JP4132394B2 - Powder and particle feeder - Google Patents

Powder and particle feeder Download PDF

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Publication number
JP4132394B2
JP4132394B2 JP12321099A JP12321099A JP4132394B2 JP 4132394 B2 JP4132394 B2 JP 4132394B2 JP 12321099 A JP12321099 A JP 12321099A JP 12321099 A JP12321099 A JP 12321099A JP 4132394 B2 JP4132394 B2 JP 4132394B2
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Japan
Prior art keywords
wall
storage tank
granular material
space
gas
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JP12321099A
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Japanese (ja)
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JP2000313526A (en
Inventor
一夫 岸本
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Shibuya Machinery Co Ltd
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Shibuya Machinery Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、重曹等の粉粒体を貯留し順次目的部へ供給するための粉粒体供給装置に関する。より詳しくは、貯留タンク内の粉粒体を乾燥するための加熱手段に関するものであり、その加熱効率を改善するための改良技術に関する。
【0002】
【従来の技術】
粉粒体供給装置において、貯留タンク内の粉粒体を加熱して乾燥するため、貯留タンクの壁部に加熱手段を付設したものや、乾燥空気を貯留タンクの下方から導入するものが従来から知られている(実開平4−70466号公報、実開昭61−202459号公報参照)。しかしながら、前者の貯留タンクの壁部に加熱手段を付設した従来技術の場合には、その加熱手段の付設された壁部近傍の粉粒体は良好に加熱されるが、壁部から離れると充分な加熱作用が得られないといった難点があった。しかも、加熱手段の外方への放熱が無駄になり熱効率もよいとはいえなかった。他方、後者の貯留タンクの下方から乾燥空気を導入する従来技術の場合には、タンク内の粉粒体に対する内側からの加熱作用は得やすいが、逆にタンク壁部からの外部への放熱により壁部近傍の粉粒体の温度は低下しやすいという問題があった。なお、乾燥空気の導入量を多くすれば、壁部からの放熱を補うことは可能であるが、あまり多くすると軽い粉粒体の場合には舞上がってしまい、粉粒体の供給状態の安定性にも影響するといった難点があった。そこで、両者の加熱手段を兼ね備えた従来技術も開示されているが、別個の加熱手段が必要とされるばかりでなく、貯留タンクの壁部に付設された加熱手段の外方への放熱による無駄は依然として解消されていない。(特開昭63−310418号公報参照)。
【0003】
【発明が解決しようとする課題】
本発明は、以上のような従来の技術事情に鑑みて開発したもので、貯留タンク内の粉粒体に対するタンク壁部からの加熱と加熱気体を用いたタンク内部からの加熱の双方の加熱をより熱効率よく実施し得る粉粒体供給装置を提供することを目的とするものである。
【0004】
【課題を解決するための手段】
