JP3056916B2 - Granulation control device using fluidized bed - Google Patents

Granulation control device using fluidized bed

Info

Publication number
JP3056916B2
JP3056916B2 JP5158433A JP15843393A JP3056916B2 JP 3056916 B2 JP3056916 B2 JP 3056916B2 JP 5158433 A JP5158433 A JP 5158433A JP 15843393 A JP15843393 A JP 15843393A JP 3056916 B2 JP3056916 B2 JP 3056916B2
Authority
JP
Japan
Prior art keywords
fluidized bed
granulation
state
detecting means
gas ejection
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP5158433A
Other languages
Japanese (ja)
Other versions
JPH078784A (en
Inventor
広行 辻本
豊和 横山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hosokawa Micron Corp
Original Assignee
Hosokawa Micron Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hosokawa Micron Corp filed Critical Hosokawa Micron Corp
Priority to JP5158433A priority Critical patent/JP3056916B2/en
Publication of JPH078784A publication Critical patent/JPH078784A/en
Application granted granted Critical
Publication of JP3056916B2 publication Critical patent/JP3056916B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Glanulating (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、流動層利用の造粒制御
装置に関し、詳述すると、気体噴出口を形成した回転盤
をケーシングの底部に設け、その気体噴出口から噴出さ
れる気流により、供給部からの造粒原料を流動層状態に
して、前記ケーシングの上方空間に設けた結合剤噴出機
構から結合剤を噴霧して造粒する流動層利用の造粒装置
において、流動層の上面高さを検出する層高検出手段
と、前記気体噴出口からの気体噴出量を調節する気体噴
出量調節手段と、前記層高検出手段により検出された流
動層の上面高さを一定に維持するように前記気体噴出量
調節手段を制御する造粒制御手段とからなる流動層利用
の造粒制御装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a granulation control device utilizing a fluidized bed, and more particularly, to a rotary disk having a gas outlet formed at the bottom of a casing, which is provided with a gas flow blown from the gas outlet. In a granulating apparatus utilizing a fluidized bed in which a granulated raw material from a supply unit is put into a fluidized bed state and a binder is sprayed from a binder ejecting mechanism provided in an upper space of the casing to granulate the fluidized bed, Bed height detecting means for detecting the height, gas ejection amount adjusting means for adjusting the gas ejection amount from the gas ejection port, and maintaining the upper surface height of the fluidized bed detected by the bed height detection means constant. Thus, the present invention relates to a granulation control device using a fluidized bed, comprising a granulation control means for controlling the gas ejection amount adjusting means.

【0002】[0002]

【従来の技術】上述の造粒装置を用いて各種造粒処理を
実行する場合、結合剤噴出機構から噴霧された結合剤に
より造粒原料が結合して粒が成長するに伴い、増加する
質量に抗して流動層状態を維持するために、気体噴出口
からの気体噴出量を増す必要がある。そのために、従来
の流動層利用の造粒制御装置を、その気体噴出量を調節
するのに、層高検出手段により検出された流動層の上面
高さを指標に、その値を一定に維持するように造粒制御
する造粒制御手段を設けて構成していた。そして、造粒
過程における流動層状態の監視は、層高検出手段による
流動層の上面高さの変化や、運転員の目視観察に頼った
ものであり、流動層状態の崩れを発見した場合には、気
体噴出口からの気体噴出量を、手動により通常よりも過
剰に増すことにより流動層状態を回復していた。ここ
に、流動層状態の崩れとは、図6に示すように、結合剤
噴出機構からの結合剤の噴霧状態の乱れにより部分的に
塊が発生し、それの塊が成長して遂には造粒物が流動層
状態から脱して全体的な塊に至るブロッキング状態や、
図5に示すように、流動層内の湿潤度が上昇した場合
に、流動層内に気体噴出口からの噴出気体の抜け道が発
生して、そのために正常な流動状態を維持するための気
流が乱れて遂には造粒物が流動層状態から脱して全体的
な塊に至るチャネリング状態が発生することをいい、か
かる事態が発生すると運転を停止し、造粒物を廃棄せざ
るを得ないのである。
2. Description of the Related Art When various types of granulation processes are performed using the above-described granulating apparatus, the mass increases as the granules grow due to the binding of the granulated raw materials by the binder sprayed from the binder ejection mechanism. In order to maintain the fluidized bed state against the above, it is necessary to increase the gas ejection amount from the gas ejection port. For this purpose, the conventional granulation control device using a fluidized bed uses the upper surface height of the fluidized bed detected by the bed height detecting means as an index to adjust the gas ejection amount, and keeps the value constant. Thus, granulation control means for controlling granulation is provided. Monitoring of the state of the fluidized bed during the granulation process relies on changes in the height of the upper surface of the fluidized bed by the bed height detection means and visual observation by the operator. However, the fluidized bed state was recovered by manually increasing the amount of gas ejected from the gas ejection port more than usual. Here, the collapse of the fluidized bed state means that, as shown in FIG. 6, a lump is partially generated due to the disorder of the spray state of the binder from the binder ejection mechanism, and the lump grows and finally forms. The blocking state where the granular material escapes from the fluidized bed state to the overall mass,
As shown in FIG. 5, when the degree of wetness in the fluidized bed rises, a passage for ejected gas from the gas outlet is generated in the fluidized bed, and therefore, an air flow for maintaining a normal fluidized state is generated. It means that the granulated material comes out of the fluidized bed state and finally forms a channeling state that leads to the whole mass.When such a situation occurs, the operation stops and the granulated material must be discarded. is there.

