JPS5920085B2 - Powder flow rate measuring device - Google Patents

Powder flow rate measuring device

Info

Publication number
JPS5920085B2
JPS5920085B2 JP15229278A JP15229278A JPS5920085B2 JP S5920085 B2 JPS5920085 B2 JP S5920085B2 JP 15229278 A JP15229278 A JP 15229278A JP 15229278 A JP15229278 A JP 15229278A JP S5920085 B2 JPS5920085 B2 JP S5920085B2
Authority
JP
Japan
Prior art keywords
flow rate
powder
layer thickness
rotating drum
measuring device
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
Application number
JP15229278A
Other languages
Japanese (ja)
Other versions
JPS5578216A (en
Inventor
利治 高野
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.)
Shinko Electric Co Ltd
Original Assignee
Shinko Electric 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 Shinko Electric Co Ltd filed Critical Shinko Electric Co Ltd
Priority to JP15229278A priority Critical patent/JPS5920085B2/en
Publication of JPS5578216A publication Critical patent/JPS5578216A/en
Publication of JPS5920085B2 publication Critical patent/JPS5920085B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Measuring Volume Flow (AREA)

Description

【発明の詳細な説明】 本発明は回転ドラムに落下する粉粒体の重量を検出して
、その流量を計測する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for detecting the weight of powder particles falling onto a rotating drum and measuring the flow rate thereof.

従来、一般に使用されるこの種装置では、ベルトスケー
ル等によりベルト上の粉粒体(荷重)を荷重検出器を用
いて検出し、これを電気信号に変換して流量を言−[I
Jする構造になっているが、斯る従来の構造ではベルト
コンベアを構成するだめの、プーリキャリアローラや或
はコンベアベルトの蛇行調整装置等、比較的複雑な機構
が必要であり、またベルトコンベアを使用しているため
、ベルトの材質によっては食品等の特殊な粉粒体には使
用できない等の欠点があった。
Conventionally, this type of device that is commonly used uses a load detector to detect the powder or granular material (load) on the belt using a belt scale or the like, and converts this into an electrical signal to express the flow rate.
However, such a conventional structure requires a relatively complicated mechanism such as a pulley carrier roller or a meandering adjustment device for the conveyor belt, which constitutes the belt conveyor. However, depending on the material of the belt, it cannot be used for special powder or granular materials such as food.

本発明は上記に鑑み、振動コンベアの切出口直下に無羽
根、若しくは層厚を必要とする場合は、所望の層厚に相
当する放射状の羽根を取付けた回転ドラムを設け、ドラ
ム上に落下した粉粒体の荷重を検出して流量を計測する
装置を提供することが目的であり、以下、図示する一実
施例について本発明を説明する。
In view of the above, the present invention provides a rotating drum equipped with radial blades corresponding to the desired layer thickness when no blades or a layer thickness is required directly below the cutting exit of the vibrating conveyor. An object of the present invention is to provide an apparatus for detecting the load of powder and granular material and measuring the flow rate, and the present invention will be described below with reference to an illustrated embodiment.

第1図は本発明の粉粒体の層厚を所望しない場合で、回
転ドラム外周に何の手段も施こされていない言わば基本
的な第1実施例を示すが、1は振動トラフによる供給装
置で、その切出口から粉粒体を排出し、直下に設ける回
転ドラム2に落下させる。
Fig. 1 shows a so-called basic first embodiment in which no desired layer thickness of the powder or granular material of the present invention is applied to the outer periphery of the rotating drum. The device discharges the granular material from the cutting port and drops it onto the rotating drum 2 provided directly below.

この回転ドラム2には第1図に例示した層厚を要求しな
い場合のものと、一定の層厚を所望する場合の2通りが
あり、第2図にはその後者を示し、放射状に羽根を取付
杆、羽根と羽根との間に所望の層厚を形成するようにし
たものである。
There are two types of rotary drum 2: one that does not require the layer thickness shown in Fig. 1, and one that requires a constant layer thickness. A desired layer thickness is formed between the mounting rod and the blade.

