JPS6245488B2 - - Google Patents
Info
- Publication number
- JPS6245488B2 JPS6245488B2 JP907979A JP907979A JPS6245488B2 JP S6245488 B2 JPS6245488 B2 JP S6245488B2 JP 907979 A JP907979 A JP 907979A JP 907979 A JP907979 A JP 907979A JP S6245488 B2 JPS6245488 B2 JP S6245488B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- storage tank
- granular material
- discharge
- screw feeder
- 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
Links
- 239000000843 powder Substances 0.000 claims description 47
- 239000008187 granular material Substances 0.000 claims description 39
- 238000003756 stirring Methods 0.000 claims description 9
- 238000013019 agitation Methods 0.000 claims 1
- 239000011295 pitch Substances 0.000 description 8
- 241000209140 Triticum Species 0.000 description 3
- 235000021307 Triticum Nutrition 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 235000013339 cereals Nutrition 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000004323 axial length Effects 0.000 description 1
- 235000012813 breadcrumbs Nutrition 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Weight Measurement For Supplying Or Discharging Of Specified Amounts Of Material (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
Description
【発明の詳細な説明】
本発明は粉粒体の定量排出装置いわゆる分量装
置に関し、特に貯槽などから所定の少量を分別し
て排出する分量装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for quantitatively discharging powder or granular material, a so-called metering device, and particularly to a metering device that separates and discharges a predetermined small amount from a storage tank or the like.
小麦粉等の粉粒体を貯槽から比較的多量に分量
する装置は種々知られているが、少量を正確に分
別する分量装置は殆んど提案されておらず長い間
望まれていた。従来少量の分量は作業者の手作業
に頼つているのが現状であり、分量作業に要する
手間と時間は決して少なくなく、正確な分量を望
めば望むほど分量作業は非能率的なものとなる。
そうかといつて多量分別に使用されている分量装
置を少量分別に使用しようとすると、排出の均一
性と分量精度の点で問題があつた。すなわち、通
常の分量装置においては予じめ粉粒体を貯槽に貯
えておき、分量時貯槽下部に配設されたフイーダ
により粉粒体を供給し排出口から所望量だけ分別
して排出するのであるが、貯槽下部からフイーダ
に送られる粉粒体の密度は貯槽内に貯えられてい
る粉体圧の影響を受けて均一でなく、この不均一
状態のままフイーダで供給されるために排出口か
らの排出も不均一となるという欠点があつた。貯
槽内における粉体圧の影響をできるだけなくして
貯槽下部における粉粒体の排出を容易にする目的
で、貯槽内壁に貯槽下方に向つて傾斜して伸びる
ノーズと呼ばれる突出部を設けることは知られて
いるが、このノーズのみでは前述した排出時にお
ける粉粒体密度の不均一の問題は完全に解決され
ていない。 Although various devices are known for dispensing relatively large amounts of powder or granular materials such as wheat flour from storage tanks, very few dispensing devices that accurately separate small amounts have been proposed and have been desired for a long time. Conventionally, the current situation is that small quantities have relied on the manual labor of workers, and the amount of effort and time required to measure portions is by no means small, and the more accurate portions are desired, the more inefficient the portion portion work becomes. .
However, when attempting to use a dispensing device used for dispensing large quantities to disassemble small quantities, problems arose in terms of uniformity of discharge and dispensing accuracy. In other words, in a normal dispensing device, powder and granules are stored in a storage tank in advance, and during dispensing, the powder is fed by a feeder installed at the bottom of the storage tank, and the desired amount is separated and discharged from the discharge port. However, the density of the powder sent from the bottom of the storage tank to the feeder is not uniform due to the influence of the powder pressure stored in the storage tank. There was also a drawback that the discharge was uneven. It is known that a protrusion called a nose is provided on the inner wall of the storage tank to extend downwardly from the storage tank in order to eliminate the influence of the powder pressure inside the storage tank as much as possible and to facilitate the discharge of powder and granular material from the lower part of the storage tank. However, this nose alone does not completely solve the above-mentioned problem of uneven density of powder and granules during discharge.
