JPH0812091B2 - Granule flow meter - Google Patents

Granule flow meter

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Publication number
JPH0812091B2
JPH0812091B2 JP62027225A JP2722587A JPH0812091B2 JP H0812091 B2 JPH0812091 B2 JP H0812091B2 JP 62027225 A JP62027225 A JP 62027225A JP 2722587 A JP2722587 A JP 2722587A JP H0812091 B2 JPH0812091 B2 JP H0812091B2
Authority
JP
Japan
Prior art keywords
granular material
plate
detection plate
buffer
detection
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 - Fee Related
Application number
JP62027225A
Other languages
Japanese (ja)
Other versions
JPS63195524A (en
Inventor
浩 富安
康成 太田
Original Assignee
三協電業株式会社
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Filing date
Publication date
Application filed by 三協電業株式会社 filed Critical 三協電業株式会社
Priority to JP62027225A priority Critical patent/JPH0812091B2/en
Publication of JPS63195524A publication Critical patent/JPS63195524A/en
Publication of JPH0812091B2 publication Critical patent/JPH0812091B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 この発明は、粉粒体の流量を測定する流量計、特に貯
槽下部にホッパを有する粉粒体供給装置の排出口から落
下する穀類の輸送流量を測定する衝撃型流量計に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a flow meter for measuring the flow rate of powder or granular material, and more particularly to the flow rate of cereals falling from the outlet of a powder or granular material supply device having a hopper at the bottom of a storage tank. The present invention relates to an impact type flow meter for measuring.

従来の技術 粉粒体の輸送量、即ち流量を測定するには、秤量装置
を使用する方法とこの発明の対象とする衝撃型流量計を
使用する方法の2種がある。前者の方法では粉粒体の重
量を測定しているため、粉粒体の種類、形状等に関係な
く測定精度は高い。しかし、その機構は複雑で、高価で
ある。更に一定の秤量期間が必要であるため、早い応答
時間で測定することはできない。
2. Description of the Related Art There are two methods for measuring the amount of powder or granular material transported, that is, the flow rate, that is, a method of using a weighing device and a method of using an impact type flow meter as an object of the present invention. In the former method, the weight of the granular material is measured, so that the measurement accuracy is high regardless of the type and shape of the granular material. However, the mechanism is complicated and expensive. Furthermore, since a constant weighing period is required, it is not possible to measure with a fast response time.

これに反して、衝撃型流量計を使用する方法では、粉
粒体を検出板に当て、その時検出板に生ずる衝撃から流
量を電気的に算出している。この流量計は応答速度が早
く、粉粒体の流量を連続的に測定する場合、あるいは流
量を所定の値に常時維持するよう制御する場合に使用さ
れている。しかしながら、この衝撃型流量計は間接測定
であるため、種々の要因により得られる精度には限界が
ある。
On the contrary, in the method of using the impact type flow meter, the granular material is applied to the detection plate, and the flow rate is electrically calculated from the impact generated on the detection plate at that time. This flow meter has a fast response speed and is used when continuously measuring the flow rate of powder or granular material or when controlling so that the flow rate is always maintained at a predetermined value. However, since this impact type flow meter is an indirect measurement, there is a limit to the accuracy that can be obtained due to various factors.

この種の流量計には測定精度を高めるため、落下する
粉粒体が横方向に飛散しないように、粉粒体供給装置の
排出口に樋または布製のシュータを取付けることがあ
る。また、粉粒体が検出板上で一時的に不連続な滞留な
いしは付着を生じる場合、この現象を防止する振動機構
を検出板内に組込んでいるものもある。
In order to improve the measurement accuracy in this type of flow meter, a gutter or a cloth shooter may be attached to the discharge port of the powder or granular material supply device so as to prevent the powder or granular material from falling laterally. Further, in some cases, when a powder or granular material temporarily stays discontinuously or adheres on the detection plate, a vibration mechanism for preventing this phenomenon is incorporated in the detection plate.

発明が解決しようとする課題 衝撃型流量計を使用する測定は長時間連続し行う場合
が多い。それ故、流量の指示値にわずかな誤差がある
と、供給した粉粒体の積算値は最終的に大きな差を与
え、実用上深刻な問題となっている。
Problems to be Solved by the Invention In many cases, measurement using an impact type flow meter is continuously performed for a long time. Therefore, if there is a slight error in the indicated value of the flow rate, the integrated value of the supplied powder or granular material finally gives a large difference, which is a serious problem in practical use.