【0003】[0003]

【発明が解決しようとする課題】上述した層高検出手段
による流動層の上面高さの変化を、造粒過程における流
動層状態の監視に適用するものは、ブロッキング状態や
チャネリング状態の発生により、通常状態で層高一定に
維持するために必要な量の気体噴出口からの気体噴出量
を確保しているにもかかわらず層高が低下する場合に初
めて検出可能となるもので、図5,6に示すように、ブ
ロッキング状態やチャネリング状態の態様によっては層
高検出手段により層高の低下が検出できないことがあっ
た。一方、運転員の目視観察に頼ったものでは、ブロッ
キング状態やチャネリング状態の発生の初期段階を迅速
に発見することが困難で、そのために、流動層状態の崩
れを発見したときにはすでに回復できない程度に進行し
ているおそれもあった。本発明は、このような実情に着
目してなされたものであり、造粒過程における流動層状
態の崩れを早期に発見して、自動的に正常な流動層状態
に回復させることができる流動層利用の造粒制御装置を
提供することを目的とする。
The method of applying the change of the upper surface height of the fluidized bed by the above-described bed height detecting means to the monitoring of the fluidized bed state in the granulation process involves the occurrence of a blocking state or a channeling state. In the normal state, the layer height can be detected for the first time when the layer height decreases despite securing the required amount of gas ejection from the gas outlet to maintain the layer height constant. As shown in FIG. 6, depending on the mode of the blocking state or the channeling state, the decrease in the layer height may not be detected by the layer height detecting means. On the other hand, it is difficult to quickly detect the initial stage of the occurrence of the blocking state or the channeling state by using the operator's visual observation, so that when the collapse of the fluidized bed state is found, it cannot be recovered anymore. There was a possibility that it was progressing. The present invention has been made by paying attention to such a situation, and detects a collapse of a fluidized bed state in a granulation process at an early stage, and can automatically recover a normal fluidized bed state. An object of the present invention is to provide a granulation control device for use.

【0004】[0004]

【課題を解決するための手段】この目的を達成するため
に、本発明による流動層利用の造粒制御装置の特徴構成
は、流動層状態の崩れを検出する異常発生検出手段を設
けて、その異常発生検出手段により流動層状態の崩れを
検出すると、気体の噴出量を一時的に急増させるように
前記気体噴出量調節手段を制御する緊急制御手段を設け
てある点にある。上述の構成において、前記異常発生検
出手段が、流動層での圧損の急激な低下を検出する圧力
検出手段であることが好ましい。さらには、前記異常発
生検出手段が、造粒物の衝突により生じる弾性波のエネ
ルギーの急激な減少を検出する弾性波検出手段であるこ
とが好ましい。
In order to achieve this object, a characteristic configuration of a granulation control device utilizing a fluidized bed according to the present invention is to provide an abnormal occurrence detecting means for detecting collapse of a fluidized bed state. An emergency control means for controlling the gas ejection amount adjusting means so as to temporarily increase the gas ejection amount when the abnormality occurrence detection means detects the collapse of the fluidized bed state is provided. In the above configuration, it is preferable that the abnormality occurrence detecting means is a pressure detecting means for detecting a sharp decrease in pressure loss in the fluidized bed. Further, it is preferable that the abnormality occurrence detecting means is an elastic wave detecting means for detecting a sudden decrease in energy of the elastic wave caused by the collision of the granulated material.

