JPH1085578A - Method and device for additive liquid feed control for tumbling granulator - Google Patents

Method and device for additive liquid feed control for tumbling granulator

Info

Publication number
JPH1085578A
JPH1085578A JP26530596A JP26530596A JPH1085578A JP H1085578 A JPH1085578 A JP H1085578A JP 26530596 A JP26530596 A JP 26530596A JP 26530596 A JP26530596 A JP 26530596A JP H1085578 A JPH1085578 A JP H1085578A
Authority
JP
Japan
Prior art keywords
additive liquid
measured
sample
water content
liquid
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.)
Pending
Application number
JP26530596A
Other languages
Japanese (ja)
Inventor
Hideaki Onishi
秀明 大西
Kazunori Shirasaki
和則 白崎
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.)
Nihon Spindle Manufacturing Co Ltd
Original Assignee
Nihon Spindle Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nihon Spindle Manufacturing Co Ltd filed Critical Nihon Spindle Manufacturing Co Ltd
Priority to JP26530596A priority Critical patent/JPH1085578A/en
Publication of JPH1085578A publication Critical patent/JPH1085578A/en
Pending legal-status Critical Current

Links

Landscapes

  • Glanulating (AREA)

Abstract

PROBLEM TO BE SOLVED: To measure the water content of a powder not changing its color by using an additive liquid so that the color does not change, since in the case the color does not change in a powder to be granulated by its water content, the water content can be measured by measuring the color change while in the case the color does not change by the water content, it is difficult to measure the water content from its outer appearance. SOLUTION: In a granulating machine 1 for feeding powder and adding liquid respectively onto an inclined bread-shaped granulating pan 3 and granulating by rotating the granulating pan 3 while controlling the feed of the additive liquid, a material to be granulated is sampled, photographed by a CCD camera and image processed and its volume is measured based on the average grain size diameter of the material to be granulated and then the average weight of particles is measured, and the particle gravity weight is measured from both of the above-referred measurements, and the particle gravity is compared with a reference data to measure the excess and deficiency of the water content and the feed amount of the additive liquid is controlled.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、転動造粒機、特に
パン型造粒機に対する添加液の供給制御方法及びその装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for controlling the supply of an additive liquid to a tumbling granulator, particularly a bread granulator.

【0002】[0002]

【従来の技術】上記転動造粒機は、パン型造粒皿を傾斜
して支持し、これに粉体と添加液(例えば水、またはこ
れに適宜の凝集剤あるいは重金属固定剤等を添加)とを
供給し、造粒皿の回転に伴う持ち上げと、その自重によ
る下方への落下により造粒し、所定の大きさの粒体に成
長させた後、オーバフローにより排出するようにしたも
のである。この際、粉体の供給は一般にスクリユーコン
ベアにより一定量を供給し、粉体供給量を計量し、供給
される粉体と添加液との比を予め設定した比率に制御保
持すべく上記計量値を基準として添加する添加液の送り
出し液量を規制する方法を提案されている(特開平5−
237358号)。
2. Description of the Related Art The above-mentioned tumbling granulator supports a pan-shaped granulating dish at an angle, and a powder and an additive liquid (for example, water or an appropriate coagulant or heavy metal fixing agent, etc. are added thereto). ) Is supplied, the granulation is performed by lifting the granulation dish with rotation and falling downward by its own weight to granulate, grow to a predetermined size, and then discharge by overflow. is there. At this time, the powder is generally supplied in a fixed amount by a screw conveyor, the amount of the supplied powder is measured, and the above-mentioned measurement is performed so as to control and maintain the ratio between the supplied powder and the additive liquid at a preset ratio. A method has been proposed in which the amount of the additive liquid to be added is regulated based on the value (see Japanese Patent Laid-Open Publication No. Hei 5-
237358).