排出のためにフイーダにより供給される粉粒体
の密度がこのように不均一であると、排出口から
分量される粉粒体の量が定量的でなく、あるとき
は短時間に多量に排出されあるときは少量排出さ
れるかまたは殆んど排出されないという状態が生
ずる。このように排出が定量的連続的に行なわれ
ないと本発明の対象とする少量分別分量装置にお
いては、分量精度が低くなる。何故なら、所定の
分量を排出すべく設定したにもかかわらず、排出
工程の最後の瞬間に排出される量が定まらず、最
後の排出量が分量精度に影響を与えるからであ
る。分量精度を高めるために、大小二連スクリユ
ーフイーダを採用したり、一本のスクリユーフイ
ーダの回転数制御によつていわゆる大出し、小出
しの二段供給方式を採用するなどの工夫は種々さ
れていたが、そのための切換え制御が複雑となり
多くの床面積を要するなどの欠点があつた。 If the density of the powder and granular material supplied by the feeder for discharge is uneven in this way, the amount of powder and granular material dispensed from the discharge port is not quantitative, and sometimes a large amount is discharged in a short period of time. In some cases, a small amount or almost no discharge occurs. If the discharge is not carried out quantitatively and continuously in this way, the accuracy in dispensing will be low in the small-volume dispensing and dispensing device that is the object of the present invention. This is because even though a predetermined amount is set to be discharged, the amount to be discharged at the final moment of the discharge process is not determined, and the final discharge amount affects the accuracy of the quantity. In order to improve the accuracy of the quantity, we have taken measures such as adopting a two-stage large and small screw feeder, and controlling the rotation speed of a single screw feeder to adopt a two-stage feeding system for large and small amounts. Various methods have been used, but the switching control required is complicated and requires a large amount of floor space.
少量分別分量装置における定量性に影響を与え
るもう1つの要素に排出口の形状がある。従来の
分量装置の排出口は排出管に形成された円形また
は矩形の開口であり、通常この開口周辺に排出案
内管が取付けられている。フイーダは通常らせん
状羽根を有し粉粒体をその羽根により押しながら
排出管内を搬送するが、搬送される粉粒体が排出
口に至ると羽根の1ピツチ間の粉粒体の殆んどが
それに続く次の1ピツチ間の粉粒体が排出口に到
達する前に一度に落下して排出されてしまうため
に、排出が不連続となり定量性を失ない、従つて
前述したと同様の理由で分量精度が低下すること
になる。 Another factor that affects quantitative performance in small-volume fractionation and dispensing devices is the shape of the outlet. The outlet of conventional dispensing devices is a circular or rectangular opening formed in a discharge tube, around which a discharge guide tube is usually attached. The feeder usually has spiral blades and conveys the powder and granules through the discharge pipe while pushing them with the blades, but when the conveyed powder and granules reach the discharge port, most of the powder and granules between one pitch of the blades are removed. However, the next pitch of powder and granules falls and is discharged all at once before reaching the discharge port, so the discharge becomes discontinuous and does not lose quantitative properties. For this reason, the measurement accuracy will be reduced.
本発明は従来の多量分量装置を少量分量装置に
適用したときに生ずる上記問題点を解決するもの
であり、貯槽内の粉粒体をその下部においてフイ
ーダに送入する際、粉粒体を貯槽外部から取り入
れた空気と共に攪拌混合することによりフイーダ
により供給される粉粒体に均一性と流動性を与え
て排出口から排出される粉粒体に定量性を付与
し、分量精度を高めようとするものである。さら
にこれとは別に、排出口を幅狭のスロツト形状と
し且つそのスロツトの長手方向をフイーダの羽根
と少なくとも交差するように定めることにより粉
粒体の定量排出をより高めようとするものであ
る。このフイーダの羽根とスロツト長手方向との
交差角は90゜以下の範囲で適宜選択されるが、交
差角が大きいほど定量性は向上する。 The present invention solves the above-mentioned problems that occur when a conventional large-volume dispensing device is applied to a small-volume dispensing device. By stirring and mixing with the air taken in from the outside, the powder and granules supplied by the feeder are given uniformity and fluidity, and the powder and granules discharged from the discharge port are given quantitative properties in order to improve the accuracy of dosing. It is something to do. Furthermore, separate from this, the discharge port is formed into a narrow slot shape, and the longitudinal direction of the slot is set so as to at least intersect with the blades of the feeder, thereby further increasing the quantitative discharge of the powder and granular material. The intersection angle between the feeder blade and the longitudinal direction of the slot is appropriately selected within a range of 90° or less, but the larger the intersection angle, the better the quantitative performance.