検出板に加わる衝撃は落下する個々の粉粒体が検出板
に当って生ずる運動量、つまり各粉粒体の重量と衝突で
生じた速度の変化(進行方向の変化も含めて)との積の
総和の統計的な値に対応している。
The impact applied to the detection plate is the product of the momentum generated by each falling powder or granule hitting the detection plate, that is, the product of the weight of each powder or granular product and the change in velocity (including the change in traveling direction) caused by collision. Corresponds to the statistical value of the sum.

他方粉粒体の流量は通常単位時間内に輸送される粉粒
体の重量で表わされる。この流量と上記の衝撃とを比較
すると、後者には速度の変化が余分に含まれていて、謂
る間接測定となっている。それ故、例えば形状または密
度が僅かに異なる類似の粉粒体を同じ流量にして流して
も、測定の指示値には往々差が認められる。更に、同じ
粉粒体であっても、流量を大幅に変えた場合、流量の指
示値と実際の値との間には完全な比例関係(直線性)が
なく、直線からのずれも認められている。
On the other hand, the flow rate of the granular material is usually expressed by the weight of the granular material transported in a unit time. Comparing this flow rate with the above-mentioned impact, the latter contains an extra change in speed, which is a so-called indirect measurement. Therefore, even if similar granular materials having slightly different shapes or densities are flowed at the same flow rate, a difference is often observed in the indicated value of measurement. Furthermore, even for the same powder or granular material, when the flow rate is changed significantly, there is no perfect proportional relationship (linearity) between the indicated value and the actual value, and deviation from a straight line is also recognized. ing.

前記の誤差は粉粒体の種類が異なると入射条件が同じ
であっても検出系の検出感度に差が生じるからである。
感度に影響を与える要因は下記のものが考えられる。即
ち、 (i) 検出板に対する入射位置のずれ、 (ii) 検出板に対する入射方向のずれ、 (iii) 粉粒体のばらつき即ち速度分布の変化、 (iv) 検出板による反射状況の変化(例えば、粉粒体
の反発係数に差があると反射後の経路が異なることによ
るもの)、 (v) 検出板は単純な衝撃でなく、粉粒体が検出板に
沿って移動する時、滞留時間の間に及ぼす重力も検知し
ている。
The above-mentioned error is caused by the difference in the detection sensitivity of the detection system even if the incident conditions are the same when the types of the granular material are different.
The following factors are considered to affect the sensitivity. That is, (i) the deviation of the incident position with respect to the detection plate, (ii) the deviation of the incident direction with respect to the detection plate, (iii) the dispersion of the granular material, that is, the change in the velocity distribution, (iv) the change in the reflection state by the detection plate (for example, , The difference in the coefficient of restitution of the particles causes the path after reflection to be different), (v) The detection plate is not a simple impact, and the residence time when the particles move along the detection plate It also detects the gravity exerted during.

従来技術である樋等は(i),(ii)に対して有効な
効果を及ぼしているが(iii)〜(v)に対して有効な
働きをしていない。この発明の課題は上記要因の全に対
して有効な検出系を構成し、単純で、経費を少なく、再
現性のある流量値を指示する粉粒体流量計を提供するこ
とにある。
The conventional technology such as gutter exerts an effective effect on (i) and (ii), but does not work effectively on (iii) to (v). SUMMARY OF THE INVENTION An object of the present invention is to provide a powder / granular flowmeter which constitutes a detection system effective for all of the above-mentioned factors, and which is simple, inexpensive, and has a reproducible flow rate value.

