JPS6161329B2 - - Google Patents
Info
- Publication number
- JPS6161329B2 JPS6161329B2 JP54096345A JP9634579A JPS6161329B2 JP S6161329 B2 JPS6161329 B2 JP S6161329B2 JP 54096345 A JP54096345 A JP 54096345A JP 9634579 A JP9634579 A JP 9634579A JP S6161329 B2 JPS6161329 B2 JP S6161329B2
- Authority
- JP
- Japan
- Prior art keywords
- weighing hopper
- powder
- weighing
- damper
- supply
- 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
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Landscapes
- Weight Measurement For Supplying Or Discharging Of Specified Amounts Of Material (AREA)
Description
【発明の詳細な説明】 本発明は粉粒体計量方法に関する。[Detailed description of the invention] The present invention relates to a method for weighing powder and granular materials.
従来の集塵装置付き粉粒体計量機について第1
図に基づき説明する。1は計量ホツパー、2は引
張型のロードセルであつて、上面のロツド2aは
固定体3に連結され、下面のロツド2bは上記計
量ホツパー1の外周面に突設したブラケツト4に
連結されており、これによつて上記計量ホツパー
1は吊り下げられている。5は計量ホツパー1の
上方において固定体(図示せず)に支持された粉
粒体6の貯蔵槽、7は計量ホツパー1の下方に配
設された排出シユートであつて、この排出シユー
ト7の上端と計量ホツパー1の下端とは、柔軟で
気密性を有する蛇腹状の伸縮カバー8により互い
に連結されている。9は排出シユート7の下端開
口部に接続されたベルトコンベア、スクリユーフ
イーダなど(図示せず)を内蔵した排出部、10
は前記貯蔵槽5の下端開口部に配設された一対の
供給ゲートであつて、シリンダ装置(図示せず)
により開閉させられるものである。11は計量ホ
ツパー1の一対の下端開口部にそれぞれ配設され
た排出ゲートであつて、シリンダ装置(図示せ
ず)により開閉させられるものである。12は前
記貯蔵槽5の下端部に外嵌固着された筒体、13
は該筒体12に固着された計量ホツパー1の上端
開口部を覆う蓋、14は該蓋13の外周縁と計量
ホツパー1の上端開口縁との間に配設された柔軟
で気密性を有する蛇腹状の伸縮カバー、15は上
記蓋13に形成された吸排気口、16は該吸排気
口15に対向して配設された集塵装置(図示せ
ず)の集塵管であつて、該集塵管16の開口端と
吸排気口15との間には若干の間隙aを形成して
ある。 About the conventional powder weighing machine with dust collector
This will be explained based on the diagram. 1 is a weighing hopper; 2 is a tension type load cell; a rod 2a on the upper surface is connected to a fixed body 3; and a rod 2b on the lower surface is connected to a bracket 4 protruding from the outer peripheral surface of the weighing hopper 1. , whereby the weighing hopper 1 is suspended. 5 is a storage tank for powder and granular material 6 supported by a fixed body (not shown) above the weighing hopper 1; 7 is a discharge chute disposed below the weighing hopper 1; The upper end and the lower end of the weighing hopper 1 are connected to each other by a bellows-shaped telescopic cover 8 that is flexible and airtight. Reference numeral 9 denotes a discharge section connected to the lower end opening of the discharge chute 7, and includes a built-in belt conveyor, screw feeder, etc. (not shown);
are a pair of supply gates disposed at the lower end opening of the storage tank 5, and are equipped with a cylinder device (not shown).
It can be opened and closed by Reference numeral 11 denotes discharge gates respectively disposed at a pair of lower end openings of the weighing hopper 1, which are opened and closed by a cylinder device (not shown). 12 is a cylindrical body externally fitted and fixed to the lower end of the storage tank 5; 13;
14 is a flexible and airtight lid that covers the upper opening of the weighing hopper 1 fixed to the cylindrical body 12; A bellows-shaped telescopic cover, 15 a suction/exhaust port formed in the lid 13, 16 a dust collection pipe of a dust collector (not shown) disposed opposite the suction/exhaust port 15, A slight gap a is formed between the open end of the dust collecting pipe 16 and the intake/exhaust port 15.
