3) centering on the condition, It is output as a vibration prediction distribution within the range.
【0029】第3の手段において振動予測値の分布を求
める範囲は、広範囲に求めると計算機負荷が大きくなる
反面、狭くすると、振動発生領域に達するまでに時間的
余裕が得られず、充分な回避操作が行なえないおそれが
あるため、両者を勘案して設定する。以上の作用によ
り、当該粉砕機の現在の状態について、該多次元状態空
間での現時点の位置、およびその周囲の状態において発
生が予測される振動の大きさの分布が得られる。当該位
置および振動の分布を参照することにより、粉砕機の状
態が、閾値を超える振動領域に近づいた場合に警報等に
より運転員に通知し回避操作を促す、または、発生する
領域を回避するために必要な補正操作量を算出すること
が可能となる。In the third means, the range for obtaining the distribution of the predicted vibration value increases the computer load if it is obtained over a wide range, but if the range is narrowed, there is no time margin to reach the vibration generation area, and sufficient avoidance is possible. It may not be possible to operate, so set it in consideration of both. With the above operation, for the current state of the crusher, the distribution of the magnitude of vibration predicted to occur at the current position in the multidimensional state space and the surrounding states can be obtained. By referring to the position and the distribution of vibration, when the state of the crusher approaches a vibration area exceeding a threshold value, an operator is notified by an alarm or the like to prompt an avoidance operation, or to avoid an area where it occurs. It is possible to calculate the correction operation amount necessary for
【0030】[0030]
【発明の実施の形態】本発明になる振動予測方式の一実
施例を図1に示す。図10と同じ構成部品については同
一の番号を付して説明を省略する。第1の演算手段10
0は、現時点で実機に与えられているものと同一の操作
量(フィーダ指令信号3、分級特性指令信号13、ロー
ラ加圧力指令信号14、搬送用気体供給量指令信号1
5)を入力とし、被粉砕物6粉砕性の仮定値(前回計算
時点での被粉砕物粉砕性推定値202)に基づき、内蔵
した動特性モデルを用いて、現時点の被粉砕物保有量推
定値101、被粉砕物粒径分布推定値102を算出し、
該保有炭量推定値より粉砕機差圧推定値103を得る。FIG. 1 shows an embodiment of a vibration prediction method according to the present invention. The same components as those in FIG. 10 are designated by the same reference numerals and the description thereof will be omitted. First computing means 10
0 is the same operation amount as that given to the actual machine at present (feeder command signal 3, classification characteristic command signal 13, roller pressing force command signal 14, carrier gas supply amount command signal 1).
5) as an input, and based on the assumed value of the pulverizability of the pulverized material 6 (estimated pulverizability of the pulverized material at the time of the previous calculation 202), use the built-in dynamic characteristic model to estimate the amount of pulverized material currently held Value 101, crushed object particle size distribution estimated value 102,
The crusher differential pressure estimated value 103 is obtained from the stored coal amount estimated value.
【0031】当該動特性モデルとしては、着目する諸量
の関係を実測データで整理した統計モデルを用いること
も可能であるが、粉砕機の諸過程(粉砕、分級、混合な
ど)を忠実に模擬した物理モデルが、最も広範囲の条件
下で高精度であるため、本実施例では物理モデルを採用
する。本実施例に適用可能な粉砕機の物理モデルの詳細
については、後述する。As the dynamic characteristic model, it is possible to use a statistical model in which relations of various quantities of interest are arranged by actual measurement data, but various processes of the crusher (crushing, classification, mixing, etc.) are faithfully simulated. Since this physical model has high accuracy under the widest range of conditions, the physical model is adopted in this embodiment. Details of the physical model of the crusher applicable to this embodiment will be described later.
【0032】第2の演算手段200は、粉砕機差圧推定
値103の当該計測値19に対する偏差201を入力と
して、被粉砕物6粉砕性仮定値(前回の被粉砕物粉砕性
推定値202)をPI機能により補正し、現時点におけ
る被粉砕物粉砕性推定値202を算出する。前述のよう
に、粉砕機差圧は当該粉砕機の被粉砕物6保有量と強い
相関をもち、同一の操作量の元では被粉砕物6保有量に
対して単調に増加することが知られている。したがっ
て、前記偏差201が正の値、すなわち粉砕機差圧の推
定値が実測値よりも大きい場合は、被粉砕物6保有量を
実際よりも多めに推定していることを示している。一
方、操作量が同一であれば、被粉砕物6保有量の変化は
被粉砕物6の粉砕性の変動に起因すると考えられる。例
えば、粉砕性が増加すれば(割れやすくなれば)、一回
の粉砕機構の通過により製品粒度にまで崩壊する粒子の
割合が増加するため、分級機構により再循環される荒い
粒子が減少する。このため、再循環分と新規投入分の場
合により形成される被粉砕物6の保有量は減少する。以
上の知見より、第2の演算手段における被粉砕物6粉砕
性推定値202の補正は、偏差201が正の値であれ
ば、増加方向に、負の値であれば減少方向に行なうよう
PI(比例積分式)制御器を設定すればよい。The second computing means 200 receives the deviation 201 of the estimated pulverizer differential pressure value 103 with respect to the measured value 19 as an input, and assumes the pulverizability assumed value of the crushed object 6 (previously estimated crushability value of the crushed object 202). Is corrected by the PI function to calculate the crushed material crushability estimated value 202 at the present time. As described above, it is known that the crusher differential pressure has a strong correlation with the crushed object 6 holding amount of the crusher, and monotonically increases with respect to the crushed object 6 holding amount under the same operation amount. ing. Therefore, when the deviation 201 is a positive value, that is, when the estimated value of the crusher differential pressure is larger than the actually measured value, it indicates that the amount of the object to be crushed 6 is estimated more than it actually is. On the other hand, if the manipulated variables are the same, it is considered that the change in the amount of the pulverized material 6 held is due to the change in the pulverizability of the pulverized material 6. For example, as grindability increases (becomes more fragile), the proportion of particles that disintegrate to the product particle size in a single pass through the grinding mechanism increases, thus reducing the coarse particles recycled by the classification mechanism. For this reason, the amount of the pulverized material 6 formed by the recirculation portion and the new input portion is reduced. Based on the above knowledge, the correction of the crushability estimation value 202 of the crushed object 6 in the second calculation means is performed in the increasing direction if the deviation 201 is a positive value, and in the decreasing direction if the deviation 201 is a negative value. (Proportional-integral type) The controller may be set.
