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JPH056854B2 - - Google Patents
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JPH056854B2 - - Google Patents

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Publication number
JPH056854B2
JPH056854B2 JP21458586A JP21458586A JPH056854B2 JP H056854 B2 JPH056854 B2 JP H056854B2 JP 21458586 A JP21458586 A JP 21458586A JP 21458586 A JP21458586 A JP 21458586A JP H056854 B2 JPH056854 B2 JP H056854B2
Authority
JP
Japan
Prior art keywords
powder
weight
granular material
sealed casing
calculated
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
JP21458586A
Other languages
Japanese (ja)
Other versions
JPS6370122A (en
Inventor
Hiromi Yamaguchi
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP21458586A priority Critical patent/JPS6370122A/en
Publication of JPS6370122A publication Critical patent/JPS6370122A/en
Publication of JPH056854B2 publication Critical patent/JPH056854B2/ja
Granted legal-status Critical Current

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  • Air Transport Of Granular Materials (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は粉粒体の定量供給機、フイーダーにお
ける粉粒体の粉粒体供給量の計量算出方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a quantitative feeder for powder and granule, and a method for measuring and calculating the amount of powder and granule supplied in a feeder.

(従来の技術) 従来、外周に粉粒体を収容する空間を形成した
回転供給盤を回転自在に嵌装したケーシングの一
方上方に粉粒体を回転供給盤に投入する供給口を
設け、又略反対側に粉粒体の排出部を設け、供給
口で収容空間に粉粒体を投入して充填し、回転供
給盤の回転とともに排出部まで移動させて排出部
で外部に排出するタイプの定量供給機、フイーダ
ーが広く使用されている。このタイプの定量供給
機の粉粒体の供給量の算出法は粉粒体収容空間の
容積(総容積)に回転数と枡比重(単位容積に充
填された粉粒体の重さ)とを乗じた値として算出
する方法が広く採用されている。あるいは粉粒体
を含めた定量供給機全体の重量を計測し、この計
測重量から一定の定量供給機自体の重量を減じる
ことによつて、粉粒体の重量を算出し、これに回
転数を乗じた値として供給量を算出する方法も或
る。又、粉体を回転供給する環状コンベアを揺動
自在に軸支するとともに、その傾動を1台のロー
ドセルで計測して環状コンベアに収容された粉粒
体を計測する方法が特開昭56−27619号公報に開
示されている。又、特公昭51−24266号公報には
粉体を回転供給する環状コンベアを揺動自在に軸
支するとともに釣合重錘で平衡させ、その平衡の
崩れを変位検出接点で検出して環状コンベアへの
投入粉体量を変えて定量状態に維持する方法が開
示されている。
(Prior art) Conventionally, a casing in which a rotary supply board having a space for accommodating powder and granules is rotatably fitted on the outer periphery is provided with a supply port for introducing powder and granules into the rotary supply board above one side, and This type has a discharge part for the powder and granular material on almost the opposite side, and fills the storage space with the powder at the supply port, moves it to the discharge part as the rotary supply plate rotates, and discharges it to the outside at the discharge part. Quantitative feeding machines and feeders are widely used. The method for calculating the supply amount of powder and granular material for this type of quantitative feeder is based on the volume of the powder storage space (total volume), the number of revolutions, and the cell specific gravity (the weight of the powder and granular material filled in a unit volume). A method of calculating as a multiplied value is widely adopted. Alternatively, you can calculate the weight of the powder by measuring the weight of the entire metering machine including the powder and granular material, and subtracting a certain weight of the metering machine itself from this measured weight. There is also a method of calculating the supply amount as a multiplied value. In addition, a method of measuring the powder and granular material contained in the annular conveyor by rotatably supporting an annular conveyor that rotates and supplies powder and measuring its tilting with one load cell was disclosed in Japanese Patent Application Laid-Open No. 1986- It is disclosed in Publication No. 27619. In addition, Japanese Patent Publication No. 51-24266 discloses that an annular conveyor that rotates and supplies powder is pivotally supported so as to be able to swing freely, is balanced by a counterweight, and the imbalance is detected by a displacement detection contact, and the annular conveyor is Disclosed is a method for maintaining a fixed amount by changing the amount of powder input into the container.

