JPH0413634Y2 - - Google Patents

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Publication number
JPH0413634Y2
JPH0413634Y2 JP1984199077U JP19907784U JPH0413634Y2 JP H0413634 Y2 JPH0413634 Y2 JP H0413634Y2 JP 1984199077 U JP1984199077 U JP 1984199077U JP 19907784 U JP19907784 U JP 19907784U JP H0413634 Y2 JPH0413634 Y2 JP H0413634Y2
Authority
JP
Japan
Prior art keywords
chute
damper
powder
weighing
weighing hopper
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
JP1984199077U
Other languages
Japanese (ja)
Other versions
JPS61112235U (en
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 filed Critical
Priority to JP1984199077U priority Critical patent/JPH0413634Y2/ja
Publication of JPS61112235U publication Critical patent/JPS61112235U/ja
Application granted granted Critical
Publication of JPH0413634Y2 publication Critical patent/JPH0413634Y2/ja
Expired legal-status Critical Current

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  • Weight Measurement For Supplying Or Discharging Of Specified Amounts Of Material (AREA)

Description

【考案の詳細な説明】 [産業上の利用分野] 本考案は、例えば穀物や石炭粉末等のような微
粉末を含む粉粒体の計量装置に関するものであ
る。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a measuring device for a powder or granular material containing fine powder such as grain or coal powder.

[従来の技術] 従来のこの種の計量装置は、例えば第2図に概
要を示すように、計量ホツパ1の上下に大型の上
部バツフアタンク2と下部バツフアタンク3とを
備え、計量ホツパ1の上部と下部バツフアタンク
3とを通気管4で連通し、計量ホツパ1の上部に
は排気孔5を設け、吸引管6を介して集塵機に接
続している。ここで、計量される粉粒体は上部バ
ツフアタンク2から投入ゲート7,8を経て計量
ホツパ1に入るが、このとき粉粒体の体積に相当
する分の空気が排斥されることになり、その排斥
空気は排気孔5を通つて吸引管6で吸引されるよ
うになつている。
[Prior Art] A conventional weighing device of this type is provided with a large upper buffer tank 2 and a lower buffer tank 3 above and below a weighing hopper 1, as shown schematically in FIG. The weighing hopper 1 is connected to a lower buffer tank 3 through a ventilation pipe 4, and an exhaust hole 5 is provided in the upper part of the weighing hopper 1, which is connected to a dust collector via a suction pipe 6. Here, the granular material to be weighed enters the weighing hopper 1 from the upper buffer tank 2 through the input gates 7 and 8, but at this time, air corresponding to the volume of the granular material is expelled. The expelled air passes through the exhaust hole 5 and is sucked in by the suction pipe 6.

そして、計量ホツパ1で計量された粉粒体は、
排出ゲート9を経て下部バツフアタンク3に排出
されるが、この時の排斥空気は通気管4を通つて
計量ホツパ1に戻り、空気による圧力平衡の崩れ
た差圧分だけが排気孔5から排気又は吸気される
ようになつている。このように、計量ホツパ1に
粉粒体を投入する度ごとに排斥空気が噴出、同時
に粉粒体に含まれる粉塵も噴出するので、このま
までは周辺が汚染されるだけでなく、粉粒体の種
類によつては粉塵爆発等を惹き起す危険性があ
る。
Then, the powder and granular material weighed by the weighing hopper 1 is
The air is discharged to the lower buffer tank 3 through the discharge gate 9, but the rejected air at this time returns to the weighing hopper 1 through the ventilation pipe 4, and only the differential pressure where the pressure balance due to the air is broken is exhausted or discharged from the exhaust hole 5. It is starting to be inhaled. In this way, each time powder is put into the weighing hopper 1, the displaced air is ejected, and at the same time, the dust contained in the powder is also ejected. Depending on the type, there is a risk of causing a dust explosion.

その対策として、従来では計量ホツパ1の上部
と投入部間を密閉型防塵カバーで覆つているが、
完全密閉のために排斥された空気が圧縮され、そ
の結果として外部の空気との間に差圧が発生し、
計量値に誤差を生ずる原因となつている。その誤
差を小さくするために、排気孔5と可撓筒10を
用いて通排気を行つて差圧の減少を図り、排気孔
5には集塵機を連結して一定の吸引圧力が吸引さ
せているのである。
As a countermeasure, conventionally the upper part of the weighing hopper 1 and the input section are covered with an airtight dustproof cover.
For complete sealing, the expelled air is compressed, resulting in a pressure difference between it and the outside air.
This causes errors in measurement values. In order to reduce this error, the exhaust hole 5 and the flexible cylinder 10 are used to ventilate air to reduce the differential pressure, and a dust collector is connected to the exhaust hole 5 to draw in a constant suction pressure. It is.