【0033】第3の演算手段300は、ローラ加圧力指
令信号14、被粉砕物保有量推定値101、被粉砕物粒
径分布推定値102、被粉砕物粉砕性推定値202、粉
砕機振動計測値30を入力として、後述する振動予測配
列を更新するとともに、該配列に記録された過去におけ
る振動発生の実績を参照し、現時点の粉砕機状態を中心
とする一定範囲の粉砕機状態空間内での振動予測値の分
布(以下振動分布予測値という)301を算出する。図
3は、2次元の状態空間における振動分布予測の例であ
り、第3の演算手段は同図中の黒点で示した現在の状態
を中心とした振動回避制御に必要十分な範囲(ハッチン
グの範囲)の振動分布を出力する。The third calculation means 300 measures the roller pressing force command signal 14, the crushed object holding amount estimation value 101, the crushed object particle size distribution estimated value 102, the crushed object crushability estimated value 202, and the crusher vibration measurement. While inputting the value 30, the vibration prediction array described later is updated, and the past record of vibration occurrence recorded in the array is referred to, and within a certain range of the crusher state space centering on the current crusher state The distribution 301 of the predicted vibration value (hereinafter, referred to as predicted vibration distribution value) is calculated. FIG. 3 is an example of vibration distribution prediction in a two-dimensional state space, and the third calculation means is a range (hatching of hatching) necessary and sufficient for vibration avoidance control centered on the current state indicated by the black dots in FIG. The vibration distribution of (range) is output.
【0034】なお、振動予測配列と同様の入出力関係
は、階層型ニューラルネットワークを逐次学習すること
でも実現可能であり、両者の選択は対象の性質と、引算
機負荷を勘案して行なう。振動予測配列の出力は、構造
上、図4のような階段状の分布となるが、必要に応じて
適当な補間、関数近似等を施すことにより、図2のよう
な連続的な分布を得ることが可能である。なお、図2〜
図4は、本実施例で振動予測に用いる状態量として被粉
砕物保有量とローラ加圧力のみを選択した場合のもので
あるが、多次元状態空間(n>2)から、他の状態量を
固定した断面についての図と看做すことも可能である。The input / output relationship similar to that of the vibration prediction array can be realized by sequentially learning the hierarchical neural network, and the selection of both is made in consideration of the target property and the subtractor load. The output of the vibration prediction array has a staircase distribution as shown in FIG. 4 due to its structure, but a continuous distribution as shown in FIG. 2 is obtained by performing appropriate interpolation, function approximation, etc., if necessary. It is possible. In addition, FIG.
FIG. 4 shows the case where only the crushed object holding amount and the roller pressing force are selected as the state quantities used for vibration prediction in the present embodiment, but other state quantities are selected from the multidimensional state space (n> 2). It can also be regarded as a diagram of a fixed cross section.
【0035】次に粉砕機の動特性モデルおよび振動予測
配列について説明する。 1.粉砕機の動特性モデル 本実施例では、発明者自身の研究に係わり、粒度分布を
わずか4つの変数で模擬可能で、高精度、低計算量な手
法(計測自動制御学会中国支部学術講演会;平3/12
/13にて発明者が講演)を採用することとし、以下詳
述する。 1.1 記号・略号・用語 1.1.1 添字 下記の添字は特定の部位、機構、関数、時点を示す。Next, the dynamic characteristic model of the crusher and the vibration prediction array will be described. 1. In this example, the dynamic characteristic model of the crusher is involved in the research of the inventor himself, and the method of simulating the particle size distribution with only four variables and having high accuracy and low calculation amount (Measurement Automatic Control Society China Branch Academic Lecture Meeting; Flat 3/12
/ 13 will be adopted by the inventor and will be described in detail below. 1.1 Symbols / abbreviations / terms 1.1.1 Subscripts The following subscripts indicate specific parts, mechanisms, functions, and time points.
【0036】b : 混合機構 ib: 粉砕機入口 ij: 第j番目の分級機構入口 ip: 粉砕機構入口 j : 第j番目の分級機構 ob: 混合機構出口 op: 粉砕機構出口 rj: 第j番目の分級機構による循環流 s : 粉砕分布定数 oj: 第j番目の分級機構による通過流 1.1.2 記号 βk : k次キュムラント μ : 平均 ξ : 対数粒径(ノミナルな値) σ : 標準偏差 b(ξ): 粉砕速度定数 c(ξ): 部分分級効率 f(ξ): 一般に確率密度関数 g(ξ): 粒度分布確率密度関数 g(ξ|η): 条件付き確率密度関数 Ξ : 粒子の対数粒径(確率変数) s(ξ): 粉砕分布定数 vk (λ,ρ): (λ,ρ)に規格化したk次モーメ
ント E(・): 期待値 E(・|・): 条件付き期待値 Var(・): 分散 Pr(・) : 確率 Q : 重量流量 Θ : 分級過程で、ある粒子が通過(Θ=1)、また
は捕集(Θ=0)の事象を現すインジケータ(確率変
数) 1.1.3 語句 確率変数 : 「揺らぎ」や情報不足のため、確率的な
変数値の評価を要す(値を確定的に知り得ない;雑音、
粉体流量、石炭性状が典型的)変数。したがって、確率
Pr{x<X≦x+Δx}(確率変数Xの値がxの近傍
となる確率)を fX (X)Δx (fX (X):xの確率密度関数)で与え、必要な統計
量を計算する。B: mixing mechanism ib: crusher inlet ij: j-th classifying mechanism inlet ip: crushing mechanism inlet j: j-th classifying mechanism ob: mixing mechanism outlet op: crushing mechanism outlet rj: j-th number Circulating flow by classifying mechanism s: Grinding distribution constant oj: Throughflow by j-th classifying mechanism 1.1.2 Symbol β k : k-th cumulant μ: average ξ: logarithmic particle size (nominal value) σ: standard deviation b ( ξ): Grinding rate constant c (ξ): Partial classification efficiency f (ξ): Generally probability density function g (ξ): Particle size distribution probability density function g (ξ | η): Conditional probability density function Ξ: Logarithm of particles Particle size (random variable) s (ξ): Milling distribution constant v k (λ, ρ): kth moment normalized to (λ, ρ) E (・): Expected value E (・ | ・): Conditional Expected value Var (•): Variance Pr (•): Probability Q: Weight Flow rate Θ: Indicator (random variable) that a particle passes through (Θ = 1) or collects (Θ = 0) in the classification process. 1.1.3 Words Random variable: Because of “fluctuation” or lack of information, Requires probabilistic evaluation of variable values (values cannot be known deterministically; noise,
Variables are powder flow rate and coal properties). Therefore, the probability Pr {x <X ≦ x + Δx} (probability that the value of the random variable X is in the vicinity of x) is given by f X (X) Δx (f X (X): probability density function of x) Calculate statistics.