前記課題を解決するため、本発明は、下部に排出口を有する粉粒体の貯留タンクを内壁と外壁の間に空間を有する二重壁から構成し、その内壁に加熱手段を付設するとともに、外気等の気体が前記空間にて加熱された後、前記貯留タンク内へ流入するように構成するという技術手段を採用した。これにより本発明によれば、内壁に付設した加熱手段によりタンク壁部が加熱されるので、壁部からの放熱による温度低下などの問題が解消されると同時に、その加熱手段の外方への放熱を有効利用して加熱した気体によって粉粒体をタンク内部から加熱することができる。したがって、貯留タンク内の粉粒体を熱効率よく内外から加熱することができる。なお、粉粒体搬送用の圧力流体の高速噴流に基づく吸引作用によって前記排出口に接続された搬出手段を介して粉粒体を供給するように構成することができる。この場合には、内壁と外壁との空間を経て加熱された後、貯留タンク内に流入する気体が粉粒体と共に排出口側に吸引されるので、タンク内での加熱気体の流通が促進される。また、粉粒体搬送用の圧力気体の供給管と前記空間とを接続して、気体を該空間を経て貯留タンク内に圧送するように構成することも可能である。
【0005】
【発明の実施の形態】
本発明は、ブラスト加工用のブラスト材としての重曹など、各種の粉粒体の供給装置に広く適用することができる。前記貯留タンクの内壁と外壁との空間を経て加熱されながらタンク内に流入して粉粒体をタンク内部から加熱する気体としては、外気をそのまま利用したものでもよいし、例えば余熱をして予め除湿をしたり静電気除去機能を付加するなどの適宜の処理を施した気体を用いることも可能である。その気体の供給に関しては、前記空間を経て貯留タンク内に吸引されるように構成してもよいし、圧力をかけて貯留タンク内に圧送するように構成してもよい。また、前記空間に対する気体の流入及び貯留タンク内への流れに関しては、その空間の下部から流入させて上部からタンク内へ流出するように構成してもよいし、逆に同空間の上部から流入させて下部からタンク内へ流出するように構成することも可能である。前記内壁に付設する加熱手段としては、シリコンラバーヒータ等の面状ヒータが好適であり、前記内壁の外面側すなわち空間側に付設してもよいし、内面側すなわちタンクの内側に付設するようにしてもよい。要するに、加熱手段の付設により、タンク内の内壁近傍から粉粒体を加熱するとともに、その加熱手段の外方への放熱を気体の加熱によって回収した上、貯留タンク内に流入して粉粒体の加熱に使用することにより全体の熱効率を向上し得るものであればよい。なお、内壁と外壁との前記空間を螺旋状に仕切って気体の加熱時間を長くすれば加熱効果を更に向上できる。貯留タンクの排出口から粉粒体を排出するための搬出手段としては、スクリュウコンベヤなどの種々のタイプのものが適用可能である。また、必要に応じて貯留タンク内に適宜の撹拌手段を配設することができる。
【0006】
【実施例】
以下、図面を用いて本発明の実施例に関して説明する。図1は本発明の一実施例の要部を示した概略構成図であり、図2はその部分拡大図である。また、図3は図1のA−A断面図である。図中、1は貯留タンクで、上方に蓋体2により閉じられた広い投入口を有し、下方に絞られた排出口3を有する変形された逆四角錐状に形成されている。図2に拡大して示したように、貯留タンク1を構成する各壁面は内壁4と外壁5から構成され、それらの内壁4と外壁5との間に気体の通路となる空間6を形成した二重壁構造が採用されている。その各内壁4の外面側すなわち空間6側には面状ヒータ7が付設されており、内壁4を通してタンク内部の粉粒体を加熱し得るように構成されている。なお、本実施例では、貯留タンク1を構成する全ての壁面を二重壁構造としているが、一部の壁面だけを二重壁構造とし、その壁面だけに面状ヒータ7を設ける形態も可能である。前記外壁5の下部には空間6に連通した多数の流入孔8が形成され、他方の内壁4の上部には貯留タンク1内に連通した多数の流出孔9が形成されており、本実施例では後述のようにそれらの流入孔8及び流出孔9を介して外気が貯留タンク1内に吸引されるように構成されている。そして、流入孔8から吸引された外気は、空間6を通過する際に面状ヒータ7の外方への放熱を吸収して加熱された上、流出孔9から貯留タンク1内に流入して内部の粉粒体を加熱することになる。図中、10は撹拌手段、11はその駆動手段であり、空間6を経て貯留タンク1内に流入した外気等からなる加熱気体と粉粒体とを混合し、タンク内全体をより効果的かつ平均的に加熱することができる。なお、12は蓋体2の取っ手である。
【0007】