【0005】[0005]

【作用】異常発生検出手段により、ブロッキング状態や
チャネリング状態といった流動層状態の崩れが検出され
ると、緊急制御手段は、気体噴出量調節手段に対して、
層高を一定に維持するのに必要な量よりも多くの噴出量
に一時的に急増させることにより、ブロッキング状態や
チャネリング状態を解消して正常な流動層状態に回復さ
せるのである。ここに、異常発生検出手段としては、流
動層に発生するブロッキング状態やチャネリング状態に
より流動層での圧損が急激に低下することを検出する圧
力検出手段とすることにより、流動層状態の崩れを間接
的ではあるが早期に検出できる。さらに、異常発生検出
手段としては、流動層に発生するブロッキング状態やチ
ャネリング状態により流動層での造粒物の運動状態が低
下することを、造粒物の衝突により生じる弾性波のエネ
ルギーの急激な減少により検出する弾性波検出手段とす
ることにより、流動層状態の崩れを直接的に、しかも極
めて初期に検出できる。
When the abnormality detection means detects the collapse of the fluidized bed state such as the blocking state or the channeling state, the emergency control means sends a gas ejection amount adjustment means
By temporarily abruptly increasing the jetting volume to an amount larger than required to maintain a constant bed height, the blocking state and the channeling state are eliminated and the state of the fluidized bed is restored to a normal state. Here, the abnormality occurrence detecting means is a pressure detecting means for detecting a sudden drop in pressure loss in the fluidized bed due to a blocking state or a channeling state occurring in the fluidized bed, thereby indirectly controlling the collapse of the fluidized bed state. Although it is a target, it can be detected early. Further, as an abnormality occurrence detecting means, the blocking state or the channeling state occurring in the fluidized bed, the motion state of the granulated material in the fluidized bed is reduced, the sudden energy of the elastic wave generated by the collision of the granulated material. By using the elastic wave detecting means for detecting by the decrease, the collapse of the fluidized bed state can be detected directly and very early.

【0006】[0006]

【発明の効果】本発明によれば、造粒過程における流動
層状態の崩れを早期に発見して、自動的に正常な流動層
状態に回復させることができる流動層利用の造粒制御装
置を提供することができるようになった。
According to the present invention, there is provided a granulation control apparatus utilizing a fluidized bed capable of detecting collapse of a fluidized bed state in a granulation process at an early stage and automatically recovering a state of a fluidized bed. Can now be offered.

【0007】[0007]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0008】図2に示すように、本発明に係る流動層利
用の造粒装置は、上部が下部よりも若干拡径した円筒状
の造粒容器1の底部に、上面が上向きに突出した円錐面
に形成された回転円盤10を、前記造粒容器1内におい
て鉛直方向の回転軸芯周りに回転自在に取り付けて、そ
の回転円盤10の上面円錐面の上方空間を造粒部3と
し、その造粒部3で、回転円盤10に形成した複数の気
体噴出口10aから噴出される気流により造粒原料を流
動層状態にするとともに、前記造粒容器1の上方空間に
設けた結合剤噴出機構8から結合剤を噴霧して造粒する
ように構成してある。
As shown in FIG. 2, in the granulating apparatus utilizing a fluidized bed according to the present invention, a cone whose upper surface protrudes upward is formed at the bottom of a cylindrical granulating vessel 1 whose upper portion is slightly larger than its lower portion. The rotating disk 10 formed on the surface is rotatably mounted around the vertical axis of rotation in the granulation container 1, and the space above the upper conical surface of the rotating disk 10 is used as the granulating unit 3. In the granulating section 3, the granulated raw material is made into a fluidized bed state by airflows blown out from a plurality of gas outlets 10 a formed in the rotating disk 10, and a binder blowing mechanism provided in a space above the granulating vessel 1. 8, the binder is sprayed and granulated.