【0037】キュムラント: 特性関数(確率密度関数
のフーリエ変換)の対数をローラン展開した際、第k次
の展開係数をk次キュムラントと呼ぶ。応用上、「モー
メントと相互変換可能」、「重畳積分(粉砕機構での粒
度分布変化)が加算に帰着」など、便利な性質がある。 Skewness: 歪度と訳され、分布の左右対称性の程度を
示す。Cumulant: When the logarithm of the characteristic function (Fourier transform of the probability density function) is Laurent expanded, the kth expansion coefficient is called a kth cumulant. In terms of application, it has convenient properties such as "interchangeable with moment" and "superimposed integral (change in particle size distribution in the crushing mechanism) results in addition". Skewness: Translated as skewness and indicates the degree of left-right symmetry of the distribution.
【0038】Excess: 尖度と訳され、分布の中心部、
裾の部分の割合を示す(正規分布では=3)。 条件付き確率密度: 2つの事象の因果関係を考えると
き、一方の情報を得たときの他方の確率密度を示す。具
体的には粉砕機構入口で粒径がη<Θip≦η+dηの粒
子が粉砕後にξ<Θip≦ξ+Δξになる確率はΘopのΘ
ipに対する確率密度関数( Conditional probability d
ensity function of Θop given by Θ ip)を用いてg
op|ip(ξ|η)dξと表される。 1.2 粉砕機内の現象 1.2.1 粒度分布の表記 断面を微小時間に通過する粒子中、粒径ξ以下なる質量
割合により粒度分布が定義可能で、その密度関数をg
(ξ)と表記し、適宜に場所を示す添字を付加する。サ
ンプルされた静止状態の質量粒度分布密度f(ξ)との
関係を質量流量Qを用いて次式となる。Excess: Translated as kurtosis, the center of the distribution,
Indicates the proportion of the skirt (= 3 for normal distribution). Conditional probability density: Considering the causal relationship between two events
The probability density of the other when the information of one is obtained is shown. Ingredient
Physically, the particle size is η <Θ at the entrance of the crushing mechanism.ip≦ η + dη grain
After the child is crushed ξ <ΘipThe probability that ≦ ξ + Δξ is ΘopΘ
ipProbability density function for (conditional probability d
ensity function of Θop given by Θ ip) With g
op | ipIt is expressed as (ξ | η) dξ. 1.2 Phenomena inside the crusher 1.2.1 Indication of particle size distribution Mass of particle size ξ or less among particles passing through the cross section in a short time
The particle size distribution can be defined by the ratio, and its density function is g
It is written as (ξ), and a subscript indicating the place is appropriately added. Sa
The sampled static mass particle size distribution density f (ξ)
The relationship is expressed by the following equation using the mass flow rate Q.
【0039】[0039]
【数1】 (Equation 1)
【0040】1.2.2 粉砕機構 粉砕前後の所量にそれぞれ添え字ip、opを与える
と、粒度分布について次の関係がある。1.2.2 Grinding Mechanism When the subscripts ip and op are given to the quantities before and after the crushing, the particle size distribution has the following relationship.
【0041】[0041]
【数2】 (Equation 2)
【0042】ここに、粒径ξを対数軸にとると条件付き
確率密度gop|ipは、L. Austin らの解明した粉砕分布
定数(Power Technology, Vol. 29, pp.263-275(1981)
、同、Vol. 33, pp.113-125(1982) 、同、Vol. 33, p
p.127-134(1982) に記載)と一致し、これをsとする。[0042] Here, the particle size probability density conditionally take on a logarithmic axis ξ g op |.. Ip is, L Austin, et al. Elucidated the grinding distribution constant (Power Technology, Vol 29, pp.263-275 (1981 )
, Ibid, Vol. 33, pp. 113-125 (1982), ibid, Vol. 33, p.
p.127-134 (1982)), and this is designated as s.
【0043】[0043]
【数3】 gOP|ip(ξ|η)=s(ξ−η) (3) この粉砕分布定数sは粉砕機構を通過する粒子粉砕性に
依存することが知られている。質量流量については、粉
砕機構内で蓄積はないと仮定して次式を得る。## EQU3 ## g OP | ip (ξ | η) = s (ξ−η) (3) It is known that this pulverization distribution constant s depends on the pulverizability of particles passing through the pulverization mechanism. As for the mass flow rate, the following equation is obtained assuming that there is no accumulation in the grinding mechanism.
【0044】[0044]
【数4】 E{Qop}=E{Qip} (4) 1.2.3 分級機構 第j番目の分級機構について、各「粒子の通過」は互い
に独立事象であって、Θjをインジケータとすれば、実
験により解明されている分級効率cj (ξ)(廻ほか、
粉体工学誌、Vol.25、pp.480-436(1988) に記載)と次
の関係がある。E {Q op } = E {Q ip } (4) 1.2.3 Classification Mechanism For the j-th classification mechanism, each “particle passage” is an independent event, and Θj can be used as an indicator. For example, the classification efficiency c j (ξ) (Mari et al.
Powder Engineering Journal, Vol.25, pp. 480-436 (1988)) and the following relationships.
【0045】[0045]
【数5】 Pr{Θj =0|(ξ,ξ+dξ)}=cj (ξ) (5) Pr{Θj =1|(ξ,ξ+dξ)}=1−cj (ξ) (6) 分級器入口、循環流、および通過流に係る諸量にそれぞ
れ添字ij、rj、ojを与えると、ベイズ定理により
粒度分布密度を表す次式を得る。Equation 5] Pr {Θ j = 0 | ( ξ, ξ + dξ)} = c j (ξ) (5) Pr {Θ j = 1 | (ξ, ξ + dξ)} = 1-c j (ξ) (6) When the subscripts ij, rj, and oj are given to the quantities related to the classifier inlet, the circulation flow, and the passing flow, respectively, the following equation representing the particle size distribution density is obtained by the Bayes theorem.
【0046】[0046]
【数6】 (Equation 6)
【0047】である。分級機構周辺の流量は次のとおり
求められる。It is The flow rate around the classification mechanism is calculated as follows.
【0048】[0048]
【数7】 E{Qrj}=E{Θj Qij}=rjE{Qij} (10) E{Qoj}=E{(1−Θj )Qij}=(1−rj)E{Qij} (11) 1.2.4 混合機構 分級機構(j=0,………,n)からの循環流と被粉砕
原料(添字ib)とを混合して流出流(添字ob)とな
す機構を考える。ここで、混合機構保有被粉砕物Gb と
Qobとの間に次の関係を仮定する。E {Q rj } = E {Θ j Q ij } = rj E {Q ij } (10) E {Q oj } = E {(1-Θ j ) Q ij } = (1- rj ) E {Q ij } (11) 1.2.4 Mixing mechanism The circulating flow from the classifying mechanism (j = 0, ..., N) and the raw material to be crushed (subscript ib) are mixed to form an outflow (subscript ob). Think about the mechanism. Here, the following relationship is assumed between the objects to be ground G b and Q ob held by the mixing mechanism.