このように従来装置では、集塵機を要するため
に設備が大掛かりとなり、設備費も高くスペース
的にも不利である。しかも一定の吸引圧力で吸引
しても、粉粒体の動きによつて計量ホツパ1の内
部空間体積が変化するから、内部空気による差圧
値は絶えず変動し、その変動が計量値に影響して
計量誤差をもたらすという問題も残されている。
更に、排気孔5と吸引管6との接合部は、調整可
能な開口を有しているため、微粉末の噴出を完全
に防止することは難しいという欠点もある。
As described above, the conventional apparatus requires a dust collector, which requires large-scale equipment, and is expensive and disadvantageous in terms of space. Furthermore, even if suction is carried out at a constant suction pressure, the internal space volume of the weighing hopper 1 changes due to the movement of the powder and granules, so the differential pressure value due to the internal air constantly fluctuates, and this fluctuation affects the measured value. However, there remains the problem that this may lead to measurement errors.
Furthermore, since the joint between the exhaust hole 5 and the suction pipe 6 has an adjustable opening, there is also the drawback that it is difficult to completely prevent the ejection of fine powder.

[考案の目的] 本考案の目的は、粉塵が外部に噴出することが
なく、集塵設備が不要で従来型よりも小型安価に
でき、しかも計量精度も優れている粉粒体の計量
装置を提供することにある。
[Purpose of the invention] The purpose of the invention is to create a powder and granule weighing device that does not emit dust to the outside, does not require dust collection equipment, is smaller and cheaper than conventional types, and has excellent weighing accuracy. It is about providing.

[考案の概要] 上述の目的を達成するための本考案の要旨は、
計量すべき粉粒体を連結的に投入する分配シユー
トと、その下方設置した計量ホツパと、更にその
下方に排出シユートとを備えた計量装置におい
て、前記分配シユートと前記計量ホツパ間及び前
記計量ホツパと前記排出シユート間とをそれぞれ
第1及び第2の防塵カバーにより連結し、前記計
量ホツパ内と前記分配シユートの上部とを通気管
により連通し、該通気管を気密に遮断するための
第1のダンパを設け、前記排出シユートの下部に
前記排出シユートとその下方の間を気密に遮断す
るための第2のダンパを設け、前記分配シユート
から前記計量ホツパへの粉粒体の大投入時におい
ては前記第1のダンパを開放し前記第2のダンパ
を閉止し小投入時においては前記第1、第2のダ
ンパを共に閉止し、前記計量シユートから前記排
出シユートへの粉粒体の排出時においては前記第
1、第2のダンパは共に開放するようにしたこと
を特徴とする粉粒体の計量装置である。
[Summary of the invention] The gist of the invention to achieve the above objectives is as follows:
In a weighing device equipped with a distribution chute into which powder and granular material to be weighed are input in a connected manner, a weighing hopper installed below the distribution chute, and a discharge chute further below the distribution chute, a discharge chute is provided between the distribution chute and the weighing hopper and between the weighing hopper and the weighing hopper. and the discharge chute by first and second dustproof covers, respectively, the inside of the weighing hopper and the upper part of the distribution chute are communicated by a ventilation pipe, and a first A second damper is provided at the bottom of the discharge chute for airtightly blocking the space between the discharge chute and the lower part thereof, and when a large amount of powder or granular material is charged from the distribution chute to the measuring hopper. When the first damper is opened and the second damper is closed, both the first and second dampers are closed during small injection, and when the powder and granular material is discharged from the measuring chute to the discharge chute. In this apparatus, both the first and second dampers are opened.

[考案の実施例] 本考案を第1図に図示の実施例に基づいて詳細
に説明する。
[Embodiment of the invention] The invention will be explained in detail based on the embodiment shown in FIG.

第1図は先に本出願人によつて出願された実願
昭58−143383号の粉粒体の計量装置に、本考案を
適用した実施例を示すものである。この第1図に
おいて、投入用コンベア11から投入された粉粒
体は分配シユート12に入り、図示しない整流板
により整流された後に攪拌回転羽根13の攪拌作
用を受け、分配シユート12の中心から等距離で
等角度に配置された適当数の例えば4個の供給ホ
ツパ14にほぼ等分に分配される。
FIG. 1 shows an embodiment in which the present invention is applied to a measuring device for powder and granular material, which was previously filed by the present applicant in Utility Application No. 143383/1983. In FIG. 1, the powder and granules input from the input conveyor 11 enter the distribution chute 12, and after being rectified by a rectifying plate (not shown), are subjected to the stirring action of the stirring rotary blades 13, and are distributed from the center of the distribution chute 12, etc. It is distributed almost equally to a suitable number of supply hoppers 14, for example four, arranged at equal angles in distance.