本発明によれば、貯槽からフイーダに送入され
る粉粒体の密度を均一にして粉粒体の排出に定量
性を与えることができ、さらに排出口をフイーダ
の羽根に対して交差して伸びるスロツト状とする
ことにより前述定量性と相俟つて定量効果を高め
ることができ、特に少量分量装置における分量精
度を高めることができるものである。 According to the present invention, it is possible to make the density of the powder and granular material sent from the storage tank to the feeder uniform, and to give quantitative properties to the discharge of the powder and granular material. By forming the elongated slot shape, it is possible to enhance the quantitative effect in conjunction with the above-mentioned quantitative property, and in particular, it is possible to improve the dosing accuracy in a small-dose dispensing device.
以下添付図面を参照して本発明をその一実施例
につき詳細に説明する。 Hereinafter, one embodiment of the present invention will be described in detail with reference to the accompanying drawings.
第1図は本発明に係る粉粒体分量装置の概略図
であり、分量装置1は装置本体2とその上部に配
置された定量供給装置3とから構成されている。
定量供給装置3の内部には第2図および第3図に
示すような貯槽31があり、その下部開口近くに
撹拌装置32とその直下にスクリユーフイーダ3
3とが配設されている。定量供給装置3の前面に
は分別すべき粉粒体の量を設定したり分量操作を
制御するための制御盤34が設けられている。装
置本体2の内部には前記定量供給装置3のスクリ
ユーフイーダ33を駆動するための駆動装置21
が設けられており、また前面にはロードセルを利
用した重量検出装置22が設けられている。重量
検出装置22上には粉粒体の所定分量を収納する
ための計量容器23が載置される。 FIG. 1 is a schematic diagram of a powder/granular material dispensing device according to the present invention, and the dispensing device 1 is composed of a device main body 2 and a metering supply device 3 disposed on the top thereof.
Inside the quantitative supply device 3, there is a storage tank 31 as shown in FIGS. 2 and 3, with a stirring device 32 near its lower opening and a screw feeder 3 directly below it.
3 are arranged. A control panel 34 is provided on the front side of the metering supply device 3 for setting the amount of powder or granular material to be separated and controlling the amount operation. Inside the device main body 2 is a drive device 21 for driving the screw feeder 33 of the quantitative feeding device 3.
A weight detection device 22 using a load cell is provided on the front surface. A weighing container 23 for storing a predetermined amount of powder or granular material is placed on the weight detection device 22 .
貯槽31には、1図に示すように、空気輸送管
またはベルトコンベア等の輸送系4を通じてその
上部装入口31aから粉粒体が投入充填される。 As shown in FIG. 1, the storage tank 31 is charged with powder and granular material from its upper charging port 31a through a transport system 4 such as a pneumatic transport pipe or a belt conveyor.
貯槽31の後部内壁31bにはその上部から下
部に向けて貯槽内部の中心寄りに傾斜するノーズ
31cが設けられており、ノーズ31cと後部内
壁31bとの間に空間Pが形成されている。ノー
ズ31cは後部内壁31bに対してたとえば約65
度傾斜して貯槽31の内部中心近くまで延在して
おり、その下側は彎曲をなして内壁31bの方向
に折り曲げられている。一方、後部内壁31bの
中央部よりやや上方には空気取入れ口31dが2
個形成されており、取入口に張設されたパンチン
グメタルまたは布を通して作動時外部空気が空
間P内に取込まれる。 The rear inner wall 31b of the storage tank 31 is provided with a nose 31c that slopes from the upper part to the lower part toward the center of the storage tank, and a space P is formed between the nose 31c and the rear inner wall 31b. For example, the nose 31c is approximately 65 mm relative to the rear inner wall 31b.
It extends to near the interior center of the storage tank 31 with a degree of inclination, and its lower side is curved and bent toward the inner wall 31b. On the other hand, there are two air intake ports 31d slightly above the center of the rear inner wall 31b.
During operation, external air is taken into the space P through a punched metal or cloth stretched over the intake port.