この回転ドラム2の軸芯には、支点3(エツジ)で支え
られたビーム4の端部が結合され、ドラム2上に落下し
た粉粒体の荷重を検出器5に伝達する。
The end of a beam 4 supported by a fulcrum 3 (edge) is connected to the axis of the rotating drum 2, and the load of the powder and granular material falling onto the drum 2 is transmitted to the detector 5.

斯して検出された荷重は増幅器6で電気信号に変換され
粉粒体の流量は計測される。
The load thus detected is converted into an electrical signal by an amplifier 6, and the flow rate of the powder is measured.

従って、本発明の回転ドラムを使用するこ(rtcより
、従来型のベルトスケール式流量計にみられるような、
ベルトコンベア機構等による複雑な構成を必要としなく
なる上、回転ドラム2は鋼板にて製作できるので、清潔
をむねとする食品等の特殊な粉粒体にも有効に利用でき
、全く悪影響を及ぼすことがない。
Therefore, the use of the rotating drum of the present invention (RTC), as found in conventional belt scale flowmeters,
In addition to eliminating the need for a complex configuration such as a belt conveyor mechanism, the rotary drum 2 can be made of steel plate, so it can be effectively used for special powder and granular materials such as foods that need to be kept clean, without causing any adverse effects. There is no.

従って、本発明は各種粉粒体のあらゆる場合に適用でき
、汎用性の極めて高い割11]装置を得ることができる
ものである。
Therefore, the present invention can be applied to all types of powder and granular materials, and it is possible to obtain an extremely versatile device.

また、今までに述べた第1実施例で示す回転ドラムは、
外周に何の手段も施こされていない円筒形であるため、
粉粒体の層厚を大きくとることはできないが、ドラムを
回転させることにより絶えず新しい重量を求めることが
できる。
Furthermore, the rotating drum shown in the first embodiment described above is
Because it is cylindrical with no measures applied to its outer periphery,
Although it is not possible to increase the layer thickness of the powder, new weights can be constantly determined by rotating the drum.

そこで、前述のドラム上で層厚所望の要求を満たすには
第2図で示すようなドラム外周に所望の層厚に相当する
高さの羽根を放射状に設けることにより、極めて容易に
解消することができる。
Therefore, in order to satisfy the above-mentioned requirement for the desired layer thickness on the drum, it is extremely easy to solve this problem by providing radial blades with a height corresponding to the desired layer thickness on the outer periphery of the drum as shown in Fig. 2. Can be done.

伺、本発明により粉粒体の実流量をてこの理を応用して
直接的に計測する場合は、次に述べる方法の何れかに求
められることを付記する。
However, it should be noted that when the actual flow rate of powder or granular material is directly measured by applying the principle of leverage according to the present invention, one of the following methods is required.

その1は、回転ドラムの回転速度が一定の場合は、増幅
器の出力のみを計測することにより求められ、その2は
、回転ドラムの回転速度が変化する時は、増幅器の出力
と回転ドラムの速度とを乗算することにより求められる
The first is that when the rotational speed of the rotating drum is constant, it can be obtained by measuring only the output of the amplifier, and the second is that when the rotational speed of the rotating drum changes, it can be obtained by measuring the output of the amplifier and the speed of the rotating drum. It is found by multiplying by.

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

第1図は本発明の第1実施例を示す構成図、第2図は本
発明の第2実施例を示す構成略図である。 1・・・・・・供給装置、2・・・・・・回転ドラム、
3・・・・・・ビームの支点、4・・・・・・ビーム、
5・・・・・・荷重検出装置6・・・・・・増幅器。
FIG. 1 is a block diagram showing a first embodiment of the present invention, and FIG. 2 is a schematic block diagram showing a second embodiment of the present invention. 1... Supply device, 2... Rotating drum,
3...Fully point of the beam, 4...Beam,
5...Load detection device 6...Amplifier.