課題を解決するための手段 この発明の課題は、この発明により、流量を可変でき
る粉粒体供給装置から落下する粉粒体を検出板に当て、
検出板に加わった力を電気信号に変換して粉粒体の流量
を測定する粉粒体流量計にあって、粉粒体供給装置下部
の排出口12と検出板2の間に一枚またはそれ以上の緩衝
板1を傾斜して設置し、最終緩衝板1を検出板2と同じ
向きに傾け、粉粒体供給装置から落下する全粉粒体を各
緩衝板1に受け、上記緩衝板1に沿って落下させ、次い
で検出板2に落し込む配置にし、この場合、最終緩衝板
1の水平面に対する傾斜角Θを検出板2の傾斜角Θ
より大きくし、最終緩衝板1の下端の直ぐ下に検出板2
の上端を配設し、検出板2に加わる力の鉛直方向の成分
を検出する検出系を備えていることにより解決されてい
る。
Means for Solving the Problems An object of the present invention is to apply a powder or granular material falling from a powder or granular material supply device capable of varying a flow rate to a detection plate according to the present invention,
A particle-granular flow meter for converting the force applied to the detection plate into an electric signal to measure the flow rate of the powder-granular material. Further buffer plates 1 are installed in a tilted manner, the final buffer plate 1 is tilted in the same direction as the detection plate 2, and all the powder particles falling from the powder particle supplying device are received by the buffer plates 1, 1 and then dropped onto the detection plate 2. In this case, the inclination angle Θ B of the final buffer plate 1 with respect to the horizontal plane is equal to the inclination angle Θ D of the detection plate 2.
It is made larger and the detection plate 2 is provided just below the lower end of the final buffer plate 1.
This is solved by disposing the upper end of the above and providing a detection system for detecting the vertical component of the force applied to the detection plate 2.

上記の構成に対して特許請求の範囲第2〜5項の構成
を付加すると、得られる効果は更に向上する。
When the configurations of claims 2 to 5 are added to the above configuration, the obtained effect is further improved.

作 用 この発明の構成は以下の作用を与える: (i) 緩衝板自体の働きで、粉粒体の流量が変わって
も、検出板に対する粉粒体の落下位置並びに落下方向を
一定にし、粉粒体供給装置から落下して来た粉粒体の速
度のばらつきを一定にする。
Operation The configuration of the present invention provides the following effects: (i) Even if the flow rate of the granular material changes due to the function of the buffer plate itself, the falling position and the falling direction of the granular material with respect to the detection plate are made constant, and The dispersion of the speed of the powder and granules falling from the granule feeder is made constant.

(ii)緩衝板と検出板の配置は両者の傾斜角度の差が小
さく、粉粒体は検出板に小さな衝撃で入射し、検出板上
を滑動しながら移動する。検出板の傾斜角が緩衝板の傾
斜角より少なく粉粒体の移動に伴って検出板に準静的な
力を加える。
(Ii) With respect to the disposition of the buffer plate and the detection plate, the difference in inclination angle between them is small, and the granular material is incident on the detection plate with a small impact and moves while sliding on the detection plate. The inclination angle of the detection plate is smaller than the inclination angle of the buffer plate, and a quasi-static force is applied to the detection plate with the movement of the granular material.

この発明の実施態様による構造から (iii)検出板を凹状に曲げ、(ii)に述べた粉粒体の
滑動により加わる力を更に高める。
From the structure according to the embodiment of the present invention, (iii) the detection plate is bent in a concave shape, and the force applied by the sliding of the powder or granular material described in (ii) is further increased.

(iv)緩衝板を凹状に曲げ、傾斜軸方向に平行な粉粒体
の発散を防止する。
(Iv) The buffer plate is bent in a concave shape to prevent the powder particles from diverging in parallel to the tilt axis direction.

(v)緩衝板の傾斜角度を微調機構により変化させるこ
とができる。
(V) The inclination angle of the buffer plate can be changed by the fine adjustment mechanism.

実施例 以下、実施例を示す図面に基づき、この発明をより詳
しく説明する。
Embodiment Hereinafter, the present invention will be described in more detail with reference to the drawings illustrating an embodiment.

第1図はこの発明による粉粒体流量計の一実施例で適
用される検出部の一部を最も単純な形にして模式的に示
す。粉粒体10は粉粒体供給装置下部の排出口12から落下
し、先ず斜めに配置してある緩衝板1に当る、次いで、
粉粒体10はこの緩衝板1に沿って移動し下端より落下す
る。この場合、緩衝板1の下端の直下に接近させて検出
板2の上端を置き、両方の板1,2の傾斜方向は同じ向き
に設置する。
FIG. 1 schematically shows a part of a detection unit applied in an embodiment of the granular material flowmeter according to the present invention in the simplest form. The granular material 10 falls from the outlet 12 at the lower part of the granular material supply device, and first hits the buffer plate 1 which is obliquely arranged, and then,
The granular material 10 moves along the buffer plate 1 and falls from the lower end. In this case, the upper end of the detection plate 2 is placed close to the lower end of the buffer plate 1 so that both plates 1 and 2 are inclined in the same direction.