前記排出口3の下部にはモータ13により駆動されるスクリュウコンベヤ14からなる搬出手段が配設されており、搬出管15を介して粉粒体を貯留タンク1から搬出するように構成されている。搬出管15は、ルーツブロア等の圧力空気供給手段16から圧力空気管17を介して供給される圧力空気がノズル18を経て高速噴射される混合室19に接続されている。しかして、ノズル18を介して混合室19に噴射された高速空気流のエジェクタ作用により粉粒体が搬出管15を経て吸引され、それらの高速空気流と粉粒体とが混合しながら供給管20を経て例えばブラスト加工用の噴射ノズル21等の目的部へ供給されることになる。なお、以上のようにノズル18を介して噴射される高速空気流のエジェクタ作用により混合室19内が負圧になるので、搬出管15を介して搬出される粉粒体と共に内壁4と外壁5との空間6を経て貯留タンク1内に流入した加熱気体も吸引されて排出される。その結果、前記流入孔8を介して新しい外気が空間6に吸引されることになる。なお、本実施例では、前記高速空気流に替えて高速水流等の他の流体を採用することも可能である。また、粉粒体の供給中は貯留タンク1内が負圧状態になることから、粉粒体の供給中を含めて適宜な時期に蓋体2をあけて粉粒体を投入することが可能である。図中、22は必要に応じて混合室19に外気を吸引補給するための通気管、23はその開閉弁である。
【0008】
図4は本発明の他の実施例の要部を示した概略構成図である。本実施例は前記実施例の変形例で、同じ構成部分には同じ符号を付して説明すると、圧力空気管17の途中から気体供給管24を分岐して貯留タンク1の内壁4と外壁5との間の空間6に接続することにより空気等の気体を強制的に供給し得るように構成した点でのみ特徴を有し、他の点では同様の機能を奏する。この場合、気体供給管24内の内圧は、途中の管路抵抗の差を捨象すると、ノズル18の流路抵抗による圧力低下分と同ノズル18を介して噴射された高速空気流のエジェクタ作用に基づく負圧分を加えた分だけ混合室19の内圧より高くなり、貯留タンク1内での加熱気体の流通が更に促進される。すなわち、本実施例では、前記空間6を経て貯留タンク1内に供給される加熱空気からなる加熱気体は、それらの気体供給管24の供給圧とノズル18を介して噴射された高速空気流のエジェクタ作用による吸引作用によって、より強制的に貯留タンク1内を流通しながら粉粒体を加熱して搬出管15から目的部へ供給されることになる。なお、本実施例では、貯留タンク1内が加圧されるため、その内圧によって前記蓋体2が開かないように構成する。例えば、図示のように蓋体2の板厚を増して自重を大きくしたり締付手段を設けるようにする。
【0009】
【発明の効果】
本発明によれば、貯留タンクを内壁と外壁との間に空間を形成した二重壁構造とし、その内壁に加熱手段を付設してタンク壁部近傍から粉粒体を加熱するとともに、前記加熱手段の外方への放熱は気体を加熱することにより回収し、その加熱気体によって粉粒体をタンク内部から加熱するように構成したので、貯留タンク内の内外から粉粒体を全般的に有効に加熱し得るとともに、その熱効率を大幅に改善できる。また、粉粒体を粉粒体搬送用の圧力流体の高速噴流に基づく吸引作用によって排出して目的部へ供給するように構成すれば、前記空間を経て加熱された後、貯留タンク内に流入する気体は、粉粒体と共に排出口側に吸引されるので、タンク内での加熱気体の流通が促進される。また、粉粒体搬送用の圧力気体を前記空間を経て貯留タンク内に圧送するように構成すれば、タンク内での加熱気体の流通を更に促進することができる。
【図面の簡単な説明】
【図1】 本発明の実施例の要部を示した概略構成図である。
【図2】 図1の部分拡大図である。
【図3】 図1のA−A断面図である。
【図4】 本発明の他の実施例の要部を示した概略構成図である。
【符号の説明】
1…貯留タンク、2…蓋体、3…排出口、4…内壁、5…外壁、6…空間、7…面状ヒータ、8…流入孔、9…流出孔、10…撹拌手段、11…駆動手段、12…取っ手、13…モータ、14…スクリュウコンベヤ、15…搬出管、16…圧力空気供給手段、17…圧力空気管、18…ノズル、19…混合室、20…供給管、21…噴射ノズル、22…通気管、23…開閉弁、24…気体供給管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a granular material supply device for storing and sequentially supplying granular materials such as baking soda to a target part. More specifically, the present invention relates to a heating means for drying powder particles in a storage tank, and relates to an improved technique for improving the heating efficiency.