【0003】この場合、添加液の供給量の許容範囲は極
めて小さく、添加液量が多いときは、造粒物は過大とな
ると共に、粒体の含有液量は限界があり、ついには造粒
皿内は余分の液が蓄積されて泥状となり、造粒不可能と
なる。また液量が不足するときは、造粒粒子径は小とな
ると共に、ついには造粒のための液量が不足し、造粒不
可能となる。このため本出願人は先に造粒される粉粒体
表面の水分を測定し、これにより供給液量の調整を正確
に行い、パン形造粒機の自動連続運転を可能ならしめる
転動造粒機の添加液供給制御方法及びその装置を提案し
た(特開平7−194960号)。その概要を図4に示
す。
[0003] In this case, the allowable range of the supply amount of the additive liquid is extremely small, and when the amount of the additive liquid is large, the granulated material becomes excessively large and the liquid content of the granules is limited. Excess liquid is accumulated in the dish and becomes muddy, making granulation impossible. When the amount of liquid is insufficient, the granulated particle diameter becomes small, and finally the amount of liquid for granulation becomes insufficient, and granulation becomes impossible. For this reason, the present applicant measures the moisture on the surface of the granules to be granulated first, thereby accurately adjusting the amount of the liquid to be supplied, and the rolling molding that enables automatic continuous operation of the bread granulator. A method and an apparatus for controlling the supply of an additive for a granulator have been proposed (Japanese Patent Application Laid-Open No. 7-194960). The outline is shown in FIG.

【0004】図において、パン形造粒機1は駆動軸2の
一端に前記パン形造粒皿3を取付け、駆動モータ4によ
り所定速度にて回転する。この駆動軸2は取付台5上に
傾斜して取付けられ、取付台5は一端を基台6に軸支7
され、他端には昇降ねじ杆8を取付け、造粒皿3を任意
の角度に調整保持する。10は処理粉体収納用ホツパ、
11はスクリユーコンベア、12は該コンベアの駆動モ
ータ、13は排出管を示し、ホツパ内の粉体を略々一定
速度で造粒皿3の適所に供給する。14は造粒皿3に対
向して配備される噴射ノズル、15は該ノズルとポンプ
Pとを連結する添加液供給管16に設けられる供給液調
整弁を示す。
In FIG. 1, a pan-shaped granulator 1 has the above-mentioned pan-shaped granulating dish 3 attached to one end of a drive shaft 2 and is rotated at a predetermined speed by a drive motor 4. The drive shaft 2 is mounted on the mounting table 5 at an angle.
At the other end, a lifting screw rod 8 is attached to adjust and hold the granulating dish 3 at an arbitrary angle. 10 is a hopper for storing processed powder,
Reference numeral 11 denotes a screw conveyor, 12 denotes a drive motor of the conveyor, and 13 denotes a discharge pipe. The powder in the hopper is supplied to an appropriate place of the granulating dish 3 at a substantially constant speed. Reference numeral 14 denotes an injection nozzle provided to face the granulation dish 3, and reference numeral 15 denotes a supply liquid regulating valve provided in an additive liquid supply pipe 16 connecting the nozzle and the pump P.

【0005】50は添加液供給制御回路を示し、造粒さ
れる粒体の水分測定器51並びに検出される粒体の水分
量に応じノズル14からの噴射水量を調整する演算回路
52とを備える。水分測定器51は、粒体の水分に応じ
てのコントラストの変化(通常白黒の変化)を検出す
る、即ち画像情報処理の容易なCCD方式の固体撮像素
子(画素)を備えたカメラ(以下CCDカメラ54とい
う)を用いる。このカメラにより撮像する粒子の色のコ
ントラストを検出し、白色部又は黒色部の面積を測定
し、これにより水分の過剰または不足を検出するように
したものである。
Reference numeral 50 denotes an additive liquid supply control circuit, which includes a moisture measuring device 51 for the granules to be granulated and an arithmetic circuit 52 for adjusting the amount of water jetted from the nozzle 14 in accordance with the detected moisture content of the granules. . The moisture meter 51 detects a change in contrast (usually a change in black and white) according to the moisture of the granules, that is, a camera (hereinafter referred to as a CCD) equipped with a CCD type solid-state imaging device (pixel) that facilitates image information processing. Camera 54). The camera detects the color contrast of the particles to be imaged, measures the area of the white portion or the black portion, and detects an excess or shortage of water.

【0006】このCCDカメラ51は場合によっては造
粒皿3から排出される造粒々子の水分を測定すべく図の
51aの位置に設けてもよい。53は演算回路52から
の指令により添加液供給量を設定する添加液供給指令回
路を示す。
In some cases, the CCD camera 51 may be provided at a position 51a in the figure to measure the water content of the granules discharged from the granulation dish 3. Reference numeral 53 denotes an additive liquid supply command circuit that sets the additive liquid supply amount according to a command from the arithmetic circuit 52.