各供給ホツパ14の下方には、それぞれ計量ホ
ツパ15が配備されており、各供給ホツパ14の
下端に設けられた大出しゲート16又は小出しゲ
ート17を通つて各計量ホツパ15へ投入された
粉粒体の荷重を、計量ホツパ15に備えた図示し
ない荷重変換器で測定するようになつている。そ
して計量済みの粉粒体は、排出ゲート18から各
計量ホツパ15の下方に設けられた排出シユート
19に落下された後、集合排出シユート20を通
つて排出され排出用コンベア等に移される。
A weighing hopper 15 is provided below each supply hopper 14, and powder particles are fed into each weighing hopper 15 through a large output gate 16 or a small output gate 17 provided at the lower end of each supply hopper 14. The body load is measured by a load converter (not shown) provided in the weighing hopper 15. The weighed powder and granules are dropped from the discharge gate 18 into the discharge chute 19 provided below each weighing hopper 15, and then discharged through the collective discharge chute 20 and transferred to a discharge conveyor or the like.

上述の構成は前述の実願昭58−143383号の粉粒
体の計量装置と殆ど同様であり、大出しゲート1
6、小出しゲート17、排出ゲート18等はそれ
ぞれの駆動機構により、制御装置からの指令に基
づいて開閉されるようになつている。
The above-mentioned configuration is almost the same as the powder weighing device of the aforementioned Utility Application No. 143383/1983, and the large output gate 1
6. The dispensing gate 17, the discharge gate 18, etc. are opened and closed by respective drive mechanisms based on commands from the control device.

本考案においては、更に次に述べるような差圧
低減機構が付設されている。即ち、分配シユート
12の外周部に計量ホツパ15と同数の防塵カバ
ー21がそれぞれ設けられ、これらの防塵カバー
21は各計量ホツパ15の上部と力を伝達しない
可撓性筒22によつて連結されている。また、防
塵カバー21の内部の空間は通気管23を介して
分配シユート12の上部に連通され、通気管23
の上端部には開閉自在の上部気密ダンパ24が設
けられている。更に、各計量ホツパ15と排出シ
ユート19の間にかけて防塵カバー25がそれぞ
れ設けられ、これらの防塵カバー25は可撓性筒
26を有しており、計量ホツパ15と排出シユー
ト19間で力が伝達されないようになつている。
また、防塵カバー25の内部空間は通気管27を
介して各計量ホツパ15の上部に通じている。更
に、排出シユート19の下端部にもそれぞれ下部
気密ダンパ28が設けられ、上部気密ダンパ24
から下部気密ダンパ28にかけて差圧低減機構が
構成されている。
The present invention is further provided with a differential pressure reduction mechanism as described below. That is, the same number of dustproof covers 21 as the weighing hoppers 15 are provided on the outer periphery of the distribution chute 12, and these dustproof covers 21 are connected to the upper part of each weighing hopper 15 by a flexible cylinder 22 that does not transmit force. ing. Further, the space inside the dustproof cover 21 is communicated with the upper part of the distribution chute 12 via the ventilation pipe 23.
An upper airtight damper 24 that can be opened and closed is provided at the upper end. Furthermore, a dustproof cover 25 is provided between each weighing hopper 15 and the discharge chute 19, and each of these dustproof covers 25 has a flexible cylinder 26, so that force is transmitted between the weighing hopper 15 and the discharge chute 19. It is becoming more and more difficult to do so.
Further, the internal space of the dustproof cover 25 communicates with the upper part of each weighing hopper 15 via a ventilation pipe 27. Further, lower airtight dampers 28 are provided at the lower ends of the discharge chute 19, respectively, and upper airtight dampers 24
A differential pressure reduction mechanism is constructed from the lower airtight damper 28 to the lower airtight damper 28.