【0009】前記造粒容器1の中段(詳しくは、前記造
粒容器1の拡径部)には、前記造粒原料のうちの原料粉
体を供給するための供給機構15を設けてあり、供給機
構15からの原料粉体を前記造粒部3に一旦貯留し、そ
の貯留物を流動層状態にして造粒を行う。
A supply mechanism 15 for supplying a raw material powder of the granulated raw material is provided at a middle stage of the granulation container 1 (specifically, an enlarged portion of the granulation container 1). The raw material powder from the supply mechanism 15 is temporarily stored in the granulating unit 3, and the stored material is made into a fluidized bed state to perform granulation.

【0010】前記造粒容器1の側方に、気体噴出量調節
手段としての風量調節自在のダンパ機構21を設けたエ
アーフィルタ4a付きの送風装置4が設けてあり、ヒー
タ5にて適宜温度に加熱された後に、前記気体噴出口1
0aを介して前記造粒部3に給気される。
A blower 4 having an air filter 4a provided with a damper mechanism 21 capable of adjusting the air flow is provided on the side of the granulation container 1 as a gas blowing amount adjusting means. After being heated, the gas outlet 1
Air is supplied to the granulating unit 3 through the air inlet 0a.

【0011】前記結合剤噴出機構8は、前記造粒容器1
の最上部に冠着された濾過部2を貫通した状態に配置さ
れた上端供給部8a(その部分には、圧縮空気供給装置
6及び結合剤供給装置7からの配管の下流端が接続され
ている)と、前記造粒容器1内の下部下方に開口したノ
ズル8cにより前記造粒部3へ噴霧供給されるようにな
っている下端噴霧部8b(その部分は、前記造粒部3へ
向けて結合剤を噴霧する噴霧口として機能する)を、前
記造粒容器1内の中心部に鉛直姿勢で配置してある。即
ち、前記結合剤供給装置7から結合剤を供給しつつ、圧
縮空気供給装置6からの圧縮空気をキャリアガスとし
て、前記ノズル8cによって前記造粒部3へ噴霧供給す
る。
The binder jetting mechanism 8 is provided in the granulating container 1.
The upper end supply portion 8a (the downstream end of the pipe from the compressed air supply device 6 and the binder supply device 7 is connected to the upper end supply portion 8a disposed so as to pass through the filtration portion 2 attached to the uppermost portion of the ), And a lower end spraying portion 8b which is sprayed and supplied to the granulating portion 3 by a nozzle 8c opened at a lower part in the granulating container 1 (the portion is directed toward the granulating portion 3). Functioning as a spray port for spraying a binder) is disposed in the center of the granulation container 1 in a vertical posture. That is, while supplying the binder from the binder supply device 7, the compressed air from the compressed air supply device 6 is sprayed and supplied to the granulation section 3 by the nozzle 8c as the carrier gas.

【0012】更に、前記濾過部2には、前記造粒容器1
内からの吸引排気を濾過するためのフィルタ2aを設け
て、その吸引排気を装置外へ排出するための排気装置9
へ通じる配管を接続してあり、前記濾過部2内には、前
記フィルタ2aを洗浄するために圧縮空気を前記フィル
タ2aに吹き付けるブローチューブ2bを設けてある。
Further, the filtration unit 2 includes the granulation container 1
An exhaust device 9 for providing a filter 2a for filtering suction / exhaust air from the inside and discharging the suction / exhaust gas to the outside of the apparatus;
The filter 2 is provided with a blow tube 2b for blowing compressed air to the filter 2a for cleaning the filter 2a.

【0013】前記回転円盤10は、前記造粒容器1の下
部に配置したモータ13の駆動力によって鉛直方向の回
転軸芯周りに回転自在に取り付けてあり、前記造粒容器
1の給気口1aを経由して導入される前記送風装置4か
らの給気が、前記気体噴出口10aを介して前記造粒部
3へ噴出される。
The rotating disk 10 is rotatably mounted around a vertical axis of rotation by a driving force of a motor 13 disposed below the granulating container 1. The air supplied from the blower 4 introduced through the gas outlet is blown out to the granulating unit 3 through the gas outlet 10a.