【0049】[0049]
【数8】 E{Qob}=E{P}E{Gb } (12) Pは粒径と独立とし、この仮定を正当化するため、混合
機構と、それに続く粉砕機構の間に仮想的な分級機構
(j=0)を設けて前出の L. Austinらが解明したξに
依存する粉砕速度定数を考慮する。E {Q ob } = E {P} E {G b } (12) P is independent of particle size, and in order to justify this assumption, a hypothesis exists between the mixing mechanism and the subsequent grinding mechanism. Considering the ξ-dependent crushing rate constant elucidated by L. Austin et al., Mentioned above, by providing a general classification mechanism (j = 0).
【0050】ここで、前出の第(1)式と第(12)式
に着目し、混合により粒径は変化しないと考えて、
(ξ,ξ+dξ)に属する粒子のマスバランス式が得ら
れる。Here, paying attention to the above equations (1) and (12), considering that the particle size does not change due to mixing,
A mass balance formula of particles belonging to (ξ, ξ + dξ) is obtained.
【0051】[0051]
【数9】 (Equation 9)
【0052】1.3 モデルの数学的記述 1.3.1 分布密度のパラメタライズ Ξが分布密度g(ξ)にしたがうときλ、ρで基準化
(アフィン変換)したモーメントを考える。1.3 Mathematical Description of Model 1.3.1 Parameterization of Distribution Density Consider a moment normalized (affine transformation) by λ and ρ when Ξ follows distribution density g (ξ).
【0053】[0053]
【数10】 (Equation 10)
【0054】このとき、キュムラントβk (λ,ρ)が
対応して求められる。本モデルでは分布密度を次のパラ
メータで整理する。At this time, the cumulant β k (λ, ρ) is correspondingly obtained. In this model, the distribution density is organized by the following parameters.
【0055】[0055]
【数11】 μ=v1(0,1),σ=〔v2(0,1)〕 1/2 (15) Skewness:β3(μ,σ)=v3(μ,σ) (16) Excess:β4(μ,σ)=v4(μ,σ) -3 (17) これらにより、一意にエッジワース展開係数αk が求ま
り、分布密度を具体的に表示できる。(11) μ = v 1 (0,1), σ = [v 2 (0,1)] 1/2 (15) Skewness: β 3 (μ, σ) = v 3 (μ, σ) (16 ) Excess: β 4 (μ, σ) = v 4 (μ, σ) −3 (17) From these, the edge-worth expansion coefficient α k can be uniquely obtained, and the distribution density can be specifically displayed.
【0056】[0056]
【数12】 (Equation 12)
【0057】ここに、p(ξ;μ,σ)はガウス分布、
hk はk次のエルミート多項式である。 1.3.2 粉砕機構 前出の第(3)式を第(2)式に代入すると重畳積分で
あって、キュムラントの和に帰着し、以下を得る。Where p (ξ; μ, σ) is a Gaussian distribution,
h k is a Hermitian polynomial of degree k. 1.3.2 Grinding mechanism Substituting equation (3) above into equation (2) gives a convolution integral, which results in the sum of cumulants, and obtains the following.
【0058】[0058]
【数13】 v1op ( μip, σip) =v1s( μip, σip) (19) v2op ( μip, σip) =1+v2s( μip, σip) (20) v3op ( μip, σip) =v3ip ( μip, σip) +v3s( μip,σip) (21) v4op ( μip, σip) =v4ip ( μip, σip) +v4s( μip,σip) +6v2s( μip,σip) (22) ここに、添字sは粉砕分布定数sを、それ以外は各粒度
分布密度gを指す。さらに、μop、σop、β3(μop,σ
op) 、β4(μop,σop) は前出の第(15)式〜第(1
7)式および次式を用いて計算できる。(13) v 1op (μ ip, σ ip ) = v 1s (μ ip, σ ip ) (19) v 2op (μ ip, σ ip ) = 1 + v 2s (μ ip, σ ip ) (20) v 3op (μ ip, σ ip ) = v 3ip (μ ip, σ ip ) + v 3s (μ ip , σ ip ) (21) v 4op (μ ip, σ ip ) = v 4ip (μ ip, σ ip ) + v 4s (μ ip , σ ip ) + 6v 2s (μ ip , σ ip ) (22) Here, the subscript s indicates the pulverization distribution constant s, and the others indicate each particle size distribution density g. Furthermore, μ op , σ op , β 3 (μ op , σ
op ), β 4 (μ op , σ op ) are the above-mentioned equations (15) to (1)
It can be calculated using the equation 7) and the following equation.
【0059】[0059]
【数14】 [Equation 14]
【0060】1.3.3 分級機構 cj (ξ)は、適当なτmj、λmj、ρmjを用いて近似で
きる。1.3.3 Classification Mechanism c j (ξ) can be approximated by using appropriate τ mj , λ mj and ρ mj .
【0061】[0061]
【数15】 gij(ξ)は第(18)式の形式であり、第(7)式お
よび第(10)式より、循環流の諸量が具体的に求めら
れる。(Equation 15) g ij (ξ) is in the form of the expression (18), and various quantities of the circulating flow are specifically obtained from the expressions (7) and (10).
【0062】[0062]
【数16】 (Equation 16)
【0063】ここに、次の関数がある。Here are the following functions:
【0064】[0064]
【数17】 [Equation 17]
【0065】また、αOrjmk は、次式にエルミート多項
式の加法定理を適用し、係数を整理して得られる。Further, α Orjmk can be obtained by applying the Hermitian polynomial addition theorem to the following equation and arranging the coefficients.
【0066】[0066]
【数18】 (Equation 18)
【0067】前出の第(25)式は分布密度の重み付き
混合であり、添字mについてαOrjm k からvk ( λmrj,
ρmrj ) が一意に求まり、同一λ、ρのvk は重み付き
加算が可能だから、結局前出の第(23)式、第(1
5)式〜第(17)式を用いて、μrj,σrj, β3(μ
rj, σrj),β4(μrj,σrj) が計算できる。添字ojの
通過流についても同様の議論である。 1.3.4 混合機構 適当に選んだλb,ρb で基準化すると、前出の第(1
3)式よりvkob についての微分方程式を得る。The above equation (25) is a weighted mixture of distribution densities, where α Orjm k to v k (λ mrj,
ρ mrj ) is uniquely obtained, and v k of the same λ and ρ can be weighted and added, so that the expression (23), the expression (1
Using equations (5) to (17), μ rj , σ rj, β 3 (μ
rj, σ rj ), β 4 (μ rj , σ rj ) can be calculated. The same argument applies to the passing flow with the subscript oj. 1.3.4 Mixing mechanism When normalized by properly selected λ b and ρ b , the above (1)
From equation 3), a differential equation for v kob is obtained.