計量時の作動順次は、制御装置の指令に基づい
て空計量→大投入→小投入→本計量→排出のサイ
クルが各計量ホツパ15ごとに繰り返されるが、
これと同期して上部気密ダンパ24と下部気密ダ
ンパ28の開閉も次にように行われる。即ち、空
計量時と大投入時には、上部気密ダンパ24が開
かれ下部気密ダンパ28が閉止される。従つて、
大出しゲート16を開いた大投入時に発生する排
斥空気は、通気管23、上部気密ダンパ24を通
て分配シユート12へ戻される。次に、小投入時
及び本計量時には、上部気密ダンパ24も下部気
密ダンパ28も共に閉止される。小投入時の排斥
空気は少量であるから可撓性筒22から防塵カバ
ー21内へ、或いは通気管27から防塵カバー2
5内へ排出可能である。更に、計量を終えた粉粒
体を排出ゲート18を開けて排出シユート19へ
落下させる排出時においては、上部気密ダンパ2
4も下部気密ダンパ28も共に開いた状態にな
り、以後は同様なサイクルを繰り返すことにな
る。
The sequence of operations during weighing is such that the cycle of empty weighing → large loading → small loading → main weighing → discharging is repeated for each weighing hopper 15 based on commands from the control device.
In synchronization with this, the upper airtight damper 24 and the lower airtight damper 28 are opened and closed as follows. That is, during empty metering and large filling, the upper airtight damper 24 is opened and the lower airtight damper 28 is closed. Therefore,
The rejected air generated when the large discharge gate 16 is opened is returned to the distribution chute 12 through the ventilation pipe 23 and the upper airtight damper 24. Next, both the upper airtight damper 24 and the lower airtight damper 28 are closed at the time of small injection and main measurement. Since the amount of expelled air during small injection is small, it is transferred from the flexible cylinder 22 into the dustproof cover 21 or from the ventilation pipe 27 to the dustproof cover 2.
It can be discharged into 5. Furthermore, when discharging the weighed powder and granules by opening the discharge gate 18 and dropping them into the discharge chute 19, the upper airtight damper 2
4 and the lower airtight damper 28 are both opened, and the same cycle is repeated thereafter.

このようにして、上部気密ダンパ24も下部気
密ダンパ28も、計量時には少なくとも1回は閉
止され、計量時に生ずる差圧を低減する役割を果
している。
In this way, both the upper airtight damper 24 and the lower airtight damper 28 are closed at least once during measurement, and serve to reduce the differential pressure that occurs during measurement.

なお、4個の計量ホツパ15は順次に作動する
ため、ほぼ連続的な計量が可能となるが、計量ホ
ツパ15が1個の場合にも本考案が適用できるこ
とは勿論である。また、時間当りの計量収納能力
の大小によつて計量ホツパ15の容量を異なるよ
うにすればよいが、前述の差圧低減機構は計量ホ
ツパ15の容量の大小に関係なく適用することが
できる。更に、このような差圧低減機構は、第2
図に例示したような従来型の計量装置にも付設す
ることが可能である。
Note that since the four weighing hoppers 15 operate sequentially, almost continuous weighing is possible, but it goes without saying that the present invention can also be applied to a case where there is only one weighing hopper 15. Further, although the capacity of the weighing hopper 15 may be made different depending on the size of the measuring storage capacity per hour, the above-described differential pressure reduction mechanism can be applied regardless of the capacity of the weighing hopper 15. Furthermore, such a differential pressure reduction mechanism
It can also be attached to a conventional metering device such as the one illustrated in the figure.

[考案の効果] 以上説明したように本考案に係る粉粒体の計量
装置は、従来必要とされていた集塵設備が不要と
なるため、小型でコンパクトに構成でき、かつ設
備コストを大幅に低減することができる。しか
も、集塵機の吸引圧力による計量値への悪影響が
無くなり、計量精度を大幅に改善することが可能
である。
[Effects of the invention] As explained above, the powder and granular material measuring device according to the invention does not require the conventionally required dust collection equipment, so it can be configured small and compact, and the equipment cost can be significantly reduced. can be reduced. Moreover, the negative influence of the suction pressure of the dust collector on the measured value is eliminated, and it is possible to significantly improve the measuring accuracy.

特に、本考案は粉塵が外部に噴出しない構造で
あるから、粉塵による公害問題や爆発の危険性等
を解消することがてき、更に微粉末は上部の分配
シユートに戻るため、従来のように微粉末が紛失
することも無く、この理由から全体的な粉粒体の
計量精度も向上する。
In particular, the present invention has a structure that prevents dust from spewing out to the outside, which eliminates the problem of pollution caused by dust and the risk of explosion.Furthermore, since the fine powder returns to the upper distribution chute, it is possible to eliminate the problem of dust pollution and the risk of explosion. No powder is lost, and for this reason the overall powder metering accuracy is also improved.