この発明による緩衝板1は一枚に限定するものでな
く、第2図にも示すように一枚以上で構成することもで
きる。緩衝板1(または緩衝板の枚数が多いときには最
下部にある板)と検出板2の傾斜角度を第1図に示すよ
うにそれぞれΘおよびΘとすると、この発明による
幾何学配置では、ΘをΘより大きく選び、両者の差
を20゜以内にすると有効である。
The buffer plate 1 according to the present invention is not limited to one, but may be composed of one or more as shown in FIG. Assuming that the inclination angles of the buffer plate 1 (or the plate at the bottom when there are many buffer plates) and the detection plate 2 are Θ B and Θ D , respectively, as shown in FIG. It is effective to select Θ B larger than Θ D and make the difference between them within 20 °.

緩衝板1自体には以下の作用がある。第1図から容易
に測定できように、排出口12から落下して来た粉粒体10
を一旦緩衝板1に当てるため、粉粒体10′では緩衝板1
の下端より落下する方向および位置とも一定になる。更
に粉粒体の落下速度にばらつきがあっても、一度この緩
衝板に当るため、ばらつきが平均化される。冒頭に述べ
た従来の技術で利用されている樋またはシュータは往々
主落下方向から外れている粉粒体のみを壁面に当て、主
落下方向に戻しているため、この発明による速度を均一
にする作用はない。
The buffer plate 1 itself has the following actions. As can be easily measured from Fig. 1, the granular material 10 has fallen from the discharge port 12
Is applied to the buffer plate 1 once, the buffer plate 1
The direction and position of the drop from the bottom end of are constant. Further, even if there is a variation in the falling speed of the powdery particles, the variation is averaged because it hits the buffer plate once. The gutter or shooter used in the prior art mentioned at the beginning often applies only the granular material that is out of the main falling direction to the wall surface and returns it in the main falling direction, so that the speed according to the present invention is made uniform. It has no effect.

更にこの発明による検出方法は従来使用されている衝
撃型流量計とは著しい相違がある。即ち、上に述べた均
一化された速度の粉粒体10′を検出板2に入射角を小さ
く保って入れている点である。この入射条件では検出板
2に加わる衝撃は少なく、むしろ粉粒体が検出板2上を
滑動して移動するとき準静的な重力を加えている。この
発明では検出板2に加わる力の垂直方向の成分のみ検出
している検出部(図示せず)を組込んでいるため、秤量
測定に近い作用を利用して流量を検出していることにな
る。
Furthermore, the detection method according to the present invention is significantly different from the conventional impact type flowmeter. That is, the powder particles 10 'having a uniform speed described above are placed in the detection plate 2 while keeping the incident angle small. Under this incident condition, the impact applied to the detection plate 2 is small, and rather, when the powdery particles slide on the detection plate 2 and move, quasi-static gravity is applied. In the present invention, since the detection unit (not shown) that detects only the component of the force applied to the detection plate 2 in the vertical direction is incorporated, the flow rate is detected by using the action close to the weighing measurement. Become.

ΘをΘより大きくしたのは次の理由による。即
ち、仮にΘがΘより小さいと、粉粒体の一部(場合
によっては全部)が検出板に当らない可能生が生ずる
(第1図で粉粒体の流れ10′の上部にある粉粒体はΘ
が大きいと、検出板を飛越す)。この発明の構成、Θ
−Θ>0で、緩衝板1の下部と検出板の上部が接近し
ている限り、全ての粉粒体は検出板2に入射する。更
に、検出板2に対する入射方向は粉粒体がこの検出板2
上を滑動して移動する向きに対応する角度より大きいの
で、検出板2に常時準静的な力を加えている。
The reason why Θ B is made larger than Θ D is as follows. That is, if Θ B is smaller than Θ D , there is a possibility that a part (in some cases, all) of the granular material does not hit the detection plate (in the upper part of the granular material flow 10 'in FIG. 1). The powder is Θ D
Is large, the detection plate will be skipped). Structure of the invention, Θ B
As long as −Θ D > 0 and the lower part of the buffer plate 1 and the upper part of the detection plate are close to each other, all the particles enter the detection plate 2. Further, in the incident direction with respect to the detection plate 2, powder particles are present on the detection plate 2.
Since it is larger than the angle corresponding to the direction of sliding and moving up, a quasi-static force is constantly applied to the detection plate 2.