上記構成において、供給ゲート10を開けて計
量ホツパー1内に粉粒体6を供給し、それをロー
ドセル2により計量し、定量に達すると、供給ゲ
ート10を閉じ、排出ゲート11を開けて定量粉
粒体を排出シユート7内に排出し、排出部9によ
つてさらに排出するわけである。ところで上記計
量ホツパー1内に粉粒体6を供給したときに粉塵
が発生するが、この粉塵は、吸排気口15を介し
て集塵管16内に吸引されるように構成されてい
る。しかし粉粒体6の大供給時において、その粉
塵が集塵管16と吸排気口15との間の間隙aか
ら外部に漏れて周囲を汚すことが多いものであ
る。そこで上記間隙aを小さくするとが考えられ
るが、そうすると小供給、定量時に計量ホツパー
1内が負圧となり、該計量ホツパー1の重量が軽
くなつて、計量誤差が生じる。また排出ゲート1
1を開けて排出シユート7内に粉粒体6を排出す
る場合において、排出シユート7内の余剰空気は
計量ホツパー1の下端開口、すなわち粉粒体6内
を通つて計量ホツパー1内に流入するため、粉塵
の発生を助長し、粉粒体6の排出落下の障害とな
つている。 In the above configuration, the supply gate 10 is opened to supply the powder or granular material 6 into the weighing hopper 1, and it is weighed by the load cell 2. When a fixed amount is reached, the supply gate 10 is closed and the discharge gate 11 is opened to supply the fixed amount of powder. The granules are discharged into the discharge chute 7 and further discharged by the discharge section 9. Incidentally, when the powder and granular material 6 is supplied into the weighing hopper 1, dust is generated, and the structure is such that this dust is sucked into the dust collecting pipe 16 through the suction and exhaust port 15. However, when a large amount of powder 6 is supplied, the dust often leaks to the outside from the gap a between the dust collecting pipe 16 and the intake/exhaust port 15 and contaminates the surrounding area. Therefore, it is conceivable to make the gap a smaller, but if this is done, the inside of the weighing hopper 1 will become negative pressure during small supply and metering, the weight of the weighing hopper 1 will become lighter, and a weighing error will occur. Also, discharge gate 1
1 is opened to discharge the powder and granular material 6 into the discharge chute 7, excess air in the discharge chute 7 flows into the weighing hopper 1 through the lower end opening of the weighing hopper 1, that is, through the inside of the powder and granular material 6. This promotes the generation of dust, which becomes an obstacle to the discharge and fall of the powder and granular material 6.
本発明はかかる問題点を解消した粉粒体計量方
法を提供するものである。 The present invention provides a method for measuring powder and granular materials that solves these problems.
以下、本発明の一実施例を第2図以下の図面に
基づいて説明する。この実施例において第1図に
示す装置の物品と同一のものについては同一符号
を付して説明を省略する。20は計量ホツパー1
の両外側面に沿つて配設された通気管であつて、
計量ホツパー1内と排出シユート7内とを互いに
連通させるものである。21は排気口15に接続
された吸排気管であつて、この吸排気管21に
は、集塵装置(図示せず)の集塵管22が接続さ
せられる集塵口23と、大気に連通する大気口2
4とを設けてある。25は吸排気管21内の集塵
口23と大気口24との分岐部において支軸26
を支点として回動自在に配設されたダンパーであ
つて、大気口24を開閉するものである。なおこ
のダンパー25はシリンダ装置などにより回動さ
せられる。27はフイルタである。 Hereinafter, one embodiment of the present invention will be described based on the drawings from FIG. 2 onwards. In this embodiment, the same parts as those in the apparatus shown in FIG. 1 are designated by the same reference numerals, and the description thereof will be omitted. 20 is measuring hopper 1
A ventilation pipe arranged along both outer surfaces of the
This allows the inside of the weighing hopper 1 and the inside of the discharge chute 7 to communicate with each other. Reference numeral 21 denotes an intake/exhaust pipe connected to the exhaust port 15, and the intake/exhaust pipe 21 includes a dust collection port 23 to which a dust collection pipe 22 of a dust collector (not shown) is connected, and an air intake/exhaust pipe 23 that communicates with the atmosphere. Mouth 2
4 is provided. 25 is a support shaft 26 at the branch point between the dust collection port 23 and the atmospheric port 24 in the intake/exhaust pipe 21.