【0007】[0007]

【発明が解決しようとする課題】しかし、この場合、粉
体として例えば上述の如く都市ゴミの焼却炉から発生す
る灰等、その色が白色またはこれに近い色で、含有水分
量により色の変化を生じるものは、その色変化を測定す
ることにより、その含有水分が測定できるが、例えば古
鉄を溶解する電気炉等から発生するダストは酸化鉄が主
体で黒色またはそれに近い色を呈しており、水分による
色変化は殆ど生ぜず、従って外観上からはその含水量を
測定することは困難な場合がある。本発明はかゝる点に
鑑み、上記添加液による色変化を生じない粉体に対しそ
の含水量を測定し、添加液の供給量を規制し、常に所要
水分の含有量を保持せしめ、造粒作用を確実に行うこと
を目的とする。
However, in this case, as a powder, for example, as described above, ash or the like generated from an incinerator of municipal garbage has a white color or a color close thereto, and changes in color depending on the water content. For those that produce, by measuring the color change, the water content can be measured, for example, dust generated from an electric furnace or the like that dissolves old iron is mainly iron oxide and has a black or similar color, The color change due to moisture hardly occurs, and therefore, it may be difficult to measure the water content from the appearance. In view of the above, the present invention measures the water content of a powder that does not cause a color change due to the above-mentioned additive liquid, regulates the supply amount of the additive liquid, and always keeps the required moisture content. The purpose is to perform the graining operation reliably.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
の本発明の転動造粒機の添加液供給制御方法は、傾斜す
るパン型造粒皿に粉体と添加液とをそれぞれ供給し、造
粒物をサンプリングし、CCDカメラにより撮影し、画
像処理して粒状物の平均粒度径からその体積を測定し、
ついで粒子の平均重量を測定して両者から粒子密度を測
定し、これを基準データと比較して含有水分量の過不足
を計測し、添加液の供給を制御することを特徴とする。
According to a first aspect of the present invention, there is provided a method for controlling the supply of an additive to a rolling granulator, wherein the powder and the additive are supplied to an inclined pan-type granulating dish. Sampling the granulated material, photographing it with a CCD camera, performing image processing, measuring the volume from the average particle size of the granular material,
Subsequently, the average weight of the particles is measured, the particle density is measured from both, and this is compared with reference data to measure the excess or deficiency of the water content, and the supply of the additive liquid is controlled.

【0009】また第2の発明は、上記方法を実施する装
置に係わり、傾斜するパン型造粒皿に粉体と添加液とを
それぞれ供給し、添加液の供給を制御しつゝ造粒皿を回
転して造粒する造粒機において、造粒物をサンプリング
するサンプリング機構と、採取されたサンプルを撮影す
るCCDカメラを備えた形状測定部と、サンプルの重量
測定部並びに基準データとの比較回路とを備え、造粒さ
れた粒子をサンプリングし、CCDカメラにより撮影し
てサンプルの数量及び単位サンプルの体積を測定し、重
量測定部により単位サンプルの重量を測定し、比較回路
において基礎データと比較してサンプルの含有添加液量
を演算し、添加液の供給量の制御を行うことを特徴とす
る。
A second aspect of the present invention relates to an apparatus for performing the above method, wherein the powder and the additive liquid are supplied to an inclined pan-type granulating dish, and the supply of the additive liquid is controlled. In a granulator that rotates and granulates, a sampling mechanism for sampling the granulated material, a shape measuring unit equipped with a CCD camera for photographing the collected sample, a comparison between the sample weight measuring unit and the reference data Circuit, the granulated particles are sampled, photographed with a CCD camera, the number of samples and the volume of the unit sample are measured, the weight of the unit sample is measured by the weight measuring unit, and the basic data is compared with the basic data in the comparison circuit. The method is characterized in that the amount of the additive liquid contained in the sample is calculated by comparison, and the supply amount of the additive liquid is controlled.