撹拌装置32は回転軸32aに図示した如き形
状の多数の羽根32bが固定されたもので、前記
駆動装置21により回転される。スクリユーフイ
ーダ33は軸33aの周囲にらせん状の羽根33
bを有するもので、羽根33bのピツチは粉粒体
の搬送方向に異なる3種類の間隔R,S,Tを有
する。ピツチをこのように軸方向に沿つて変化さ
せたのは、貯槽内の粉粒体が排出される際その表
面レベルの形状をくずすことがないようにいわゆ
るマスフローの状態にするためである。スクリユ
ーフイーダ33はその一方の側が貯槽31を越え
て水平に伸びており、その延長部分は装置本体2
の前面に取付けられた排出管24で包まれている
(第2図参照)。第4図は断面が円形の排出管24
の斜視図であり、排出管24の先端近くにはスロ
ツト状の粉粒体排出口24aが形成されている。
このスロツト状排出口24aはスクリユーフイー
ダ33の回転数と排出管24の直径とにより決定
される排出量により決められる幅と長さとを有し
ており、排出管24の中心を通る水平面以下に位
置するように設けられている。排出口24aの長
手方向は後述する理由により排出管24の内部に
納められたスクリユーフイーダ33の羽根33b
と交差するように定められている。 The stirring device 32 has a large number of blades 32b fixed to a rotating shaft 32a, and is rotated by the drive device 21. The screw feeder 33 has spiral blades 33 around a shaft 33a.
b, and the pitches of the blades 33b have three different pitches R, S, and T in the conveying direction of the powder and granular material. The reason why the pitch is changed along the axial direction in this way is to create a so-called mass flow state so that the shape of the powder and granules in the storage tank does not change at the surface level when being discharged. One side of the screw feeder 33 extends horizontally beyond the storage tank 31, and the extended portion extends beyond the storage tank 31.
It is surrounded by a discharge pipe 24 attached to the front surface of the tube (see Figure 2). Figure 4 shows a discharge pipe 24 with a circular cross section.
2, a slot-shaped powder discharge port 24a is formed near the tip of the discharge pipe 24.
This slot-shaped discharge port 24a has a width and length determined by the discharge amount determined by the rotation speed of the screw feeder 33 and the diameter of the discharge pipe 24, and is below the horizontal plane passing through the center of the discharge pipe 24. It is set up to be located at. The longitudinal direction of the discharge port 24a is parallel to the blade 33b of the screw feeder 33 housed inside the discharge pipe 24 for reasons to be described later.
It is set to intersect with
次に本発明に係る分量装置の動作を説明する。
貯槽31内に貯えられた粉粒体から所定の少量を
分別するに当り、先ず制御盤34を操作して所定
分量を設定する。次に分量開始ボタンを押すと、
分量装置本体2内の駆動装置21が付勢されて撹
拌装置32とスクリユーフイーダ33とが回転を
始め、撹拌装置32により粉粒体がスクリユーフ
イーダ33に供給される。このとき、撹拌に伴な
い貯槽31の空気取入口31dから貯槽内に取込
まれた空気は矢印で示すように空間Pを経て撹拌
されている粉粒体に巻込まれ粉粒体層を流動化す
るとともに均質化するのでスクリユーフイーダ3
3に送入される粉粒体層は貯槽内部に残留する粉
粒体量に影響されることなく均一化される。撹拌
される粉粒体に巻込まれる空気は空気取入口31
dに張設されたパンチングメダルまたは布で清
浄にされている。こうしてスクリユーフイーダ3
3に送入された粉粒体はらせん状羽根33bの間
に充填された軸33aの回転とともに貯槽31か
ら排出管24に向けて搬送され排出管24端部の
排出口24aに到達する。排出口24aにおける
粉粒体の落口面積の変化はスクリユーフイーダ3
3が段階的に進行するにつれて、小さな変化率で
ほぼ直線的に増加していく。その結果排出口24
aから排出される粉粒体量の変化は比較的小さく
なる。これに対して従来の排出口の形状は円形ま
たは矩形であるために、落口面積の増加率は非直
線的で且つ初期の段階で急激に変化するために、
排出口から排出される粉粒体量の変化は極めて大
きくなりしかも不連続である。このことから、従
来の分量装置において定量排出が困難であつたこ
とが容易に理解できるであろう。このように、排
出口の形状を幅狭のスロツトとしさらにその長手
方向をスクリユーフイーダの羽根と交差する方向
に形成することにより、落口面積の増加率をほぼ
直線的でしかもゆるやかにすることができその結
果排出口から排出される粉粒体量の変化を小さく
且つ連続的にすることができる。定量性をさらに
高めるためには、スロツトの排出管方向の長さを
スクリユーフイーダの1ピツチよりやや長くする
のが好ましい。一例として、直径70cmピツチ7cm
のスクリユーフイーダを使用して毎分200Kg/時
の搬送量を有する分量装置においては、スロツト
状排出口の幅は1cm長手方向長さは10cmである。
上述したように、排出口の軸方向長さはピツチと
無関係に決めることはできないが、その幅および
排出管軸方向に対する角度またはスクリユーフイ
ーダの羽根との交差角は任意に決定することがで
きる。また貯槽後壁に形成される空気取入れ口3
1dの面積は撹拌装置、スクリユーフイーダの回
転速度により設計上任意に設定される。 Next, the operation of the dispensing device according to the present invention will be explained.