(発明が解決しようとする問題点) このタイプの定量供給機において、回転供給盤
の粉粒体収容空間の粉粒体が排出部で全量排出さ
れず一部の粉粒体が粉粒体収容空間を形成する壁
面に付着した状態で投入部に戻つて次の粉粒体の
充填を受けていた。そのため実際排出部で排出さ
れる粉粒体量が上記計算の重量値より低い値とな
り、誤差を生じるという問題点があつた。又、環
状コンベアの傾動をロードセル又は変位検出接点
で検出して、環状コンベアに収容された粉粒体の
重量を計測又はその変動を検出する特開昭56−
27619号公報記載の重量計測方法では、重量の情
報量がロードセル、又は変位検出信号のみである
ので、重量の変動が環状コンベアの送給側・帰還
側・投入口付近・吐出口付近に発生しているか、
又は増減いずれであるかの情報を得ることができ
ず、正確な重量の変動の把握と計算ができなかつ
た。特に環状コンベアの帰還側に付着した粉体量
を正確に計測できず、正確な粉粒体供給量の算出
が難しかつた。
(Problem to be solved by the invention) In this type of quantitative feeder, the powder and granules in the powder and granule storage space of the rotary supply plate are not all discharged at the discharge section, and some of the powder and granules are stored in the powder and granule storage space. The particles adhered to the walls forming the space and returned to the charging section to be filled with the next powder or granular material. Therefore, there was a problem in that the amount of powder and granular material actually discharged at the discharge section was lower than the weight value calculated above, resulting in an error. In addition, Japanese Patent Application Laid-Open No. 1983-1997 discloses a method of detecting the tilting movement of the annular conveyor using a load cell or a displacement detection contact to measure the weight of the powder or granular material contained in the annular conveyor or to detect its fluctuation.
In the weight measurement method described in Publication No. 27619, the amount of weight information is only the load cell or displacement detection signal, so weight fluctuations occur on the feeding side, return side, near the input port, and near the discharge port of the annular conveyor. Are you there?
Or, it was not possible to obtain information on whether it was an increase or decrease, and it was not possible to accurately understand and calculate weight fluctuations. In particular, it was not possible to accurately measure the amount of powder adhering to the return side of the annular conveyor, making it difficult to accurately calculate the amount of powder and granular material supplied.

(問題点を解決するための手段) 本発明はかかる問題点を解消し、粉粒体収容空
間壁面に付着した粉粒体量を計測してそれによる
誤差を補正して真の粉粒体供給量を算出方法を提
供せんとするものであり、外周に粉粒体を収容す
る空間を形成した回転供給盤を密閉ケーシング内
に回転自在に嵌装し、同密閉ケーシングの上壁一
周端部に粉粒体を回転供給盤の粉粒体収容空間に
投入する供給口を開口し、又同供給口と反対側の
密閉ケーシングの周端部の上下壁面を開口し、同
開口部それぞれに空気流によつて垂直に粉粒体を
排出する垂直管を接続し、しかも密閉ケーシング
の供給口とこれに粉粒体を投入する粉粒体投入装
置との間及び垂直管とこれに接続される空気輸送
本管との間を密閉ケーシング側に周辺機器の重量
が荷重されない構造で接続するとともに、密閉ケ
ーシングの供給口と垂直管とを結ぶ中央線に対し
中心を通つて直交する直角線上の密閉ケーシング
の対称周端下面位置に1個と2個のロードセル使
用の重量計測器を配置し、この三つのロードセル
の重量計測器で装置全体を支持し、これら三つの
重量計測器の計測値から力とモーメントの平衡式
に基づいて帰還路上にある回転供給盤の粉粒体収
容空間に付着した粉粒体重量を算出し、この付着
粉粒体の算出重量を回転供給盤の粉粒体収容空間
の容積と回転数と単位容積当りの充填粉粒体重量
を乗じた粉粒体重量算出値又は上記複数の重量計
算器から算出した移送路上にある粉粒体総重量値
から減じることによつて真の粉粒体供給量を算出
することを特徴とする粉粒体供給量の計量補正法
にある。
(Means for Solving the Problems) The present invention solves these problems, and measures the amount of powder adhering to the wall surface of the powder storage space and corrects the resulting error to ensure true powder supply. In order to provide a method for calculating the amount, a rotary supply plate with a space for accommodating powder and granules is rotatably fitted into a sealed casing, and a rotating supply board with a space formed on the outer periphery for accommodating powder and granules is rotatably fitted into the sealed casing, and a A supply port for introducing powder and granular material into the powder storage space of the rotating supply board is opened, and the upper and lower walls of the peripheral end of the sealed casing on the opposite side to the supply port are opened, and air flows through each of the openings. A vertical pipe for vertically discharging powder and granular material is connected by a vertical pipe, and also between the supply port of the sealed casing and a powder charging device for charging powder and granular material into this, and between the vertical pipe and the air connected to this. The sealed casing is connected to the transportation main in a structure that does not load the weight of peripheral equipment on the sealed casing side, and the sealed casing is located on a perpendicular line passing through the center and perpendicular to the center line connecting the supply port of the sealed casing and the vertical pipe. A weight measuring device using one and two load cells is placed at the lower surface of the symmetrical peripheral edge of the device, the entire device is supported by the weight measuring devices of these three load cells, and the force and force are calculated from the measured values of these three weight measuring devices. The weight of the powder adhering to the powder storage space of the rotating supply board on the return path is calculated based on the moment balance equation, and the calculated weight of the adhering powder is calculated as the weight of the adhering powder to the powder storage space of the rotating supply board. The powder weight calculated by multiplying the volume, rotation speed, and packed powder weight per unit volume, or by subtracting it from the total weight of the powder on the transfer path calculated from the above-mentioned multiple weight calculators. The present invention provides a measurement correction method for the amount of powder and granular material supplied, which is characterized by calculating the amount of powder and granular material supplied.