[0002]
[Prior art]
In the powder supply device, in order to heat and dry the powder in the storage tank, a heating tank is attached to the wall of the storage tank, or dry air is introduced from below the storage tank. It is known (see Japanese Utility Model Laid-Open No. 4-70466, Japanese Utility Model Laid-Open No. 61-202459). However, in the case of the prior art in which the heating means is attached to the wall of the former storage tank, the granular material in the vicinity of the wall to which the heating means is attached is satisfactorily heated. There was a problem that a proper heating action could not be obtained. In addition, heat radiation to the outside of the heating means is wasted and it cannot be said that the thermal efficiency is good. On the other hand, in the case of the prior art in which dry air is introduced from below the latter storage tank, it is easy to obtain a heating action from the inside to the powder particles in the tank, but conversely by heat radiation from the tank wall to the outside. There existed a problem that the temperature of the granular material near a wall part fell easily. If the amount of dry air introduced is increased, it is possible to compensate for heat dissipation from the wall, but if it is increased too much, it will rise in the case of light particles, and the supply state of the particles will be stable. There was a difficulty of affecting the sex. Therefore, the prior art having both heating means is disclosed, but not only a separate heating means is required, but also waste due to heat radiation to the outside of the heating means attached to the wall of the storage tank. Is still not resolved. (Refer to Unexamined-Japanese-Patent No. 63-310418).
[0003]
[Problems to be solved by the invention]
The present invention has been developed in view of the above-described conventional technical circumstances, and both heating from the tank wall to the granular material in the storage tank and heating from the inside of the tank using a heated gas are performed. It aims at providing the granular material supply apparatus which can be implemented more efficiently.
[0004]
[Means for Solving the Problems]
In order to solve the above problems, the present invention comprises a storage tank of granular material having a discharge port in the lower part, comprising a double wall having a space between an inner wall and an outer wall, and a heating means is attached to the inner wall, A technical means is adopted in which a gas such as outside air is heated in the space and then flows into the storage tank. Thus, according to the present invention, the tank wall portion is heated by the heating means attached to the inner wall, so that problems such as a temperature drop due to heat radiation from the wall portion are solved, and at the same time, the heating means is moved outward. The granular material can be heated from the inside of the tank by the gas heated by effectively utilizing the heat radiation. Therefore, the granular material in the storage tank can be heated efficiently from inside and outside. In addition, it can comprise so that a granular material may be supplied via the carrying-out means connected to the said discharge port by the attraction | suction effect | action based on the high-speed jet of the pressure fluid for granular material conveyance. In this case, after heating through the space between the inner wall and the outer wall, the gas flowing into the storage tank is sucked together with the particulates to the discharge port side, so the circulation of the heated gas in the tank is promoted. The It is also possible to connect the pressure gas supply pipe for conveying the granular material and the space so as to pressure-feed the gas into the storage tank through the space.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
The present invention can be widely applied to various powder and granular material supply devices such as baking soda as a blasting material for blasting. As the gas that flows into the tank while being heated through the space between the inner wall and the outer wall of the storage tank and heats the granular material from the inside of the tank, the outside air may be used as it is. It is also possible to use a gas that has been subjected to an appropriate treatment such as dehumidifying or adding a static electricity removing function. Regarding the supply of the gas, the gas may be sucked into the storage tank through the space, or may be configured to be pumped into the storage tank under pressure. In addition, regarding the inflow of gas into the space and the flow into the storage tank, it may be configured to flow in from the lower part of the space and flow out from the upper part into the tank. It is also possible to make it flow out from the lower part into the tank. The heating means attached to the inner wall is preferably a planar heater such as a silicon rubber heater, and may be attached to the outer surface side of the inner wall, that is, the space side, or may be attached to the inner surface side, that is, the inside of the tank. May be. In short, by adding the heating means, the granular material is heated from the vicinity of the inner wall in the tank, and the heat radiation to the outside of the heating means is recovered by heating the gas, and then flows into the storage tank and flows into the storage tank. Any material can be used as long as it can improve the overall thermal efficiency. Note that the heating effect can be further improved if the space between the inner wall and the outer wall is partitioned in a spiral manner to increase the gas heating time. Various types of devices such as a screw conveyor can be applied as the carrying-out means for discharging the granular material from the discharge port of the storage tank. Moreover, a suitable stirring means can be arrange | positioned in a storage tank as needed.