This damper is rotatably disposed about the fulcrum and opens and closes the air vent 24. Note that this damper 25 is rotated by a cylinder device or the like. 27 is a filter.
上記構成の作用を説明する。まず第2図に示す
通常停止時(計量開始前)において、両ゲート1
0,11を閉じ、粉塵の発生はないのでダンパー
25を半開きとする。これにより大気口24から
外気が吸い込まれて通気管20の風速が小さくな
り、計量ホツパー1内は正常圧状態となつてい
る。したがつて正しい計量がおこなえる状態であ
つて、この状態においてロードセル2の零調また
はオートゼロをかける。 The operation of the above configuration will be explained. First, at the normal stop (before the start of measurement) as shown in Figure 2, both gates 1
0 and 11 are closed, and the damper 25 is left half open since no dust is generated. As a result, outside air is sucked in through the air vent 24, the wind speed in the ventilation pipe 20 is reduced, and the inside of the weighing hopper 1 is brought into a normal pressure state. Therefore, it is a state in which correct measurement can be performed, and in this state, zero adjustment or auto-zero is applied to the load cell 2.
次に第3図に示すごとく供給ゲート10を全開
して計量ホツパー1内に粉粒体6を大供給する。
またこれと同時にダンパー25を全閉または少し
だけ開けた状態にする。すると粉粒体6の計量ホ
ツパー1内への大流入により、このホツパー1内
に生じた余剰空気は粉塵と共に排気口15および
集塵口23を介して集塵管22内に吸引される。 Next, as shown in FIG. 3, the supply gate 10 is fully opened to supply a large amount of powder 6 into the weighing hopper 1.
At the same time, the damper 25 is fully closed or slightly opened. Then, due to the large flow of the powder 6 into the weighing hopper 1, the excess air generated in the hopper 1 is sucked into the dust collecting pipe 22 together with the dust through the exhaust port 15 and the dust collecting port 23.
次に第4図に示すごとく供給ゲート10を半開
きにして計量ホツパー1内に粉粒体6を小供給す
る。またこれと同時にダンパー25を半開きとす
る。この小供給の際は、計量ホツパー1内の余剰
空気、粉塵は少量となるが、集塵管22の吸引力
は変らない。したがつてダンパー25が大供給時
のままであると、吸引力が強すぎることになり、
計量ホツパー1内が負圧となつて計量誤差が生じ
るが、上記したごとくダンパー25を半開きにし
てあるので計量ホツパー1内が負圧にならず、計
量開始前と同じ条件になるので、計量誤差が生じ
ない。 Next, as shown in FIG. 4, the supply gate 10 is opened halfway and a small amount of the powder 6 is supplied into the weighing hopper 1. At the same time, the damper 25 is also half-opened. During this small supply, the amount of excess air and dust in the metering hopper 1 will be small, but the suction force of the dust collecting pipe 22 will not change. Therefore, if the damper 25 remains in the large supply mode, the suction force will be too strong.
The inside of the weighing hopper 1 becomes negative pressure, which causes a measurement error. However, as mentioned above, since the damper 25 is left half-open, the inside of the weighing hopper 1 does not become negative pressure, and the conditions are the same as before the start of measurement, so there is no measurement error. does not occur.