【0010】上記の構成からなる本発明の転動造粒機の
添加液供給制御方法及びその装置によるときは、造粒物
をサンプリングし、サンプルをCCDカメラにより撮影
してサンプルの個数及びその断面積から球状としたとき
の体積を算出し、重量測定部によりサンプルの重量を測
定し、これらよりサンプルの密度を算出して比較回路に
おいて基礎データと比較して含有添加液量を算出し、そ
の過不足を算出し、これに基づいて添加液の供給量を規
制する。
When the method and the apparatus for controlling the supply of an additive for a tumbling granulator according to the present invention having the above-described structure are used, the granulated material is sampled, the sample is photographed by a CCD camera, and the number of samples and the cutoff thereof are measured. Calculate the volume when spherical from the area, measure the weight of the sample by the weight measuring unit, calculate the density of the sample from these, compare it with the basic data in the comparison circuit, calculate the amount of additive solution contained, The excess or deficiency is calculated, and the supply amount of the additive liquid is regulated based on this.

【0011】[0011]

【発明の実施の形態】図1は本発明の実施例を示す。な
お、パン型造粒機1については、前記図4に示す構造と
同一であり、同一部品に対しては同一符号を付して説明
を省略する。20は添加液供給制御装置を示し、造粒皿
3より排出される造粒物Wを一定時間毎にサンプリング
するためのサンプリング機構21と、取り出されたサン
プリングの形状、寸法を測定するための形状測定部22
と、サンプリングの重量測定部23及び予め設定された
基礎データ24との比較回路25並びに添加液量を調整
する液量調整回路26とを備える。
FIG. 1 shows an embodiment of the present invention. The bread granulator 1 has the same structure as that shown in FIG. 4, and the same components are denoted by the same reference numerals and description thereof will be omitted. Reference numeral 20 denotes an additive liquid supply control device, which includes a sampling mechanism 21 for sampling the granulated material W discharged from the granulation dish 3 at regular intervals, and a shape for measuring the shape and size of the extracted sampling. Measuring unit 22
A weight measuring unit 23 for sampling, a comparison circuit 25 for comparison with preset basic data 24, and a liquid amount adjusting circuit 26 for adjusting the amount of added liquid.

【0012】サンプリング機構21は、サンプリング取
り出し用スプーン30と、これを進退させるエアシリン
ダ31とを備える。エアシリンダ31の作動により一定
時間毎にスプーン30を前進し、造粒皿3から排出され
る造粒物Wを受取り(約20個前後)、後退して転倒
し、サンプルwをシュート32上に供給するようにした
ものである(図2に実施例を示す)。
The sampling mechanism 21 includes a sampling take-out spoon 30 and an air cylinder 31 for moving the spoon 30 forward and backward. The spoon 30 is advanced at regular intervals by the operation of the air cylinder 31, receives the granules W discharged from the granulation dish 3 (about 20 pieces), retreats and falls down, and places the sample w on the chute 32. This is supplied (an embodiment is shown in FIG. 2).

【0013】形状測定部22は、上記シュート32上の
サンプルwを撮影する撮影機33を備える。この際、該
撮影機33は前述のCCDカメラを用いる。これにより
前記シュート上を順次落下するサンプルwを撮影し、供
給されるサンプルの個数、各サンプルの投影面積または
外周の長さからサンプルが球形と仮定したときの平均直
径及び平均体積を演算部34により計算する。この演算
部34において計算された数値は比較回路25に印加さ
れる。
The shape measuring section 22 includes a photographing device 33 for photographing the sample w on the chute 32. At this time, the above-mentioned CCD camera is used as the photographing device 33. Thereby, the sample w which sequentially falls on the chute is photographed, and the average diameter and average volume when the sample is assumed to be spherical are calculated from the number of supplied samples, the projected area of each sample or the length of the outer circumference. Is calculated by The numerical value calculated by the arithmetic unit 34 is applied to the comparison circuit 25.

【0014】サンプル重量測定部23は、上記シュート
32から供給されたサンプルを受け入れるホッパ35
と、電気的重量測定器例えばロードセル36とを備え、
ホッパ35に供給されたサンプル総重量を測定し、演算
部37により前記演算部34により計算した個数とによ
り、単位サンプルの重量を演算し、比較回路25に印加
する。40は排出コンベアを示し、計量を終了後のサン
プルを適所に返還するようにしたものである。
The sample weight measuring section 23 is provided with a hopper 35 for receiving the sample supplied from the chute 32.
And an electric weighing device such as a load cell 36,
The total weight of the sample supplied to the hopper 35 is measured, and the weight of the unit sample is calculated by the calculation unit 37 based on the number calculated by the calculation unit 34, and is applied to the comparison circuit 25. Numeral 40 denotes a discharge conveyor in which the sample after the measurement is returned to an appropriate place.