[0006]
【Example】
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a schematic diagram showing the main part of one embodiment of the present invention, and FIG. 2 is a partially enlarged view thereof. FIG. 3 is a cross-sectional view taken along the line AA in FIG. In the figure, reference numeral 1 denotes a storage tank, which is formed in a modified inverted quadrangular pyramid shape having a wide inlet closed by a lid 2 at the top and a discharge outlet 3 throttled downward. As shown in an enlarged view in FIG. 2, each wall surface constituting the storage tank 1 is composed of an inner wall 4 and an outer wall 5, and a space 6 serving as a gas passage is formed between the inner wall 4 and the outer wall 5. Double wall structure is adopted. A planar heater 7 is provided on the outer surface side of each inner wall 4, that is, on the space 6 side, and is configured to heat the granular material inside the tank through the inner wall 4. In this embodiment, all the wall surfaces constituting the storage tank 1 have a double wall structure. However, only a part of the wall surfaces has a double wall structure, and the planar heater 7 is provided only on the wall surface. It is. A number of inflow holes 8 communicating with the space 6 are formed in the lower part of the outer wall 5, and a number of outflow holes 9 communicating with the interior of the storage tank 1 are formed in the upper part of the other inner wall 4. Then, as will be described later, the outside air is sucked into the storage tank 1 through the inflow hole 8 and the outflow hole 9. The outside air sucked from the inflow hole 8 is heated by absorbing heat radiated outward from the planar heater 7 when passing through the space 6, and then flows into the storage tank 1 from the outflow hole 9. The internal powder will be heated. In the figure, 10 is an agitation means, and 11 is a drive means for mixing the heated gas composed of the outside air and the like flowing into the storage tank 1 through the space 6 and the powder and more effectively the entire tank. It can be heated on average. Reference numeral 12 denotes a handle of the lid 2.
[0007]
Unloading means comprising a screw conveyor 14 driven by a motor 13 is disposed below the discharge port 3, and is configured to unload powder particles from the storage tank 1 via a discharge tube 15. . The carry-out pipe 15 is connected to a mixing chamber 19 in which pressurized air supplied from a pressurized air supply means 16 such as a Roots blower through a pressurized air pipe 17 is jetted through a nozzle 18 at a high speed. Thus, the powder particles are sucked through the carry-out pipe 15 by the ejector action of the high-speed air flow injected into the mixing chamber 19 through the nozzle 18, and the supply pipe is mixed while the high-speed air flow and the powder particles are mixed. 20 is supplied to a target portion such as an injection nozzle 21 for blasting. In addition, since the inside of the mixing chamber 19 becomes a negative pressure due to the ejector action of the high-speed air flow injected through the nozzle 18 as described above, the inner wall 4 and the outer wall 5 together with the powder particles carried out through the carry-out pipe 15. The heated gas flowing into the storage tank 1 through the space 6 is also sucked and discharged. As a result, new outside air is sucked into the space 6 through the inflow hole 8. In this embodiment, other fluids such as a high-speed water flow can be employed instead of the high-speed air flow. Moreover, since the inside of the storage tank 1 is in a negative pressure state during the supply of the powder, the cover 2 can be opened at an appropriate time including the supply of the powder and the powder can be charged. It is. In the figure, 22 is a vent pipe for sucking and supplying outside air to the mixing chamber 19 as necessary, and 23 is an opening / closing valve thereof.
[0008]
FIG. 4 is a schematic configuration diagram showing the main part of another embodiment of the present invention. This embodiment is a modification of the above embodiment, and the same components are denoted by the same reference numerals. When the gas supply pipe 24 is branched from the middle of the pressure air pipe 17, the inner wall 4 and the outer wall 5 of the storage tank 1 are branched. It has a feature only in that it is configured to be able to forcibly supply a gas such as air by being connected to the space 6 between them, and the same function is exhibited in other points. In this case, if the internal pressure in the gas supply pipe 24 is discarded, the pressure drop due to the flow path resistance of the nozzle 18 and the ejector action of the high-speed air flow injected through the nozzle 18 are eliminated. The internal pressure of the mixing chamber 19 becomes higher by the amount of the negative pressure based on it, and the circulation of the heated gas in the storage tank 1 is further promoted. In other words, in the present embodiment, the heated gas composed of heated air supplied into the storage tank 1 through the space 6 is supplied from the supply pressure of the gas supply pipe 24 and the high-speed air flow injected through the nozzle 18. By the suction action by the ejector action, the granular material is heated while being forced to flow through the storage tank 1 and supplied from the carry-out pipe 15 to the target portion. In this embodiment, since the inside of the storage tank 1 is pressurized, the lid body 2 is configured not to be opened by the internal pressure. For example, as shown in the drawing, the thickness of the lid 2 is increased to increase its own weight or to provide tightening means.