次に第5図に示すごとくロードセル2による計
量によつて計量ホツパー1内の粉粒体6が定量に
達すると、供給ゲート10を全閉する。またゲー
ト25はそのまま(半開き)にしておく。この場
合、たとえ集塵管22の吸引力に変化があつて
も、ダンパー25が半開きで、大気口24から外
気を吸い込んでいるため、計量ホツパー1に与え
る影響は少なく、また通気管20の容量が充分で
あれば、該通気管20内の風速も小さくなり、計
量ホツパー1の内外の圧力差はなく、実質的に計
量誤差が生じない。 Next, as shown in FIG. 5, when the powder or granular material 6 in the weighing hopper 1 reaches a fixed amount by weighing by the load cell 2, the supply gate 10 is completely closed. Further, the gate 25 is left as it is (half-open). In this case, even if there is a change in the suction force of the dust collection pipe 22, the damper 25 is half-open and sucks in outside air from the atmosphere port 24, so the influence on the weighing hopper 1 is small, and the capacity of the ventilation pipe 20 is small. If this is sufficient, the wind speed inside the ventilation pipe 20 will be small, there will be no pressure difference between the inside and outside of the weighing hopper 1, and there will be virtually no measurement error.
次に第6図に示すごとく排出ゲート11を全開
にして計量ホツパー1内の粉粒体6を排出シユー
ト7内に排出する。またこれと同時にダンパー2
5を全閉または全閉に近い状態にする。この粉粒
体6の排出は短期間におこなわれるため、排出シ
ユート7内の余剰空気は粉塵とともに通気管20
を経て計量ホツパー1内に入り、この計量ホツパ
ー1内の負圧状態を解除する。また粉塵は集塵管
22に吸引される。この場合、排出シユート7内
の余剰空気は通気管20を通つて逃げ、計量ホツ
パー1の下端開口部、すなわち粉粒体6内を通つ
て逃げないため、粉粒体6の排出はスムーズにお
こなわれる。 Next, as shown in FIG. 6, the discharge gate 11 is fully opened to discharge the powder 6 in the weighing hopper 1 into the discharge chute 7. At the same time, damper 2
5 is fully closed or close to fully closed. Since this powder and granular material 6 is discharged in a short period of time, the excess air in the discharge chute 7 is discharged into the ventilation pipe 20 along with the dust.
It enters the weighing hopper 1 through the hopper 1, and releases the negative pressure inside the weighing hopper 1. Further, dust is sucked into the dust collecting pipe 22. In this case, excess air in the discharge chute 7 escapes through the ventilation pipe 20 and does not escape through the lower end opening of the weighing hopper 1, that is, inside the powder 6, so that the powder 6 can be discharged smoothly. It can be done.
次に第7図に示すごとく粉粒体6の排出を完了
すると排出ゲート11を閉じる。またこれと同時
にダンパー25を半開きにして第2図に示す状態
に戻す。したがつてこれにより1回分の計量が完
了することになる。 Next, as shown in FIG. 7, when the discharge of the granular material 6 is completed, the discharge gate 11 is closed. At the same time, the damper 25 is opened halfway and returned to the state shown in FIG. Therefore, this completes one measurement.
次に第2回目の計量をつづけておこなう場合に
は、第8図に示すごとく供給ゲート10を全開し
て粉粒体6を大供給し、それと同時にダンパー2
5を全閉または少しだけ開けた状態にする。この
場合、排出シユート7内の粉粒体6が排出される
ことから、このシユート7内が負圧になるが、計
量ホツパー1内の余剰空気が通気管20を通つて
流入し、負圧状態を解消する。 Next, when continuing the second measurement, the supply gate 10 is fully opened to supply a large quantity of powder and granular material 6 as shown in FIG. 8, and at the same time, the damper 2
5 is fully closed or slightly open. In this case, since the powder and granular material 6 in the discharge chute 7 is discharged, the inside of this chute 7 becomes a negative pressure, but excess air in the weighing hopper 1 flows in through the ventilation pipe 20, causing a negative pressure state. Eliminate.