【0068】[0068]
【数19】 [Equation 19]
【0069】第(23)式第(15)式〜第(17)式
を適用すれば、一般にμ、σ、β3( μ, σ) 、β4(μ,
σ) 、とvk (λ,σ)の相互変換が可能だから、1.
3.2、1.3.3 の結論を代入して(30)を解くことがで
きる。このとき、Pade近似の採用で、安定な数値計算が
可能となった。したがって、初期条件としてE
{Qob}、vkob ( λb,ρb ) を与え、実機粉砕機と同
様の操作量を与え、以上の諸式を逐次解くことにより、
被粉砕物6保有量E{Gb }および、その粒度分布であ
るvkb( λib, ρib) を求めることができる。 2.振動予測配列 本発明の目的となる、対象とするn次元状態空間内での
振動分布を求めることは、次のn入力関数を求めること
に他ならない。By applying the equations (15) to (17), in general, μ, σ, β 3 (μ, σ), β 4 (μ,
Since σ) and v k (λ, σ) can be mutually transformed, 1.
(30) can be solved by substituting the conclusions of 3.2 and 1.3.3. At this time, stable numerical calculation became possible by adopting the Pade approximation. Therefore, as an initial condition, E
By giving {Q ob }, v kob (λ b, ρ b ), giving the same amount of operation as the actual crusher, and solving the above equations sequentially,
The amount E {G b } of the object to be crushed 6 and its particle size distribution v kb (λ ib, ρ ib ) can be obtained. 2. Vibration prediction array Obtaining the vibration distribution in the target n-dimensional state space, which is the object of the present invention, is nothing but obtaining the following n-input function.
【0070】[0070]
【数20】 h(x1 ,x2 ,………,xn ) (31) ここに、 h(x): 振動分布を表すn入力関数 x1 ,……,xn : n次元状態空間内での座標 である。計算機において関数hの形を求める手段として
は、なんらかの仮定に基づいて関数hの形を既知の数学
的な関数(対数関数、放物線など)で近似し、近似誤差
が最少となるよう近似関数のパラメータを調整する方法
がよく用いられる。しかしながら、このような方法は、
関数の形がある程度予想され、また、入力の数が少ない
場合にのみ有効であり、本発明で対象とするような、多
入力かつ形の予測が困難な対象には適用は難しい。Equation 20] h (x 1, x 2, ........., x n) (31) Here, h (x): n input function x 1 representing the vibration distribution, ......, x n: n-dimensional state space It is the coordinate within. As a means for obtaining the shape of the function h in a computer, the shape of the function h is approximated by a known mathematical function (logarithmic function, parabola, etc.) based on some assumption, and the parameters of the approximation function are minimized so that the approximation error is minimized. The method of adjusting is often used. However, such a method
It is effective only when the shape of the function is expected to some extent, and is effective only when the number of inputs is small, and it is difficult to apply it to an object, such as the object of the present invention, which has many inputs and whose shape is difficult to predict.
【0071】したがって、本発明では、n次元状態空間
を適当な大きさのメッシュに分割し、各メッシュ内で発
生した振動を記録、参照することにより振動分布を模擬
する、振動予測配列を採用する。本振動予測配列は、具
体的には、計算機上のメモリに確保された配列として実
現される。最も単純な構成では、対象とするn次元状態
空間を図5(2次元での例)のように均等な大きさのメ
ッシュに分割し、各メッシュに含まれる領域において、
発生する振動の予測値を格納するn次元(nは入力数)
配列Y(y1 ,y 2 ,……,yn ) を用いる。Therefore, in the present invention, the n-dimensional state space is
Is divided into meshes of appropriate size, and
Simulates vibration distribution by recording and referencing generated vibration
The vibration prediction array is adopted. This vibration prediction array is
Physically, it is actually implemented as an array secured in the memory on the computer.
Will be revealed. In the simplest configuration, the target n-dimensional state
As shown in Fig. 5 (two-dimensional example), the space should have a uniform size.
In the area included in each mesh,
N dimensions (n is the number of inputs) that stores the predicted value of the generated vibration
Array Y (y1, Y Two, ……, yn) Is used.
【0072】該振動予測値の更新は、第3の演算手段の
計算周期ごとに実施される。また、該振動予測値の算出
手段については、過去の最大値、過去の平均値など、種
々の設定方法があるが、ここでは最近の一定期間内に発
生した振動の最大値を振動予測値として採用する。例え
ば、対象とするメッシュに含まれる領域内において、過
去1カ月間に発生した振動の最大値を、のメッシュの振
動予測値とするものである。The vibration predicted value is updated every calculation cycle of the third calculating means. Further, there are various setting methods such as the maximum value in the past and the average value in the past for the calculation means of the vibration predicted value, but here, the maximum value of the vibration that has occurred in a certain recent period is used as the vibration predicted value. adopt. For example, the maximum value of vibrations generated in the past one month in the area included in the target mesh is used as the vibration predicted value of the mesh.
【0073】[0073]
【数21】 Y(y1 ,y2 ,……,yn ) =MAX{H(y1 ,y2 ,……,yn ) } (32) ここに、MAX{K}は、集合Kの中に含まれる最大値
を出力する関数であり、H(y1 ,y2 ,……,yn )
は、最近の一定期間内に、対応する領域内で計測された
粉砕機振動値の集合である。Y (y 1 , y 2 , ..., Y n ) = MAX {H (y 1 , y 2 , ..., Y n )} (32) where MAX {K} is the set K. Is a function that outputs the maximum value included in H (y 1 , y 2 , ..., Y n ).
Is a set of crusher vibration values measured in the corresponding region over a recent period of time.
【0074】これは、安全側の評価を重視するととも
に、運転の継続による、粉砕機構(保有手段5、および
粉砕ローラ7)の磨耗などにより、振動の分布が移動す
ることを考慮するものである。対象とする粉砕機の操作
量の変動に伴い、該内部状態は刻々変動し、多次元状態
空間内を移動していく。これに伴って、当該座標に対応
する振動予測配列の要素が更新され、図4に示すような
多次元状態空間内での振動分布が得られる。This emphasizes the evaluation on the safety side and considers that the vibration distribution moves due to abrasion of the crushing mechanism (holding means 5 and crushing roller 7) due to continuous operation. . As the operation amount of the target crusher changes, the internal state changes every moment and moves in the multidimensional state space. Along with this, the element of the vibration prediction array corresponding to the coordinate is updated, and the vibration distribution in the multidimensional state space as shown in FIG. 4 is obtained.