【0015】上記構成において、造粒皿3から排出され
る造粒々子に対し、一定時間毎にサンプリング機構21
のスプーン30を前進し、例えば20個前後のサンプル
を取り出しシュート32上に供給する。このシュート上
のサンプルwをCCDカメラ33により撮影し、演算部
34において落下するサンプルの個数、及びその投影面
積からサンプルを球形としたときの直径と体積とを演算
し、その数値を比較回路25に入力する。
In the above configuration, the sampling mechanism 21 is attached to the granules discharged from the granulation dish 3 at regular intervals.
Is moved forward, and for example, about 20 samples are taken out and supplied onto the chute 32. The sample w on the chute is photographed by the CCD camera 33, and the arithmetic unit 34 calculates the diameter and volume when the sample is formed into a sphere from the number of the falling samples and the projected area thereof, and compares the numerical value with the comparison circuit 25. To enter.

【0016】ついでシュート上のサンプルは重量計測部
23のホッパ35に投入され、その重量をロードセル3
6により測定する。その測定値は演算部37に入力さ
れ、前記演算部34からのサンプル個数の入力により、
単位サンプルの重量を算出し、これを比較回路25に入
力する。
Next, the sample on the chute is put into the hopper 35 of the weight measuring section 23, and the weight is transferred to the load cell 3.
Measure according to 6. The measured value is input to the calculation unit 37, and the number of samples is input from the calculation unit 34,
The weight of the unit sample is calculated and input to the comparison circuit 25.

【0017】比較回路25は、上記演算部34、37か
らの入力数値と基礎データ24とを比較する。この比較
回路25では、入力されたサンプルの体積と重量との比
(密度)を計算し、基礎データ24と比較する。この基
礎データの一例を図3に示す。図において基礎データの
基準密度Gは、造粒粒子の体積と標準含有液量(例えば
含有水分率7%)の粒子の体積変化(直径の変化)と重
量との比、即ち密度のグラフを示すもので、予め実験等
の経験則から最適の基礎データとしたもので、その上下
に許容範囲a、bを設定し、前記測定結果をこれと比較
する。但し、サンプルwの直径が、基礎データの最大許
容範囲GX以上の大きさのときは、含有液量が過大であ
り、直ちに供給液量を減少または停止する。また最小許
容範囲GM以下のときは、添加液量が不足しており、添
加液の増量指令を発する。
The comparison circuit 25 compares the input values from the operation units 34 and 37 with the basic data 24. The comparison circuit 25 calculates the ratio (density) between the input sample volume and weight and compares it with the basic data 24. FIG. 3 shows an example of this basic data. In the figure, the reference density G of the basic data is a graph of the ratio of the volume of the granulated particles, the volume change (diameter change) of the particles and the weight of the standard liquid content (for example, a water content of 7%), that is, the density. The optimum basic data is set in advance based on empirical rules such as experiments, and allowable ranges a and b are set above and below the basic data, and the measurement results are compared with these. However, when the diameter of the sample w is larger than the maximum allowable range GX of the basic data, the liquid content is excessive, and the supply liquid amount is immediately reduced or stopped. If it is less than the minimum allowable range GM, the amount of the additive liquid is insufficient, and a command to increase the amount of the additive liquid is issued.

【0018】その測定結果に基づき、液量調整回路26
に所要の信号を付与し、供給液調整弁29による造粒皿
3に対する供給液量を規制する。供給液量の規制として
は単なるON、OFF制御でもよいが前記供給液調整弁
29の開度調整によりシビヤに行ってもよい。
Based on the measurement result, the liquid amount adjusting circuit 26
To regulate the amount of the liquid supplied to the granulating dish 3 by the supply liquid adjusting valve 29. As the regulation of the supply liquid amount, simple ON / OFF control may be used, but it may be severely controlled by adjusting the opening degree of the supply liquid adjustment valve 29.