以後、小供給→定量→排出の動作がくり返され
る。 Thereafter, the operation of small supply → fixed amount → discharge is repeated.
上記実施例では集塵口23と大気口24とを有
する吸排気管21を設けたが、蓋13に集塵口2
3と大気口24とをそれぞれ別個に形成し、集塵
口23には集塵装置の集塵管22を接続し、大気
口24にはダンパー25を配設するようにしても
よい。またロードセル2以外に、てこ系などの計
量装置を用いてもよいのはいうまでもない。 In the above embodiment, the intake/exhaust pipe 21 having the dust collection port 23 and the atmosphere port 24 is provided, but the dust collection port 22 is provided in the lid 13.
3 and the atmosphere port 24 may be formed separately, the dust collection port 23 may be connected to the dust collection pipe 22 of the dust collector, and the atmosphere port 24 may be provided with a damper 25. Moreover, it goes without saying that a measuring device such as a lever system may be used in addition to the load cell 2.
以上述べたごとく本発明の粉粒体計量方法によ
れば、計量ホツパー1内に粉粒体6を大供給した
際、および排出シユート7内に粉粒体6を排出し
た際に生じる粉塵は、ダンパー25を全閉または
全閉に近い状態にしてあることから、集塵管22
を介して回収され、従来のように粉塵が外部に漏
れて周囲を汚すおそれはない。供給ゲート10を
半開きにして計量する際には、ダンパー25を半
開きにしてあるとともに計量ホツパー1内と排出
シユート7内とを通気管20で互いに連通させて
あるから、粉粒体の小供給時および定量時におい
て大供給時と同じ吸引力で集塵管22から吸引し
ても計量ホツパー内が負圧状態になることはな
く、計量誤差が生じないものである。 As described above, according to the powder weighing method of the present invention, the dust generated when a large amount of powder 6 is fed into the weighing hopper 1 and when the powder 6 is discharged into the discharge chute 7 is Since the damper 25 is fully closed or close to fully closed, the dust collection pipe 22
There is no risk of dust leaking outside and contaminating the surrounding area, unlike in the past. When weighing with the supply gate 10 half-open, the damper 25 is left half-open, and the inside of the weighing hopper 1 and the inside of the discharge chute 7 are communicated with each other through the ventilation pipe 20, so that when a small amount of powder or granules is supplied. Even when suctioning from the dust collection pipe 22 with the same suction force as during large supply during metering, the inside of the metering hopper does not become a negative pressure state, and no metering error occurs.
第1図は従来例を示す縦断面図、第2図〜第8
図は本発明の一実施例を示す動作説明縦断面図で
ある。
1……計量ホツパー、2……ロードセル(計量
装置)、5……貯蔵槽、6……粉粒体、7……排
出シユート、10……供給ゲート、11……排出
ゲート、13……蓋(密閉体)、15……吸排気
口、20……通気管、21……排気管、22……
集塵管、23……集塵口、24……大気口、25
……ダンパー。
Figure 1 is a longitudinal sectional view showing a conventional example, Figures 2 to 8
The figure is a longitudinal sectional view illustrating the operation of an embodiment of the present invention. 1...Measuring hopper, 2...Load cell (measuring device), 5...Storage tank, 6...Powder/granular material, 7...Discharge chute, 10...Supply gate, 11...Discharge gate, 13...Lid (closed body), 15... intake/exhaust port, 20... ventilation pipe, 21... exhaust pipe, 22...
Dust collection pipe, 23...Dust collection port, 24...Atmospheric port, 25
...damper.