【0075】本推定装置の稼動を開始する際には、振動
予測配列の初期値として、経験的に知られている振動領
域を概略与えておけばよい。その後、振動予測配列は逐
次更新されるため、充分な運転期間が経過した後には、
該プラントの特性を反映した配列が形成される。図6
は、本発明になる振動予測方式を制御装置に応用した場
合の実施例である。When the operation of the present estimation device is started, it is sufficient to roughly give an empirically known vibration region as an initial value of the vibration prediction array. After that, the vibration prediction array is updated sequentially, so after a sufficient period of operation,
An array is formed that reflects the characteristics of the plant. FIG.
Is an embodiment when the vibration prediction method according to the present invention is applied to a control device.
【0076】第4の演算手段400は、振動分布予測値
301に基づき、閾値を超える振動が発生する領域の、
現時点の粉砕機状態から見た距離、および方向を算出
し、該距離および方向に基づいて、ファジィ推論により
ローラ加圧力補正信号401、および分級特性補正指令
信号402を求める。一般的には、閾値を超える振動が
発生する領域に接近するに従い、ローラ加圧力を減少、
または分級特性を緩める(50%通過粒径を大径化す)
る方向に補正すればよい。The fourth computing means 400 calculates, based on the vibration distribution predicted value 301,
The distance and direction viewed from the current state of the crusher are calculated, and the roller pressing force correction signal 401 and the classification characteristic correction command signal 402 are obtained by fuzzy reasoning based on the distance and direction. Generally, the roller pressing force is reduced as it approaches the area where vibration exceeding the threshold value occurs.
Or loosen the classification characteristics (increasing the 50% passing particle size)
It may be corrected in the direction of
【0077】従来技術による振動発生時の対応を図2上
で示したものが図7である。従来技術では、黒点で表さ
れる状態より、白点で表される状態に移行しようとする
場合、移行経路中に閾値を超える振動発生領域が含まれ
ていても、それを知る手段がないために回避することが
できない。このため、検出器19により、激しい振動の
発生を検知後に、ローラ加圧力を急激かつ大幅に減ずる
などの振動抑制操作を手動介入、または自動操作により
行なっていた。図8は、このような回避操作を行なった
場合の、粉砕機生成物流量および同粒径分布の挙動をシ
ミュレーションにより求めたものであるが、回避操作に
よる影響がはっきりと現れている。FIG. 7 shows the correspondence when the vibration occurs according to the prior art in FIG. In the prior art, when trying to shift from a state represented by a black dot to a state represented by a white dot, there is no means to know that even if the transition path includes a vibration generation area exceeding a threshold value. Cannot be avoided. For this reason, after detecting the occurrence of severe vibration by the detector 19, a vibration suppressing operation such as sharply and drastically reducing the roller pressing force is performed by manual intervention or automatic operation. FIG. 8 shows the behavior of the pulverizer product flow rate and the same particle size distribution obtained by simulation when such an avoiding operation is performed, but the effect of the avoiding operation is clearly shown.
【0078】本実施例では、図9に示すように、現在の
状態の周辺における振動の分布を参照し、閾値を超える
振動領域に接近すると、該振動領域から遠ざかるように
補正操作が行なわれる結果、図9のように、閾値を超え
る振動が発生する領域を最少限度に迂回した運転操作を
行なうことが可能となる。この場合、操作量の急激な変
更は必要なく、前述のような悪影響は発生しない。ま
た、例えば、ローラ加圧力の低減など、粉砕機の特性に
影響を与える振動回避操作を必要最低限に抑えることが
可能となるため、粉砕機の特性を良好に保つことが可能
となる。In the present embodiment, as shown in FIG. 9, referring to the vibration distribution around the current state, when a vibration area exceeding the threshold value is approached, a correction operation is performed so as to move away from the vibration area. As shown in FIG. 9, it is possible to perform a driving operation that detours a region where vibration exceeding a threshold value occurs to the minimum limit. In this case, it is not necessary to drastically change the operation amount, and the above-mentioned adverse effect does not occur. Further, for example, it is possible to suppress the vibration avoiding operation that affects the characteristics of the crusher, such as reduction of the pressure applied to the roller, to the minimum necessary, so that the characteristics of the crusher can be kept good.
【0079】[0079]
【発明の効果】本発明により、被粉砕物の性状が頻繁に
変動するプラントにあっても、粉砕機の状態空間内にお
ける振動予測値の分布が与えられる。該分布を用いるこ
とにより、閾値を超える振動の予測、該振動の発生を回
避するに必要な操作の算出が可能となり、その結果、激
しい振動の発生によるプラントの破損、抑制操作による
悪影響の発生を事前に回避し、プラントの安定した運転
が実現されるという効果がある。EFFECTS OF THE INVENTION According to the present invention, even in a plant where the properties of the material to be ground frequently change, the distribution of the predicted vibration value in the state space of the grinding machine can be provided. By using this distribution, it is possible to predict vibrations that exceed the threshold and to calculate the operation required to avoid the occurrence of the vibrations. It has the effect of avoiding it in advance and realizing stable operation of the plant.
【図1】本発明の第一の実施例を示す図。FIG. 1 is a diagram showing a first embodiment of the present invention.
【図2】多次元状態空間内の振動分布の模式図を示す
図。FIG. 2 is a diagram showing a schematic diagram of vibration distribution in a multidimensional state space.
【図3】一定範囲の振動分布予測の説明図。FIG. 3 is an explanatory diagram of prediction of vibration distribution in a certain range.
【図4】振動予測配列によって与えられる振動予測分布
の例を示す図。FIG. 4 is a diagram showing an example of a vibration prediction distribution given by a vibration prediction array.
【図5】振動予測配列の説明図。FIG. 5 is an explanatory diagram of a vibration prediction array.
【図6】本発明による振動予測結果を粉砕機の制御装置
に応用した場合の実施例説明図。FIG. 6 is an explanatory view of an embodiment in which the vibration prediction result according to the present invention is applied to a control device for a crusher.
【図7】従来技術による振動回避操作の説明図。FIG. 7 is an explanatory diagram of a vibration avoidance operation according to a conventional technique.
【図8】従来技術による振動回避操作時の粉砕機の生成
物流量、粒径分布の挙動の例を示す説明図。FIG. 8 is an explanatory diagram showing an example of the behavior of the product flow rate and particle size distribution of the crusher during the vibration avoidance operation according to the conventional technique.