【0014】上述の造粒装置には、目標とする粒径に造
粒するために前記造粒部3へ噴出すべき最適な風量を調
節する造粒制御装置を設けてある。前記造粒制御装置
は、図1に示すように、流動層の上面高さを検出する超
音波を用いた層高検出手段20と、前記気体噴出口10
aからの気体噴出量を調節する気体噴出量調節手段21
と、前記層高検出手段20により検出された流動層の上
面高さを一定に維持するように前記気体噴出量調節手段
21を調節して造粒するコンピュータ利用の造粒制御手
段22とで構成してあり、さらに、前記流動層状態の崩
れを検出する異常発生検出手段23を設けて、その異常
発生検出手段23により流動層状態の崩れを検出する
と、気体の噴出量を一時的に急増させるように前記気体
噴出量調節手段21を制御する緊急制御手段を設けてあ
る。
The above-mentioned granulating apparatus is provided with a granulating control device for adjusting an optimal air volume to be blown to the granulating section 3 in order to granulate to a target particle diameter. As shown in FIG. 1, the granulation control device includes a bed height detecting unit 20 using ultrasonic waves for detecting the height of the upper surface of the fluidized bed;
gas ejection amount adjusting means 21 for adjusting the amount of gas ejection from a
And computer-assisted granulation control means 22 for granulating by adjusting the gas ejection amount adjustment means 21 so as to maintain the upper surface height of the fluidized bed detected by the bed height detection means 20 constant. Further, an abnormality occurrence detection means 23 for detecting the collapse of the fluidized bed state is provided, and when the abnormality occurrence detection means 23 detects the collapse of the fluidized bed state, the amount of gas ejected is temporarily increased suddenly. Thus, an emergency control means for controlling the gas ejection amount adjusting means 21 is provided.

【0015】前記異常発生検出手段23は、造粒容器1
内での造粒物同士の衝突、造粒物と回転円盤や造粒容器
1内壁との衝突により生じる弾性波を検出する弾性波検
出手段で構成してあり、造粒容器1で造粒層が形成され
ている範囲の外壁に金属製の取り付け部材を介して固定
設置してある。前記弾性波検出手段は、ピエゾ効果圧電
素子で検出される弾性波から造粒物の衝突により生じる
特定周波数の信号を増幅器で選択増幅して、単位時間内
に発生する数(衝突回数と正の相関がある)を出力する
ものである。
The abnormality occurrence detecting means 23 is provided in the granulation container 1.
And an elastic wave detecting means for detecting an elastic wave generated by a collision between the granulated materials in the chamber and a collision between the granulated material and the rotating disk or the inner wall of the granulation container 1. Is fixedly installed via an attachment member made of metal on the outer wall in the area where is formed. The elastic wave detecting means selectively amplifies, by an amplifier, a signal of a specific frequency generated by the collision of the granulated material from the elastic wave detected by the piezo effect piezoelectric element, and generates a signal generated within a unit time (the number of collisions and the positive number). (With correlation).

【0016】前記造粒制御手段22は、コンピュータ2
2e、及び、前記層高検出手段20からの検出信号を入
力するバッファ回路22b、前記異常発生検出手段23
からの検出信号を入力するバッファ回路22a、前記気
体噴出量調節手段21を駆動するドライバ回路22d、
前記結合剤噴出機構8を駆動するドライバ回路22c等
の周辺回路で構成してある。
The granulation control means 22 includes a computer 2
2e, a buffer circuit 22b for inputting a detection signal from the layer height detection means 20, and the abnormality occurrence detection means 23
A buffer circuit 22a for inputting a detection signal from the CPU, a driver circuit 22d for driving the gas ejection amount adjusting means 21,
A peripheral circuit such as a driver circuit 22c for driving the binder ejection mechanism 8 is provided.