When separating a predetermined small amount from the powder and granular material stored in the storage tank 31, first, the control panel 34 is operated to set a predetermined amount. Next, press the start portion button.
The drive device 21 in the metering device main body 2 is energized, the stirring device 32 and the screw feeder 33 begin to rotate, and the stirring device 32 supplies the powder to the screw feeder 33. At this time, the air taken into the storage tank from the air intake port 31d of the storage tank 31 due to the stirring passes through the space P as shown by the arrow and is drawn into the powder and granules being stirred, fluidizing the powder and granule layer. At the same time, it becomes homogenized, so screw feeder 3
The layer of powder and granules fed into the storage tank 3 is made uniform without being affected by the amount of powder and granules remaining inside the storage tank. Air drawn into the powder and granules being stirred is passed through the air intake port 31.
It is cleaned with a punched medal or cloth stretched over d. In this way Screw Feeder 3
As the shaft 33a filled between the spiral blades 33b rotates, the granular material fed into the storage tank 31 is conveyed from the storage tank 31 toward the discharge pipe 24, and reaches the discharge port 24a at the end of the discharge pipe 24. The change in the area of the powder and granular material at the discharge port 24a is determined by the screw feeder 3.
As 3 progresses step by step, it increases almost linearly with a small rate of change. As a result, the outlet 24
The change in the amount of powder discharged from a is relatively small. On the other hand, since the conventional outlet has a circular or rectangular shape, the rate of increase in the outlet area is non-linear and changes rapidly in the initial stage.
Changes in the amount of powder discharged from the discharge port are extremely large and discontinuous. From this, it can be easily understood that it is difficult to discharge a fixed amount using conventional dispensing devices. In this way, by forming the outlet into a narrow slot with its longitudinal direction intersecting the blades of the screw feeder, the rate of increase in the outlet area is made almost linear and gradual. As a result, changes in the amount of powder and granular material discharged from the discharge port can be made small and continuous. In order to further improve quantitative performance, it is preferable that the length of the slot in the direction of the discharge pipe be slightly longer than one pitch of the screw feeder. As an example, the diameter is 70 cm and the pitch is 7 cm.
In a dosing device using a screw feeder with a transport rate of 200 kg/hour, the width of the slot-shaped outlet is 1 cm and the longitudinal length is 10 cm.
As mentioned above, the axial length of the discharge port cannot be determined independently of the pitch, but its width and angle with respect to the axial direction of the discharge pipe or intersecting angle with the screw feeder blades can be arbitrarily determined. can. Also, the air intake port 3 formed on the rear wall of the storage tank
The area 1d is arbitrarily set according to the rotational speed of the stirring device and the screw feeder.
なお、本発明の分量装置は小麦粉等の微粉体の
ほか小麦粒、米穀類、パン粉のような粒状体にも
利用することができることはもちろんである。 It goes without saying that the metering device of the present invention can be used not only for fine powders such as wheat flour but also for granular materials such as wheat grains, rice grains, and bread crumbs.