第2aと2b図にこの発明による流量計の緩衝板を1枚以
上で形成した例を2種示す。全ての緩衝板1は第2a図で
同じ向きに、第2b図で交互に傾けて配置してある。緩衝
板の枚数を増すことは、落下速度をより低減し、検出板
上に滞在する時間が長くなり、検出感度を高める。第2b
図の配置は横方向の設置面積を少なくする。
2a and 2b show two kinds of examples in which one or more buffer plates of the flowmeter according to the present invention are formed. All buffer plates 1 are arranged in the same orientation in FIG. 2a and alternately tilted in FIG. 2b. Increasing the number of buffer plates further reduces the falling speed, prolongs the time of staying on the detection plate, and increases the detection sensitivity. 2b
The arrangement shown in the figure reduces the footprint in the lateral direction.

第3図にこの発明を適用した流量計の検出部の一実施
例を示す。この場合、緩衝板1と検出板2には何ずれも
僅かな反りが与えてある。緩衝板1の反りは傾斜軸5に
直交していて、この板1の中央を通る平面に対して対称
に上方に向けて凹状に形成されている。従って、粉粒体
が傾斜軸方向に発散するのを防止する働きがある。検出
板2の反りに付いては第4図でその作用効果を説明す
る。更に、この緩衝板1の支持機構にはノブ3で傾斜角
度を微調する傾斜機構が組み込まれ、流量計本体4に回
動可能に設置されている。傾斜機構の取付方法は、第3
図の実施例以外に、ノブ3を本体4の内部に設置し、一
旦調整を終えたら人手に触れないような場所に取付けて
おくこともできる。
FIG. 3 shows an embodiment of the detector of the flow meter to which the present invention is applied. In this case, the buffer plate 1 and the detection plate 2 are slightly warped by any displacement. The warp of the buffer plate 1 is orthogonal to the tilt axis 5 and is formed in a concave shape upward in a symmetrical manner with respect to a plane passing through the center of the plate 1. Therefore, it has a function of preventing the powdery particles from diverging in the direction of the tilt axis. With respect to the warp of the detection plate 2, its function and effect will be described with reference to FIG. Further, a tilting mechanism for finely adjusting the tilt angle with the knob 3 is incorporated in the support mechanism of the buffer plate 1, and is rotatably installed on the flowmeter main body 4. The mounting method of the tilting mechanism is the third
In addition to the illustrated embodiment, the knob 3 can be installed inside the main body 4 and, once the adjustment is completed, can be installed in a place where it cannot be touched by human hands.

第4図にこの発明による検出板2の一実施例を示す。
この検出板2は第5a図に示す流量測定に使用した寸法を
記入してある。検出板2の下半分に反りを与えてある。
この反りは第1図で説明したときと同じように、この検
出板2上を出る粉粒体が滑動する時、検出板2に加わる
準静的な力を更に大きくする作用がある。従って検出感
度も向上する。
FIG. 4 shows an embodiment of the detection plate 2 according to the present invention.
The detector plate 2 has the dimensions used for measuring the flow rate shown in FIG. 5a. The lower half of the detection plate 2 is warped.
This warp has the effect of further increasing the quasi-static force applied to the detection plate 2 when the powder or granules leaving the detection plate 2 slide, as in the case described with reference to FIG. Therefore, the detection sensitivity is also improved.

この発明の構成による効果を知るため、表Iに示す緩
衝板と検出板の2種の組合せを用いて表IIに示す2種の
小麦の流量を測定した。この発明による配置αでは緩衝
板の下端と検出板の上端は水平面に投影したとき一致す
る位置にし、HとH′はそれぞれ第1図に示す垂直方向
の距離である。検出板および緩衝板の大きさは20×20cm
2である。
In order to know the effect of the constitution of the present invention, the flow rates of two kinds of wheat shown in Table II were measured by using two kinds of combinations of the buffer plate and the detection plate shown in Table I. In the arrangement α according to the present invention, the lower end of the buffer plate and the upper end of the detection plate are located at the same position when projected on the horizontal plane, and H and H ′ are vertical distances shown in FIG. 1, respectively. The size of the detection plate and buffer plate is 20 x 20 cm
2