【0017】図3に示すように、前記造粒制御手段22
の構成要素であるコンピュータ22eは、先ず、前記供
給機構15から原料粉体を前記造粒部3に注入し、その
貯留物を流動層状態にすべく前記気体噴出量調節手段2
1、即ち、ダンパを開く。ダンパの開度は、上述の層高
検出手段20の出力が設定値に到達するまでとし、その
後、前記結合剤供給装置7から結合剤を噴霧供給しなが
ら、造粒すると粒径の成長とともに層高が低下するの
で、それに抗して層高を一定に維持するべくダンパの開
度を次第に大きく調節する。ここに、調節される層高値
は、造粒対象により予め設定された任意の値である。一
方、前記弾性波検出手段の出力値は、造粒の進行に伴い
初期には過剰気味であった気体噴出量調節手段21から
の送風量が次第に適量となるにつれて低下傾向を示す
が、途中で、ブロッキング状態やチャネリング状態が発
生して流動層状態が崩れた場合、前記層高検出手段20
の出力がそれらを検出できずに一定であっても、前記弾
性波検出手段の出力値は必ず低下する。そこで、前記コ
ンピュータ22eは、通常の制御状態の制御信号と緊急
状態の制御信号を切り換えるスイッチ回路である緊急制
御手段を作動させて、前記気体噴出量調節手段21のダ
ンパの開度を急激に大きく調節して、その風圧によりブ
ロッキング状態やチャネリング状態をその発生の初期段
階で解消する。このときのダンパの開度は、最大開度で
ある必要はないが、ブロッキング状態やチャネリング状
態を解消するに十分な送風量を確保できる値であり、前
記弾性波検出手段の出力値が急激な低下を示す以前の値
とほぼ等しい値に復帰し、しかも、前記層高検出手段2
0の出力が同時に低下している場合には、その値が低下
を示す以前の値とほぼ等しい値に復帰するまでその開度
を維持する。正常状態に復帰した後は、再び、前記層高
検出手段20の出力が設定値に維持するようにダンパの
開度を調節する。前記コンピュータ22eによる通常状
態における前記気体噴出量調節手段21の調節制御は、
前記層高検出手段20の出力を基とするPID制御、或
いは、ファジー制御や推論機構を設けたAI制御等を適
宜用いることができる。
As shown in FIG. 3, the granulation control means 22
First, the computer 22e, which is a component of the apparatus, injects the raw material powder from the supply mechanism 15 into the granulating section 3 and sets the gas ejection amount adjusting means 2 so that the stored material is in a fluidized bed state.
1: Open the damper. The opening degree of the damper is set until the output of the layer height detecting means 20 reaches a set value. Thereafter, while the binder is spray-supplied from the binder supply device 7, the granulation is carried out together with the growth of the particle size. As the height decreases, the opening degree of the damper is gradually increased to maintain the layer height constant. Here, the layer height value to be adjusted is an arbitrary value set in advance by the granulation target. On the other hand, the output value of the elastic wave detecting means shows a tendency to decrease as the amount of air blown from the gas ejection amount adjusting means 21 which was initially excessively large as the granulation progresses gradually becomes an appropriate amount. When the fluidized bed state is disrupted due to the occurrence of a blocking state or a channeling state, the bed height detecting means 20
, The output value of the elastic wave detecting means always drops. Therefore, the computer 22e activates the emergency control means, which is a switch circuit for switching between the control signal in the normal control state and the control signal in the emergency state, so as to sharply increase the opening degree of the damper of the gas ejection amount adjusting means 21. By adjusting the wind pressure, the blocking state and the channeling state are eliminated at an early stage of the occurrence. At this time, the opening of the damper does not need to be the maximum opening, but is a value that can secure a sufficient air flow to eliminate the blocking state and the channeling state, and the output value of the elastic wave detecting unit is abrupt. It returns to a value substantially equal to the previous value indicating the decrease, and the layer height detecting means 2
If the output of 0 is decreasing at the same time, the opening is maintained until the value returns to a value substantially equal to the previous value indicating the decrease. After returning to the normal state, the opening of the damper is adjusted again so that the output of the layer height detecting means 20 is maintained at the set value. Adjustment control of the gas ejection amount adjustment means 21 in the normal state by the computer 22e
PID control based on the output of the layer height detection means 20, or fuzzy control or AI control provided with an inference mechanism can be used as appropriate.