【0019】[0019]

【発明の効果】以上の如く本発明によるときは、造粒物
をサンプリングし、造粒物の大きさを光学的に即ちCC
Dカメラにより撮影し、画像処理して粒状物の平均粒度
径からその体積を測定し、ついで粒子の平均重量を測定
して粒子の質量即ち密度を把握し、基礎データと比較す
ることにより含有する添加液量を計測するようにしたか
ら、造粒々子の添加液量は確実に測定することが出来、
これにより添加液の供給量を制御するようにしたから、
造粒作業を自動的かつ無人で良好に行うことができる。
As described above, according to the present invention, the granulated material is sampled, and the size of the granulated material is optically measured, that is, CC.
Photographed by a D camera, image processed, the volume is measured from the average particle size of the granular material, then the average weight of the particles is measured to grasp the mass, that is, the density of the particles, and contained by comparing with the basic data. Since the amount of added liquid is measured, the amount of added liquid of granulated particles can be reliably measured.
Because the supply amount of the additive liquid is controlled by this,
The granulation operation can be performed automatically and unattended and satisfactorily.

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

【図1】本発明の転動造粒機の添加液供給量制御方法の
全体説明図である。
FIG. 1 is an overall explanatory view of a method for controlling an additive liquid supply amount of a tumbling granulator of the present invention.

【図2】添加液供給量制御機構の概略説明図である。FIG. 2 is a schematic explanatory view of an additive liquid supply amount control mechanism.

【図3】基礎データのグラフを示す。FIG. 3 shows a graph of basic data.

【図4】従来の転動造粒機の添加液供給量制御方法の説
明図である。
FIG. 4 is an explanatory view of a conventional method for controlling the supply amount of an additive liquid in a rolling granulator.

【符号の説明】[Explanation of symbols]

1 転動造粒機 3 造粒皿 20 添加液供給量制御装置 21 サンプリング機構 22 形状測定部 23 重量測定部 24 基礎データ 25 比較回路 33 CCDカメラ DESCRIPTION OF SYMBOLS 1 Rolling granulator 3 Granulating dish 20 Additive liquid supply control device 21 Sampling mechanism 22 Shape measuring unit 23 Weight measuring unit 24 Basic data 25 Comparison circuit 33 CCD camera

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 傾斜するパン型造粒皿に粉体と添加液と
をそれぞれ供給し、造粒皿を回転して造粒する造粒機に
おいて、造粒物をサンプリングし、CCDカメラにより
撮影し、画像処理して粒状物の平均粒度径からその体積
を測定し、ついで粒子の平均重量を測定して両者から粒
子密度を測定し、これを基準データと比較して含有水分
量の過不足を計測し、添加液の供給を制御することを特
徴とする転動造粒機の添加液供給制御方法。
1. A granulating machine for supplying a powder and an additive liquid to an inclined pan-type granulating dish and rotating the granulating dish to granulate the granulated material, and photographing the granulated material with a CCD camera. Then, image processing is performed, the volume is measured from the average particle size of the granular material, then the average weight of the particles is measured, and the particle density is measured from both, and this is compared with the reference data to determine whether the water content is insufficient or insufficient. And controlling the supply of the additive liquid by controlling the supply of the additive liquid.
【請求項2】 傾斜するパン型造粒皿に粉体と添加液と
をそれぞれ供給し、添加液の供給を制御しつゝ造粒皿を
回転して造粒する造粒機において、造粒物をサンプリン
グするサンプリング機構と、採取されたサンプルを撮影
するCCDカメラを備えた形状測定部と、サンプルの重
量測定部並びに基準データとの比較回路とを備え、造粒
された粒子をサンプリングし、CCDカメラにより撮影
してサンプルの数量及び単位サンプルの体積を測定し、
重量測定部により単位サンプルの重量を測定し、比較回
路において基礎データと比較してサンプルの含有添加液
量を演算せしめ、添加液の供給量の制御を行うことを特
徴とする転動造粒機の添加液供給制御装置。
2. A granulator for supplying a powder and an additive liquid to an inclined pan-type granulating dish and controlling the supply of the additive liquid and rotating the granulating dish to granulate. A sampling mechanism for sampling an object, a shape measuring unit having a CCD camera for photographing the collected sample, a sample weight measuring unit and a comparison circuit with reference data are provided, and the granulated particles are sampled. Take a picture with a CCD camera to measure the number of samples and the volume of a unit sample,
A tumbling granulator characterized in that the weight of a unit sample is measured by a weight measuring unit, the amount of additive liquid contained in the sample is calculated in a comparison circuit with basic data, and the supply amount of additive liquid is controlled. Liquid supply control device.
JP26530596A 1996-09-13 1996-09-13 Method and device for additive liquid feed control for tumbling granulator Pending JPH1085578A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26530596A JPH1085578A (en) 1996-09-13 1996-09-13 Method and device for additive liquid feed control for tumbling granulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26530596A JPH1085578A (en) 1996-09-13 1996-09-13 Method and device for additive liquid feed control for tumbling granulator