[0009]
【The invention's effect】
According to the present invention, the storage tank has a double wall structure in which a space is formed between the inner wall and the outer wall, and the heating means is attached to the inner wall to heat the granular material from the vicinity of the tank wall, and the heating The heat radiation to the outside of the means is collected by heating the gas, and the powder is heated from the inside of the tank by the heated gas, so the powder is generally effective from inside and outside the storage tank. And the thermal efficiency can be greatly improved. Further, if it is configured so that the granular material is discharged by a suction action based on a high-speed jet of pressure fluid for conveying the granular material and supplied to the target portion, it is heated through the space and then flows into the storage tank. Since the gas to be drawn is sucked to the discharge port side together with the granular material, the circulation of the heated gas in the tank is promoted. Moreover, if the pressure gas for conveying the granular material is configured to be pumped into the storage tank through the space, the flow of the heated gas in the tank can be further promoted.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram showing a main part of an embodiment of the present invention.
FIG. 2 is a partially enlarged view of FIG.
FIG. 3 is a cross-sectional view taken along the line AA of FIG.
FIG. 4 is a schematic configuration diagram showing a main part of another embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Storage tank, 2 ... Cover, 3 ... Discharge port, 4 ... Inner wall, 5 ... Outer wall, 6 ... Space, 7 ... Planar heater, 8 ... Inflow hole, 9 ... Outflow hole, 10 ... Stirring means, 11 ... Drive means, 12 ... handle, 13 ... motor, 14 ... screw conveyor, 15 ... unloading pipe, 16 ... pressure air supply means, 17 ... pressure air pipe, 18 ... nozzle, 19 ... mixing chamber, 20 ... supply pipe, 21 ... Injection nozzle, 22 ... vent pipe, 23 ... on-off valve, 24 ... gas supply pipe

Claims (3)

下部に排出口を有する粉粒体の貯留タンクを内壁と外壁の間に空間を有する二重壁から構成し、その内壁に加熱手段を付設するとともに、外気等の気体が前記空間にて加熱された後、前記貯留タンク内へ流入するように構成したことを特徴とする粉粒体供給装置。The powder storage tank having a discharge port in the lower part is composed of a double wall having a space between the inner wall and the outer wall, and heating means is attached to the inner wall, and gas such as outside air is heated in the space. After that, it is configured to flow into the storage tank. 粉粒体搬送用の圧力流体の高速噴流に基づく吸引作用によって前記排出口に接続された搬出手段を介して粉粒体を供給するように構成した請求項1に記載の粉粒体供給装置。The granular material supply apparatus according to claim 1, wherein the granular material is supplied through a discharging means connected to the discharge port by a suction action based on a high-speed jet of pressure fluid for conveying the granular material. 粉粒体搬送用の圧力気体の供給管を前記空間に接続し、気体を該空間を経て貯留タンク内に圧送するように構成した請求項1又は2に記載の粉粒体供給装置。The granular material supply apparatus according to claim 1 or 2, wherein a pressure gas supply pipe for conveying granular material is connected to the space, and the gas is pumped into the storage tank through the space.
JP12321099A 1999-04-28 1999-04-28 Powder and particle feeder Expired - Fee Related JP4132394B2 (en)

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Publication number Priority date Publication date Assignee Title
JP2002179250A (en) * 2000-12-13 2002-06-26 Fujisash Co Reserving method and reserving device of fly ash
CN105966648A (en) * 2016-06-30 2016-09-28 哈尔滨尼亚农业有限公司 Bagging device for producing granular fertilizer raw materials
CN111263875B (en) 2017-10-26 2022-04-08 惠而浦公司 Vacuum-assisted heating screw feeder for improving packaging efficiency of powder insulation material in vacuum insulation structure
EP3869132B1 (en) * 2018-09-05 2023-08-09 Whirlpool Corporation A filling system for a vacuum insulated structure

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