実流量値は一定期間流した小麦の重量を秤量して定
め、指示流量値は両方の配置α,βともA種の小麦で実
流量値を約8t/hにして検出器の指示値を実流量値に合わ
せ、検出器をこのままの状態にしてA種の小麦では他の
流量値、B値の小麦では全ての流量について測定した。
検出器はセンサはインダクションコイルであり、検出板
の垂直方向の力を検出するように配置した。流量測定は
各測点で5回行いその平均値を示してある。平均値から
のばらつきは0.5%よりも少なかった。
The actual flow rate is determined by weighing the weight of wheat that has flowed for a certain period of time, and the indicated flow rate for both arrangements α and β is the wheat of type A and the actual flow rate is set to about 8 t / h and the indicated value of the detector is measured. According to the flow rate value, the detector was left as it was, and the other flow rate values were measured for wheat of A type and all the flow rates were measured for wheat of B value.
The sensor of the detector is an induction coil and is arranged so as to detect the force in the vertical direction of the detection plate. The flow rate measurement was performed 5 times at each measurement point, and the average value is shown. The deviation from the average value was less than 0.5%.

従来技術による構成の配置βの測定結果を第5b図に示
す。A,B種の比重は3%程度の差で反発係数は経験上か
なりあることが知られている。この配置βでは両種の麦
で測定の差は約7%生ずる。流量をかえると直線からの
ずれも認められる。
FIG. 5b shows the measurement result of the arrangement β of the configuration according to the prior art. It is known from experience that the repulsion coefficient is fairly large with a difference of about 3% in the specific gravity of A and B types. With this configuration β there is a difference of about 7% in the measurement between both species of wheat. When the flow rate is changed, deviation from the straight line is also recognized.

この発明の配置αでは第5a図に示すように著しい改善
が見られ、両者の測定値は図中に描いた直線に対して約
1%の範囲で一致している。
The arrangement α of the present invention shows a significant improvement as shown in FIG. 5a, and both measured values agree with the straight line drawn in the figure within a range of about 1%.

発明の効果 検出板の前に設置した緩衝板により、検出板に対する
粉粒体の落下位置、落下方向を一定にするだけでなく、
速度のばらつきも均して測定感度の再現性を高めてい
る。
Advantageous Effects of the Invention With the buffer plate installed in front of the detection plate, not only the drop position and the falling direction of the powder particles with respect to the detection plate are constant,
Reproducibility of measurement sensitivity is improved by evenly adjusting speed variations.

粉粒体が検出板に入射する時、緩衝板が浅い角度で入
射させているので、検出板に大きな衝撃を加えなくて、
むしろ検出板に沿って落下する時の重量による力を加え
ている。このことは秤量測定の状態に近くなっているこ
とを意味し、測定の再現性を向上させている。
When the powder particles enter the detection plate, the buffer plate is incident at a shallow angle, so a large shock is not applied to the detection plate,
Rather, the force due to the weight when falling along the detection plate is applied. This means that it is close to the state of weighing measurement and improves the reproducibility of measurement.

検出板の反りは検出感度を高め、緩衝板の傾斜機構は
検度の再現性を一定にする作用があり、製作、保守を容
易にする。
The warp of the detection plate enhances the detection sensitivity, and the tilting mechanism of the buffer plate has the effect of making the reproducibility of the measurement constant, which facilitates the production and maintenance.

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

第1図、この発明による検出板と緩衝板の配置を示す模
式断面図、 第2図、複数の緩衝板の可能な配置を示す側面図、 第3図、この発明による流量計の外観図、 第4図、この発明による検出板の一実施形状を示す断面
図、 第5aと5b図、それぞれ検出系の2種の配置αとβによっ
て2種の小麦に対して得られた流量測定値を示すグラ
フ。 図中参照符号:1……緩衝板、2……検出板
1, a schematic cross-sectional view showing the arrangement of a detection plate and a buffer plate according to the present invention, FIG. 2, a side view showing a possible arrangement of a plurality of buffer plates, FIG. 3, an external view of a flow meter according to the present invention, FIG. 4 is a cross-sectional view showing one embodiment of the detection plate according to the present invention, FIGS. 5a and 5b, showing flow rate measurement values obtained for two kinds of wheat by two arrangements α and β of the detection system, respectively. The graph that shows. Reference symbols in the figure: 1 ... Buffer plate, 2 ... Detection plate