Claims (1)
計量装置2と、上記計量ホツパー1の上方に設け
られた粉粒体貯蔵槽5と、上記計量ホツパー1の
下方に配設された排出シユート7とを有する粉粒
体計量機において、上記計量ホツパー1と貯蔵槽
5との間を密閉する該密閉体13に、計量ホツパ
ー1内に連通する集塵口23と大気口24とを形
成し、集塵口23に集塵装置の集塵管22を接続
し、大気口24にダンパー25を配設するととも
に上記計量ホツパー1内と上記排出シユート7内
とを互いに通気管20を介して連通し、集塵装置
を作動させた状態において粉粒体貯蔵槽5の供給
ゲート10を全開して計量ホツパー1内に粉粒体
6を大供給し、またこれと同時にダンパー25を
全閉または少しだけ開け、次に供給ゲート10を
半開きにして計量ホツパー1内に粉粒体6を小供
給し、またこれと同時にダンパー25を半開きに
し、次に計量ホツパー1内の粉粒体が定量にたつ
したならば供給ゲート10を全閉し、次に計量ホ
ツパー1の排出ゲート11を全開し、またこれと
同時にダンパー25を全閉または全閉に近い状態
にし、次に計量ホツパー1内の粉粒体6の排出が
完了した後、排出ゲート11を全閉することを特
徴とする粉粒体計量方法。1 A weighing hopper 1, a weighing device 2 that supports the hopper 1, a powder storage tank 5 provided above the weighing hopper 1, and a discharge chute 7 provided below the weighing hopper 1. In the powder and granular material weighing machine, a dust collection port 23 and an atmospheric air port 24 communicating with the inside of the weighing hopper 1 are formed in the sealing body 13 that seals between the weighing hopper 1 and the storage tank 5. A dust collection pipe 22 of a dust collection device is connected to the dust port 23, a damper 25 is provided to the atmosphere port 24, and the inside of the weighing hopper 1 and the inside of the discharge chute 7 are communicated with each other via the ventilation pipe 20, With the dust collector in operation, the supply gate 10 of the powder storage tank 5 is fully opened to supply a large amount of powder and granules 6 into the weighing hopper 1, and at the same time, the damper 25 is fully closed or slightly opened. Next, the supply gate 10 is opened half-open to supply a small amount of powder 6 into the weighing hopper 1, and at the same time, the damper 25 is half-opened, and then, when the powder and granular material in the weighing hopper 1 reaches a fixed amount, For example, the supply gate 10 is fully closed, then the discharge gate 11 of the weighing hopper 1 is fully opened, and at the same time, the damper 25 is fully closed or close to fully closed, and then the powder and granular material 6 in the weighing hopper 1 is completely closed. A method for weighing powder or granular material, characterized in that the discharge gate 11 is fully closed after the discharge of the powder is completed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9634579A JPS5619410A (en) | 1979-07-27 | 1979-07-27 | Pulverulent body meter with dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9634579A JPS5619410A (en) | 1979-07-27 | 1979-07-27 | Pulverulent body meter with dust collector |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5619410A JPS5619410A (en) | 1981-02-24 |
| JPS6161329B2 true JPS6161329B2 (en) | 1986-12-25 |
Family
ID=14162411
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9634579A Granted JPS5619410A (en) | 1979-07-27 | 1979-07-27 | Pulverulent body meter with dust collector |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5619410A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2019207139A (en) * | 2018-05-29 | 2019-12-05 | テクニカル北原株式会社 | Dust prevention system of weighing apparatus |
| JP2020139827A (en) * | 2019-02-28 | 2020-09-03 | 赤武エンジニアリング株式会社 | Powder weighing device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4820779B2 (en) * | 2007-06-15 | 2011-11-24 | 富士夫 堀 | Granule measurement system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6035652B2 (en) * | 1978-02-03 | 1985-08-15 | 株式会社日立製作所 | lcd display cell |
-
1979
- 1979-07-27 JP JP9634579A patent/JPS5619410A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2019207139A (en) * | 2018-05-29 | 2019-12-05 | テクニカル北原株式会社 | Dust prevention system of weighing apparatus |
| JP2020139827A (en) * | 2019-02-28 | 2020-09-03 | 赤武エンジニアリング株式会社 | Powder weighing device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5619410A (en) | 1981-02-24 |
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