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

第1図は本考案に係る粉粒体の計量装置の一実
施例を示す断面図であり第2図は従来装置の断面
図である。 符号11は投入用コンベア、12は分配シユー
ト、13は攪拌回転羽根、14は供給ホツパ、1
5は計量ホツパ、16は大出しゲート、17は小
出しゲート、18は排出ゲート、19は排出シユ
ート、20は集合排出シユート、21,25は防
塵カバー、22,26は可撓性筒、23,27は
通気管、24は上部気密ダンパ、28は下部気密
ダンパである。
FIG. 1 is a cross-sectional view showing an embodiment of a measuring device for powder or granular material according to the present invention, and FIG. 2 is a cross-sectional view of a conventional device. Reference numeral 11 is a charging conveyor, 12 is a distribution chute, 13 is a stirring rotary blade, 14 is a supply hopper, 1
5 is a weighing hopper, 16 is a large output gate, 17 is a small output gate, 18 is a discharge gate, 19 is a discharge chute, 20 is a collective discharge chute, 21 and 25 are dust-proof covers, 22 and 26 are flexible tubes, 23, 27 is a ventilation pipe, 24 is an upper airtight damper, and 28 is a lower airtight damper.

Claims (1)

【実用新案登録請求の範囲】 1 計量すべき粉粒体を連続的に投入する分配シ
ユートと、その下方に設置した計量ホツパと、
更にその下方に排出シユートとを備えた計量装
置において、前記分配シユートと前記計量ホツ
パ間及び前記計量ホツパと前記排出シユート間
とをそれぞれ第1及び第2の防塵カバーにより
連結し、前記計量ホツパ内と前記分配シユート
の上部とを通気管により連通し、該通気管を気
密に遮断するための第1のダンパを設け、前記
排出シユートの下部に前記排出シユートとその
下方の間を気密に遮断するための第2のダンパ
を設け、前記分配シユートから前記計量ホツパ
への粉粒体の大投入時においては前記第1のダ
ンパを開放し前記第2のダンパを閉止し、小投
入時においては前記第1、第2のダンパを共に
閉止し、前記計量シユートから前記排出シユー
トへの粉粒体の排出時においては前記第1、第
2のダンパは共に開放するようにしたことを特
徴とする粉粒体の計量装置。 2 前記計量ホツパ及び排出シユートはそれぞれ
複数固設けるようにした実用新案登録請求の範
囲第1項に記載の粉粒体の計量装置。
[Scope of Claim for Utility Model Registration] 1. A distribution chute into which powder and granular materials to be measured are continuously fed, a measuring hopper installed below the chute,
In the weighing device further provided with a discharge chute below the distribution chute, the distribution chute and the weighing hopper and the weighing hopper and the discharge chute are connected by first and second dustproof covers, respectively, and the inside of the weighing hopper is connected. and an upper part of the distribution chute through a ventilation pipe, a first damper is provided to airtightly block the ventilation pipe, and a first damper is provided at a lower part of the discharge chute to airtightly isolate the space between the discharge chute and the lower part thereof. A second damper is provided for the purpose of opening the first damper and closing the second damper when a large amount of powder or granular material is being charged from the distribution chute to the measuring hopper, and opening the first damper and closing the second damper when a small amount is being charged. The first and second dampers are both closed, and both of the first and second dampers are opened when the powder or granular material is discharged from the measuring chute to the discharge chute. Granule weighing device. 2. The powder and granular material weighing device according to claim 1, wherein a plurality of the weighing hoppers and discharge chute are each fixedly provided.
JP1984199077U 1984-12-26 1984-12-26 Expired JPH0413634Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1984199077U JPH0413634Y2 (en) 1984-12-26 1984-12-26

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1984199077U JPH0413634Y2 (en) 1984-12-26 1984-12-26

Publications (2)

Publication Number Publication Date
JPS61112235U JPS61112235U (en) 1986-07-16
JPH0413634Y2 true JPH0413634Y2 (en) 1992-03-30

Family

ID=30758669

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1984199077U Expired JPH0413634Y2 (en) 1984-12-26 1984-12-26

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JP (1) JPH0413634Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4699718B2 (en) * 2004-07-29 2011-06-15 大和製衡株式会社 Combination scale

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6014185Y2 (en) * 1979-04-11 1985-05-07 株式会社クボタ Dust collector for powder weighing machine
JPS5619410U (en) * 1979-07-25 1981-02-20
JPS6145456Y2 (en) * 1980-05-26 1986-12-20

Also Published As

Publication number Publication date
JPS61112235U (en) 1986-07-16

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