(実施例) 以下実施例をもつて詳細に説明する。(Example) A detailed explanation will be given below using examples.

図面に示す実施例は円形密閉ケーシング1の供
給口2と垂直管とを結ぶ中央線4に対し中心を通
つて直交する直角線4′上の密閉ケーシング1の
対称周端下面位置に1個と2個のロードセル5,
6,7を配置して、この三つのロードセルでもつ
て密閉ケーシング1、回転供給盤8、粉粒体9、
駆動装置10及びこれら付属品の装置全体の重量
を分散支持している。回転供給盤8は外周に放射
状羽根11を多数突設し、同羽根と密閉ケーシン
グ1の内周上・下・側壁とによつて粉粒体収容空
間12が形成されている。又垂直管3と空気輸送
本管14との間は伸縮管15で接続され、しかも
空気輸送本管14は地上側に固定支持されている
ため上下の空気輸送本管14側の重量は密閉ケー
シング側には荷重されない。同様に供給口2と粉
粒体投入装置側の粉粒体投入管16との間も伸縮
管17でもつて接続され且つ粉粒体投入管16は
地上側に固定支持され、粉粒体投入管16側の重
量が密閉ケーシング側に荷重されない様になつて
いる。
The embodiment shown in the drawings has one piece located on the lower surface of the symmetrical end of the sealed casing 1 on a right angle line 4' passing through the center and perpendicular to the center line 4 connecting the supply port 2 of the circular sealed casing 1 and the vertical pipe. 2 load cells 5,
6 and 7 are arranged, and these three load cells are used to transport the sealed casing 1, the rotary supply plate 8, the powder and granular material 9,
The entire weight of the drive device 10 and its accessories is distributed and supported. The rotary supply plate 8 has a large number of radial blades 11 protruding from its outer periphery, and the granular material storage space 12 is formed by the radial blades 11 and the upper, lower, and side walls of the inner periphery of the sealed casing 1 . Also, the vertical pipe 3 and the pneumatic transport main pipe 14 are connected by a telescopic pipe 15, and since the pneumatic transport main pipe 14 is fixedly supported on the ground side, the weight of the upper and lower pneumatic transport main pipes 14 is absorbed by the sealed casing. There is no load on the side. Similarly, the supply port 2 and the granular material input pipe 16 on the side of the granular material input device are also connected by a telescopic tube 17, and the granular material input pipe 16 is fixedly supported on the ground side. The weight of the 16 side is not applied to the closed casing side.

図中20は回転供給盤8の回転数を検出するロ
ータリーエンコーダー、21は残留付着粉粒体の
重量を算出する付着粉粒体重量計算回路、22は
回転供給盤8の移送路側にある粉粒体の総重量を
算出する移送粉粒体重量算出回路、23は真の粉
粒体供給量を算出する供給量計算回路、24は表
示器、25は回転供給盤の粉粒体収容空間の容
積、粉粒体の単位容積当りの重さ、粉粒体の比重
等の諸元数値を設定入力する入力回路、26は回
転供給盤8の回転数制御回路、27は比較回路、
28は粉粒体供給量の目標設定値入力回路29は
圧力及び重量調整用ダミーである。
In the figure, 20 is a rotary encoder that detects the rotation speed of the rotary supply board 8, 21 is an adhered powder weight calculation circuit that calculates the weight of the remaining adhered powder, and 22 is a powder on the transfer path side of the rotary supply board 8. 23 is a supply amount calculation circuit that calculates the true powder supply amount, 24 is a display, and 25 is the volume of the powder storage space of the rotating supply board. , an input circuit for setting and inputting numerical values such as the weight per unit volume of the powder and granular material, specific gravity of the powder and granular material, 26 a rotation speed control circuit of the rotary supply board 8, 27 a comparison circuit,
Reference numeral 28 denotes a target setting value input circuit 29 for the amount of powder and granular material supplied, which is a dummy for pressure and weight adjustment.