Claims (1)

【特許請求の範囲】[Claims] 1 振動コンベアの切出口直下に、粉粒体の層厚を所望
しない場合は無羽根で、層厚を必要とする場合は所望の
層厚に相当する放射状の羽根を取付けた回転ドラムを設
け、該回転ドラムに落下する粉粒体の荷重を、エツジを
支点とするビームの回動によりロードセルに伝え、これ
を増幅器を介して電気信号に変換し、上記回転ドラム上
の流量を計測するように構成したことを特徴とする粉粒
体流量計測装置。
1. Directly below the cutting port of the vibrating conveyor, a rotary drum is provided without blades when the layer thickness of the powder or granular material is not desired, and with radial blades installed corresponding to the desired layer thickness when the layer thickness is required, The load of the powder falling onto the rotating drum is transmitted to the load cell by the rotation of the beam with the edge as a fulcrum, and this is converted into an electrical signal via an amplifier to measure the flow rate on the rotating drum. A powder or granular material flow rate measuring device characterized by comprising:
JP15229278A 1978-12-08 1978-12-08 Powder flow rate measuring device Expired JPS5920085B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15229278A JPS5920085B2 (en) 1978-12-08 1978-12-08 Powder flow rate measuring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15229278A JPS5920085B2 (en) 1978-12-08 1978-12-08 Powder flow rate measuring device

Publications (2)

Publication Number Publication Date
JPS5578216A JPS5578216A (en) 1980-06-12
JPS5920085B2 true JPS5920085B2 (en) 1984-05-10

Family

ID=15537331

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15229278A Expired JPS5920085B2 (en) 1978-12-08 1978-12-08 Powder flow rate measuring device

Country Status (1)

Country Link
JP (1) JPS5920085B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6056234U (en) * 1983-09-27 1985-04-19 のむら産業株式会社 Powder flow rate measuring device
JPS6070316A (en) * 1983-09-27 1985-04-22 Nomura Sangyo Kk Apparatus for measuring flow rate of powdery material
JPS6085331A (en) * 1983-09-27 1985-05-14 Haruhisa Takatani Flow-rate measuring method of bulk material
JPH067665U (en) * 1992-03-09 1994-02-01 俊蔵 市村 scissors

Also Published As

Publication number Publication date
JPS5578216A (en) 1980-06-12

Similar Documents

Publication Publication Date Title
US4201093A (en) Ultrasonic sheet material testing apparatus
US5002140A (en) Method of and apparatus for weighing a continuous stream of fluent material
GB2130371A (en) Determining the charge of solids on a centrifuge drum
JPH06194202A (en) Device for measuring flowing amount of mass body
US5970802A (en) Relating to mass flow measuring apparatuses
US4336851A (en) Loop conveyor type flow weigher
JPS5920085B2 (en) Powder flow rate measuring device
JPS5646426A (en) Volumetric device of powder/grain substance
JPH0718733B2 (en) Method and apparatus for continuously measuring the amount of material flow in bulk
JPS55166022A (en) Digital type dynamic balance measurement device
US4520677A (en) Solids mass flow indication with radiation
JPS60502228A (en) Device for measuring the liquid part of a two-phase flow of gas and liquid
US5253535A (en) Apparatus and method for monitoring mass flow of solids
US6185983B1 (en) Method and apparatus for automatically determining zero setting of impeller-type mass flow rate-measuring device when flow is absent
JPS6035879Y2 (en) Coal powder moisture measuring device
US4066406A (en) Process and apparatus for the voltammetric measurement of the quantity or mass of separated sample components
JPH06186069A (en) Powder flowmeter
SU451940A1 (en) Method for determining the angle of repose of powdered materials
JPH0519781Y2 (en)
JP2627943B2 (en) Method and apparatus for measuring flow rate of granular material
SU890155A1 (en) Device for measuring particle dimensions
JPS55140117A (en) Measuring apparatus for vibration of rotating vane
JPS54158255A (en) Angular displacement detector
JPS55140114A (en) Automatically unravelling and measuring apparatus for adherent, thready products
SU1728730A2 (en) Device for monitoring granulometric composition of ground grain