【0018】以下に別実施例を説明する。先の実施例で
は、弾性波検出手段を、単位時間内に発生する弾性波の
数を出力するように構成したものを説明したが、弾性波
検出手段としては、単位時間に発生する弾性波の数とそ
の強度の積をエネルギーとして出力するものであっても
よい。先の実施例では、単一の弾性波検出手段を造粒容
器1で造粒層が形成されている範囲の外壁に金属製の取
り付け部材を介して固定設置ししたものを説明したが、
外壁の周部に沿って複数個取り付けて、いずれかの弾性
波検出手段の出力が他の弾性波検出手段の出力よりも著
しく低くなっている場合には、流動層状態が部分的に崩
れている事などを検出できる。先の実施例では、異常発
生検出手段23として、造粒物の衝突により生じる弾性
波のエネルギーの急激な減少を検出する弾性波検出手段
を用いたものを説明したが、異常発生検出手段23とし
ては、図4に示すように、流動層での圧損の急激な低下
を検出する圧力検出手段を用いるものであってもよい。
つまり、圧力検出手段は、流動層の下部と上部との間の
圧力差、即ち、圧損を検出する圧力センサを流動層の下
部と上部をつなぐバイパス管路に配置して構成されるも
ので、チャネリング現象やブロッキング現象により流動
層内に供給された気流の多くが素通りして圧損値が急激
に低下することを利用して流動層状態が崩れたことを識
別するものである。尚、バイパス管の下部側開口を、回
転円盤10とその下部に設けられたエアー噴出口の多孔
板との間に配置させても良く、それにより多孔板の目詰
まり等による圧力損失の変動による影響を排除すること
が出来る。
Another embodiment will be described below. In the above embodiment, the elastic wave detecting means is configured to output the number of elastic waves generated in a unit time, but as the elastic wave detecting means, the elastic wave detecting means The product of the number and its intensity may be output as energy. In the above embodiment, the single elastic wave detecting means is fixedly installed on the outer wall of the granulation vessel 1 in the range where the granulation layer is formed via the metal attachment member.
If the output of any one of the elastic wave detecting means is significantly lower than the output of the other elastic wave detecting means, the fluidized bed state is partially collapsed by mounting a plurality of pieces along the outer wall periphery. Can be detected. In the above embodiment, the abnormality occurrence detecting means 23 using the elastic wave detecting means for detecting a sudden decrease in the energy of the elastic wave caused by the collision of the granulated material has been described. As shown in FIG. 4, a pressure detecting means for detecting a rapid decrease in pressure loss in a fluidized bed may be used.
That is, the pressure detecting means is configured by arranging a pressure sensor for detecting a pressure difference between the lower part and the upper part of the fluidized bed, that is, a pressure loss, in a bypass pipe connecting the lower part and the upper part of the fluidized bed, This is to identify that the state of the fluidized bed has collapsed by utilizing the fact that much of the airflow supplied into the fluidized bed due to the channeling phenomenon or the blocking phenomenon passes through and the pressure drop value sharply decreases. The lower opening of the bypass pipe may be arranged between the rotating disk 10 and the perforated plate of the air outlet provided thereunder, so that the pressure loss due to clogging of the perforated plate or the like may be reduced. The effect can be eliminated.

【0019】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.

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

【図1】造粒装置の要部を示す概略構成図FIG. 1 is a schematic configuration diagram showing a main part of a granulating apparatus.

【図2】造粒制御装置のブロック構成図FIG. 2 is a block diagram of a granulation control device.

【図3】造粒制御装置の制御タイミング図FIG. 3 is a control timing chart of a granulation control device.

【図4】別実施例を示す要部のブロック構成図FIG. 4 is a block diagram of a main part showing another embodiment.

【図5】チャネリング減少の説明図FIG. 5 is an explanatory diagram of channeling reduction.

【図6】ブロッキング減少の説明図FIG. 6 is an explanatory diagram of blocking reduction.