第6図はスクレーパー方式の回転供給盤の例で
あり、30はスクレーパー方式回転供給盤、31
は同回転供給盤の粉粒体収容棚、32はスクレー
パーである。
Figure 6 shows an example of a scraper type rotary supply board, 30 is a scraper type rotary supply board, 31
32 is a powder storage shelf of the same rotating supply plate, and a scraper.

この第1〜5図に示す実施例では粉粒体は粉粒
体投入管16から供給口2を通つて密閉ケーシン
グ1内に投入され、回転供給盤8の放射状羽根1
1の間の粉粒体収容空間12に充填され、密閉ケ
ーシング1の内壁面又はスリ切り板によつてスリ
切られて定量状態で回転移送され、反対側の垂直
管3の空気流によつて下から上又は上から下へ排
出され空気輸送本管14によつて所要地へ輸送さ
れるものである。
In the embodiment shown in FIGS. 1 to 5, the powder is introduced into the closed casing 1 from the powder input pipe 16 through the supply port 2, and the radial blades 1 of the rotary supply plate 8
The powder is filled in the powder storage space 12 between the closed casing 1, is cut by the inner wall surface of the closed casing 1 or by the slit plate, and is rotatably transferred in a fixed amount, and is then transported by the air flow of the vertical pipe 3 on the opposite side. It is discharged from the bottom to the top or from the top to the bottom and transported to the desired location by the pneumatic transport main 14.

密閉ケーシング1にある粉粒体及びその装置全
体の重量は粉粒体移送路側にある一個のロードセ
ル5と帰還路側にある二個のロードセル6,7に
よつて支持される。二組のロードセル5,6,7
に作用する密閉ケーシング1装置及び粉粒体の荷
重分布は第5図に示す様なものになつている。密
閉ケーシング等の装置重量の荷重分布(a)は計測以
前に決定されるものである。密閉ケーシング1の
周辺機器の供給口2に接続された粉粒体投入管1
6及び垂直管3に接続された空気輸送本管14は
ゴム等の伸縮管15,17で接続されているので
その重量は密閉ケーシング側に荷重されていな
い。
The weight of the powder in the sealed casing 1 and the entire device is supported by one load cell 5 on the powder transfer path side and two load cells 6 and 7 on the return path side. Two sets of load cells 5, 6, 7
The load distribution of the closed casing 1 device and the powder and granular material acting on it is as shown in FIG. The load distribution (a) of the weight of equipment such as a closed casing is determined before measurement. Powder input pipe 1 connected to supply port 2 of peripheral equipment in sealed casing 1
6 and the vertical pipe 3 are connected by elastic tubes 15, 17 made of rubber or the like, so that their weight is not applied to the closed casing side.

三個のロードセル5,6,7に作用する粉粒体
荷重は移送路にある粉粒体重量分布(b)と帰還路に
ある付着した粉粒体による粉粒体重量分布(c)及び
供給口2に貯つた粉粒体重量分布(d)である。
The powder loads acting on the three load cells 5, 6, and 7 are the powder weight distribution in the transfer path (b), the powder weight distribution due to the attached powder in the return path (c), and the supply. This is the weight distribution (d) of the powder particles accumulated in mouth 2.