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】流量を可変できる粉粒体供給装置から落下
する粉粒体を検出板に当て、検出板に加わった力を電気
信号に変換して粉粒体の流量を測定する粉粒体流量計に
おいて、粉粒体供給装置下部の排出口(12)と検出板
(2)の間に一枚またはそれ以上の緩衝板(1)を傾斜
して設置し、最終緩衝板(1)を検出板(2)と同じ向
きに傾け、粉粒体供給装置から落下する全粉粒体を各緩
衝板(1)に受け、上記緩衝板(1)に沿って落下さ
せ、次いで検出板(2)に落し込む配置にし、この場
合、最終緩衝板(1)の水平面に対する傾斜角(Θ
を検出板(2)の傾斜角(Θ)より大きくし、最終緩
衝板(1)の下端の直ぐ下に検出板(2)の上端を配設
し、検出板(2)に加わる力の鉛直方向の成分を検出す
る検出系を備えていることを特徴とする粉粒体流量計。
1. A granular material for measuring the flow rate of a granular material by applying a granular material falling from a granular material supply device whose flow rate is variable to a detection plate and converting the force applied to the detection plate into an electric signal. In the flow meter, one or more buffer plates (1) are installed at an angle between the discharge port (12) at the bottom of the powder and granular material supply device and the detection plate (2), and the final buffer plate (1) is installed. Tilt in the same direction as the detection plate (2), receive all the powder and granules falling from the powder and granular material supply device in each buffer plate (1), drop them along the buffer plate (1), and then detect the detection plate (2). ), In this case, the inclination angle (Θ B ) of the final buffer plate (1) with respect to the horizontal plane.
Is larger than the inclination angle (Θ D ) of the detection plate (2), the upper end of the detection plate (2) is arranged just below the lower end of the final buffer plate (1), and the force applied to the detection plate (2) is A granular material flowmeter, comprising a detection system for detecting a vertical component.
【請求項2】検出板(2)の下端半分を上方に向けて凹
状に曲げてあることを特徴とする特許請求の範囲第1項
に記載の粉粒体流量計。
2. The granular material flowmeter according to claim 1, wherein the lower half of the lower end of the detection plate (2) is bent upward to form a concave shape.
【請求項3】緩衝板(1)は傾斜軸(5)に直交し、こ
の板(1)の中心を通る平面に対して対称に上方に向け
て凹状に曲げてあることを特徴とする特許請求の範囲第
1項または第2項に記載の粉粒体流量計。
3. A buffer plate (1) which is orthogonal to the tilt axis (5) and is bent upward in a concave shape symmetrically with respect to a plane passing through the center of the plate (1). The granular material flowmeter according to claim 1 or 2.
【請求項4】複数の緩衝板(1)の場合、各緩衝板
(1)を交互に交差する向きに傾けてあるか、あるいは
同じ向きに傾けてあるかの何ずれか一方の配置にしてあ
ることを特徴とする特許請求の範囲第1〜3項の何ずれ
か1項に記載の粉粒体流量計。
4. In the case of a plurality of buffer plates (1), the respective buffer plates (1) are arranged so as to be alternately tilted in a direction intersecting with each other or tilted in the same direction, or with some displacement. The granular material flowmeter according to any one of claims 1 to 3, which is characterized by being present.
【請求項5】緩衝板(1)の支持機構に傾斜角を可変に
する傾斜機構(5)が組み込まれていることを特徴とす
る特許請求の範囲第1〜4項の何ずれか1項に記載の粉
粒体流量計。
5. A tilting mechanism (5) for varying a tilt angle is incorporated in a support mechanism of a buffer plate (1), and any one of claims 1 to 4 is set. The granular material flowmeter described in.
JP62027225A 1987-02-10 1987-02-10 Granule flow meter Expired - Fee Related JPH0812091B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62027225A JPH0812091B2 (en) 1987-02-10 1987-02-10 Granule flow meter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62027225A JPH0812091B2 (en) 1987-02-10 1987-02-10 Granule flow meter

Publications (2)

Publication Number Publication Date
JPS63195524A JPS63195524A (en) 1988-08-12
JPH0812091B2 true JPH0812091B2 (en) 1996-02-07

Family

ID=12215148

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62027225A Expired - Fee Related JPH0812091B2 (en) 1987-02-10 1987-02-10 Granule flow meter

Country Status (1)

Country Link
JP (1) JPH0812091B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5798466A (en) * 1996-01-26 1998-08-25 Satake Corporation Flow meter and method of calibrating same
JP3750125B2 (en) * 1996-12-26 2006-03-01 株式会社サタケ Impact type flow rate detector
JP6135874B2 (en) 2015-04-09 2017-05-31 三協パイオテク株式会社 Impact type powder flow meter

Also Published As

Publication number Publication date
JPS63195524A (en) 1988-08-12

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