【符号の説明】[Explanation of symbols]

1 造粒容器 8 結合剤噴出機構 10a 気体噴出口 20 層高検出手段 21 気体噴出量調節手段 22 造粒制御手段 23 異常発生検出手段 DESCRIPTION OF SYMBOLS 1 Granulation container 8 Binder ejection mechanism 10a Gas ejection port 20 Layer height detection means 21 Gas ejection amount adjustment means 22 Granulation control means 23 Abnormality detection means

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 造粒容器(1)の底部に設けた気体噴出
口(10a)から噴出される気流により、造粒原料を流
動層状態にして、前記造粒容器(1)の上方空間に設け
た結合剤噴出機構(8)から結合剤を噴霧して造粒する
流動層に対し、 その流動層の上面高さを検出する層高検出手段(20)
と、前記気体噴出口(10a)からの気体噴出量を調節
する気体噴出量調節手段(21)と、前記層高検出手段
(20)により検出された流動層の上面高さを一定に維
持するように前記気体噴出量調節手段(21)を制御す
る造粒制御手段(22)とからなる流動層利用の造粒制
御装置であって、 前記流動層状態の崩れを検出する異常発生検出手段(2
3)を設けて、その異常発生検出手段(23)により流
動層状態の崩れを検出すると、気体の噴出量を一時的に
急増させるように前記気体噴出量調節手段(21)を制
御する緊急制御手段を設けてある流動層利用の造粒制御
装置。
1. A granulation raw material is made into a fluidized bed state by an air flow ejected from a gas ejection port (10a) provided at the bottom of a granulation container (1), and is placed in a space above the granulation container (1). A bed height detecting means (20) for detecting the height of the upper surface of the fluidized bed to be granulated by spraying the binder from the provided binder ejection mechanism (8).
A gas ejection amount adjusting means (21) for adjusting the gas ejection amount from the gas ejection port (10a); and a constant upper surface height of the fluidized bed detected by the bed height detection means (20). And a granulation control means (22) for controlling the gas ejection amount adjusting means (21) as described above, wherein the abnormality occurrence detection means (U) detects the collapse of the fluidized bed state. 2
3) is provided, and when the abnormality occurrence detecting means (23) detects the collapse of the fluidized bed state, the emergency control for controlling the gas ejection amount adjusting means (21) so as to temporarily increase the ejection amount of gas temporarily. A granulation control device using a fluidized bed provided with a means.
【請求項2】 前記異常発生検出手段(23)が、流動
層での圧損の急激な低下を検出する圧力検出手段である
請求項1記載の流動層利用の造粒制御装置。
2. The granulation control device using a fluidized bed according to claim 1, wherein the abnormality occurrence detecting means is a pressure detecting means for detecting a sudden decrease in pressure loss in the fluidized bed.
【請求項3】 前記異常発生検出手段(23)が、造粒
物の衝突により生じる弾性波のエネルギーの急激な減少
を検出する弾性波検出手段である請求項1記載の流動層
利用の造粒制御装置。
3. The granulation using a fluidized bed according to claim 1, wherein the abnormality occurrence detecting means (23) is an elastic wave detecting means for detecting a sudden decrease in energy of the elastic wave caused by the collision of the granulated material. Control device.
JP5158433A 1993-06-29 1993-06-29 Granulation control device using fluidized bed Expired - Lifetime JP3056916B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5158433A JP3056916B2 (en) 1993-06-29 1993-06-29 Granulation control device using fluidized bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5158433A JP3056916B2 (en) 1993-06-29 1993-06-29 Granulation control device using fluidized bed

Publications (2)

Publication Number Publication Date
JPH078784A JPH078784A (en) 1995-01-13
JP3056916B2 true JP3056916B2 (en) 2000-06-26

Family

ID=15671660

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5158433A Expired - Lifetime JP3056916B2 (en) 1993-06-29 1993-06-29 Granulation control device using fluidized bed

Country Status (1)

Country Link
JP (1) JP3056916B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014042656A (en) * 2012-08-27 2014-03-13 Itoki Corp Cushion for chair

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1218416A1 (en) * 1999-08-03 2002-07-03 Union Carbide Chemicals & Plastics Technology Corporation Method of detecting and correcting local defluidization and channeling in fluidized-bed reactors for polymerization

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014042656A (en) * 2012-08-27 2014-03-13 Itoki Corp Cushion for chair

Also Published As

Publication number Publication date
JPH078784A (en) 1995-01-13

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