ここで回転供給盤8の複数の粉粒体収容空間1
2には移送路において均一に充填され、又帰還路
においては均一に付着しているとの近似モデルを
仮定することによつて瞬間における粉粒体重量分
布(b)(充填率)、粉粒体重量分布c(付着率)、粉
粒体重量分布(d)がカ・モーメントの平衡式とロー
ドセル5,6,7に作用した荷重計測値から算出
できる。これから付着粉粒体重量を求め、粉粒体
重量分布(b)から計算された移送粉粒体重量あるい
は粉粒体収容空間容積×単位容積粉粒体重量×回
転数の式から求めた移送粉粒体重量値から差し引
くことによつて排出された真の粉粒体供給量を求
めることができる。これらの計算は移送粉粒体重
量算出回路22、付着粉粒体重量計算回路21、
供給量計算回路23によつてなされる。
Here, a plurality of powder storage spaces 1 of the rotary supply board 8
2, the instantaneous powder particle weight distribution (b) (filling ratio), the powder particle weight distribution (b) (filling ratio), and The weight distribution c (adhesion rate) and the particle weight distribution (d) can be calculated from the force moment equilibrium equation and the measured values of the loads acting on the load cells 5, 6, and 7. From this, the weight of attached powder particles is determined, and the weight of the transferred powder is calculated from the powder weight distribution (b), or the transferred powder is calculated from the formula of powder storage space volume x unit volume powder weight x rotation speed. By subtracting from the grain weight value, the true amount of powder supplied can be determined. These calculations are performed by a transferred powder weight calculation circuit 22, an attached powder weight calculation circuit 21,
This is done by the supply amount calculation circuit 23.

尚粉粒体供給量の計算式は上記モデル計算方式
に限定するものでなく他のモデル・算出式でもよ
いことは勿論である。
It goes without saying that the calculation formula for the powder supply amount is not limited to the above model calculation method, and other models and calculation formulas may be used.

特に本実施例では密閉ケーシング1の供給口2
と垂直管3とを結ぶ中央線4に対し中心を通つて
直交する直角線4′上の密閉ケーシング1の対称
周端下面にロードセル5とロードセル6,7とを
配置することによつて供給口2に貯つた粉粒体重
量分布(d)及び粉粒体の供給口2への投入衝激荷重
及び垂直管3からの排出時の衝激荷重を二組のロ
ードセル5、ロードセル6,7に同じ様に作用す
る様にしてその影響を抑えている。更に空気輸送
本管14からの空気圧は上下の伸縮管15及び伸
縮管17とダミー29とに同じ様に作用してその
空気圧の影響を少くしている。
In particular, in this embodiment, the supply port 2 of the sealed casing 1
By arranging the load cell 5 and the load cells 6 and 7 on the lower surface of the symmetrical peripheral end of the sealed casing 1 on the right angle line 4' passing through the center and perpendicular to the center line 4 connecting the vertical pipe 3 and The powder weight distribution (d) stored in 2, the impact load when the powder is introduced into the supply port 2, and the impact load when it is discharged from the vertical pipe 3 are transmitted to two sets of load cells 5, 6, and 7. The effect is suppressed by making it work in the same way. Furthermore, the air pressure from the air transport main pipe 14 acts on the upper and lower telescopic pipes 15, the telescopic pipes 17, and the dummy 29 in the same way, thereby reducing the influence of the air pressure.

本実施例では更に粉粒体供給量を目標設定値に
なる様に回転供給盤8の回転数を制御できるもの
としている。
In this embodiment, the rotational speed of the rotary supply plate 8 can be further controlled so that the amount of powder and granular material supplied reaches a target setting value.

(発明の効果) 以上の様に本発明によれば回転供給盤に付着し
て残留した粉粒体重量を補正して、吐出した真の
粉粒体の供給量を計測できるという効果がある。
(Effects of the Invention) As described above, according to the present invention, it is possible to correct the weight of the powder particles remaining on the rotary supply plate and measure the true supply amount of the discharged powder particles.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の実施例の粉粒体供給装置の構
造を示す縦断面図、第2図は同平面図、第3図は
ロードセルの配置を示す平面図、第4図は同実施
例の回路ブロツク図、第5図はロードセルに作用
する重量分布図、第6図はスクレーパー方式の粉
粒体供給装置の構造を示す説明図である。 1……密閉ケーシング、2……供給口、3……
垂直管、4……中央線、4′……直角線、5,6,
7……ロードセル、8……回転供給盤、9……粉
粒体、10……駆動装置、11……放射状羽根、
12……粉粒体収容空間、14……空気輸送管、
21……付着粉粒体重量計算回路、22……移送
粉粒体重量算出回路、23……供給量計算回路。
FIG. 1 is a longitudinal cross-sectional view showing the structure of a powder supply device according to an embodiment of the present invention, FIG. 2 is a plan view of the same, FIG. 3 is a plan view showing the arrangement of load cells, and FIG. 4 is a plan view of the same embodiment. FIG. 5 is a diagram of the weight distribution acting on the load cell, and FIG. 6 is an explanatory diagram showing the structure of a scraper type powder supply device. 1... Sealed casing, 2... Supply port, 3...
Vertical pipe, 4... Center line, 4'... Right angle line, 5, 6,
7... Load cell, 8... Rotating supply plate, 9... Powder, 10... Drive device, 11... Radial vane,
12... Powder storage space, 14... Air transport pipe,
21... Adhesive powder particle weight calculation circuit, 22... Transfer powder particle weight calculation circuit, 23... Supply amount calculation circuit.