Publications (1)

Publication Number Publication Date
JPH1085578A true JPH1085578A (en) 1998-04-07

Family

ID=17415359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26530596A Pending JPH1085578A (en) 1996-09-13 1996-09-13 Method and device for additive liquid feed control for tumbling granulator

Country Status (1)

Country Link
JP (1) JPH1085578A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1213051A1 (en) * 2000-12-08 2002-06-12 Basf Aktiengesellschaft Process for monitoring and regulation of an industrial granulation process
JP2003275570A (en) * 2002-03-19 2003-09-30 Kobe Steel Ltd Pellet particle size control method
CN111041194A (en) * 2019-10-29 2020-04-21 江苏省沙钢钢铁研究院有限公司 Preparation device for improving green pellet quality of mineral powder pellets and application method thereof
CN114505012A (en) * 2022-03-24 2022-05-17 东南大学 Microbial repairing agent production line and production process thereof
CN115540624A (en) * 2022-09-20 2022-12-30 合肥水泥研究设计院有限公司 Cement kiln batching control system based on DCS control

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1213051A1 (en) * 2000-12-08 2002-06-12 Basf Aktiengesellschaft Process for monitoring and regulation of an industrial granulation process
JP2003275570A (en) * 2002-03-19 2003-09-30 Kobe Steel Ltd Pellet particle size control method
CN111041194A (en) * 2019-10-29 2020-04-21 江苏省沙钢钢铁研究院有限公司 Preparation device for improving green pellet quality of mineral powder pellets and application method thereof
CN114505012A (en) * 2022-03-24 2022-05-17 东南大学 Microbial repairing agent production line and production process thereof
CN115540624A (en) * 2022-09-20 2022-12-30 合肥水泥研究设计院有限公司 Cement kiln batching control system based on DCS control

Similar Documents

Publication Publication Date Title
KR101815327B1 (en) Device for determining particle sizes
EP0391530B1 (en) Method of measuring average particle size of granular material
JP5886266B2 (en) Particle mass inspection device
JPH1085578A (en) Method and device for additive liquid feed control for tumbling granulator
JP2004016983A (en) Automatic control method of particle size of coal
CN111968173A (en) Method and system for analyzing granularity of mixture
US5992245A (en) Particle measuring device for granule processing apparatus and particle measuring method
CN115461155B (en) Grinding method and installation with material input recognition
JP3071137B2 (en) Method and apparatus for controlling supply of additive liquid in tumbling granulator
JP2951849B2 (en) Method and apparatus for controlling additive liquid supply amount in tumbling granulator
JP3528119B2 (en) How to measure powders
JPH0673621B2 (en) Automatic control method for bread granulator
JPH0889780A (en) Powder granulator and method for measuring grain size
JPH11123498A (en) Reclaiming method for used casting sand
JPH10104035A (en) Pellet measuring device and controller for dished granulator
JPH09290144A (en) Controlling method for additive liquid supply to tumbling granulator and apparatus therefor
KR100436409B1 (en) Method and apparatus for controlling additive supply of electric particle maker
JP2777921B2 (en) Method and apparatus for estimating actual rate of aggregate
CN115323168B (en) Granulating control device and granulating control method applied to rotary hearth furnace
JP3505440B2 (en) Material supply monitoring method and apparatus for metal injection molding machine
JPH10291650A (en) Alloy steel powder quantitative taking-out device
JPH0436422A (en) Method for pelletizing sintering raw material
JPS6058810A (en) Kneading and granulating machine of polymer
US20210379798A1 (en) Powdery-material mixing degree measurement device and compression molding system
JPH10174859A (en) Method of controlling feed quantity of additional liquid quantity to rolling granulator and device therefore