【図9】本発明による振動回避操作の説明図。FIG. 9 is an explanatory diagram of a vibration avoidance operation according to the present invention.
【図10】従来技術による粉砕機の制御装置の説明図。FIG. 10 is an explanatory view of a control device for a crusher according to a conventional technique.
1…被粉砕原料、2…フィーダ、3…フィーダ指令信
号、4…ホッパ、5…保有手段、6…被粉砕物、7…粉
砕ローラ、8…搬送気体、9…回転分級機、10…再循
環流、11…粉砕機生産物、12…ダンパ、13…分級
特性指令信号、14…加圧力指令信号、15…搬送気体
供給量指令信号、16、17、18…関数要素、19…
(振動)検出器、20…(差圧)検出器、21…(搬送
気体入口温度)検出器、22…(搬送気体出口温度)検
出器、25…粉砕機、100…第一の演算手段、101
…被粉砕物保有量推定値、102…被粉砕物粒度分布推
定値、103…粉砕機差圧推定値、200…第二の演算
手段、201…粉砕機差圧推定偏差、202…被粉砕物
粉砕性推定値、300…第三の演算手段、301…振動
予測値分布。1 ... Material to be ground, 2 ... Feeder, 3 ... Feeder command signal, 4 ... Hopper, 5 ... Holding means, 6 ... Object to be ground, 7 ... Grinding roller, 8 ... Carrier gas, 9 ... Rotary classifier, 10 ... Re Circulating flow, 11 ... Grinder product, 12 ... Damper, 13 ... Classification characteristic command signal, 14 ... Pressurization command signal, 15 ... Carrier gas supply command signal, 16, 17, 18 ... Function element, 19 ...
(Vibration) detector, 20 ... (Differential pressure) detector, 21 ... (Carrier gas inlet temperature) detector, 22 ... (Carrier gas outlet temperature) detector, 25 ... Grinder, 100 ... First computing means, 101
... Estimated amount of crushed object held, 102 ... Estimated value of particle size distribution of crushed object, 103 ... Estimated value of crusher differential pressure, 200 ... Second computing means, 201 ... Estimated deviation of crusher differential pressure, 202 ... crushed object Grindability estimated value, 300 ... Third calculation means, 301 ... Vibration predicted value distribution.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 山中 幹夫 広島県呉市宝町6番9号 バブコック日立 株式会社呉工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Mikio Yamanaka 6-9 Takaracho, Kure City, Hiroshima Prefecture Babcock Hitachi Kure Factory
Claims (4)
の保有手段と、該保有手段に押圧されつつ回転し該保有
手段とともに被粉砕物の粉砕手段を構成する複数個の粉
砕ローラと、該粉砕手段を通過した被粉砕物の粗粒分を
保有手段へ再循環させるとともに微粒分を粉砕機生産物
として取出すための分級手段と、該分級手段の分級特性
の調整手段と、粉砕機差圧を計測する手段とを有する粉
砕機の振動予測装置において、現時点の粉砕機への操作
量計測値と、前回計算時点における粉砕機状態量推定値
と、粉砕機が保有する被粉砕原料性状の前回計算時点に
おける推定値に基づき、現時点での粉砕機状態量推定値
を算出する第一の演算手段と、第一の演算手段で算出し
た一以上の粉砕機状態量推定値と、該状態量の計測値と
の一致状況とを用い、粉砕機が当該計算時点で保有する
被粉砕物の性状を推定する第二の演算手段と、第一の演
算手段で算出した当該粉砕機の状態量の一部または全部
と、該粉砕機の操作量の一部または全部とで構成する多
次元空間における現時点での座標を中心とする一定範囲
での粉砕機振動の大きさの予測値の分布を算出する第三
の演算手段とを備えたことを特徴とする粉砕機の振動予
測装置。1. A holding means for holding an object to be ground which rotates in a horizontal plane in a grinder, and a plurality of grinding rollers which rotate while being pressed by the holding means to constitute a means for grinding the object to be ground together with the holding means. Classifying means for recirculating the coarse particles of the material to be crushed that has passed through the crushing means to the holding means and for taking out fine particles as a crusher product, a means for adjusting the classification characteristics of the classifying means, and a crusher difference In the vibration predicting device of the crusher having a means for measuring the pressure, the operation amount measurement value to the crusher at the present time, the crusher state amount estimated value at the time of the previous calculation, and the crushed raw material property held by the crusher. Based on the estimated value at the time of the previous calculation, first calculating means for calculating the current estimated value of the crusher state amount, one or more estimated values of the crusher state amount calculated by the first calculating means, and the state amount Using the matching situation with the measured value of A second calculation means for estimating the property of the crushed object held by the crusher at the time of the calculation, a part or all of the state quantity of the crusher calculated by the first calculation means, and And a third calculation means for calculating the distribution of the predicted value of the magnitude of the crusher vibration within a certain range centered on the coordinates at the present time in the multidimensional space formed by a part or all of the manipulated variables. A vibration prediction device for a crusher, which is characterized in that
と、加圧手段により該保有手段に押圧されつつ回転し、
保有手段とともに被粉砕物の粉砕手段を構成する複数個
の粉砕ローラと、該粉砕手段を通過した被粉砕物の粗粒
分を前記保有手段へ再循環させるとともに微粒分を粉砕
機生産物として排出するための分級手段とを有し、粉砕
機への被粉砕原料供給指令信号に基づき、粉砕機への原
料供給量を調整する手段、前記分級手段の分級特性を調
整する手段、粉砕手段の加圧力を調整する手段および粉
砕機への搬送気体供給量調整手段とを備えた粉砕機の振
動予測装置において、現時点の粉砕機への被粉砕原料の
供給量と、粉砕ローラを保有手段に押付けるローラ加圧
力と、分級手段の分級特性を定める分級特性指令信号
と、搬送気体供給量信号と、前回計算時点の粉砕機の被
粉砕物保有量推定値と、被粉砕物の粉砕性推定値とを用
いて、現時点の粉砕機の被粉砕物保有量推定値と、保有
手段上の被粉砕物粒径分布推定値と、被粉砕物保有量推
定値に基づく粉砕機の粉砕機差圧推定値とを算出する第
一の演算手段と、第一の演算手段で算出した粉砕機差圧
推定値と該粉砕機差圧実測値との偏差に基づき、現時点
の被粉砕物の粉砕性を算出する第二の演算手段と、第一
の演算手段で算出した現在の粉砕機の被粉砕物保有量推
定値と、保有手段上の被粉砕物粒径分布推定値と、第二
の演算で算出した被粉砕物の粉砕性推定値と、現時点の
ローラ加圧力とに基づいて、この4変数により構成され
る粉砕機の状態空間において、現時点の粉砕機状態を中
心とする一定範囲の粉砕機状態空間内における粉砕機振
動の大きさの予測値の分布を算出する第三の演算手段と
を備えたことを特徴とする粉砕機の振動予測装置。2. A holding means for rotating an object to be ground which rotates in a crusher, and a rotating means while being pressed by the holding means by a pressurizing means,
A plurality of crushing rollers which constitute a crushing means for crushing the object to be crushed, and coarse particles of the crushed object which have passed through the crushing means are recirculated to the holding means, and fine particles are discharged as a crusher product. And a means for adjusting the amount of raw material supplied to the crusher based on the crushed raw material supply command signal to the crusher, a means for adjusting the classification characteristics of the classifying means, and a crushing means. In a vibration predicting device of a crusher equipped with means for adjusting pressure and means for adjusting the amount of carrier gas supplied to the crusher, the current supply amount of the material to be crushed to the crusher and the crushing roller are pressed against the holding means. Roller pressing force, classification characteristic command signal that determines