添付図面の第1図は本発明に係る粉粒体分量装
置の概略図、第2図は分量装置の要部である貯槽
と粉粒体搬送排出系との関係を示す概略図、第3
図は第2図のA―A線に沿つて見た断面図、第4
図は粉粒体排出管の斜視図である。
1……分量装置、2……装置本体、21……駆
動装置、22……重量検出装置、23……計量
器、24……排出管、24a……排出口、3……
定量供給装置、31……貯槽、31a……装入
口、31b……内壁、31c……ノーズ、31d
……空気取入れ口、32……撹拌装置、32a…
…回転軸、32b,33b……羽根、33……ス
クリユーフイーダ、33a……軸、34……制御
盤。
FIG. 1 of the accompanying drawings is a schematic diagram of a powder/granular material dispensing device according to the present invention, FIG. 2 is a schematic diagram showing the relationship between a storage tank, which is a main part of the dispensing device, and a powder/granular material conveyance/discharge system, and FIG.
The figure is a cross-sectional view taken along line A-A in Figure 2.
The figure is a perspective view of a powder discharge pipe. DESCRIPTION OF SYMBOLS 1... Measuring device, 2... Apparatus body, 21... Drive device, 22... Weight detection device, 23... Measuring device, 24... Discharge pipe, 24a... Discharge port, 3...
Quantitative supply device, 31...Storage tank, 31a...Charging port, 31b...Inner wall, 31c...Nose, 31d
... Air intake, 32 ... Stirring device, 32a...
...rotating shaft, 32b, 33b...blade, 33...screw feeder, 33a...shaft, 34...control panel.
Claims (1)
た粉粒体を攪拌する攪拌装置と、粉粒体を排出口
へ供給する排出装置とからなる粉粒体の分量装置
において、前記貯槽の側壁のほぼ中央部に空気取
入口と、貯槽の内部中心付近まで側壁より延在す
るノーズとを設け、前記空気取入口は貯槽の側壁
内面と前記ノーズとにより形成される内部空間に
連通していて、前記空気取入口から取入れられる
空気は前記内部空間を通して攪拌される粉粒体に
接触せしめられるようにした分量装置。 2 前記排出装置をらせん状羽根を有するスクリ
ユーフイーダで構成し、前記スクリユーフイーダ
を前記スクリユーフイーダのらせん状羽根と交差
する方向に長手方向を有する幅狭のスロツト状と
して形成した特許請求の範囲第1項に記載の分量
装置。[Scope of Claims] 1. Amount of powder and granular material consisting of a storage tank for storing powder and granular material, an agitation device provided at the bottom of the storage tank for stirring the powder and granular material, and a discharge device that supplies the powder and granular material to a discharge port. In the device, an air intake port is provided approximately in the center of a side wall of the storage tank, and a nose extends from the side wall to near the interior center of the storage tank, and the air intake port is formed by the inner surface of the side wall of the storage tank and the nose. A dispensing device communicating with an internal space, the air taken in from the air intake port being brought into contact with powder and granular material being stirred through the internal space. 2. The discharge device is constituted by a screw feeder having a spiral blade, and the screw feeder is formed in a narrow slot shape having a longitudinal direction in a direction intersecting the spiral blade of the screw feeder. Dispensing device according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP907979A JPS55101820A (en) | 1979-01-31 | 1979-01-31 | Granular solid distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP907979A JPS55101820A (en) | 1979-01-31 | 1979-01-31 | Granular solid distributor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55101820A JPS55101820A (en) | 1980-08-04 |
| JPS6245488B2 true JPS6245488B2 (en) | 1987-09-28 |
Family
ID=11710601
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP907979A Granted JPS55101820A (en) | 1979-01-31 | 1979-01-31 | Granular solid distributor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS55101820A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61152926U (en) * | 1985-03-14 | 1986-09-22 | ||
| JPH06241869A (en) * | 1992-05-21 | 1994-09-02 | Ishimura Kogyo Kk | Metering apparatus |
| JP5705638B2 (en) * | 2011-04-27 | 2015-04-22 | 大和製衡株式会社 | Weighing object supply device |
| JP6805486B2 (en) * | 2015-11-09 | 2020-12-23 | 大同特殊鋼株式会社 | Transport device |
-
1979
- 1979-01-31 JP JP907979A patent/JPS55101820A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55101820A (en) | 1980-08-04 |
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