Claims (1)

【特許請求の範囲】[Claims] 1 外周に粉粒体を収容する空間を形成した回転
供給盤を密閉ケーシング内に回転自在に嵌装し、
同密閉ケーシングの上壁一周端部に粉粒体を回転
供給盤の粉粒体収容空間に投入する供給口を開口
し、又同供給口と反対側の密閉ケーシングの周端
部の上下壁面を開口し、同開口部それぞれに空気
流によつて垂直に粉粒体を排出する垂直管を接続
し、しかも密閉ケーシングの供給口とこれに粉粒
体を投入する粉粒体投入装置との間及び垂直管と
これに接続される空気輸送本管との間を密閉ケー
シング側に周辺機器の重量が荷重されない構造で
接続するとともに、密閉ケーシングの供給口と垂
直管とを結ぶ中央線に対し中心を通つて直交する
直角線上の密閉ケーシングの対称周端下面位置に
1個と2個のロードセル使用の重量計測器を配置
し、この三つのロードセルの重量計測器で装置全
体を支持し、これら三つの重量計測器の計測値か
ら力とモーメントの平衡式に基づいて帰還路上に
ある回転供給盤の粉粒体収容空間に付着した粉粒
体重量を算出し、この付着粉粒体の算出重量を回
転供給盤の粉粒体収容空間の容積と回転数と単位
容積当りの充填粉粒体重量を乗じた粉粒体重量算
出値又は上記複数の重量計算器から算出した移送
路上にある粉粒体総重量値から減じることによつ
て真の粉粒体供給量を算出することを特徴とする
粉粒体供給量の計量補正法。
1. A rotating supply plate with a space formed around the outer periphery for accommodating powder and granular material is rotatably fitted into a sealed casing,
A supply port for introducing powder and granular material into the powder storage space of the rotating supply board is opened at one circumferential end of the upper wall of the sealed casing, and the upper and lower wall surfaces of the circumferential end of the sealed casing opposite to the supply port are opened. A vertical pipe is connected to each opening to vertically discharge powder and granular material by air flow, and between the supply port of the sealed casing and a powder and granular material input device that introduces powder and granular material into this. The vertical pipe and the pneumatic transport main pipe connected to it are connected in a structure that prevents the weight of peripheral equipment from being loaded on the sealed casing side, and the center line is connected to the center line connecting the supply port of the sealed casing and the vertical pipe. A weight measuring device using one and two load cells is placed at the bottom surface of the symmetrical peripheral edge of the sealed casing on a perpendicular line passing through the The weight of the powder adhering to the powder storage space of the rotating supply board on the return path is calculated based on the force-moment equilibrium equation from the measured values of the two weight measuring instruments, and the calculated weight of the adhering powder is calculated. Powder weight calculation value obtained by multiplying the volume and rotation speed of the powder storage space of the rotating supply plate by the packed powder weight per unit volume, or the powder or granule on the transfer path calculated from the above-mentioned multiple weight calculators. A measurement correction method for the amount of powder and granular material supplied, characterized in that the true amount of powder and granular material supplied is calculated by subtracting it from the total weight value.
JP21458586A 1986-09-10 1986-09-10 Method for correction measurement of supply quantity of particulate material Granted JPS6370122A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21458586A JPS6370122A (en) 1986-09-10 1986-09-10 Method for correction measurement of supply quantity of particulate material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21458586A JPS6370122A (en) 1986-09-10 1986-09-10 Method for correction measurement of supply quantity of particulate material

Publications (2)

Publication Number Publication Date
JPS6370122A JPS6370122A (en) 1988-03-30
JPH056854B2 true JPH056854B2 (en) 1993-01-27

Family

ID=16658153

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21458586A Granted JPS6370122A (en) 1986-09-10 1986-09-10 Method for correction measurement of supply quantity of particulate material

Country Status (1)

Country Link
JP (1) JPS6370122A (en)

Also Published As

Publication number Publication date
JPS6370122A (en) 1988-03-30

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