the classification characteristics of the classification means, carrier gas supply amount signal, estimated value of crushed material possessed by the crusher at the time of previous calculation, and estimated crushability of the crushed object Using the current grinding First calculation for calculating the crushed object holding amount estimated value, the crushed object particle size distribution estimated value on the holding means, and the crusher differential pressure estimated value of the crusher based on the crushed object holding amount estimated value Means for calculating the pulverizability of the object to be pulverized at the present time based on the deviation between the estimated value of the pulverizer differential pressure calculated by the first arithmetic means and the actual measured value of the pulverizer differential pressure; The current estimated value of the crushed object possessed by the crusher calculated by one calculating means, the estimated value of the particle size distribution of the crushed object on the holding means, and the estimated pulverizability of the crushed object calculated by the second operation And the pressure of the roller at the present time, in the state space of the crusher constituted by these four variables, the magnitude of the crusher vibration in the crusher state space within a certain range centered on the current crusher state And a third calculation means for calculating the distribution of predicted values of Prediction device.
有手段と、加圧手段により該保有手段に押圧されつつ回
転し保有手段とともに被粉砕物の粉砕手段を構成する粉
砕ローラと、該粉砕手段を通過した被粉砕物の粗粒分を
前記保有手段に再循環させるとともに微粒分を粉砕機外
に排出するための分級手段と、該分級手段の分級特性の
調整手段と、粉砕機差圧を計測する手段とを有する粉砕
機の振動予測装置において、粉砕機の動特性モデルを用
い、現時点の当該粉砕機への被粉砕原料供給量と、粉砕
ローラを前記保有手段に押圧するローラ加圧力と、分級
特性指令信号、前回計算時点の被粉砕物保有量推定値
と、被粉砕物の粉砕性推定値とを用いて、現時点の粉砕
機内被粉砕物保有量推定値と、保有手段上の被粉砕物粒
径分布推定値とを算出し、さらに被粉砕物保有量推定値
に基づき粉砕機差圧推定値とを算出する第一の演算手段
と、前記粉砕機差圧推定値と該差圧実測値との偏差から
現時点の被粉砕物の粉砕性を推定する第二の演算手段
と、ローラ加圧力と被粉砕物保有量推定値と、保有手段
上の被粉砕物粒径分布推定値と、被粉砕物の粉砕性推定
値と、逐次学習する過去の振動発生履歴に基づいて、現
時点の粉砕機状態量を中心とする一定範囲の粉砕機状態
量空間内における振動の大きさの予測値の分布を算出す
る第三の演算手段とを備えたことを特徴とする粉砕機の
振動予測装置。3. A holding means for the object to be crushed which horizontally rotates in the crusher, a crushing roller which rotates while being pressed by the holding means by a pressure means and constitutes a crushing means for the object to be crushed together with the holding means, Classifying means for recirculating the coarse particles of the material to be crushed that has passed through the crushing means to the holding means and discharging fine particles to the outside of the crusher, means for adjusting the classification characteristics of the classifying means, and crusher difference In a vibration predicting device for a crusher having a means for measuring pressure, a dynamic characteristic model of the crusher is used, and the amount of raw material to be crushed supplied to the crusher at present, and a roller addition for pressing the crushing roller against the holding means. Using the pressure, the classification characteristic command signal, the estimated value of the crushed object holding amount at the time of the previous calculation, and the crushability estimated value of the crushed object, the current estimated value of the crushed object held in the crusher and the holding means Calculate the estimated particle size distribution of the crushed object In addition, the first calculation means for calculating the crusher differential pressure estimated value based on the crushed object holding amount estimated value, and the current crushed object based on the deviation between the crusher differential pressure estimated value and the measured differential pressure value. A second calculation means for estimating the pulverizability of the object, a roller pressing force, an estimated value of the amount of the object to be pulverized, an estimated value of the particle size distribution of the object of pulverization on the retaining means, an estimated value of the pulverizability of the object A third calculating means for calculating a distribution of predicted values of vibration magnitude in a crusher state quantity space within a certain range centered on the crusher state quantity at the present time, based on the past vibration occurrence history that is sequentially learned And a vibration predicting device for a crusher.
動予測装置によって算出された振動予測値分布に基づき
ローラ加圧力補正信号と、分級特性補正信号を算出する
手段と、上記算出された上記補正信号に基づき粉砕機の
ローラ加圧力と分級手段の分級特性を調整する手段とを
設けたことを特徴とする粉砕機の振動予測に基づく制御
装置。4. A means for calculating a roller pressing force correction signal and a classification characteristic correction signal based on the vibration predicted value distribution calculated by the crusher vibration prediction device according to claim 1, and the above calculation. A controller based on vibration prediction of a crusher, characterized in that it is provided with means for adjusting the roller pressure of the crusher and the classification characteristics of the classifying means based on the correction signal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30164295A JPH09141116A (en) | 1995-11-20 | 1995-11-20 | Vibration estimation device of crusher and control device based on vibration estimation of crusher |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30164295A JPH09141116A (en) | 1995-11-20 | 1995-11-20 | Vibration estimation device of crusher and control device based on vibration estimation of crusher |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH09141116A true JPH09141116A (en) | 1997-06-03 |
Family
ID=17899402
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30164295A Pending JPH09141116A (en) | 1995-11-20 | 1995-11-20 | Vibration estimation device of crusher and control device based on vibration estimation of crusher |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH09141116A (en) |
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- 1995-11-20 JP JP30164295A patent/JPH09141116A/en active Pending
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